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Heat Treat Radio #42: Justin Rydzewski on CQI-9 Rev.4 (Part 1 of 4) – Pyrometry

Heat Treat Radio host, Doug Glenn, begins a 4-part series with Justin Rydzewski about Revision 4 of CQI-9. Having served on the 4th revision of CQI-9, this expert is full of interesting information and practical advice on how to understand and comply with CQI-9 Rev.4.

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): Today, we’re beginning a new four-part series on the latest revisions to the CQI-9 specification.  If you want to learn more about this series or related content, stick around ‘til the end of this episode.

We’re here with Justin Rydzewski who is the director of sales and marketing at Controls Service, Inc. in lovely Livonia, Michigan.  At least, this time of year it’s still lovely, right?

Justin Rydzewski (JR):  Yes, we’ve got a few weeks left, I think.

DG:  Justin is involved with the new revision of CQI-9.  First off, I want to welcome you.  Thank you so much for joining us on Heat Treat Radio.  If you wouldn’t mind, let’s give listeners/readers just a sense of who you are and what your qualifications are to talk about CQI-9 and a little bit about Controls Service.

JR:  I am the director of sales and market development for Controls Service.  I got my start with this company around 2009/2010 working just as a sales rep, making phone calls and quoting work.  Around 2010, the then president of the company was making a presentation to the AIAG, the Automotive Industry Action Group, the organization that publishes CQI-9, regarding their standard CQI-9.  We had some questions and concerns, and so they allowed us an audience.  After our presentation, they inquired whether or not we’d be interested in assisting them with drafting the third edition.  We obviously said yes.  I indirectly helped support at that point, and then when the third edition was released, we started working on the next one almost right away.  After the third was rolled out, it wasn’t too long before the fourth edition meetings started, and then I began participating in a support role, and finally as a full blown participant at the end.  The fourth edition took about 8 or 9 years to complete.  It’s was an involved process, but it was fun.  I learned a lot, and I’m proud of what we’ve been able to kick out.

As far as Controls Service is concerned, we’re an accredited calibration laboratory.  We provide various on-site calibration and pyrometry testing services within the metro Detroit area, northern Illinois, Indiana, and Ohio.

DG:  According to your website, the company is an ISO/IEC 17025 accredited provider of process control systems, calibration, maintenance, and services.  Just to be clear, you were, in fact, fully engaged in this Revision 4.  It wasn’t that you were standing on the sidelines; you were on the committee doing the work.

CQI-9 4th Edition vs. CQI-9 3rd edition (photo source: Control Services Inc.)

JR:  Yes, I, myself.  The president of the company was heavily involved with the third edition, so he was firsthand in the trenches on that one.  My participation was directly hands-on with the fourth edition.

DG:  The point is, you can speak with a good bit of authority, and that’s great.  You’ve hit on it, but give us information again on CQI-9.  Give us a brief history.  When did it start?  Who owns it? Maintains its update? To whom does it apply? And what’s its scope?

JR:  The best way I know to describe it, because perhaps the most widely known pyrometry specification is AMS2750, is CQI-9 is the automotive equivalent of AMS2750.  There are obviously some differences between the two documents, but, in a nutshell, that’s the comparison.  It is a document supported by the AIAG, the Automotive Industry Action Group.  They oversee the publication of it, the drafting of it, and supervise the whole thing through that process.  CQI-9 is the number.  Officially, I think it’s called the Special Process Heat Treat System Assessment and that kind of gets the nomenclature of CQI-9 that applies to automotive heat treaters, or any performing heat treat work within the automotive industry; and several processes fall into that category.  It can be from commercial heat to in-house heat treat, to organizations like mine that support.  It applies to anyone participating in that effort of heat treat.

DG:  Let’s talk about Rev 4.  You said as soon as “3” was out, you started on “4” and it took 8 – 9 years to get done with “4.”  What was the main reason why you needed to abandon “3,” if you will?

JR:  They schedule these things out to be rewritten on a routine basis.  Like most specifications, they are reviewed on some established interval of time.  When the third edition came out, the biggest difference between the second edition of CQI-9 and the third edition was that the third edition removed all references to AMS2750.  When 2750 was in the document, it created a world of confusion, and the guidance and errata sheets that followed were just so numerous that they made it a somewhat difficult document to adhere to.  One of the ideas we brought to the table was that maybe we should just remove all reference to it [2750] and write our own specification.  So, the third edition removed the 2750 references.  In doing so, it ended up being a very well written document.  It was effective.  The OEMs – your GMs, Fords, FCAs – were happy with the results of the document. The prolonged active interval of that document allowed us to collect a lot of really good data about what was working, what wasn’t, what was confusing, and where additional clarity was needed.  The more data we collected, the more confident we were that the fourth edition would truly make a stride toward being a more effective document.  It was longer than what we would have probably prepared for – in terms of that interval of review – but I think, all in all, the result shows for itself that it is better than it was.

Click here to read the Expert Analysis Article to hear more voices on this CQI-9 Revision 4.

DG:  You would say this Rev 4 is a major revision?  Or is it just minor?

JR:  The way the drafting process works is that you get all this feedback from the industry and review it. Everyone who participates in that work group brings their notes about things they noticed or things that they would like to see different; then we compile all of those notes together, review it, and establish a charter that drives every effort thereafter.  The major items on our charter was to increase clarity and guidance, simplify, and make it easier for the end user to adapt.  Largely, the changes within the fourth edition are towards that primary focus of our charter.

