QUENCHING TECHNICAL CONTENT

How CQI-9 Compliant Quench Oil Analysis Can Aid in Proper Care of Quench Oil

OCCQI-9 compliance demands adherence to the standards for the purpose of excellence in automotive heat treating. Poorly maintained quench oil can cost heat treaters in many areas. 

In this Heat Treat Today Technical Tuesday featureGreg Steiger, senior key account manager at Idemitsu Lubricants America, shares how costly quench oil issues can be addressed through proper adherence to the CQI-9 quench oil testing protocols. Let us know if you’d like to see more Original Content features by emailing editor@heattreattoday.com.


Greg Steiger
Sr. Key Account Manager
Idemitsu Lubricants America

Introduction

A poorly maintained quench oil can cost a heat treater in more ways than simply the cost of having to replace the oil.  The costs can quickly expand to include those associated with poor quality.  For example, costs associated with part rejects, or rework and downstream costs for shot blasting, or third-party inspection are often the cause of poor quench oil maintenance.  Dirty or poorly maintained oils can affect part cleanliness, surface hardness, and surface finish.  For instance, it is well known that a heavily oxidized oil may create surface stains that must be shot blasted to remove.  High molecular weight sludge or excessive water can create surface hardness issues.  Many of these issues can be addressed through proper adherence to the quench oil testing protocols established by CQI-9.

How can CQI-9 help?

CQI-9 is designed as a tool to help heat treaters produce consistent parts.  Using a CQI-9 compliant quench oil analysis can also be a very powerful tool in a heat treaters tool kit.  Just as the level of carburization is influenced by the carbon potential of a carburizing atmosphere, the cooling speed of the oil influences microstructure formation and microstructure composition along with mechanical properties such as hardness as well as tensile and yield strength. Furthermore, the cooling speed is dependent upon the viscosity of the oil, the amount of sludge, moisture level, and oxidation of the oil.  All of these are tested on a regular basis under the requirements of CQI-9, ISO TS 16949, and most quality systems adopted by modern heat treaters.  All of the tested parameters required under CQI-9 will be addressed individually later in this paper.

What is CQI-9?

The member companies of the Automotive Industry Action Group (AIAG) encompassing automotive manufacturers and their Tier I suppliers have enacted an industry heat treating standard called CQI-91.  This standard was originally a standalone standard designed and adhered to primarily by North American OEMs and Tier I suppliers as a quality tool to create consistent documented processes within the heat treating industry with the goal of producing consistent reproducible results.  Since that first implementation of CQI-9, the standard has now been incorporated into the ISO TS 16949 standard and is now adhered to by most automotive OEMs and their Tier I suppliers.  The full range of management responsibilities, material handling, and equipment operations of the CQI-9 standard is beyond the scope of this paper.   Instead we will be discussing the used quench oil analysis requirements of CQI-9, why the tests are required, and how heat treaters need a CQI-9 compliant quench oil analysis to properly care for their quench oils.

Utilizing a compliant CQI-9 analysis and the supplier provided operating parameters for the CQI-9 required tests is the first step in the proper care of a quench oil.

CQI-9 Compliant Analysis

Most quench oil suppliers provide a quench oil analysis.  Although the quench oil supplier may provide a quench oil analysis, for the analysis to be CQI-9 compliant the analysis must contain the following tests or their equivalent:

  • Water content; ASTM D6304
  • Suspended solids; ASTM D4055
  • Viscosity; ILASD509
  • Total acid value; ASTM D664
  • Flash point; ASTM D92
  • Cooling curve; JIS K2242

The frequency of the above testing must be a minimum of semiannually.  A more frequent sampling interval does not violate CQI-9.  In fact, the more often a quench oil is analyzed, the easier it is to use the quench oil analysis as a tool in the proper care of a quench oil.  It is important to note that the CQI-9 standard does not prescribe specific test methods be used in the above testing; however, they must be performed to a traceable standard.  The CQI-9 standard only states that the above values, along with a cooling curve, must be reported.   The following sections will describe each test in a CQI-9 compliant analysis.

Water Content

Everyone knows water in a quench oil can be have catastrophic safety and performance consequences.  However how much water is too much?  That is a question that is difficult to answer.  The answer depends on a variety of factors such as the quench oil used and all of the variables associated with a furnace atmosphere.  A general rule of thumb when it comes to water levels is to keep the water level below 200PPM.  At levels above 200PPM of water, uneven cooling begins to occur.2  It is important to remember a quench oil is not a pure homogenous fluid.   Samples taken at various places throughout the quench tank will be similar but will also have differences.  These differences will include water and solids levels.  Therefore, in areas where the water content exceeds the 200PPM level, uneven cooling will begin.  Parts coming into contact with this “localized” quench oil with high water can potentially begin to crack, have a high surface hardness, or have staining problems.  Yet parts in other areas of the load continue to behave normally.  For this reason, and also because water is much heavier than oil, it is imperative the oil be under agitation. In addition to the potential uneven cooling issues high water may create, a high level of water can also influence the rate of oxidation in an oil.

Suspended Solids

Because solids are typically denser and more viscous than liquids they do not have the same heat transfer properties as a liquid. Due to the inequality of heat transfer capacities between liquids and solids, it is very important to keep the solids level, especially high molecular weight sludge, at a minimum.  Sludge reacts in an opposite manner of water.  Where water can increase quench speed, high molecular weight sludge will decrease quench speed through uneven cooling.2 The result of the uneven cooling from sludge is typically seen in soft surface microstructures or soft surface hardness.  Also, like water, sludge is heavier than oil and the lack of homogeneity in the oil means having proper agitation is paramount when sampling.

Viscosity

Changes in viscosity can lead to both faster quench rates and slower quench rates.  As the quench oil is used in the quench process, it undergoes thermal degradation.3  This degradation process can be seen when the oil becomes thinner or less viscous.  During this process, a small portion of the base oil and a small amount of the quench oil additives undergo a process called thermal cracking.  In this process, heavier molecules are broken into smaller molecules through the use of heat. This thermal cracking creates lighter less viscous oil from heavier oils.  The newer lighter viscosity of the quench oil can potentially lead to changes in the quench speed of the oil.  These changes can have an impact on the microstructure, case depth, core hardness, and surface hardness on the quenched parts.

As an oil is subjected to the high temperatures of a quenching operation, oxidation is a natural occurrence in the oil.    As the oil oxidizes it will begin to increase in viscosity until it reaches the point of forming an insoluble sludge.  Therefore, an increase in viscosity typically means the oil is oxidizing.  Just as an oil that becomes thinner and less viscous may have a change in cooling properties, an oil that becomes thicker and more viscous may see a change in cooling performance.   A thicker oxidized quench oil may affect surface hardness, microstructure, case depth, and core hardness.  In severe cases of oxidation staining may result.  Such stains typically require post quench and temper processing such as shot blasting.

Total Acid Value

The Total Acid Value, or TAV, is a measure of the level of oxidation in a quench oil.  The amount of oxygen in a quench oil cannot be measured without a sophisticated laboratory analysis.  However, the formation of organic acids within a quench oil can be easily determined via a titration method.  It is well understood that these organic acids are the precursors in a chain of chemical reactions that will eventually form sludge. As the TAV increases so will the levels of oxidation, and in turn, the amount of sludge will also increase.  Consequently, as the TAV increases, the amount of staining due to oxidation may increase.  The cooling properties of the oil may decrease due to the increased sludge formation as well.  Figure #1 shows an example of how the acid value increases the viscosity of a quench oil due to the formation of polymeric sludge in the quench oil.2

Figure #1. Acid number vs kinematic viscosity for Daphne Hi Temp A

 

Flash point

The flash point of a quench oil is another check to ensure the safety of the quench oil user.   As oil thermally cracks, the heavier base oils become not only lighter in viscosity, but their flash points also decrease.  If left unchecked, the decrease in flash point could result in a higher risk of fire.   In addition to serving as a watchdog against the results of excessive thermal cracking, a flash point is also a safeguard against human error and adding the wrong quench oil to a quench tank.  High temperature oils typically have a higher flash point than conventional oils.  An increase in flash point, along with no change in TAV, and an increase in viscosity could indicate a contamination issue between oils has occurred.

Cooling curve

There are many different methods of running a cooling curve. Many Asian suppliers of quench oil will use the Japanese Industrial Standard (JIS) K 2242.  European suppliers will use the ISO 9950 and North American suppliers rely on the ASTM D 6200 method.  All of these standards measure the same basic property, the ability of an oil to reach martensite formation.  However, they differ in one basic item.  The JIS K-2242 and methods used in China and France use a 99.99% silver probe that is smaller than the size of the Inconel probe used in the ASTM and ISO methods of Europe and North America.  Because of this difference, it is important to note that cooling curves and cooling rates between the methods should not be compared.  Figure # 2 shows the comparison between the two probes and their dimensions.

Figure # 2. ASTM D-6200/ ISO- 9950 and JIS K 2242 quenchometer probes^2
ISO/ASTM Inconel probe 12.5mm x 60mm.
JIS K 2242 Silver probe 10mm x 30 mm

 

In addition to comparing the cooling curve against the standard for the quench oil used, the Grossman H value should also be calculated and used as an indicator of cooling performance.  Unlike the old GM nickel ball test that tracked the time to cool a 12mm nickel ball to 352°C, the Grossman H value measures the severity of the quench6.

In using the Grossman H value, the lower the value, the slower and less severe the quench.   For use as a rough guide in comparing the quench speed in seconds to the Grossman H value measured in cm-1 the table below can be used.

Table #1

For example, air has an approximate H value of 0.01 cm-1 and water has an approximate H value of 0.4 cm-1 compared to oil with an approximate H value of ___ cm-1

The calculation used to determine the Grossman H factor has historically been:

H=h/2k

Where h is the heat transfer coefficient of the part when measured at the surface of the part and k is the thermal conductivity of the steel.  Typically the heat transfer coefficient is measured at 705°C. A steel’s thermal conductivity does not typically change according to alloy composition or temperature.  Therefore, the Grossman H value is proportional to the heat transfer coefficient of the part.

Interpreting a CQI-9 quench oil analysis
Table #2

Discussion

In examining the test parameters for CQI-9, it becomes apparent that many of the test results should be compared with other test results.  For example an increase in the amount of sludge or solids should also increase the viscosity of the quench oil.  As the sludge increases, the level of oxidation increases, and therefore, the level of organic acids formed in the quench oil should be increasing the TAV.  Finally, as the sludge increases, the cooling property of the quench oil should decline as indicated in the lower H value.

Figure #3. Total Acid Value (TAV) and Grossman H value

 

Likewise, as the flash point decreases the amount of thermal cracking is increasing, which should reduce the viscosity and thereby increase the H value and the overall cooling speed of the quench oil. Conversely, if the test parameters are not working in concert with each other, there may be other issues going on within the quench oil.  For instance, an increase in the water content can be detected before the increased water levels begin the oxidation process thereby increasing the TAV.  Or a viscosity change without a change in other parameters could be an addition of the wrong quench oil to the quench tank.  The graph below for Idemitsu Daphne Hi Temp A helps illustrate this point.

Figure #4. Graph for Idemitsu Daphne Hi Temp A demonstrating viscosity change

In the graph above, it can be seen when the water H value increases and the viscosity remains stable, the likely explanation is an increase in water.   When both the H value and viscosity decrease, additive consumption is the most likely reason.  Likewise, when the viscosity increases and the H value decreases, the formation of sludge from oxidation is the culprit.

Having test parameters that work in conjunction with each other is only beneficial if sample frequencies are often enough.  While CQI-9 only stipulates a semi-annual sampling frequency, the conditions of a quench tank can change in very short order.  There are the obvious changes when water is added to the tank.  However, many of the changes are more subtle, and left unchecked over time can create potential costly solutions such as a partial dump and recharge of the quench tank, poor part quality, or an increase in downstream processing such as shot blasting.  For this reason, many quench oil suppliers request a minimum of quarterly sampling.  In addition, if a sample is missed on a quarterly sample frequency, there is still time to sample the quench tank and remain in compliance with CQI-9.

Conclusion

Over time the condition of a quench oil will change and corrective measures will be needed to bring the quench oil back into the suggested supplier’s operating parameters.   The chart below helps understand what some of the methods need to be.

With proper care and maintenance, a quench oil can last a very long time.  A conventional oil should last 10 to 15 years or longer while a marquench oil should last seven to 10 years. The proper care of a quench is simple and straight forward.  A quality quench oil should not need the use of additives to improve oxidation resistance or quench speed. Simply adding enough fresh virgin oil to replace the oil that is being dragged out through normal operations should replenish the oxidation protection and quench speed to within the normal operating parameters. The table below offers recommendations for treating out of normal operating parameters for the required CQI-9 tests.