There are a lot of things in there that are different, but the difference there was merely to try to make it more clear: adjust syntax of a sentence, use a different choice of words, etc. One of the things I’ve learned in this process is that this document, while it might be clear as day in English, when it translates to German, it’s not.  Or, when it translates to a different language, whatever the language, it’s not as clear; so, when you find out what it says in the other language, you say, “Hey, that’s not what we meant to say.  We’ve got to think of another way to say it.”  Largely, the changes are to increase clarity, but there are some real big changes in that effort.  Like the heat treat assessment questions.  The formatting was completely revamped, we changed that up dramatically, expanded it in some instances, and removed some that were redundant in terms of requirements.

So, there are some big changes, but, for the most part, it was an effort to enhance the clarity.  It’s not a complete rewrite, but it is a different document.

DG:  Substantial enough that people need to pay attention.  You and I have talked in the past about the addition of a number of process tables.  Wasn’t there a lot added there?

JR:  There was one process table added to the primary document and it was Process Table I, which is regarding hot stamping.  Process Table I technically existed in the third edition of the document.  It was issued as an errata sheet in 2014, three years after the third edition, but it was never part of the primary document, so issuing it as an errata sheet had its complications.  Not only did you have to make sure that the end user was aware of the document requirements, they had to be aware that there was an errata sheet also available to them, and this complicated things.  It was very frequent for me to be out in my travels and talk to customers that were performing hot stamping that would say, “Well, it’s tough to tell what requirements in CQI-9 apply to us because we don’t have a process table.”  Well, yes you do, actually; it’s an errata sheet.  That caused frustration because, again, most people want to adhere to the requirements– they just want to know what the requirements are.  When they don’t, it’s frustrating.

DG:  For those who might not know, or have not been baptized into CQI-9 in the past, what are the major sections?  Can you break it down into the three or four major sections and a very, very brief description of those sections?

JR:  It is structured very similar to the way of AMS2750 in that regard.  You have four sections that divvy up a pyrometry section: thermocouples, instrumentation, system accuracy testing and temperature uniformity survey.  But, unlike AMS2750, CQI-9 is a system assessment, it is a process, it is a heat treat management system.  It encompasses more than just pyrometry.  Where AMS2750 is a pyrometry specification, CQI-9 is a process specification; it encompasses everything.  It also includes your heat treat system assessment, which is three sections of questions regarding your heat treat operation, then you have your pyrometry which is those four sections I mentioned.  Then you have your process tables.  Your process tables drive all of your requirements for your particular operation, in terms of frequencies and tolerances.

Process tables from Rollout Webinar (Source: Rollout Webinar PowerPoint)

DG:  Let’s jump into the section that, I think, you would probably say you’re most comfortable with- the pyrometry section.  You mentioned in that section there are four subsections.  Let’s run down through those.  I’d like to do two things.  First, let’s just talk about, very briefly, what are the major changes in each of those four sections and then let’s come back and revisit each of those sections with maybe some very practical advice.  Let’s talk thermocouples first; that’s the first section.

JR:  The thermocouple section had a fair amount of changes made to that portion of the document, but again, they were mostly for the clarity aspect of things.  I would say, from a significant standpoint, one of the things that we had in the third edition that was rather confusing was in regards to grace periods.  The only area in which a grace period was stated within the third edition was within the thermocouple section, which is funny because it doesn’t apply to thermocouples, in terms of CQI-9.  It applies to instrumentation and system accuracy tests, and so that portion was removed and placed into a more appropriate area within the document.

Another aspect of it was the requirement for the calibration report to include an accreditation symbol.  It was already a requirement that if the thermocouples were calibrated by an outside provider or third party, that they had to be accredited.  But one of the areas that that doesn’t address is that if I am an accredited calibration laboratory, and my scope includes instrument calibration, whether it be for measure or source, it doesn’t necessarily mean that I’m accredited to perform a thermocouple calibration.  So, instead of trying to overcomplicate the document and write something that says that the calibration that I’m performing on the thermocouple has to be included on my scope and create something more difficult than it has to be, we decided to just establish that the accreditation symbol needed to be included on the report. Also, as an accredited lab, I can’t place that symbol on a report for calibrations that aren’t part of my scope.  It kind of allows that portion of the industry to self-police a little bit.  That was one of the more significant changes.

Another one was that we made some adjustments to the usage side of things.  There was a requirement – in lieu of tracking uses of nonexpendable thermocouples –  which allowed you could to put a nonexpendable thermocouple in use for a duration of time, and you could have unlimited uses essentially for that duration, and then you could remove it from service at that point.  However, that duration of time was absent of some critical information, that being, for usage of the elevated temperatures.  In the usage table, it was 90 uses for over 1800 degrees and 180 for under 1800 degrees, and you had 6 months for a placement interval.  That didn’t necessarily convey what we were trying to do, so we added some usage in there for the nonexpendable for over that 1800 degree mark.

We also included RTDs.  I come across them, but just because of the temperature range that most of the processes within the automotive heat treat world are operating RTDs are necessarily applicable.  But, they exist and a common approach that I would come across at least, was “well, they’re not included, so I don’t have to do anything.”  So, we just included them to wipe that off the board, and now we know that any sort of temperature sensor is critical to address, if that portion of the process is temperature critical.

We added some caveats around resident thermocouples and their usage, which, in the previous one, were only allowed for comparative method SAT.  We added some caveats for requirements when they’re used for probe methods within the realm of CQI-9.

DG:  Before we go on to the next section which will be calibration, let’s back up just for a half a second.  You and your team actually did a rollout webinar.  Can you briefly tell the listeners where they can find a little more thorough description of the rollout on this thing, because we’re not going to cover all the details here, obviously.

Rollout Webinar PowerPoint Cover Image. Get the webinar here.

JR:  Yes. It would be really tough to dive into everything; some of the changes are so insignificant, that it’s not worthy of discussion, really.  The AIG’s website has a page assigned to automotive heat treat and on that page they have some links to different content that we produced for that rollout presentation back in mid-September.  There is also a page 3 of the document itself which outlines the majority of the changes, (at least the significant ones), made within the fourth edition.  So there is a list, 3 ½ pages long, of the different changes made.  There are summaries of those changes that exist in several different places, but one of them being the document itself.

DG:  Did you not do a webinar?  Is there a webinar?  Can people actually see the webinar?

JR:  I’ve not seen the webinar posted yet, I’ve not checked in a little while, but the intent was to post a version of that webinar.

DG:  In our transcript of this podcast, we will look for it first off, and if we find it, we will put a link to it when we put this online.  So if you’re listening and you want to see that webinar, if it’s out there, we’ll put the link in.

OK, let’s move on then, Justin, to the second of the four pyrometry sections which is calibration.  What were the major changes?

JR:  Again with reporting, the reporting requirements for calibration are updated; they are different.  There are some minor revisions to the requirements for the calibration report.  Those sort of things can be easily overlooked, so I wouldn’t ignore that.  They are different.  The biggest, perhaps most significant difference within the instrumentation section is that in June 2023, all control monitoring recording instrumentation must be digital.  It is very similar to the approach taken by 2750 in removal of analog instrumentation, CQI-9 as well, is going to follow suit there, as well. [Listen to the AMS2750F episode with this update here.]

DG:  I think AMS is by 2022, so you guys are an extra year, but nonetheless, you’ve got to start getting away from analog over to digital.

JR:  For the most part, that’s the biggest change within the instrumentation section.

DG:  Let’s move on to system accuracy tests.

JR:  Within system accuracy tests, again reporting requirements are updated.  They include some new requirements there.  The illustrations within the system accuracy test section have all been updated and revamped.  I believe the old ones, that were in the third edition, were very similar in nature to the illustrations that were included in AMS2750 C, so they were well overdue for an update.  We cleaned those up.  We removed nonessential information just to make it clear what it is we’re actually discussing there.

Also, we established grace periods that are specific to each method of system accuracy test.  There are three different accepted methods for SAT within CQI-9- probe method A, probe method B, and a comparative method, and we established grace periods for each of those individually so that it’s clear and not an assumed grace period.

DG:  And grace periods being, for example, “Well, the due date falls on a holiday, how many days afterwards do I have?” That type of thing?

JR:  Yes.  If my system accuracy tests were due on a Friday, let’s say they’re due on the 1st, technically. I don’t lose my compliance on that system from a system accuracy test standpoint for x period of days after the fact.  It’s to allow for, like you said, a weekend coming up, a holiday coming up.  You can still maintain your compliance interval without having to shut everything down and start fresh.  A practical application would be, say you order some test thermocouples and they’re delayed.  So now, all of a sudden, you don’t have the test materials that you need to perform the task, or your instrument that you sent out for calibration got delayed and it’s not back yet.  Those uncontrollable sort of events don’t prevent you from operating.

DG:  The final section under pyrometry would be temperature uniformity surveys.  Any major changes there?

JR:  There were a few.  First, the reporting requirements are now different; they’ve been updated.  They include some new things.  Perhaps most notable is the requirement for when you perform a test on a semi-continuous or continuous system to indicate the soak time required versus soak time achieved.  That has to be included on the report.  Technically, it probably should have been there for the third edition as well, since one of the requirements is that you have to have obtained your desired soak time.  This just calls it out to the forefront and makes it a bit clear.  That information of the report makes assessing that aspect of things a bit more simple.

We added a specific grace period for temperature uniformity surveys so that it’s clear, it’s not assumptive.  Where I’ve seen it most often is within the hot stamping world.  You have a single stack furnace with multiple individually controlled chambers that are all separated by insulation or wall or some sort of means of differentiating them, so that they’re all essentially individual furnace cavities.  We added in some clarity to say that it’s not good enough just to test one of those chambers, you need to test all of them, because they all can be different.

[blockquote author=”Justin Rydzewski ” style=”1″]Perhaps the most significant change within the temperature uniformity survey section is to the alternative temperature uniformity survey testing methods.[/blockquote]

Perhaps the most significant change within the temperature uniformity survey section is to the alternative temperature uniformity survey testing methods.  In instances when I can’t perform a survey with sensors being trailed in, or I can’t send a data pack sort of unit or a PhoenixTM  unit through that furnace system itself to collect the data, for systems like that, in the third edition, there were three or four paragraphs of information about what you could do.  It was not entirely clear what other aspects of the section applied, what reporting was required, what sort of procedures needed to exist, and so you found a lot of variance in that testing practice.  A lot of times, I’d have customers that say, “I don’t know how to perform a TUS on it, or I don’t think that I can, or it’s not practical, so I guess I don’t have to do anything.”  And that’s not proper.  It wasn’t clear that these surveys applied in instances where you couldn’t do the other, like a traditional TUS.  So that whole entire section got rewritten from ground up to include a structure that is very similar to the other aspects of that TUS section, structured in the same way, in terms of data collection, when you need to perform the tests, these alternative tests like property surveys and whatnot, the procedure that needs to exist, what needs to be included in the procedure, and what needs to be included in the reporting.  Basically, just more clear guidance so that in those instances where a survey can’t be performed, the heat treater at least has a degree of confidence that what it is they are going to be doing is going to be up to snuff, that it’s going to pass muster with their auditor.