Recommendations for treating out of normal operating parameters for the required CQI-9 tests

Most heat treaters make weekly quench oil additions to their quench tanks.  The most popular type of filtration system is a kidney loop style where the quench oil is constantly filtered.  There are two basic types of these systems.  They differ in the number of filters used.  For a single filter system, a 25 micron filter is sufficient for quench oil filtration.  In a two-stage filtration system, a 50 micron filter is typically used in the first stage and a 25 micron filter is used in the second stage.  In a two-stage filter, the cheaper 50 micron filter will be replaced more often than the 25 micron filter in the second stage.

Utilizing a compliant CQI-9 analysis and the supplier provided operating parameters for the CQI-9 required tests is the first step in the proper care of a quench oil.  The next basic steps are ensuring there is enough fresh quench oil available for regular additions to replace the oil that is lost through drag out and proper filtration of the quench oil in a constant kidney loop type of a system.  With these steps in place, a quench oil will offer consistent performance for years and will be one less concern heat treaters face in the operation of their furnaces.

 

 

References:

  1. Automotive Industry Action Group, “CQI9 “Special Process: Heat Treatment System Assessment;” AIAG version 3, 10/2011.
  2. Rikki Homma, K. Ichitani, M. Matsumoto, and G. Steiger, “Evaluation and Control Technique of Cooling Unevenness by Quenching Oil,” 2017 ASM Heat Treat Expo, https://asm.confex.com/asm/ht2017/webprogram/Paper43594.html.
  3. G. Steiger, “Preventing the Degradation of Quench Oils in the Heat Treatment Process,” Metal Treating Institute, https://www.heattreat.net/blogs/greg-steiger/2018/10/03/preventing-degradation-of-quench-oils-in-the-heat.
  4. M.A. Grossman and M. Asimov. Hardenability and Quenching. 1940 Iron Age Vol. 107 No.17 Pp 25-29.

 

About the Author:

Greg Steiger is the senior key account manager of Idemitsu Lubricants America for quench products.  Previous to this position, Steiger served in a variety of technical service, research and development, and sales marketing roles for Chemtool, Inc., Witco Chemical Company, Inc., D.A. Stuart Company, and Safety-Kleen, Inc. He obtained a BSc in Chemistry from the University of Illinois at Chicago and is currently pursuing a Master’s Degree in Materials Engineering at Auburn University.  He is also a member of ASM International.

 

 

 

 

(photo source: Free Images at unsplash.com)

 

 

 

 

 

 

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Heat Treater vs. Water: Best Practices to Avoid Water Contamination

Heat treaters have their processes down to a science, literally. But what factor can compromise your heat treated part, let alone possibly cause detrimental damage to your facility? 

Greg Steiger
Sr. Key Account Manager
Idemitsu Lubricants America

Michelle Bennett
Quality Assurance Sr. Coordinator
Idemitsu Lubricants America

Heat Treat Today is pleased to present this original content article for today's Technical Tuesday. Greg Steiger, senior key account manager at Idemitsu Lubricants America, and Michelle Bennett, quality assurance senior coordinator at Idemitsu Lubricants America, describe water contamination in quench oil, the effects of this contamination, and how to test and safely remove the water from the quench oil.


Introduction

Water is an amazing substance.  Water helped create the Grand Canyon and Niagara Falls.  When water freezes, it doesn’t contract like most materials.  Instead, it expands and creates potholes that swallow up our cars every winter.  As the temperature rises, water also expands.  This property allows water to heat our homes and is why steam engines work.  The thermal expansion of water as it turns into steam is what can create catastrophic events in a quench oil.   This paper will look at potential water contamination sources in a quench oil, what the effects of the water can be, how to test for the presence of water in a quench oil, and how to safely remove the water from a quench oil.

Sources of water contamination

There are two major classifications of potential water contamination.  The first source can be classified as potential internal sources of water.  These potential sources are typically a part of heat treating furnace or oil cooling system.  They include water-cooled bearings, fans, doors or heat exchangers.  These water-cooled components are under a contestant pressure and will eventually leak.  Because the quench tank is usually below these sources of water, the water will eventually find its way into the quench tank. Water-cooled bearings and fans are located within the furnace and are often directly above the quench tank. While a water-cooled door is typically not directly above a quench tank, it is in close proximity to the quench tank. This proximity will allow leaking water to enter the quench tank.  Heat exchangers are typically situated away from the furnace.  However, in a water-cooled heat exchanger, the water is never more than the wall thickness of the cooling tubes away from the oil.  Should a cooling tube form a leak, the water and quench oil would simply mix within the cooling stream and the quench oil water mixture would return to the quench tank.

"The greatest risk of external water contamination lies in preventable operator or maintenance mistakes, especially when the equipment is down and open for maintenance."

The second classification is external sources.  These sources of water contamination are not part of the heat treating furnace.  Examples of external sources can be further broken down into leaks and operator or maintenance personnel mistakes.  Leaks typically include fire extinguishers and fire suppression systems leaks, leaking fire resistant hydraulic systems, atmosphere leaks, pneumatic cylinders and building leaks.   To prevent the leak type of contamination, routine maintenance, like a daily “Gemba” walk to spot any leaks, is the best defense against water entering a quench oil through a leak.  The greatest risk of external water contamination lies in preventable operator or maintenance mistakes, especially when the equipment is down and open for maintenance.

Quite often when a furnace undergoes repairs, the quench oil is pumped out into empty totes to be reused after the furnace repair is finished.  There is nothing wrong with doing this if the totes are clean.  However, there have been reports of heat treaters doing this without first inspecting the totes to ensure that they are clean and free of any type of contamination.  There have also been instances when the totes were not properly sealed and then stored outside, thus allowing rain water to get into the quench oil.  But, the potential to add an incorrect product to the quench tank is a preventable operator error.

How water affects a quench oil

As previously mentioned, water expands as it turns into steam.  At 212°F, water has a density of 0.96g/cm3.1  One gallon of water occupies 0.14 ft3.  At one degree above boiling the steam from the boiling water has increased to occupy 224 ft3 and a density of 0.0006 g/cm3.  The thermal expansion rate of water is approximately 1600%.   What this means is the single gallon of water that was in the quench oil before it turned into steam now has a volume approaching 1600 gallons.  In order for the 1600 gallons of steam to escape from the quench tank, it must displace an equal amount of quench oil.  With nowhere to go, this displaced oil will find hot spots and open flames to create a catastrophic event.

Quench severity

Fig.1 Schematic of ASTM D-3520 (ref. 7)

Historically, the severity of the quench has been measured by ASTM D-35202.  In this method, a chromized nickel ball is heated to 885°C and is dropped through an electronic sensor, which starts a timer, and into a steel cylinder of quench oil in a magnetic field.  Once the chromized nickel ball reaches the Currie temperature of nickel at 354°C, the ball becomes magnetic and closes the timing circuit when the ball comes into contact with the cylinder. The popularity of this test has always been that it provides a number that is easily interpreted by heat treaters to “rate” the oil as fast (9 – 11 seconds), “medium” (12 – 14 seconds), “slow” (15 – 20 seconds) or marquench (20 - 25 seconds). A schematic of the test method is shown in Figure #1.

This test worked well to differentiate between different how well the quench oils cooled the nickel ball. The test really didn’t distinguish between the cooling characteristics of a quench oil. The test result in Figure #2 show a time in seconds for the nickel ball to reach 354°C for three separate oils.  However, when the actual cooling curves of the oils are examined there are three distinct cooling curves shown.

Fig. 2 Three separate cooling curves with the same quench speed as measured by ASTM D-3520 (ref. 7)

Because mechanical properties such as yield strength and hardness are dependent on the severity of the quench, the Grossman H value3 has become more popular over the years.  In using the Grossman H value the lower the value the slower and less severe the quench.  For instance air has an approximate H value of 0.01 cm-1 and water has an approximate H value of 0.4 cm-1.  The calculation used to determine the Grossman H factor has historically been:

Where h is the heat transfer coefficient of the part when measured at the surface of the part and k is the thermal conductivity of the steel.  Typically the heat transfer coefficient is measured at 705°C. A steel’s thermal conductivity does not typically change according to alloy composition or temperature.  Therefore the Grossman H value is proportional to the heat transfer coefficient of the part.

Cooling curve

The basic cooling curve consists of three stages: the vapor blanket, nucleate boiling and convection. A basic cooling curve with the three different cooling phases is shown in Figure #3.

Fig.3 Three stage cooling curve (ref. 4)

In the vapor blanket stage, the load and the quench oil coming into contact with the load are above the evaporation temperature of the oil.  An insulating vapor blanket forms around the load and no cooling occurs.  Because the vapor blanket is insulating and does not allow for cooling, the vapor stage carries the highest risk of distortion.4  Once the vapor pressure decreases to a point where the oil can once again condense on the load and the temperature of the oil falls below the evaporation temperature, the nucleate boiling stage begins.  In this stage, the load undergoes the most aggressive cooling.  After sufficient cooling has occurred and the quench oil temperature is below the boiling temperature of the oil, a smooth transition into the convection stage begins.

Stabilization of the vapor stage

As water is dispersed throughout the oil, the viscosity of the oil changes.  As the amount of water increases, the viscosity of the oil also increases.5  A careful examination of Figure #4 will also show a slight movement of the cooling curve to the left and a lengthening of the vapor stage as the amount of water increases.  Furthermore the water in the oil is not uniformly dispersed, and this non-uniform dispersion creates uneven cooling rates throughout the oil.  To restore even cooling, it is recommended the water in the quench oil be reduced to below 200 PPM.

Fig. 4 Cooling curve change due to water contamination (ref. 4)

Types of water found in a quench oil

In simplistic terms, water in a quench oil can be thought of as being dispersed in the quench oil due to agitation or as free water having exceeded the saturation point of the oil.  As a general rule of thumb in the industry, the saturation point is considered to be 0.1% or 1,000 PPM.  However, the saturation point will vary according to the temperature of the oil and the additives within the quench oil.  Daphne Hi Temp A-U is a good example of a clear amber quench oil.  Figure #5 shows a picture array of the appearance of the oil as the amount of water approaches and then exceeds the 1000 PPM industry standard.

Fig. 5 Daphne Hi Temp A-U appearance as the amount of water dispersed within the oil nears and exceeds the saturation point of the oil. (Used with permission Idemitsu Lubricants America)

 

Notice in the data above that as the amount of water increases in the Daphne Hi Temp A-U, so does the viscosity as measured at 100°C.  In addition to the viscosity rising as the amount of dispersed water increases, so also does the quench severity as measured by the Grossman H value.  Furthermore, the appearance of the quench oil changes as the amount of water increases as well.  (See Fig. 5 for the Daphne Hi Temp A-U.) With small amounts of dispersed water—45 PPM—the quench oil is clear and there is no water that is precipitated out after centrifuging for 15 minutes at 5500 RPM.  However, as the amount of water begins to approach the 1000 PPM level, the appearance of the quench oil begins to become hazy. As the saturation point is exceeded, the appearance remains hazy and water precipitates out after centrifuging for 15 minutes at 5500 RPM.

Testing for oil in a quench oil

There are two basic types of testing methods for determining if there is water dispersed in a quench oil.  One of the methods is subjective and the other is quantitative.  The crackle test involves heating a metal coupon to approximately 400°F and placing a few drops of the quench oil on the surface.  If there is a sufficient amount of water in the oil visible bubbling within the oil and audible crackling will occur.  Unfortunately, this is typically above the saturation point of the quench oil. At which point it is often too late.  Figure #6 shows examples of crackle testing.

Fig. 6 Crackle test results for Daphne Hi Temp A-U

The second and preferred testing method is through ASTM D-6304 Standard Test Method for Determination of Water in Petroleum Products, Lubricating Oils and Additives by Coulometric Karl Fisher Titration6.  The Karl Fisher test uses the Bunsen electrochemical reaction to calculate the amount of water in a used oil and is accurate in used oil from 1 PPM to 50,000 PPM.

Removing water from a quench oil

Removing excessive water from a quench oil can be achieved economically through several methods. Table #1 is a brief trouble shooting guide to the safe removal of water from a quench oil.

Table 1 Trouble shooting guide for removal of water from a quench oil

Conclusion

Finding small amounts of water, less than 50 PPM is very common in a used quench oil sample.  This small amount could simply be condensation within the bottle and quench tank. However,when the amount of water begins to reach levels above 200 PPM, troubles can begin.  At levels above 200 PPM of water, the following may occur:

  • Uneven cooling due to non-uniform dispersing of the water within the quench oil
  • Increase in viscosity
  • Increase in Grossman H Value
  • Lengthening of the vapor blanket stage
  • Increase in the severity of the quench

Like most materials, water expands as it changes from a liquid into a vapor.  With a thermal expansion rate of 1600%, a gallon of water turns into considerable more steam.  Therefore excessive water transitioning into steam in a quench oil creates safety concerns when the steam forces the quench oil from the tank.  Examples of these safety concerns are:

  • Risk of harm and injury to plant personnel
  • Damage to furnaces and related equipment
  • Damage to the heat treat facility the surrounding plant and nearby buildings
  • Severe cases can result in a quench oil fire or a building fire

The importance of a “Gemba" walk should not be overlooked.  Water can enter into quench oil systems through normal heat treating operations such as a leak in a water-cooled piece of equipment, others can be from preventable sources such as a building leak or other human error.  No matter what the source is, if water is suspected in a quench oil, the quench tank should be sampled and tested before it is used.

 

References:

  1. Handbook of Chemistry and Physics. 60th edition CRC Press, p. E-18.
  2. ASTM International, “Standard Test Method for Standard Time of Heat Treating Fluids (Magnetic Quenchometer Method),” American Society for Standards and Materials.
  3. M. A. Grossman and M. Asimov, “Hardenability and Quenching,” 1940, Iron Age Vol. 107 no.17, p. 25-29.
  4. Rikki Homma, K. Ichitani, M. Matsumoto, and G. Steiger, "Evaluation and control technique of cooling unevenness by quenching oil," 2017 ASM Heat Treat Expo, https://asm.confex.com/asm/ht2017/webprogram/Paper43594.html.
  5. G. Steiger, "Preventing the degradation of quench oils in the heat treatment process," Metal Treating Institute, https://www.heattreat.net/blogs/greg-steiger/2018/10/03/preventing-degradation-of-quench-oils-in-the-heat.
  6. ASTM International, "ASTM D-6304 Standard Test Method for Determination of Water in Petroleum Products, Lubricating Oils and Additives Coulometric Karl Fischer Titration," West Conshohocken, ASTM International, 2016.
  7. B. Lisic and G.E. Totten, "From GM Quenchometer Via Cooling Curve Analysis to Temperature Gradient Method,"  ASM Proceedings: Heat Treating, 18th Conference, 1998.

 

About the Authors:

Greg Steiger is the senior key account manager of Idemitsu Lubricants America for quench products.  Previous to this position, Steiger served in a variety of technical service, research and development, and sales marketing roles for Chemtool, Inc., Witco Chemical Company, Inc., D.A. Stuart Company, and Safety-Kleen, Inc. He obtained a BSc in Chemistry from the University of Illinois at Chicago and is currently pursuing a Master’s Degree in Materials Engineering at Auburn University.  He is also a member of ASM International.

Michelle Bennett is the quality assurance senior coordinator at Idemitsu Lubricants America, supervising the company's I-LAS used oil analysis program. Over the past 9 years, she has worked in the quality control lab and the research and development department. Her bachelor’s degree is in Chemistry from Indiana University.

 

 

 

(Photo source: non on unsplash.com)

 

 

 

 

 

 

 

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Heat Treat Radio #37: Rethinking Heat Treating for the 21st Century with Joe Powell (Part 1 of 4)

In this 4-part series, Heat Treat Radio host, Doug Glenn, talks with Joe Powell of Integrated Heat Treating Solutions about bringing heat treating into the 21st century.

According to Joe, the real focus should be on the quenching portion of the process where distortion often happens. In many instances, distortion is able to be eliminated. Find out how in this episode.

Below, you can either listen to the podcast by clicking on the audio play button, or you can read an edited version of the transcript.

 


Click the play button below to listen.


The following transcript has been edited for your reading enjoyment.

Doug Glenn (DG):  On today’s episode, I sit down with Joe Powell, president of Akron Steel Treating Company to hear what he and his team are doing to combat heat treat distortion.  Joe Powell is a veteran in the industry and carries a wealth of knowledge with him.  Joe, your company has 75 years of experience working with different part makers, and after a very brief conversation with you, pretty much anyone would conclude that you’re a man on a mission to bring heat treating into the 21st century.  Before we turn you loose on that topic, first tell us a little bit about Akron Steel Treating and how it got started.

Joe Powell (JP):  It was founded by my father in our garage in 1943 at the behest of the Department of the Army who wanted him to heat treat some parts, and it grew along with all the tool and dye makers in Akron, OH by making machinery for making various rubber products like tires, belts and hoses . . . you name it.

DG:  You’ve also spearheaded another company: Integrated Heat Treating Solutions.  What are you doing with that company?

[blocktext align=”right”]”It should be ‘quench treating’ not ‘heat treating.’  That’s the way I look at it.” -Joe Powell[/blocktext]JP:  Integrated Heat Treating Solutions is the culmination of 75 years of commercial heat treating experience with literally over a 1000 different part makers.  What we’ve learned that if we can integrate our heat treating solutions with the part-making design and the optimal material selection, we can produce better parts.  And what I mean by “better parts” is they could be lighter, they could have longer fatigue life, and they could have less distortion after heat treating.  All of these benefits are brought to the table to part makers so that heat treating becomes a fully integrated part of lean manufacturing.

Once heat treating becomes a lean, integrated part of manufacturing, everybody wins.  It enables the use of leaner alloy materials; it eliminates oil quenching; it eliminates long carburizing cycles and batch carburizing cycles; and we now are able to literally do the heat treating in the manufacturing cell where the parts are made.

DG:  What do those two companies look like now?

JP:  We have about 50,000 square feet and are currently in the process of acquiring another building to our east.  We have 48 employees and there are three shifts; and again, we do salt heat treatment, vacuum heat treatment and controlled atmosphere heat treatment.  Also, we are currently getting into induction heat treating with our friends at Induction Tooling.

For the last 23 years, we have been concentrating on finding the best way to quench parts and to drive the distortion out of the part-making process.  The heat treat distortion has been a problem for centuries.  Parts crack, they distort, they come out of the heat treat process unpredictably with size change that is absolutely necessary to get the mechanical properties, but also, if it’s nonuniform, that size change can cause major problems down the line that have to be corrected by hard turning, grinding, flattening, straightening, you name it.

Dynamics of uniform and Uniform Intensive Quenching model (Source: integratedheattreatingsolutions.com)

We’ve also delved into the science of computer modeling, finite element modeling as well as computation of fluid dynamic modeling with our friends at DANTE Solutions.  What has happened from that modeling is seeing this concept: the surface of the part contains a bunch of grains, and those finite elements – if they are not quenched uniformly – will transform nonuniform, leading to nonuniform thermal shrinkage upon beginning quenched. Then they will also transform to martensite nonuniformly, which means that the thin and thick sections of a part will have different amounts of distortion and size change.  In order to control that, we’ve developed what we call “quench to fit” technologies where we literally build a shell on the outside of the part, using a gas quench or a uniform salt quench or uniform water quench.  Once you’ve built that shell in the first few seconds of the quench on the outside of the part, that martensite shell acts like a custom-made quench dye, and that custom-made quench dye allows the part core to cool by conduction through that shell.  So, if that cooling by conduction happens by very uniform conduction through the geometry and the mass of a given part, you will have a predictable size change after heat treat. And, you will enable the part designer to go back to the initial part design and adjust it accordingly so that it quenches to fit during the quench process.

When a commercial heat treater receives the part, 99 times out of 100, that part is using a material that was selected many, many years ago, because that is what they’ve always used.  Additionally, it’s going to be heat treated in legacy equipment that has always been used.  For instance, case carburized 8620 steel valve seats have been used for decades now, and they last about 40-70 hours in the fracking pump, but a ductile iron valve seat can be made to last many times longer; it’s cheaper to buy the material and our heat treating equipment can heat treat it in 5 minutes instead of a 20 hour case carburizing cycle in batches.  That single part flow of that new induction heat treating equipment and quenching equipment that is built into it can be built in right at the end of the CNC machines.

I am a commercial heat treater who believes that part design should be integrated for heat treating by the part-maker.  It’s a nuance, but what it really boils down to is that sometimes commercial heat treaters do it best, but sometimes the part-maker can do it better.  [Side bar quote: I am a commercial heat treater who believes that part design should be integrated for heat treating by the part-maker.  It’s a nuance, but what it really boils down to is that sometimes commercial heat treaters do it best, but sometimes the part-maker can do it better.]

[blockquote author=”Joe Powell” style=”2″]I am a commercial heat treater who believes that part design should be integrated for heat treating by the part-maker. It’s a nuance, but what it really boils down to is that sometimes commercial heat treaters do it best, but sometimes the part-maker can do it better.[/blockquote]DG:  So, the importance in the part design process of including the heat treater is that you can more consistently predict what the distortion will be, because if I understand it correctly, you can actually predict distortion in the part and therefore design the part with the distortion that will come consistently every time you design that part, yes?

JP:  Yes.  And it doesn’t matter if it’s an air quench or a hot salt quench or a uniform water quench, it just has to be very, very uniform from the initiation of the quench.  In other words, you can’t take it out of the furnace and air cool it for 45 seconds and then begin a water quench, it doesn’t work that way.  That shell is starting to form instantaneously when the heat is turned off.  An air quench is very slow compared to an intensive water quench and so you have to introduce that quench all over the part surface shell as instantaneously, and with as much uniform impact, as possible.  That’s what we do in terms of designing equipment to do the quench process.

DG: Right now, there are a lot of companies, a contractor or commercial heat treater, that send you parts to heat treat.  Is it not possible that if the part designer and the heat treater talk in advance as they design the part, that some of these parts could be, in fact, heat treated in-house and not be sent out to a commercial heat treater?  Is that possible?

JP:  They could actually be heat treated not only in-house, but directly after the CNC machine, right in the manufacturing cell, right after the forge.  It takes the proper selection of the optimal hardened ability material. In other words, part of that part design with the heat treater has to be considerations like, “Is it going to get too hard in the core?  Is it going to swell up too much in the core?  Is it going to be unable to build that shell on the surface without blowing it off, because the core starts to harden up?”  So again, the optimal material selection and the design of the mass and the geometry of the part need to be considerations that the heat treater gets a chance to look at.

A “textbook” example of the bell curve. (Source: integratedheattreatingsolutions.com)

DG:  So, if the part designer and the heat treater get together and talk about the part design before the part is finalized, or if they’ve got a legacy part, they can sit down and talk with a heat treater that understands what you’re doing over at Akron Steel and Integrated Heat Treating Solutions. If they can understand that, and if they can talk with you about how that part might be redesigned, it’s very possible that you could use lower cost materials to get the same thing, minimize the amount of time to actually heat treat, and you may be able to put that part in a single piece or at least possibly a small batch flow so that there’s not a bottleneck at heat treat, yes?

JP:  Yes.

Sponsorship for this episode is Furnaces North America the Virtual Show.

DG:  Joe, let’s talk about the quenching bell curve as it relates to distortion.

JP:  There are many, many metallurgists and many metallurgical textbooks that indicate that the faster the quench cooling rate, the higher the probability of distortion.  There is a curve that is generated that basically says that if you quench very slowly in gas, or if you increase that quench rate and go to a hot salt or a martemper bath or an austemper bath or you increase it even further with warm oil or highly agitated oil, or you go to a brine quench where you do a polymer or a polymer water quench where you increase the rate of quench cooling, there is a point at which most of the parts are going to crack and you’re going to have major distortion.  It is not because of the quench speed being faster, it is because the uniformity tends to be less the faster your quenchant.  In other words, you need to keep the water from film-boiling and creating a situation where the initial quench is actually done under a steam blanket, or gas, very slowly.  Once the thin sections of the part quench-out under gas, then you have the thick sections that are still under that gas blanket, and you have very rapid cooling and very rapid martensite transformations that cause a shift in the size of the part where the shell now cannot contain the core swelling that’s happening underneath the surface.

Whereas 21st century heat treating practice is, what I call, a “uniform quench renewal rate” and an instant impact.  In other words, you instantly impact the shell, create that shell, and once it’s created with uniform cooling, then the rest of the cooling happens by conduction through that shell.  Whatever the geometry and the mass of the part is will determine that uniform conduction cooling which ends up being very predictable.  Once it’s predictable, then you can morph the green size of the part before heat treating so that it predictably quenches to fit during the quench process.

(source: integratedheattreatingsolutions.com)

DANTE Solutions has a method where they use their model to model the finite elements in the part so that the thin and thick sections of the part quench uniformly. IQ Technologies Inc. and my company, Integrated Heat Treating Solutions, have gone on the other side and shown that it is really a bell-shaped curve, and that the probability of distortion goes back down if you can create that shell on the outside of the part instantaneously, and then provide a uniform quench renewal rate to the part surface so that the core can cool by uniform conduction through that shell.