DG:  I want to go back and go all through those four sections again and ask you the same basic question for each of those four sections.  When your company, or companies like yours, walk into a prep for an audit situation, what are the things that you’re seeing, practically, on the thermocouple end of things, the calibration end of things, the SAT and the TUS?  Let’s start with the thermocouple: When you walk in, what do you most often see and what do you tell people?

JR:  When I first walk into a facility, one of the first things I’m looking for is how the flow down of information is conducted.  How are they approaching the flow down of information?  Because, in order for me to assess whether or not you’re compliant with the document, I need certain bits of information.  And it’s not just me, anyone would need it.  As I go through a plant, and I’m looking for information on thermocouples, I want to know when the thermocouple was installed, I want to know if it was calibrated, what’s the number of the calibration certificate that it ties back into, what’s the location of that thermocouple and where it’s installed, what’s its purpose?  I can tell you that often it happens where I ask, “What’s this thermocouple?”  “Well, that’s my control thermocouple.”  “Are you sure?”  “Yes, I’m sure.”  Then, when you go to remove it, it turns out to be the high limit.  There are these little things where people ask, “Well, what’s it matter if one is a control or one is the high limit?”  Especially if they’re both in the same well and it’s a dual element sort of thermocouple.  It’s important for a multitude of reasons.  If you don’t know that basic sort of information, or you don’t find that information to be important, what other information won’t you find important?  It becomes like a mentality aspect of things.  I like seeing that sort of information available and ready, that you don’t have to go digging for it.  So, that’s the first thing I look for any time I walk in a plant.  More often than not, I find that aspect of things can be lacking, from a documentation standpoint, from an availability of documentation standpoint, or “Can I see the calibration certificate for this specific thermocouple?” and I get, “Well, here are all of my certificates.”  “Well, which one applies to that thermocouple?”

Justin Rydzewski explains the importance in knowing your thermocouple system inside and out from an auditing perspective. (Photo source: Pelican Wire)

What I also try to convey is that the more difficult that you make this for me – for someone who’s coming out to audit you or to perform this assessment to check on you – the more difficult you make it, the harder they’re going to start scratching.  You want this to be easy.  You want to convey confidence.  You want to convey the repeatability of things.  I can’t stress enough strong documentation and great documentation systems for easy recall, like availability of information at the actual thermocouple itself is such a nice convenience, and when someone sees that, it conveys confidence.  Outside of just a basic compliance issue, it’s that support system for thermocouples, because everything starts there.  All of it starts there.  Even from the basic things like knowing what it is you have there, from a thermocouple aspect.

With one of my closer customers in our first interaction together, he called and asked for a 30” long thermocouple and to just make sure that it’s type K.  “Well, I need just a little bit more information than that.  What else can you tell me about it?”  “That’s all I have.  Just get me one.”  “Well, I have a binder on my desk that’s an inch and a half thick and every thermocouple in there just about matches your description.  I need more.  Should I just flip a page and pick one?”  There are a lot of variants that can exist there and when you introduce variants, you have an opportunity to introduce variance in your performance of that system.

So, consistency, repeatability, and assuring those things on a perpetual basis is critical.  Things like insertion depth, length, diameter, type, calibration, where you have it calibrated.  All of those things should be documented and standardized and that documentation should be readily available to anyone who needs it so that you can ensure that you’re replacing like with like, what was there before, if it was compliant, and what you replace it with is also compliant.  The performance that you had on that system on day 1 versus day 180, you want to be able to assess that variance in performance, not based on the variables that have changed, like are they new thermocouples, are they in new locations; you want to assess it in terms of those other exterior factors.  That’s why you call out thermocouples instrumentation and the like within pyrometry and CQI-9.  Those things, to me, are really important, and they’re the first things that give that indicator of what things are going to be like as I go through a job site initially.

DG:  Anything else under thermocouples, or should we move on to calibration?

JR:  That pretty much covers it.  From a thermocouple standpoint, just ensuring that you have solid documentation surrounding those things.  It can be an overlooked piece of equipment, but they are so incredibly critical.

[blockquote author=”Justin Rydzewski ” style=”1″]From a thermocouple standpoint, just ensuring that you have solid documentation surrounding those things.  It can be an overlooked piece of equipment, but they are so incredibly critical.[/blockquote]

DG:  Right.  And be able to easily access it and instill confidence in the auditor so that they know you know what’s going on.

Let’s move on to calibration then.  When you walk into some place and you’re going to check their calibration processes and whatnot, what do you see usually?

JR:  Especially when a new edition comes out, or a newer revision of a pyrometry specification, the first thing that I typically go there with is – again, similar to the thermocouple side of things – I want to look at documentation.  If I have a new Rev, the first thing I’m going to ask is what are the new requirements for reporting? I want to know what was on the report yesterday and what needs to be different tomorrow, so that I can make sure from a documentation standpoint, I’m going to be covered, because that’s what I’m going to put in front of someone.  That’s the thing they’re going to evaluate initially.  And so, I want to make sure that this first impression is solid and that it checks every box that it’s supposed to.  I’ll review all of the reporting requirements initially, just to make sure my reporting is going to pass muster with an audit.  And I will scrutinize that thing up and down to the Nth degree, just to make sure that I’ve got it to a point where I’m comfortable with it.  That’s where I typically start.