DG:  Let’s just put in our listener’s minds the standard bell curve.  Most of the quenching and most of the textbooks that we see these days is done on the left hand side of that bell curve, and as you approach the peak of that bell curve, the probability of distortion and/or cracking occurs.  People are saying – don’t quench too fast because you’ll get cracking.  You’re kind of switching the whole paradigm to say that it’s not the speed at which you quench, but more so: Can you create, almost instantaneously, a hard shell because of exceptionally rapid cooling on the whole part so that that shell basically holds the part in place?  If you can get that, then you can cool the rest of the part, however slow or fast, in a sense, you want, because it’s not going to distort because it’s already locked in.

JP:  Right, and this is cooling by conduction which is the physics of the material.  How fast will it give up the heat through its mass?  It’s the difference between 100 degrees or 50 degrees or 10 degrees per second of cooling and 400 to 600 degrees centigrade cooling per second, so it’s very, very intensive.  The middle of the bell curve, where most parts are cracking, is because there is not a uniform quench renewal rate.  You start off with a gas quench, then you end up with a very intensive evaporative cooling quench with nucleate boiling.  You then end up with water quenching without boiling, and so you have three different phases of cooling happening on different parts of the part. This is exacerbated by different parts in different sections of the batch which will have different cooling rates.

It’s almost impossible to get the full benefits of very, very intensive quenching or even very, very uniform gas quenching in a vacuum furnace unless you have staged the cooling in such a way that you create that uniform shell at the beginning of the quench, and you hit that martensite start temperature and cool to that martensite start temperature all over the shell of the part uniformly.  That’s the key.

DG:  There are several things that jump into my mind like questions that might arise from people.  You’ve already hit on the differences in part thickness – you may have thick sections, you may have thin sections.  It’s very possible to maybe get down to the martensite start temperature on the thin section right away, but the thick section may not be, and therefore you’re going to distort because you haven’t created that “frozen shell” uniformly around the entire part.  Let’s talk about, not just part thickness, but part geometry in the sense of the awkward curves and turns or lips and things of that sort on parts.  How would we deal with that?

JP:  That’s where new 21st century heat treating equipment needs to be designed.  Every furnace company that is selling furnaces to either captive heat treaters or commercial heat treaters calls itself a furnace company.  The reality is, yes, heating is important and it is the precursor to getting the mechanical properties, but the heat treatment is actually done, and the mechanical properties are actually obtained, in the quenching process.  It should be “quench treating” not “heat treating.”  That’s the way I look at it.

Image from Smarter Everyday YoutTube video on Prince Rupert’s Drop (source: https://www.youtube.com/watch?v=xe-f4gokRBs&ab_channel=SmarterEveryDay)

For the last 23 years that’s what has been more apparent to me.  My dad taught me how to quench stamps that were used for marking the inside of tire molds, and these steel stamps would uniformly blow up if you just quenched them.  But if you were able to uniformly quench the marking end, you could get it hard as hell and it would last a long, long time, but you had to kind of bifurcate the quench.  You had to make sure that you created that shell in the marking area of the stamp and let the rest of the stamp kind of cool much more slowly.  In other words, create the shell in the face of the stamp where the lettering is, and set those letters.  Then the rest of the stamp can basically cool much slower because you don’t need the hardness there; it’s not the working part of the part.

Also, the designers of the stamps had to integrate the right radius in the face of the stamp.  If they had sharp corners, those sharp corners would blow off during the heat treat.  So, over time, we said, “If you don’t want us to crack this stamp, you’re going to have to put a radius over here and change the design slightly.”  It didn’t take much change, but it did take a recognition of the fact that this was not going to work.  There’s no way to eliminate the nonuniform cooling in the shell if you’ve got a corner.  Steam collects in that corner and it doesn’t quench, so you can’t create the hardened shell.

DG:  Let’s take a little deviation and talk about something non-metal.  Let’s talk about the Prince Rupert’s drop to illustrate residual compressive stresses.

JP: The mystery of the Prince Rupert’s drop of glass is that glass makers noticed that if they dropped a drop of molten glass into a bucket of cold water it would form a drop that has a head and then a tail – it almost looks like a tadpole.  If you hit the head of that glass drop with a hammer or try to break it with a pair of pliers, you can’t do it.  It is literally unbreakable at the head.  However, if you snap the tail off, it instantaneously explodes.  This is because there are counterbalancing tensile stresses that are below the surface in the tail that once you break the compressive stresses off, it’s like taking the hoop off a barrel and the barrel staves explode; the elements on the surface just explode.  The reason they don’t explode on the drop of glass at the other end is because there are sufficiently high compressive stresses on that surface that hold the drop of glass and keep it from fracturing.

DG:  This is a fascinating video where you take a Prince Rupert’s drop, actually hang this Prince Rupert’s drop and shoot it with a .38 or a .45 or a 9 mm, hitting the head of that tadpole, if you will, and it shatters the bullet while the glass remains untouched.  However, if a guy just simply takes his finger, or whatever, and snaps the tail, not just the tail shatters, but the whole tadpole blows up.

JP:  What we’ve been able to do with all of the research that we’ve done is to harness those compressive stresses and make them available to the part-marker for making their parts more robust, making them lighter, and making them basically carbide hard and hammer tough.  They don’t chip when hit with a hammer.

DG:  Let’s jump back to some of the projects you’ve done at Integrated Heat Treating Solutions.  Do you have any current projects that you’re working on where this integrated solution – where you were involved with part design or improvement of part design – worked well?

JP:  Yes.  There are several case studies.  The first case study was a punch that lasts 2 – 9 times longer than an oil quench punch.

DG:  A punch for what?

JP:  Punching holes in metal plates. And the other thing that has happened is that since we’ve begun working with Induction Tooling, we’re able to then bring this down to the level of thinner parts and more complex geometry parts.  We’re able to get more hardenability out of lean hardenability alloy such as ductile iron. Plain ductile irons are now acting as carbides.  Even the people that make the material said it couldn’t be done, but we’re doing it.

DG:  Can you give an example of that?

Watch more resources at Integrated Solutions website. Click the image above to access these resources.

JP:  Yes, that would be a fracking pump valve seat made out of ductile iron and heat treated with our special heating and quenching technologies.

DG:  What was the performance prior to the treatment and afterwards?

JP:  40 to 60 hours and our initial testing we got 166 hours, so 2 ½ times longer.

DG:  So 2 ½ times better performance on this fracking valve seat, and you were using the same material?

JP:  No.  Rather, we replaced an 8620 carburized steel that needed to be carburized for 20 hours in the furnace, and we did it with a 5 minute induction heating process.

DG:  Of what type of material?

JP:  Ductile iron.

DG:  So we’ve got a punch, a valve seat in the fracking industry.  What else?

JP:  We have bevel gears that we do.  We have worked with the part manufacturer and they’ve adjusted their CNC program so that it actually quenches to fit and doesn’t require a final grind.

DG:  Expensive hard machining or hard grinding after heat treat.

JP:  Right.  And it saves them about $750 per gear in final grind costs.  And, the gear lasts longer because it has high residual compressive surface stresses versus a standard carburization process and quenching in oil that does not have as high of a residual compressive surface stress.  Especially after you grind it all off to get the final dimensions you want.

DG:  Right.  So you put all these nice hard stresses in, then you grind them off.

JP:  Exactly.

DG:  Any other examples?

JP:  We have a company that wanted to have a weldable gear rack that could be welded on in the field on mining equipment that’s out on the side of a mountain.  Because it might be cold up there, and they didn’t want to have to pre- and post-heat in order to weld on the gear rack, or repair a tooth on the gear rack, they wanted to have a material that had less hardenability but still wanted to have all of the mechanical properties.  We were able to get the mechanical properties of 4330 from a 4130 material that doesn’t need to be pre- and post-heated to prevent it from cracking when welding it onto the machinery.  They call that “field repairability.” So, we were able to enable field repairability and still maintain the mechanical properties’ requirements.

DG:  In future episodes, we’ll go into some depth on some of those applications you just described, but before we wrap up things for this episode, is there a last impression you’d like to leave with us?

JP: Professor Jack Wallace* did not believe that there was a right half of the bell-curve, he did not believe that intensive quenching would work, but, again, he became a believer. It is all key to understanding the dynamics and uniformity of quenching over time. If you get the uniformity, you’re in good shape and eliminate a lot of heat treating problems.

DG: Thanks, Joe. Looking forward to you joining us for future episodes.

JP: Thanks so much.

 

 

*Professor Jack Wallace was the “Dean of the College of Metallurgical Engineering at Case Western Reserve University in Cleveland Ohio – who said in 1997, ‘Intensive water quenching would not work!  – The parts will blow up in the quench!’  He became a convert once he figured out how compressive surface stresses worked during uniform quenching.” Information provided by Joe Powell.

 

Doug Glenn, Publisher, Heat Treat Today
Doug Glenn, Heat Treat Today publisher and Heat Treat Radio host.


To find other Heat Treat Radio episodes, go to www.heattreattoday.com/radio and look in the list of Heat Treat Radio episodes listed.

Heat Treat Radio #37: Rethinking Heat Treating for the 21st Century with Joe Powell (Part 1 of 4) Read More »

Heat Treat TV: The Quenching Mystery of Prince Rupert’s Drop

Heat Treat TV pulls the best heat treat videos from the web for your viewing, and today Heat Treat TV highlights the pressurizing effect of quenching.

The mystery of Prince Rupert’s Drop is a well-known phenomenon. Somehow, the glass will not break under significant pressure, but a breakage to compromise the structure of the tail of the drop leads to absolute combustion, similar to a chemical explosion.

In this video, you won’t only simply learn about what the drop is, but also why it works and where it comes from. The relationship between glass and metal is the effect that the quench process has on the structural integrity of the materials. Learn more about external surface tension and its role in heat treat in this Heat Treat Radio podcast about Rethinking Heat Treating, Part 1 with Joe Powell of Integrated Heat Treating Solutions.

 

For more information about the contributor, visit Integrated Heat Treating Solutions.

If you have a video you’d like included on Heat Treat TV, please send an email to editor@HeatTreatToday.com and include a link to the video.

Heat Treat TV: The Quenching Mystery of Prince Rupert’s Drop Read More »

Best of Both Worlds in Polymer Quenching

Jerry Dwyer, Marketing Manager, Hubbard-Hall

"The success of most heat treating processes comes down to the battle between time v. temperature..." In this Heat Treat Today Technical Tuesday article, Jerry Dwyer of Hubbard-Hall describes innovative heat treating practices with organic polymer quenchants.

If you are interested in learning about what these polymer quenchants can do, and want to know specifically how a high-performing polymer reacts in the quenching process, read on for the details from a specific case study. Between time and temperature, you may just get the best of both worlds.


The success of most heat treating processes comes down to the battle between time vs. temperature, better known as isothermal transformation. The delicate balance between how long to quench a part and at what temperature often comes down to which media is being used to do the quenching.

Image of a clean machine

For decades, water and oil have been the go-to solution for quenching heat-treated parts in order to harden them to proper specifications. Of the two, water has the highest cooling rates (between 2,000°F/sec to 10,000°F/sec), which often leads to high distortion rates in parts and more cracking because of the high residual stresses. Oil-based solutions have been used extensively in the metalworking industry on larger, thicker parts because it has basically three cooling speeds: slow for lower hardness and less distortion, medium for when moderate to high hardenability is needed, and high for carburized and carbo-nitriding part applications.

But with increasing concern for both environmental disposal and safety issues, many heat treaters have been searching for an alternative quenching technology that meets their needs. With water and oil so prevalent, industry researchers developed a hybrid of the two in order to come up with a series of polymer quenchants that serve numerous functions and also reduce some concerns.

Development of Polymer Quenchants

Image of polymer

The polymer quenchants contain organic inhibitors and other additives that produce concentrates, which are diluted for use. The advantage of polymer solutions is that they have widely variant properties, which give a heat treater flexibility in how they use the product compared to just water or oil. They are also non-flammable, which eliminates the need for operators to install needed fire suppressant equipment that might be needed with other quenching methods.

There are several different types of organic polymer quenchants, including polyalkylene glycol (PAG), sodium polyacrylate (ACR), polyvinyl pyrrolidone (PVP), and polyethyl oxazoline (PEO).

The polyalkylene glycol (PAG) polymer is one of the most widely used in the heat treating industry and provides an ideal uniform cooling for minimizing distortion and preventing crack formation during hardening machine components and tools. Scott Papst, vice president of specialty sales and business development at Hubbard-Hall, says that many of their customers have inquired about adding a polymer quenching alternative to their process.

“The technology of the polymer process has grown tremendously over the years, and we wanted to make sure we had that technology in their hands,” Papst says.

Partnership with Idemitsu Grows Offerings

Hubbard-Hall, which has a line of several heat-transfer and heat-treat salts for annealing, martempering, isothermal quenching and other applications, began to look for a partner company to supply its customers with polymer quenchants and set their sights on Idemitsu Kosan Co., a Japanese energy company that owns and operates oil platforms and refineries, and manufactures numerous petroleum, oils and petrochemical products.

“We found Idemitsu to be a wonderful partner which has a tremendous focus on advanced technology, especially when it came to heat treating,” Papst says. “We were very happy when we could put together a partnership to offer their polymer quenches to the U.S. market.”

Polymer quenches are used primarily in what is called an “induction hardening operation.” An electric current is put through a copper coil to create a magnetic flux that heats up the target section of the part. Induction hardening uses a shorter time to harden the targeted section of the part instead of using an atmosphere furnace to heat treat the entire part.

Where salt quenches are used to heat treat an entire part, the polymer quenches can be targeted to certain areas of a parts, such as gear teeth. Greg Steiger, a senior key account manager for quench products at Idemitsu, says polymer quenches work great on parts like gears because it treats the most vital sections of the part.

“A gear has to be hardened because it needs to withstand a lot of wear-and-tear; but the teeth take the brunt of the load when the part is in use,” Steiger says. “The teeth of the gear have to be harder than the rest of the part; if the entire gear was as a hard as just the teeth, then that part would fracture and shatter.”

Benefits of Inverse Solubility

Polyalkylene glycols utilize inverse solubility in water; while they are completely soluble at room temperature, they become insoluble at higher temperatures from 140°F to 195°F, depending upon chemical structure. Inverse solubility controls the cooling and quenching mechanism. The ability to vary the concentration of a polymer quench provides great flexibility of the cooling rate. The polymer separates from water as an insoluble phase, and the ensuing deposited layer becomes as an insulator that determines the rate of heat extraction from the quenched part.

“The polymer slows the cooling compared to water, and controls the heat treating process” Steiger says. “The transformation rate is much more controllable, which makes the heat treating more tailorable to the part.”

Image with the door closed

Image of a door before process

Idemitsu’s high-performance polymer quenchant is its Daphne Plastic Quench HF, which has excellent oxidation stability performance that protects the integrity of the quenchant even after contamination by metalworking fluids. Steiger says Daphne Plastic Quench HF virtually eliminates the formation of sticky films common in most quenching polymers, which reducing the amount of drag out and thus reducing consumption.

“It is formulated to provide superior biocidal protection, preventing bacterial contamination in the recirculating induction hardening systems,” he says. “It also offers outstanding rust and corrosion prevention to better protect quenched parts. It is highly resistant to degradation.”

Lower Viscosity, Improved Efficiency

The Daphne Plastic Quench HF has a viscosity (at 104°F/40°C) of 29.5 mm2/s, which bests its two top competitors at 536.1 and 301.7. The lower viscosity improves handling and production efficiency, and also reduces or eliminates sticky build-up on machines, gauges, fixtures and parts.

The product also has excellent rust preventative properties and is thermally stable. In fact, Steiger says, testing with a Tier I parts supplier who was having rust issues with a competitor’s product showed that Daphne Plastic Quench HF has stable cooling performance after six months of use, and they only recharged their system twice in a year, reducing consumption by over 66%.

Further, when a global automotive OEM switched to Daphne Plastic Quench HF from a competitor, the result was better separation from tramp oils. The previous product was causing unstable cooling performance that resulted in cracks on the parts; it turns out the OEM was dumping machines and recharging every three months because tramp oil contamination become more than 5%.

“The actual quench oil usage by the OEM was reduced by up to 75% after just four months, and their sump life was much longer at more than six months,” Steiger says. “Lower concentrate usage and a significant reduction in residue directly correlates to improved productivity, reduced maintenance costs and lower disposal costs.”

 

About the Author: Jerry Dwyer is Hubbard-Hall’s market manager for product groups pertaining to heat treating, phosphates and black oxide. To learn more or get in touch, please visit Hubbard-Hall's website.

(photo source: Bill Oxford on unsplash.com)

 

 

 

 

 

Best of Both Worlds in Polymer Quenching Read More »

Demonstrating Oil Quenching Effectiveness

In this article by Lee Gearhart, Principal Engineer, Materials and Processes, Moog, Inc., and Chair, Aerospace Metals Engineering Committee, read about a “real time” heat treat inquiry regarding the interpretation of changed oil quenching effectiveness testing in AMS 2759, and Lee’s desire to ensure that the heat treater’s system maintains its effectiveness.

This article article first appeared in the latest edition (June 2020) of Heat Treat Today’s Automotive Heat Treat magazine.

* Please see the bottom of the article to view the AMS2759 sections to which Lee refers.


The Query:

Lee Gearhart, Principal Engineer, Materials and Processes, Moog, Inc., Chair, Aerospace Metals Engineering Committee

A gentleman, to whom I’ll refer as Mr. XXXX, sent the following query to SAE, the publisher of Aerospace Materials Specifications. The subject line was as follows: “Clarification of AMS 2759G for Committee ‘E’.”

The letter read:

I would like to get some clarification about AMS 2759, Revision G, paragraphs 3.10.3 through 3.10.3.1.5.5. My issue, as an independent testing lab, is the terminology used in 3.10.3.1.5.1 and 3.10.3.1.5.3., and how

I am to determine the acceptance criteria for the hardness in the center diameter of the quench effectiveness samples supplied to us by heat treating companies. Let me walk through the steps that lead up to the determination of minimum hardness at the center of the diameter of the coupon prepared.

Paragraph 3.10.3.1.2 states specific size test bars to use for the quench effectiveness testing, based on the alloy, in sub-paragraphs a., b., c., and d. For 4130 (a.), use 1.5” long, 0.50” diameter bar and for 4330V (c.), use 7.5” long, 2.5” diameter bar. Then, we cut the test coupon from this specimen todetermine hardness at the center diameter, per 10.3.1.4.

Next, we have to determine whether this hardness result, taken at the center diameter, conforms to the spec, and here is where my issue is. Paragraphs 10.3.1.5.1 and 10.3.1.5.3 both state, “…shall not be less than the hardness on the end-quench hardenability curve corresponding to the diameter of the specimen…” So, if I am to use the diameter of the specimen as my guide from paragraph 3.10.3.1.2, a.and c., then the end-quench result on the mill cert corresponding to 8/16 would represent the 0.50”diameter, and 40/16 would represent the 2.5” diameter. ASTM A255 has you stop taking readings on the Jominy bar at 32/16 (2.0”), so there would not be a result on the Mill Cert for the 40/16 requirement.

I don’t believe this is the correct depth. I believe the end-quench result corresponding to one-half the diameter would be the appropriate depth to use as a minimum requirement, since we are taking the hardness reading at one-half the diameter; in the center of the diameter. So, the end-quench result on the mill cert corresponding to 4/16 would represent the 0.50” diameter and 20/16 would represent the 2.5” diameter bar. These requirements are more stringent and would better represent the effectiveness of the quench media to properly quench the specimens and correlate this back to the certified values of the material based on the mill cert reading for the corresponding J values.

Please review this and consult with the Committee to see if this would better represent the intent of these paragraphs for acceptance of quench effectiveness.

The Response:

Because of my position as chairperson of the Aerospace Metals Engineering Committee, the question eventually made its way to my desk. Here is my response:

When reading your question, it suddenly struck me – you’re missing the secret decoder ring! In other words, you cannot directly compare an oil quenched sample to a water quenched (Jominy) test coupon.

Allow me to give you a long-winded explanation that I wrote for Committee E on Steel for the Aerospace Materials Division, the committee that has jurisdiction of AMS2759 on Heat Treating of Steel. The committee had been asked for an explanation of what the 3.10.3 Quench System Monitoring is supposed to do; after the text in italics, I’ll directly answer you.

Let me start by noting the whole purpose of 3.10.3.1, which was to provide a means for a heat treater to demonstrate that their oil quenching system continues to work well. If they do the steps outlined in 3.10.3.1, they do not need to seek approval from their customers for this method. If they choose a different method for monitoring the quench system, they need approval by the cognizant engineering organization (CEO). Since a heat treat firm will probably have many customers with different CEO’s, it makes sense to have one test procedure on which all can agree.

The method starts with the heat treat quality function choosing one of the suggested alloys and bar size configurations noted in 3.10.3.1.2. The constraints of the choice are that the hardenability of the sample has to be enough that they will get full hardening in the center, but not so much that a bar 1.25 times the diameter chosen would get full hardening. (That prevents me from using an air hardening steel, which will not show any difference when my quench system degrades.) If the three choices in 3.10.3.1.2 (a-c) will not work, then (d) offers an out, using other materials and dimensions, established in pre-production testing.

Prior to initial production, and quarterly afterward, the heat treater runs one of the test bars in a typical or simulated production load. They then section out a half-inch slice from the middle of the length of the bar and test the hardness. If in the quarterly testing it remains above the acceptance criterion established by the pre-production testing, their quench system passes.

Figure 1. Cert 4130

Accept/reject criteria is that the hardness in the center meets the hardness of the end-quench hardenability curve done by the original mill, or someone else, per ASTM A255, on the material used for the test. AMEC wanted this because using the generic curves in ASTM A304 is too general, and the curves are routinely done by the steel mills. I’ve attached an example cert (Figure 1) for some 4130 we bought not long ago, and at the bottom of the page are the Jominy numbers! They range from 51 to 24; so, which should I use?

To find the correct accept/reject hardness, I go to a curve that shows what Jominy distance in sixteenths of an inch reflects the cooling at the center of the size of test bar I use. If I’m using 4130 steel from my certified lot of material, the specimen is half inch in diameter, and the attached Timken curves say that the center of a half inch bar cooled with an H of 5 (good agitation) corresponds to a Jominy distance of 3/16, so the hardness required is 49 HRC. If I use a different curve, like the other one attached from an old Copperweld brochure (Figure 2), I get a Jominy distance of 31⁄2, so my acceptance number is somewhere between 49 and 46, so I’ll use 48 HRC. This difference is small, and unimportant, since I’m only using it to show if there is degradation in the oil quench performance.

Figure 2. Jominy Cooling Rates (Copperweld Steel Brochure)

This “compare it with the Jominy curve done by the mill” is only for the 4130 and 4330V specimens noted in 3.10.3.1.5.1 and 3.10.3.1.5.3. For specimens made of 4140, we call out HRC 44 in the center and HRC 50 in the 3⁄4 radius position of the 11⁄2 inch diameter specimen.

So, the 8/16 position on the Jominy curve doesn’t mean it’s appropriate for a half inch diameter specimen – it’s just pointing to the spot on the Jominy bar that’s 8/16 inch from the end that gets sprayed with water. The “secret decoder ring” I mentioned are the “Jominy cooling rates” or the “Pages from Timkin” attachment (Figures 3). These translate the speed of quenching at any sixteenth- inch position of a Jominy bar to the equivalent rate of quenching of surface, mid-radius, and center of bars of different size quenched in various coolants. I tend to use the “Jominy cooling rates” attachment, which I got from an old Copperweld Steel brochure, but since the Timkin Practical Data Handbook for Metallurgists is on the web for free, it’s probably a more universal reference.

Hence for 0.50” diameter 4130 bar, the center hardness should be that corresponding to between 3 and 4 sixteenths of an inch. For the 2.5” diameter bar, quenched in mildly agitated oil, the cooling rate at the center would be represented by the 14/16” position on the Jominy bar. Maybe 15/16” – it’s kind of hard to read. Hence you read the data from the mill cert FOR THE STEEL FROM WHICH THE PIECES WERE MADE and use those numbers as accept/reject. HTT

About the author: Lee Gearhart, P.E., has worked for Moog, Inc. since 1982 and is currently Principal Engineer, Materials and Process Engineering.  In addition to being a worldwide resource for the company, Lee is the current chair of the Aerospace Metals Engineering Committee, where much of the discussion on heat treating specifications occurs. 

 For more information, contact Lee at lgearhart@moog.com or 716-687-4475 


*Section 3.10.3 from AMS2759 Heat Treatment of Steel Parts (This section is one of the big changes to AMS2759 revision F, April 2018, which was then tweaked to revision G in August 2019) 

 The sections to which the article discusses is 3.10.3.1, 3.10.3.1.2 (a-d)3.10.3.1.5.1 and 3.10.3.1.5.3 

 3.10.3 Quench System Monitoring 

The quench system includes the quench volume, type of fluid, recirculation velocity and uniformity, and heat exchange capacity. The consistency of the quench system shall be monitored quarterly, by processing test parts, as outlined below, which are capable of detecting changes in the cooling characteristics of the system. Testing of water quench systems is not required. Quench system monitoring test procedures other than those described in 3.10.3.1 shall be approved by the cognizant engineering authority. When destructive mechanical property testing is required for part acceptance, quench system monitoring is not required.  