Again, similar to thermocouples, I want to make sure that I have a solid support system for my facility in terms of instrumentation.  I know what instruments I have there, I know what’s required of all of them, I know where I want them calibrated, I know how I want them calibrated, I know where they operate, all of those sorts of things.  I find often, especially on new job sites, an instrument and they’ll have offset in there.  “Well, what’s this offset for?”  “I don’t know.”  “OK.  What was it the last time you had calibrations?  Has this changed?  Is this a value that changes?”  “I couldn’t tell you.”  And sometimes, the level of offset there, it’s possible for it to be at a level that is not compliant with the document without that documentation to support it, without something calling out what it’s there for, what the intended purpose is of it.  Anytime you have that “I don’t know” answer, or “It’s in someone else’s hands,” let’s say the provider of pyrometry services that are out there perform the calibration, they’re not aware that they have to go through some sort of approval process to change offset, pay the instruments out, I’m going to pump in some offset, and there you go.  In the worlds of CQI-9, and especially within AMS, you can’t do that.

There is a right way to go about doing things, and a ladder of things to climb before you can just go ahead and jump.  Having a solid foundation of understanding of your instruments, documenting the details of those instruments, and having that readily available.  If you have that, the likelihood that you’re going to be compliant and have a favorable audit in terms of your instrumentation, is going to be so much higher than if you don’t.  So, strong support system.  Strong documentation as well.

DG:  Let’s move on to the system accuracy tests.

JR:  The system accuracy test is often something that we encourage our customers to take on themselves because it’s not an overly complicated process, by and large.  From a third edition to fourth edition, again my first stop is at reporting.  I want to make sure whatever it is the data I need to collect is going to be there at the end of the day and is going to be presented in a manner where anyone can understand at glance.  I don’t have to have a training session on how to understand my reporting.  I want it to be very clear, very forthright in terms of information that it’s clear.  And then understanding the differences between the acceptable methods.

Probe method A in CQI-9 is most like the comparison method within AMS2750 where you have a test instrument system alongside your process instrument system and doing a comparative in terms of the calculated difference there.  Understanding the math and the order of operations out there is essential.  It is so easy to mess that up or forget how to do it properly.  One of the benefits of the illustration within the fourth edition is that we made a very concerted effort to make sure that the means in which that math is performed is clear, and how it’s reported is clear, so that there’s no too much confusion.  The goal here isn’t, “Aha, gotcha! You don’t know how to do an SAT.”  The goal is that you do an SAT and that you do it in a manner that produces you with a level of confidence that you’re okay and that everything is going to have the best likelihood or repeatability and coming out as expected.

Understanding the math is also critical.  The only real thing of note in the third edition that wasn’t explicitly called out, that in the fourth edition is explicitly called out, is that the SATs only apply to the control and monitoring and recording thermocouples; it does not apply to thermocouples that are dedicated to the purpose of over-temp protection.  That can be a nice break for most users who were thinking that they had to do it in the previous edition.

For the most part I see that the act of actually performing it— again, that flow down of information becomes critical.  If I know how long my thermocouple is, the process thermocouple is at that process thermocouple.  Say, for instance, it’s identified on a tag at the thermocouple and it says it’s 40”.  If I go insert my test thermocouple and it goes in 20” and I feel like I’ve bottomed out, the only indicator that I would have that I’ve not bottomed out my thermocouple and I’ve lined my measuring junctions, would be that measurement at the thermocouple, would be an indication of how long it’s supposed to be or an awareness of how long it’s supposed to be.  If I don’t have that, and I drop my test thermocouple in and it feels like it bottomed out.  Cool, they’re lined up.  They could be dramatically different.  In that case, I would go ahead and guess that you would notice that instantly as you’re failing that SAT, but an inch or two inches can make a significant difference in misalignment of junctions.  Having an awareness of insertion depth of your process thermocouple, length of process thermocouple, and what’s required for insertion depth on your test thermocouple is critical to perform in that test and it’s something I see lacking often when I’m out in the field assessing how my customers are performing the tests in-house.

DG:  And finally, let’s talk about what you’re seeing when you walk into a shop for temperature uniformity surveys.

JR:  Uniformity surveys, again, the first thing I’m doing is assessing the reporting requirements to make sure everything is up to snuff, because that’s your first impression you’re going to convey to everyone.  The requirements within the fourth edition are of note, that would require something to be done differently, for the most part, you’re going to be find them to be very similar.  The thing that I’m looking for most is the repeatability of that test.  How like is one test to the next one?  What is your means of collecting data and what is your response plan when that data is unfavorable?  Having that predetermined, so that you’re not doing in on the fly, can be incredibly helpful and it adds to expedite that process of getting good tests out of there.

[blockquote author=”Justin Rydzewski” style=”1″]How like is one test to the next one?  What is your means of collecting data and what is your response plan when that data is unfavorable?  Having that predetermined, so that you’re not doing in on the fly, can be incredibly helpful.[/blockquote]

One of things I’ve always recommended my customers doing is that before you perform that survey, have some sort of pre-survey list that you go through of tasks that you want to verify before that test is run, just to make sure that you’re collecting all the data that you need to collect before you perform it.  In an instance where that test data is unfavorable, you can go back and take a look at it and compare it against previous tests performed and not have to be concerned about whether or not this test was performed differently than the one prior.

Consistency is the key.  And again, strong documentation systems.  Understanding what the operating temperature ranges are for each system, where your sensors are placed, how they’re traversed, where they’re installed at if it’s a continuous furnace.  There are so many variables to performing that test, having a handle on them is incredibly important.  Otherwise, the test data performed on day X compared to on day Y is a meaningless comparison, and you want that value to be there, to be able to compare them, so that you can see where performance has varied or where it’s different, and have something pointing at where you need to go investigate.

DG:  Justin Rydzewski of Controls Service up in Livonia, MI, thank you very much.  I think this is going to be our first.  We’re going to have either three or four of these podcasts.  I think next time, we’ll either deal with heat treat assessments or we’ll talk about the process tables some.

 

 To contact Justin Rydzewski, go to www.controlsservice.com.

 

 

 

 

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 #42: Justin Rydzewski on CQI-9 Rev.4 (Part 1 of 4) – Pyrometry Read More »

Vacuum Gauges in Heat Treatment

Source: Vac Aero International Inc.

Which vacuum gauges are most often found on a heat treater's vacuum furnaces? What are the conditions for selecting a vacuum gauge? And how do you adapt a vacuum gauge to service floor requirements?

Today's feature article is a "best of the web," that gives you a roadmap when selecting the best vacuum gauge for your heat treating purposes. In this piece, you will also learn how gauges perform differently depending on their type. Read to learn more and see these differences.

An excerpt: "There are several types of vacuum gauges, each engineered for a specific function over a specific range of vacuum pressure. Common types include:

  • Mechanical gauges
  • Absolute pressure gauges
  • Thermocouples or Pirani gauges..."

Read more: "Vacuum Gauges"

(photo source: Collage with images from Vac Aero featured article, Peter's Heat Treat, and Linde website)

Vacuum Gauges in Heat Treatment Read More »

Considerations for Base Metal Thermocouple Wire Diameters

OC

Ed Valykeo
Thermocouple Specialist
Pelican Wire

John Niggle
Business Development Manager
Pelican Wire

“What size wire should I use in my thermocouple assembly?” While this is a pretty direct question, the answer is more complex. In this fascinating Technical Tuesday article, learn how both the type of thermal processing as well as the stability and performance of the thermocouple contribute to selecting the right size wire. Read more in this Heat Treat Today Original Content article by John NiggleBusiness Development Manager, and Ed ValykeoThermocouple Specialist, at Pelican Wire, Naples, FL.


This article will discuss influences that should be considered when choosing the wire diameter in a base metal thermocouple circuit. It is important to keep in mind each thermal process will dictate the type and size of thermocouple. It is also important to understand there are several factors which influence the life expectancy of a thermocouple circuit.

We often get asked, “What size wire should I use in my thermocouple assembly?” The quick and simple answer is, “Use the largest practical size.” While this may be true, the individual thermal process should dictate the proper wire size.

The selection of a specific wire size for a given thermal process is related to the question of “expendability.” A thermocouple not exposed to harsh environments or excessive temperatures should have a long and useful life. Thermocouples exposed to corrosive atmospheres and elevated temperatures should be considered expendable. In general, if a thermocouple wire is deemed expendable then the wire should be no larger than necessary. If the thermocouple wire is exposed to excessive temperatures, or harsh environments, a larger diameter wire may be required.

There are several factors that affect the stability of thermocouple alloys:

  • Evaporation – Especially at higher temperatures certain elements evaporate more readily than others.
  • Diffusion – Alloying elements from one leg to the other.
  • Oxidation – In most cases oxidation in clean air is beneficial for thermocouple performance. As oxide film thickens with time and temperature, the overall composition of the thermoelement changes.
  • Contamination – Changes in wire composition can affect thermocouple drift. Contamination from sulfur, iron, and furnace refractories can be sources of contamination.

Each of the above factors can induce EMF (electromotive force) drift, caused by a change in alloy composition. EMF drift is the potential for the thermocouple to lose its accuracy over time. Typically, this change takes place on the surface of the wires. Since smaller diameter wire has increasing ratios of surface to volume exposure, they are more rapidly affected by surface effects. The rate at which this phenomenon progresses accelerates as the temperature increases.

(Source: Pelican Wire)

It is important to keep in mind each base metal thermocouple type has its advantages and disadvantages. The environment and temperature range contribute to the overall thermocouple performance. Using a thermocouple in the wrong environment or incorrect temperature range could increase the opportunity for adverse surface effects, regardless of the wire size.

There are other considerations when choosing a wire size in a thermocouple circuit:

  • Stem Loss – Stem conduction is heat conduction along the length of a wire. When the heat source end and the cold junction end of the wire are at different temperatures, stem conduction occurs. This temperature discrepancy produces a reading different from the actual heat source temperature. Using a larger gauge conductor could produce an error due to stem loss conduction.
  • Resistance – The industry standard is to keep total loop resistance of your circuit under 100 ohms. Loop resistance is determined by multiplying the length in feet by the resistance per double feet. Double feet is the resistance per foot of each thermocouple element. Decreasing the wire size results in the increase of resistivity of each thermoelement, which affects total circuit resistance.
  • Flexibility – Some thermocouple assemblies are run through conduit or inserted in protection tubes. As you increase the wire diameter you lose some flexibility.

Useful thermocouple life is difficult to predict, even when most of the details of an application are known.  The best test for any application is to install, use, and evaluate the performance of a design that is thought likely to succeed.  Thermocouple type descriptions are good source for determining recommendations, and prohibitions for thermocouple use.

Keeping in mind these recommendations, as well as having a better understanding on what affects thermocouple performance, should help you select the proper wire diameter for your specific application.

 

About the Authors: John Niggle has been the business development manager at Pelican Wire since 2013 and has prior sales experience in process instrumentation. Ed Valykeo, a 40-year veteran in the wire industry, many with Hoskins, is a thermocouple specialist who has worked with Pelican for 10 years.

 

Considerations for Base Metal Thermocouple Wire Diameters Read More »

Vacuum Furnace to be Shipped to Heat Treater in South Carolina

HTD Size-PR LogoA heat treater in Greenville, South Carolina, Solar Atmospheres, will receive a vacuum furnace from its sister company in Sellersville, Pennsylvania. The 12 foot horizontal, car bottom-loading vacuum furnace is capable of processing up to 50,000 lbs of material.