3.10.3.1 Test Specimen Requirements  

3.10.3.1.1 Test Specimen Alloy/Configuration  

3.10.3.1.1.1 Round specimens of carbon or low alloy steel, of appropriate hardenability and dimensions shall be used. Selection of the specimen dimensions/hardenability combination shall be aimed at achieving full hardening (e.g., 95% martensite) at the center of the specimen. The specific combination of alloy/dimensions chosen shall be such that the specimen would not be capable of achieving full hardening at 1.25 times the diameter chosen for the test specimen. The length of the test specimen shall be at least three times the diameter.  

3.10.3.1.1.2 The test specimens used for the initial and subsequent evaluation of a particular quenchant shall be from the same alloy and preferably the same chemistry heat of material to eliminate material chemistry and hardenability differences from the alloy selection. Hardenability results shall not be lower than that represented by requirements in 3.10.3.1.5.  

3.10.3.1.2 Test specimen alloy/dimensions shall be one of the following:  

  1. 4130 round bar, minimum 1.50 inches (3.81 cm) long, 0.50 inch (1.27 cm) nominal diameter
  2. 4140 round bar, minimum 4.50 inches (11.43 cm) long, 1.50 inches (381 cm) nominal diameter. 
  3. 4330V round bar, minimum 7.50 inches (19.05 cm) long, 2.5 inches (6.35 cm) nominal diameter. 
  4. Other material and dimensional requirements established in pre-production testing or as specified by the cognizant engineering organization. See 8.5 for shape equivalent guidelines. 

3.10.3.1.3 Test Specimen Processing  

Quarterly quench system monitoring tests shall be run with a typical or simulated production load. Heat treat loads shall be processed in accordance with the appropriate AMS2759 slash specification requirements.  

3.10.3.1.4 Specimen Testing Requirements  

After quenching the test specimen, a 0.5-inch-thick specimen shall be cut from the center of the test specimen length and prepared for hardness testing in the untempered condition. Specimen shall be prepared to ensure it is free from overheating. The minimum hardness at the center of the diameter shall meet the hardness requirements of the approved procedure in 3.10.3.  

3.10.3.1.5 Test Specimen Hardenability  

3.10.3.1.5.1 Round Bar Specimen 4130  

After quenching, the center of the diameter shall not be less than the hardness on the end-quench hardenability curve corresponding to the diameter of the specimen when tested in accordance with ASTM E18. The end-quench hardenability curve shall be the actual hardenability curve determined in accordance with ASTM A255 on the material used for the test specimen.  

3.10.3.1.5.2 Round Bar Specimen 4140  

The hardness in the center of the diameter shall not be less than HRC 44 and the 3/4 radius shall not be less than HRC 50 when tested in accordance with ASTM E18.  

3.10.3.1.5.3 Round Bar Specimen 4330V  

The hardness in the center of the diameter shall not be less than the hardness on the end-quench hardenability curve corresponding to the diameter of the specimen when tested in accordance with ASTM E18. The end-quench hardenability curve shall be the actual hardenability curve determined in accordance with ASTM A255 on the material used for the test specimen.  

3.10.3.1.5.4 If other combinations are established, the accept/reject criteria shall be as specified in the ordering information.  

3.10.3.1.5.5 It is the responsibility of the heat treater to provide the material and hardenability data specified above.  

3.10.3.2 Any failures shall be documented by the heat treater’s corrective action system.  

3.10.3.2.1 As a minimum, if the test specified in 3.10.3 fails, the quench medium shall be analyzed as specified in 3.10.3.3.  

3.10.3.3 Quench Media Control  

3.10.3.3.1 Each new shipment of quenchant from a vendor shall meet the requirements for the particular quenchant listed in 3.10.3.3.1.1 through 3.10.3.3.1.3 as applicable. The vendor shall furnish a certificate of conformance stating that the quenchant meets the requirements including, in addition to the vendor designation, the cooling curve, the cooling rate curve, the maximum cooling rate, and:  

3.10.3.3.1.1 For mineral oil based quenchants, the certificate shall also include the viscosity, flash point, temperature at the maximum cooling rate.  

3.10.3.3.1.2 For vegetable or ester-based oil quenchants, the certificate shall also include the viscosity, flash point, temperature at the maximum cooling rate.  

3.10.3.3.1.3 For polymer quenchants, the certificate shall also include the undiluted pH and viscosity. The pH, viscosity, maximum cooling rate and the temperature at the maximum cooling rate shall be provided at 20% concentration by weight.  

3.10.3.3.2 Cooling curve tests shall be performed semi-annually, or when required by corrective action (3.10.3.2), in accordance with ASTM D6200, ISO 9950 or JIS K 2242, ASTM D6482, or ASTM D6549, as applicable to the specific quench medium. If no alternative limits have been established by pre-production tests or specified by the cognizant engineering authority, exceeding the following limits compared to the initial shipment of quenchant shall be cause for corrective action:  

  • For mineral oils: Temperature of the Maximum Cooling Rate: (±68 °F) (37.8 °C) Maximum Cooling Rate: (±25 °F/s) (13.9 °C/s) 
  • For vegetable or ester-based oils: Maximum Cooling Rate: (±25 °F/s) (13.9 °C/s) Temperature of the Maximum Cooling Rate: (±68 °F) (37.8 °C) 
  • For polymer quenchants: Maximum Cooling Rate: ±15% Temperature of the Maximum Cooling Rate: ±15% 

(Photo source: global.ihs.com)

 

Demonstrating Oil Quenching Effectiveness Read More »

Process Innovation to Reduce Distortion During Gas Quenching

“High-pressure gas quenching (HPGQ) attempts to reduce temperature nonuniformities by reducing the cooling rate; however, this is generally not sufficient to eliminate shape change. Shape change can be predicted by heat treatment simulation software, but it is difficult to reproduce the exact same cooling conditions in the vessel for each batch. Therefore, the distortion of the components will not be consistent from batch to batch.”

Read the case study to see one response to this issue in this original content from Heat Treat Today by Justin Sims, lead engineer at DANTE Solutions.

This article first appeared in the latest edition (March 2020) of Heat Treat Today’s Aerospace Heat Treating magazine.


Distortion is generally described by a size change and a shape change. In heat treatment of steels, size change is unavoidable and is mainly due to the volumetric difference between the starting microstructural phase and the final microstructural phase. Shape change of steel parts from heat treatment is due to nonuniform thermal and nonuniform microstructural strains as a result of nonuniform cooling or heating, alloy segregation, poor support of the component while at high temperature, thermal expansion or contraction restrictions, or residual stresses from prior forming operations. Nonuniform cooling or heating can be as fundamental as the temperature gradient from the part surface to its core, or as complex as the flow of fluid around a component feature. Both can result in nonuniform strains, resulting in a shape change. If the stresses causing these strains exceed the yield strength of the material, then permanent shape change will occur. Size change can be anticipated and is predictable, while shape change, or distortion, is usually unanticipated and more difficult to predict.[1-2] 

Justin Sims,
Lead Engineer,
DANTE Solutions

Most thermal processes try to control these nonuniformities using methods of low complexity such as part orientation and rack design. Quenching systems, for example, are generally designed to remove as much thermal energy from the work pieces as possible and to do this as quickly as possible. High-pressure gas quenching (HPGQ) attempts to reduce temperature nonuniformities by reducing the cooling rate; however, this is generally not sufficient to eliminate shape change. Shape change can be predicted by heat treatment simulation software, but it is difficult to reproduce the exact same cooling conditions in the vessel for each batch. Therefore, the distortion of the components will not be consistent from batch to batch.

In response to this issue, a prototype gas quenching unit capable of controlling the temperature of the quench gas entering the quench chamber was devised. With the DANTE Controlled Gas Quench (DCGQ) unit, it is possible to have control of the thermal and transformation gradients in the component by controlling the temperature of the incoming quench gas, thereby significantly reducing, or eliminating entirely, the shape change caused by quenching. In doing so, the size change can easily be predicted by heat treatment simulation software, and post-hardening finishing operations can be reduced or eliminated. This process is ideal for thin parts or components with significant cross-sectional changes. Atmosphere Engineering (now part of United Process Controls) in Milwaukee, Wisconsin constructed the unit and provided the logic to control it. All experiments with the unit were conducted at Akron Steel Treating Company in Akron, Ohio. The project was funded by the U.S. Army Defense Directorate (ADD).

Figure 1 (left) shows the front of the unit, while Figure 1 (middle) shows the back of the unit. The back of the unit contains the human machine interface (HMI), shown in Figure 1 (right), where process parameters can be modified and DCGQ recipes entered. The prototype unit has a working zone of nine cubic ft. and is capable of quenching loads up to 100 lbs. at one atmosphere of pressure.

Figure 2. Comparison of quench gas temperature entering the
quench chamber versus the recipe setpoint temperature for
two different DCGQ process recipes

The ability of the unit to maintain continuity between the recipe setpoint temperature and the actual temperature entering the quench chamber is absolutely paramount. Figure 2 shows two schedules, one aggressive and one conservative, comparing the recipe setpoint (Chamber Inlet SP) to the actual quench gas temperature (Chamber Inlet PV). Figure 2 also shows that the prototype unit has good control of the quench gas temperature between 752°F (400°C) and room temperature, the martensite transformation range for most high hardenable steel alloys. There is some deviation between the two temperatures below 392°F (200°C) for the aggressive schedule as the setpoint reaches its set temperature, due to the relatively small temperature difference between the quench gas and the shop air. This small temperature difference makes it slightly difficult for the air-to-air heat exchanger used in the design to keep up with the rapid drop in temperature, but overall there is very good control of the quench gas temperature.

Figure 3. Micrograph of DCGQ (left) and HPGQ (right) processed coupons, mag. 1000X
There is a copper layer on the surface of the DCGQ processed coupon.

Microstructural examination was conducted on Ferrium C64 coupons processed using the DCGQ process and coupons processedusing a 2-bar HPGQ. C64 was chosen for this study due to its extremely high hardenability and its high tempering temperature. Figure 3 compares the microstructures of the two processes at a magnification of 1000X, and no significant difference is detected. The DCGQ coupons required two hours to complete the transformation, whereas the HPGQ coupons transformed in a few minutes. There is no indication that the slow rate of transformation damaged the microstructure or mechanical properties in any way. Tensile and Charpy properties were equivalent between the two processes.

Distortion coupons, thick disks with eccentric bores, were designed and manufactured with the goal of evaluating the distortion response when subjected to a DCGQ process, and then compared to coupons subjected to a standard 2-bar HPGQ operation. All coupons were manufactured from the same Ferrium C64 bar stock. All coupons were cryogenically treated and tempered at 595°C for eight hours after quenching.

Figure 4. Nomenclature and locations used for out-of-round measurements on the distortion coupon

Figure 4 shows a distortion coupon with the nomenclature and locations used for measuring the out-of-round distortion of the eccentric bore. Due to the uneven mass distribution, the north-south direction will generally be larger than the east-west direction. Five measurements were then made along the axis of the coupon using a Fowler Bore Gauge.

Table 1. Out-of-round distortion measurements of the distortion coupon for a DCGQ and HPGQ process

Table 1 shows the results from four coupons; two hardened using the DCGQ process and two processed using the standard 2 bar HPGQ for C64. The individual measurements (EW1, NS5, etc.) are relative and are dependent on the reference value used for the bore gauge. The individual measurements give an indication of the variation in distortion in the axial direction. The out-of-round measurements are actual values, as they are the difference between the actual measurements. The DCGQ process gave significantly less distortion than the HPGQ process.

While the values reported show a 50% reduction in out-of-round distortion for the DCGQ process, a larger gain could have been realized if two other conditions were addressed. First, the coupon for DCGQ was placed directly into a 1832°F (1000°C) preheated furnace since the prototype unit does not have austenitizing capabilities. Controlled heating, just like controlled cooling, should be utilized to realize the full potential of this process. Second, the DCGQ schedule was designed for another coupon geometry that was processed together with these distortion coupons. Therefore, the schedule was not optimum for this coupon geometry.

Table 2. DANTE simulation results comparing HPGQ and DCGQ using the experimental conditions and a DCGQ with optimized heating and cooling schedulesMARCH 2020

Table 2 compares the DCGQ simulation results in which the two processes executed on the experimental coupons were compared to an optimized process, including controlled heating and cooling schedules designed for this coupon. The optimized schedule predicts an order of magnitude reduction in out-of-round distortion. Comparison of the measurements from the HPGQ and DCGQ experiments in Table 1 to the model predictions in Table 2 shows that the model predictions agree closely with the experimental results.

Simulating the application of the DCGQ process to a gear geometry, the predicted warpage of a bevel gear was examined. The simulation looked at the differences between an oil quench, 10 bar HPGQ, and a 10 bar DCGQ process. From Figure 5, it is clear that the HPGQ process is predicted to produce the most distortion. Even though the 10 bar gas quench has a slower cooling rate than the oil quench, less distortion is not guaranteed since a slower rate does not guarantee a more uniform phase transformation.[3] In this case, both heating and cooling were controlled for the DCGQ simulation.

Figure 5. Comparison of oil quench, HPGQ, and DCGQ processes for a bevel gear

In summary, a prototype gas quenching unit has been constructed with the ability to accurately control the temperature of the quench gas entering the quench chamber. Experimental results have shown that mechanical properties and microstructure are equivalent between the DCGQ process and a 2-bar HPGQ process for Ferrium C64. Thick disks with eccentric bores were machined and then heat treated using DCGQ and HPGQ. It was shown that the DCGQ process reduced distortion in these disks by 50%. Simulation using DANTE then showed that the distortion could be reduced further if controlled heating and cooling are used. Finally, a comparison was made between an oil quench, HPGQ, and DCGQ processes for a bevel gear. This comparison showed that the HPGQ process was predicted to cause the most distortion. HTT

References

[1] Prabhudev, K.H., Handbook of Heat Treatment of Steels, Tata McGraw-Hill Publishing, 1988, p.111-114

[2] Sinha, Anil Kumar, ASM Handbook, Vol. 4: Heat Treating, ASM International, 1991, p.601-619

[3] Sims, Justin, Li Zhichao (Charlie), Ferguson B. Lynn, Causes of Distortion during High Pressure Gas Quenching Process of Steel Parts, Proceedings of the 30th ASM Heat Treating Society Conference, ASM International, 2019, p.228-236

 

About the Author: As an analyst of steel heat treat processes and an expert modeler of quench hardening processes, Justin Sims was the lead engineer for designing and building the DANTE Controlled Gas Quenching (DCGQ) prototype unit. This system was developed to minimize distortion of quenched parts made of high hardenability steels, while still achieving the required properties and performance.

For more information, contact Justin at DANTE Solutions

 

Process Innovation to Reduce Distortion During Gas Quenching Read More »

Heat Treat Tips: Aqueous Quenching

One of the great benefits of a community of heat treaters is the opportunity to challenge old habits and look at new ways of doing things. Heat Treat Today’s 101 Heat Treat Tips is another opportunity to learn the tips, tricks, and hacks shared by some of the industry’s foremost experts.

For Heat Treat Today’s latest round of 101 Heat Treat Tips, click here for the digital edition of the 2019 Heat Treat Today fall issue (also featuring the popular 40 Under 40).

Today’s tips come to us from Quaker Houghton and Contour Hardening, covering Aqueous Quenching. This includes advice about effective filtration in removing particulates in aqueous quench systems and tips for aqueous quenchant selection.

If you have a heat treat-related tip that would benefit your industry colleagues, you can submit your tip(s) to anastasia@heattreattoday.com  or editor@heattreattoday.com.


Heat Treat Tip #5

Remove Particulates

Adding a strong magnetic filter in line after the main filtration system is an effective way to remove fine, metallic particulates in an aqueous quench system.

Submitted by: Contour Hardening


Heat Treat Tip #9

Aqueous Quenchant Selection Tips

Greenlight Unit (source: Quaker Houghton)

1. Determine your quench: Induction or Immersion? Different aqueous quenchants will provide either faster or slower cooling depending upon induction or immersion quenching applications. It is important to select the proper quenchant to meet required metallurgical properties for the application.
2. Part material: Chemistry and hardenability are important for the critical cooling rate for the application.
3. Part material: Minimum and maximum section thickness is required to select the proper aqueous quenchant and concentration.

Aqueous Quenching (source: Quaker Houghton)

4. Select the correct aqueous quenchant for the application as there are different chemistries. Choosing the correct aqueous quenchant will provide the required metallurgical properties.
5. Review selected aqueous quenchant for physical characteristics and cooling curve data at respective concentrations.
6. Filtration is important for aqueous quenchants to keep the solution as clean as possible.
7. Check concentration of aqueous quenchant via kinematic viscosity, refractometer, or Greenlight Unit. Concentration should be monitored on a regular basis to ensure the quenchant’s heat extraction capabilities.

Greenlight Display (source: Quaker Houghton)

8. Check for contamination (hydraulic oil, etc) which can have an adverse effect on the products cooling curves and possibly affect metallurgical properties.
9. Check pH to ensure proper corrosion protection on parts and equipment.
10. Check microbiologicals which can foul the aqueous quenchant causing unpleasant odors in the quench tank and working environment. If necessary utilize a biostable aqueous quenchant.
11. Implement a proactive maintenance program from your supplier.

 

 

Submitted by: Quaker Houghton


 

Heat Treat Tips: Aqueous Quenching Read More »

Using Virtual Tools for Quenching Process Design

By validating CFD simulation results with thermocouple data, Ford Motor Company is now using virtual tools to study aluminum cylinder head quenching process and gains valuable information for process design and optimization. James Jan and Madhusudhan Nannapuraju presented a study titled “CFD Investigation of Quench Media and Orientation Effects on Structural Stress Induced in the Intense Quenching Processes for Aluminum Cylinder Heads” at Heat Treat 2017 as part of the proceedings of the 29th ASM Heat Treating Society Conference, October 24–26, 2017, Columbus, Ohio, USA. (Copyright © 2017 ASM International® All rights reserved.)

This article is a synopsis of the study, which can be read in its entirety here: “CFD Investigation of Quench Media and Orientation Effects on Structural Stress Induced in the Intense Quenching Processes for Aluminum Cylinder Heads”


Heat treatment is a common manufacturing process to produce high-performance components. Although heat treatment incorporating a quenching process can produce parts with durable mechanical properties, an unwanted effect of intense quenching is the induced thermal residual stress, which often is a leading cause for quality issues associated with high cycle fatigues. During the product development cycle, it is not uncommon to switch between air and water quenching and change quench orientation in order to minimize residual stress. However, the choice of quench media and quench orientation is often determined by intuitive engineering judgment at best and trial-and-error iterative method at worst.

In recent years, digital verification using finite element analysis (FEA) is gaining popularity because of its efficiency. The computational method to predict the residual stress involves two calculations. The first step is to calculate the temperature history; then the temperature data is used as thermal-load-to-structure analysis for stress and deformation calculation.

A popular method for temperature calculation is the heat transfer coefficient (HTC) method, however, the biggest drawback of HTC method is that the method relies on thermocouple measurement for calibration and the calibrated HTC may not be applicable to different design and quenching process. With the advancement in computation fluid dynamics CFD technologies, the temperature history in quenching now can be accurately calculated. Since thermal residual stress is directly linked to non-uniform temperature distribution in the metal, spatial temperature gradient is evaluated to study the performance of different quench media and configuration.

Figure 1: Heat treatment process for aluminum cylinder heads and quality concern associated with quenching process.

Air Quench Process for Cylinder Heads

The main heat extraction mechanism in air quenching is forced convection. In our CFD model, it is assumed that the buoyancy effect and radiation heat transfer have a negligible impact on the accuracy. The CFD simulation results are compared with thermocouple readings, and the overlapping curves illustrate an excellent agreement and validate our model.

Figure 2: CFD model and comparison to thermocouple measurement for air quenching a cylinder block with riser attached.

We use CFD to study and compare four different air quenching configurations. One unique advantage of CFD simulation over physical testing is its capability to visualize flow patterns and to identify low heat transfer regions under stagnant air pockets. The quenching configuration (a), (b) and (c) represent a conveyer style quenching environment, (d) represents a basket style quenching environment. See Figure 3.

Figure 3: Air flow and air pockets surrounding cylinder head for all air quenching configurations, 60 seconds into quenching.

The cooling curve plot shows that the cylinder head quenched in a basket (d) cools faster compared to those quenched on a conveyer (a), (b), and (c). According to the temperature gradients plot, basket quenching (d) cools faster at a higher temperature gradient than conveyer quenching (a) and (c). The only exception is (b). In-depth investigation of the location of high-temperature gradient indicates that the regions between the water jacket and intake port are susceptible to high residual stress.

Figure 4: Cooling curve and temperature gradient for all air quenching configurations.

Figure 5: High-temperature gradient locations for conveyer quenching (a) and basket quenching (d), 60 seconds into quenching.

Water Quench Process for Cylinder Heads

The physics of water quenching is much more involved than air quenching. Ford Motor Company adapted the quench model framework by AVL FIRE™, which is based on the Eulerian-Eulerian multiphase model, and developed our own proprietary database to simulate the water boiling process. Extensive work has been done on computation and experiments to validate the numerical methods. The CFD simulations compared to lab experiment on cooling curves provide strong evidence that our CFD model is accurate and that it can predict temperature profile on every quenching orientation without calibration.

Figure 6: Experimental and CFD simulation for cylinder block; cooling curves from CFD and thermocouple are plotted together for comparison.

Six different quench orientations are studied, and the vapor patterns and vapor pockets are plotted for in-depth investigation. The cooling curve and temperature gradient plot illustrate that orientation has little impact on overall cooling characteristics, and maximum temperature gradient is similar except that they occur at different time, even though the vapor pattern and locations of vapor pockets are drastically different in each quenching orientations.

Figure 7: Vapor Pattern and Vapor Pocket Entrapped inside Cylinder Heads, 20 seconds into quenching.

Figure 8: Cooling curve and maximum temperature gradient for all water quenching configurations.

Observing the location of the high-temperature gradient, for rear face up (RE) and cam cover face up (CC) quenching, high-temperature gradient appears in the intake port area, similar to the air quenching cases. Since the high-temperature gradient is observed near the intake port for all quenching cases, both air quenching and water quenching, very likely it is a design-related issue.

Figure 9: High-Temperature Gradient Locations for Rear Face up (RE) and Cam Cover Face up Quenching (CC), 20 seconds into Quenching.

Comparison of Air and Water Quenching Process

The underlying heat extraction for air and water quenching is very different. While air quenching relies on convection heat transfer to cool the metal, water quenching relies on water to vapor phase change to take the heat away. Therefore, metal cools significantly faster in water quenching than in air quenching. The maximum temperature gradient for water quenching is also much larger than air quenching. Since water only vaporizes in areas in contact with a hot surface, the heat loss is a local phenomenon subject to vapor escape route and the supply of fresh water. In other words, the heat transfer may not be as smooth as air quenching and it is reflected in the fluctuation of high-temperature gradient plot.

A much higher temperature gradient in water quenching does not necessarily generate much higher residual stress. We can also see in the plot that the duration of peak temperature gradient only lasts about 15 seconds. In this duration, the metal may exceed yielding stress and plastic deformation starts. However, the final deformation also depends on how long the state of stress stays in plastic deformation zone.

Figure 10: Cooling curve and maximum temperature gradient for selected air and water quenching configurations.

Conclusions

The rapid, large temperature drop in the quenching process has two opposite effects on the eventual outcome. On one hand, the large cooling rate produces metals with better quality, but it also induces residual stress. Thanks to the advancement of 3D CFD methodology, now the metal cooling in the quenching process can be much better understood using computer simulations. By using validated air and water quench modeling method, we compared the cooling curves and temperature gradient to evaluate quenching performance for various quenching configurations.

For air quenching processes, the study finds that cylinder heads cool faster in basket quenching than in conveyer quenching environment. The explanation is that airflow is accelerated when passing through the narrow gaps between cylinder heads in basket quenching. For water quenching processes, the study finds the orientation has little effect on the overall cooling rate as well as maximum temperature gradient except for a time shift in the maximum gradient. The results also show that the temperature gradient in water quenching is significantly larger than air quenching but last a much shorter period of time. Studying the temperature gradient for all air and water quenching case reveals a weak spot between the intake port and water jacket. Since this spot appears in all quenching cases, it should be remedied by a design change rather than changing the manufacturing process alone.

References

  • Koc, M., Culp, J., Altan, T. “Prediction of Residual Stresses in Quenched Aluminum Blocks and Their Reduction through Cold Working Processes,” Journal of materials processing technology, 174.1 (2006), pp342-354.
  • Wang, D.M., Alajbegovic, A., Su, X.M., Jan, J., “Numerical Modelling of Quench Cooling Using Eulerian Two-Fluid Method”, Proceedings of IMECE 2002, ASME-33499 Heat Transfer, vol. 3, 2003, pp. 179-185. LA, USA.
  • Srinivasan, V., Moon, K., Greif, D., Wang, D.M., Kim, M., “Numerical Simulation of Immersion Quench Cooling Process”: Part I, Proceedings in the International Mechanical Engineering Congress and Exposition, IMECE2008, Paper no: IMECE2008-69280, Boston, Massachusetts, USA, 2008.
  • Srinivasan, V., Moon, K., Greif, D., Wang, D.M., Kim, M., “Numerical Simulation of Immersion Quench Cooling Process”: Part II, Proceedings in the International Mechanical Engineering Congress and Exposition, IMECE2008, Paper no: IMECE2008-69281, Boston, Massachusetts, USA, 2008.
  • Kopun, R., Škerget, L., Hriberšek, M., Zhang, D., Stauder, B., Greif, D., “Numerical simulation of immersion quenching process for cast aluminium part at different pool temperatures”, Applied Thermal Engineering 65, pp. 74-84, 2014
  • Jan, J., Prabhu, E., Lasecki, J., Weiss, U, “Development and Validation of CFD Methodology to Simulate Water Quenching Process,” Proceedings of the ASME 2014 International Manufacturing Science and Engineering Conference, Detroit Michigan, 2014.