The sister company providing the furnace, Solar Manufacturing, has it painted and ready to go. Check out the video that they posted on Twitter to see preparations for the vacuum furnace’s shipment.

 

 

Images and video sourced from Solar Manufacturing Twitter Account.

Vacuum Furnace to be Shipped to Heat Treater in South Carolina Read More »

This Week in Heat Treat Social Media


Welcome to Heat Treat Today’s This Week in Heat Treat Social MediaAs you know, there is so much content available on the web that it’s next to impossible to sift through all of the articles and posts that flood our inboxes and notifications on a daily basis. So, Heat Treat Today is here to bring you the latest in compelling, inspiring, and entertaining heat treat news from the different social media venues that you’ve just got to see and read!

Check out today’s line-up of Halloween Costumes, Thanksgiving and your heat treat furnace, a video on the details of stress relieving, and more!

If you have content that everyone has to see, please send the link to editor@heattreattoday.com.


1. Get Ready for Thanksgiving

Typically, we like to start these posts with an intriguing or exciting metallurgical post from the industry. But with Thanksgiving right around the corner, we know you would like to contribute with the skills that you use every. Single. Day. Still, be careful… Enjoy this video from Ipsen USA.

 


2. Technically Know How

We see you! And we think it’s awesome! Here are several videos and images of heat treat techniques and shared knowledge. Feel free to @HeatTreatToday when you post these videos so that we can see them!

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In-House Heat Treating Looking Pink

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Standing Ovation for Your Traditional Flames

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A Series in a Heat Treater’s “Expedition”

Check out their video here!

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Carbon Content and Heat Treatment

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3. Historical Heat Treat

Talk about throwbacks, these videos and images from the “social-inter-webs” share some interesting factoids and knowledge from the past. Check out heat treating video from the 1970s, heat treatment in Japanese culture, and 6,500 year-old copper workshop.

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1973 – Properties and Grain Structure Video

Check out this video, “Properties and Grain Structure: BBC 1973 Engineering Craft Studies,” and let us know if you agree with one of the commenters: “Please never remove this video from youtube. This video is a majestic gem in an ocean of gray pebbles.” If you share it on your LinkedIn page, @HeatTreatToday so we know what you think!

.

The Art of Mokume Gane

Full disclosure: this is NOT at the high temps that you are used to. But still…get a load of Mokume Gane: “it is an ancient Japanese technique used to make jewelry, blade guards and many other things. It is basically Damascus or pattern welded steel, but made from non ferrous metals such as gold, silver, copper, brass, platinum, bronze etc.” (Source: HomemadeTools.Net)

.

Secrets of the Desert 

Tel Aviv University and Israel Antiquities Authority believe copper-producing technology was closely guarded secret in the Neveh Noy neighborhood of Beer Sheva, capital of the Negev Desert. This emergency archeological excavation came about to safeguard threatened antiquities. Now, “The new study also shows that the site may have made the first use in the world of a revolutionary apparatus: the furnace.” (Source: Tel Aviv University: American Friends)

Work on the dig in Beer Sheva. Photograph credit: Anat Rasiuk, Israel Antiquities Authority.
(Source: “6,500-year-old copper workshop uncovered in the Negev Desert’s Beer Sheva,” Tel Aviv University: American Friends)

 


4. Reading and Podcast Corner

Free Classes Anyone? Thank you, C3 Data

.

Heat Treat Radio: Rethinking Heat Treating (Part 3 of 4) — The Fracking Pump Valve Seat

The latest episode is with integrated heat treating professional Joe Powell and Doug Glenn as they talk about the fascinating heat treatment of a fracking pump valve seat.

 

 

.

Heat Treat Radio: Andrew Bassett on AMS2750F (Part 2 of 3) — SATs

Get ready for the next episode in this series being released in early December with this podcast! Doug Glenn continues his conversation with AMS2750F expert Andrew Bassett. This time, the pair discusses Revision F changes to System Accuracy Tests (SATs).

 

 

.

Heat Treat Radio: Rethinking Heat Treating (Part 2 of 4) — 18″ Bevel Gear

Savings of over $700.00 in hard grinding costs PER GEAR on an 18-inch bevel gear? Listen to  Joe Powell of Integrated Heat Treating Solutions tell how they did it. [Go to Heat Treat Radio with Joe].

[blockquote author=”Joe Powell” style=”1″]“It’s a win-win-win.  The customer is happy, we’re happy and it works.  This demonstrates that you can indeed quench very, very intensively.  We’re talking about 400-600 degrees Centigrade/second of quenching.”[/blockquote]

 

 


5. Scary Manufacturing…Maybe

While this is not exactly metal, could any of you make this? Or maybe the more important question is, would any of you make this?

 

 

 

Have a great weekend!

 

This Week in Heat Treat Social Media Read More »

Predictive Maintenance and Saving Money

Source: TAV-The Vacuum Furnace Blog

We hear the term “preventative maintenance” often used in the industry. Setting up procedures in advance to avoid unplanned downtime and other avoidable costs is certainly a hot topic. But this Heat Treat Today Best of the Web feature highlights a maintenance strategy that has become increasingly popular in creating better industrial efficiency: predictive maintenance. Read today’s feature article to learn about what predictive maintenance is, how it is implemented in a vacuum furnace system, and how this strategy saves you money.

An excerpt: “Predictive maintenance (PdM) evaluates the condition of equipment by performing periodic or on-line asset condition monitoring. Most PdM is performed while vacuum furnace is operating normally to minimize disruption of everyday operations. This maintenance strategy leverages the principles of statistical process control.”