 

Photo credit for all images: Ford Motor Company; cited in “CFD Investigation of Quench Media and Orientation Effects on Structural Stress Induced in the Intense Quenching Processes for Aluminum Cylinder Heads”, Heat Treat 2017: Proceedings of the 29th ASM Heat Treating Society Conference October 24–26, 2017, Columbus, Ohio, USA.

 

Using Virtual Tools for Quenching Process Design Read More »

Distortion Analysis of Landing Gear During Oil Quench: A Case Study

Charlie Li

A thermal process modeling company used its heat treatment simulation software to explore oil quench sensitivities on the distortion of a large landing gear made of 300M, a vacuum melted low alloy steel that includes vanadium and a higher silicon composition.

DANTE Solutions, an engineering consulting and software company specializing in metallurgical process engineering and thermal/stress analyses of metal parts and components, was approached to examine local stagnant oil flow and immersion, among other sensitivities, for this critical aerospace component.

Zhichao (Charlie) Li, Ph.D., vice president of DANTE Solutions, was the lead researcher and author of this study.


Case Study

Problem Statement

Part:

3 modes of distortion that are of concern

  • 2.5 meter tall landing gear
  • 0.25 meter main tube diameter
  • AISI 300M material

Problem:

  • Large distortions after oil quenching in the following distortion modes:
    • Bow in XY-Plane
    • Bow in YZ-Plane
    • Straightness of a Blind Hole
  • All distortion modes shown in the figures make assembly of the entire structure very difficult.
  • Immersion into the oil tank is the main focus of the distortion analysis.

Process Description

  • Part is austenitized in pit furnace at 1607°F (875°C).
  • A 45-second step is included for the removal of the landing gear from the pit furnace.
  • 75-second open-air transfer from pit furnace to oil quench tank. The landing gear is immersed into the oil with a speed of 203.2 mm/sec, with the immersion direction shown in the figure. It takes 11.885 seconds to immerse the entire gear in the oil tank.
  • The landing gear is held in the oil for 5 minutes.
  • Tempering not considered, due to negligible effects on distortion.

Temperature (°C), Austenite (fraction), horizontal displacement (mm), and vertical displacement (mm) at the end of the immersion process; section cut, looking inside the part.

Model Description

  • Model contains 281,265 nodes and 258,272 hex elements.
  • 3 surfaces defined for heat transfer boundary conditions.
  • Oil flow stagnation is expected inside the main tube (Inner Surface) and the blind hole.
  • Different thermal boundary conditions are applied to the outer surface and the inner surface, as shown to the right.
  • The blind hole and the inner surface have the same thermal boundary conditions in the baseline model.
  • During immersion, oil enters the blind hole first and then begins to fill up the main tube.
  • In the baseline model, the oil level rising speed inside the bore is assumed to be 20% of the landing gear immersion speed.

 

 

Modeling Approach

  • Define heat transfer coefficients as a function of temperature for the oil tank.
    • Thermocouples placed at various locations on a dummy landing gear, which was
      approximately the same overall dimensions and mass. Improve 300M material data in DANTE material database using dilatometry testing.
  • Improve 300M material data in DANTE material database using dilatometry testing.
  • Perform sensitivity study to determine phenomena critical to distortion modes of interest.
    • Oil flow stagnancy in blind hole during immersion: The more stagnancy, the lower the heat transfer on this surface. Baseline assumed to be the most stagnant. Two faster heat transfer rates examined.
    • Oil flow stagnancy around structural support arm: The more stagnancy, the lower the heat transfer on this surface. Baseline assumed to be least stagnant. Two slower heat transfer rates examined.
    • Oil fill rate of the main tube during immersion into the oil: The slower the oil fills up the main tube, the larger the temperature and phase transformation gradient is in the axial direction of the tube. Baseline assumed the slowest fill rate. Three faster fill rates were examined.
    • Immersion direction: Immersion direction sets up axial temperature/phase transformation gradients and also determines how the main tube is filled. The Baseline immersion direction causes oil to enter through the blind hole first and then into the main tube. Opposite immersion direction is examined, which causes oil to enter the open end of the main tube first.

Blind Hole Quench Rate Sensitivity

Figure 8. Temperature (°C) in the blind hole at the end of immersion for the three cases.

  • Heat transfer is increased in the blind hole during the
    immersion process; all other heat transfer rates
    remain the same as the baseline model during
    immersion.
  • All heat transfer rates are identical to the baseline
    after the part is fully immersed in the oil.
  • Baseline model assumes blind hole heat transfer is
    equivalent to the main tube inner diameter heat
    transfer during and after the immersion process.
  • Rate 2 has a faster heat transfer rate than the baseline.
  • Rate 1 has a faster heat transfer rate than Rate 2.
  • Figure 8 shows a significant difference in temperature between the three cases at the end of the immersion process.
  • Heat transfer rates explored in the blind hole do not contribute
    to the tilting of the blind hole.
  • Figure 9 shows that the angle of the hole is the same, regardless of the quench rate.
  • Modification of the blind hole to increase the heat transfer rate
    in the hole to help improve the straightness of the blind hole is not necessary.
  • Heat transfer rates explored in the blind hole do not contribute significantly to the bow distortion in the XYPlane or the YZ-Plane.
  • Figure 10 shows that the bow distortion is made slightly worse by increasing the heat transfer rate in the blind hole during immersion, but is not significantly worse.
  • Modification of the blind hole to increase the heat transfer rate in the hole to help improve the bow distortion is not necessary.

Figure 9

Figure 10.

Structural Beam Quench Rate Sensitivity

  • Reduced heat transfer of the structural arm is examined.
    • Oil flow stagnancy is assumed to reduce heat transfer rate on arm.
    • 2 slower heat transfer rates compared with baseline.
    • Baseline assumes the same heat transfer rate on the structural arm as on the main tube OD.
  • Figure to the left shows the reduced heat transfer rate surfaces of the structural arm.
  • Rate 1 is slower than Baseline.
  • Rate 2 is slower than Rate 1.
  • Figure below shows the temperature difference in the structural beam at the end of the immersion process.
  • Approximately 212°F (100°C) difference between Baseline and Rate 1
  • Approximately 392°F (200°C) difference between Baseline and Rate 2

 

  • Bow distortion in xy-plane has a non- Distortion of Blind Hole linear response to oil stagnancy around the structural beam.
  • Rate 1 produced the least amount of bow in xy-plane.
  • Baseline produces the greatest amount of bow in xy-plane.
  • Distortion of blind hole has a non-linear response to oil stagnancy around the structural beam.
  • Rate 1 produced the straightest blind hole.
  • Baseline produces the greatest amount of distortion of the blind hole.
  • Bow distortion in yz-plane has no sensitivity to oil stagnancy around the structural beam.
  • The non-symmetric mass near the top of the landing gear has the most influence on the yz-plane bow distortion.

  • Figure 15 shows lower bainite phase fraction at the end of the quenching process.

    Figure 15
  • Slower heat transfer rate of the structural beam results in significantly different amounts of lower bainite.
    • The slower the heat transfer, the more lower bainite formed.
  • Increased amounts of bainite reduce bow distortion in xy-plane, but the response is non-linear.
    • Rate 2 caused slightly more distortion than Rate 1, but less distortion than the Baseline.
  • Increased amounts of bainite reduce distortion of the blind hole, but the response is non-linear.
    • Rate 2 caused slightly more distortion than Rate 1, but less distortion than the Baseline.

Oil Fill Rate in Main Tube Sensitivity

  • The rate at which the oil fills the main tube is critical to the phase transformation timings and the phases formed.
  • The immersion speed of the landing gear is 203.2 mm/sec.
  • Baseline assumes the inside of the tube fills up at 20% of this value (40.64 mm/sec).
  • Three different fill speeds were explored:
    • 50% (101.6 mm/sec)
    • 100% (203.2 mm/sec)
    • 200% (406.4 mm/sec) Assumes pressure build up forces oil up the inside of the tube.
  • Figure 16 compares temperature inside tube at end of immersion for four cases.

Figure 16

 

  • The oil fill rate of the main tube during the immersion process has a very significant effect on all three modes of distortion.

From top left clockwise

  • Bow distortion in yz-plane has a non-linear response to the fill speed (Figure 17)
    • 50% produces the worst bow
    • 100% & 200% are very similar, with 200% slightly worse
  • Bow distortion in xy-plane has a non-linear response to the fill speed (Figure 18)
    • 50% produces the least bow
    • 100% produces the worst bow
  • Straightness of the blind hole has a linear response to the fill speed (Figure 19)
    • Slowest fill speed has least distortion
    • Fastest fill speed has the worst distortion

  • Difference in lower bainite was the cause for differences in distortion with respect to oil stagnancy around the structural beam previously shown.
  • Differences in distortion from the oil fill rate of the main tube are not caused by microstructural phase differences.
  • Figure 18 shows that Martensite and Lower Bainite are the same for all fill speeds.
  • Differences in distortion are caused by the transformation timing along the axis of the landing gear.

 

 

 

 

 

Immersion Direction Sensitivity

Figure 19

  • Distortion sensitivity to the immersion direction was examined.
  • Figure 19 compares temperature profile at the end of the immersion process for the two immersion directions.
  • The Baseline has oil enter the blind hole first and then fill up the tube at a rate that is 20% of the immersion speed.
    • Oil spills over the top of the tube and the tube is flooded with oil.
  • The reversed immersion has oil enter the tube first and fills at the immersion speed.
  • Figure 20

    Reversing the immersion direction also reverses the axial temperature gradient.

    • Martensite transformation starts at the open tube end when the immersion direction is reversed.
    • Martensite transformation starts by the blind hole first for the Baseline.
    • Reversing the axial phase transformation gradient can have significant effects on bow distortion and axial displacement.
  • Figure 20 shows the vertical displacement around the blind hole for the Baseline and the Reversed Immersion.
  • Reversing the immersion direction had a very minor impact on the straightness of the blind hole.
    • Closed side of blind hole was pulled further down by reversing the immersion direction, but the closed side

      Figure 21

      was not pulled up as much.

  • Figure 21 shows the bow distortion in the XY-Plane for the Baseline and the Reversed Immersion.
  • Reversing the immersion direction has a significant effect on the bow distortion in the XY-Plane, nearly doubling it.
  • Reversing the immersion direction has no effect on the bow distortion in the YZ-Plane.

 

 

 

Conclusions

  • Four process parameters were evaluated for distortion sensitivities for a large landing gear component:
    • Oil stagnancy inside a blind hole, oil stagnancy around a structural support beam, oil fill rate into the main tube as the landing gear is lowered into the oil tank, and immersion direction of the landing gear.
  • Three distortion modes were evaluated:
    • Bow distortion in XY-Plane, bow distortion in YZ-Plane, and straightness of a blind hole.
  • Bow distortion in the XY-Plane IS significantly affected by oil stagnancy around structural support beam, oil fill rate up the main tube, and the immersion direction.
    • Bow distortion in the XY-Plane is mainly controlled by the behavior of the structural support beam.
  • Bow distortion in the XY-Plane IS NOT significantly affected by oil stagnancy in the blind hole.
  • Bow distortion in the YZ-Plane IS significantly affected by oil fill rate of the main tube.
    • Bow distortion in the YZ-Plane is mainly controlled by a fitting near the open end of the tube that contributes to non-symmetric mass around the main tube in that area.
  • Bow distortion in the YZ-Plane IS NOT significantly affected by oil stagnancy in the blind hole, oil stagnancy around the structural support beam, or the immersion direction.
  • Straightness of the blind hole IS significantly affected by oil stagnancy around structural support beam and the oil fill rate up the main tube .
    • Straightness of the blind hole is mainly controlled by the structural support beam behavior.
  • Straightness of the blind hole IS NOT significantly affected by oil stagnancy inside the blind hole or the immersion direction.
  • Modifications to the quenching process were made to improve the distortion response of the landing gear.
    • Modeling results were used to direct the modifications.
    • Customer considered changes proprietary and did not share.
  • Benefit of using heat treatment simulation over physical experiments to perform sensitivity studies was shown.
    • Ability to modify, and see the effects of, just one process parameter with simulation is easy.
    • Ability to modify, and see the effects of, just one process parameter with experiments is very difficult, if not impossible.
    • Cost of simulation is minimal.
    • Cost of physical experiments can be very high.

 

Text developed from powerpoint version. Click here to view or for more information on DANTE case studies.

 

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