Read more: “Save Time and Money with Vacuum Furnace Maintenance [2/2]

 

 

 

(Source: TAV Vacuum Furnace Blog)

 

 

 

 

 

Predictive Maintenance and Saving Money Read More »

What to Expect When Remodeling a Kiln Control System

OC

jose sanchez
José P. Sanchez
Ceramics Business Unit
Nutec Bickley

Heat Treat Today brings you an article from Jose Pablo Sanchez at Nutec Bickley on what to expect when giving a kiln or furnace an upgrade.

How much time does it take to replace or upgrade your heat treat kiln or furnace? What are the best questions to ask when preparing to upgrade a control system on your furnace or kiln? What about the availability of replacement parts? How can you be sure that your upgrade will deliver the overall best experience once it is said and done? Read on to consider the case study of one client’s experience when remodeling a kiln control system.


About the Client

One of the most renowned sanitaryware manufacturers in the world wanted to update the control system on one of their older tunnel kilns. The 30–40 year-old equipment had an outdated control system which ended up leading to a lengthy installation process

Since the kiln’s control system was obsolete, the client could not access the controller’s program, making any required modification impossible. Additionally, the kiln did not have a HMI screen, only a board with LEDs. The SCADA system was DOS based, very unfriendly and difficult to operate. This made sourcing any necessary replacement parts extremely difficult in the event of failure.

The Challenge

The client had been forced to search for spare parts on eBay and other online sites as they had been discontinued by the part manufacturer. But even with these searches, it had become impossible to find replacement parts.

Tunnel kilns handle a substantial throughput and are generally only idle when they are closed down for a week at the end of the year for maintenance.

So, the challenge that the client and our engineers faced was to uninstall the current system, install the new one, and get everything ready, all before the plant resumed operations.

To this end, we worked 24 hours a day continuously, conducting tests during the final week of the year with our team of programmers and commissioning engineers.

Equipment Supplied and Technology Employed

Installation of new SCADA and PLC equipment

1.- Allen-Bradley ControlLogix® PLC

  • A high-performing PLC
  • Improved processing power

2.- New SCADA from FactoryTalk®

  • Replaced the obsolete system the client was using
  • More programming versatility on screens

The Solution

In updating the system, we proposed replacing the old controller with an Allen-Bradley ControlLogix® PLC and installed a new FactoryTalk® SCADA for screen control. These updates took time both prior to installation and during the installation itself.

First, the existing program could not be accessed, so multiple visits to the client’s factory were necessary to study the kiln’s operation philosophy. Second, since the control panel wiring had no labels, we took time to label every component and ensure that the wirings corresponded to the correct signals. Additionally, we brought in a commissioning engineer who checked the functionality of the instrumentation before any intervention.

When it came to installation, a systematic process was essential. Every time a component was connected it was tested immediately. We had up to 5 automation engineers at a time for quick troubleshooting.

Results Obtained

A key part of the process was the client’s cooperation. They always had someone there with us to help us with anything we needed. With our engineers, the facility was able to obtain:

  1. The latest hardware and software systems
  2. Technical support and easy refurbishment capabilities
  3. The ability to add more cards in the future to improve monitoring
  4. Increased flexibility to customize systems
  5. Better monitoring and data analysis of kiln performance results
  6. Remote access from the Nutec Bickley plant for testing and troubleshooting purposes

 

This proves that the client’s cooperation is always key for a successful project.

 

Images provided by Nutec Bickley.

About the Author: José P. Sanchez is part of the Ceramics Business Unit in Nutec Bickley, in charge of sales in LATAM for kilns and major retrofits in the ceramic industry. He has been an active participant of multiple projects involving kilns and ovens in numerous industrial sectors, mostly refractories for the steel & aluminum industry.

 

What to Expect When Remodeling a Kiln Control System Read More »

Case Study: The Low-Pressure Carburizing Process Improvement for a Ring Gear

Justin Sims
Lead Engineer
DANTE Solutions

OC“The original LPC schedule, consisting of six boost-diffuse steps, was producing large amounts of carbides during the process. With large amounts of primary carbides in the case of the heat treated gear, rolling contact fatigue performance was decreased.”

Heat Treat Today‘s Technical Tuesday feature, “Low Pressure Carburizing Process Improvement for a Ring Gear: Controlling Carbide Formation during LPC,” explores a case study, written by Justin Sims, lead engineer at DANTE Solutions, about how software modeling aids heat treaters in improving their low pressure carburizing process. Enjoy today’s Original Content.


Introduction

Low pressure carburizing (LPC) processes are becoming more widespread throughout industry due to the reduced cycle times and the control over the carbon profile through the case. Unlike gas carburizing, which utilizes a constant carbon potential to maintain the available carbon on the part surface at a specific value, LPC utilizes a series of boost and diffuse steps. A boost step involves the temporary addition of a carbon carrying gas to the furnace chamber, usually acetylene, to increase the surface carbon to the saturation limit of austenite. If not properly controlled, the carburized case may have an excessive amount of carbon, which damages the final microstructure. After a requisite amount of boost time, generally half minute to several minutes, the carbon carrying gas is evacuated from the chamber. The concentrated carbon in the shallow surface layer from the boost step is then allowed to diffuse into the part, reducing the surface carbon. These two steps are then repeated until the required case depth and carbon profile are achieved.

For steel alloys that do not contain a significant amount of strong carbide forming elements, the LPC process is relatively easy to control. However, with the advent of high strength steels for the aerospace industry, most of which contain substantial amounts of strong carbide forming elements, such as chromium, molybdenum, and vanadium, the LPC process can be challenging. The primary carbides formed during the LPC process, if not properly dissolved, can damage fatigue performance.

While Fick’s Second Law describes the diffusion of carbon through a low alloy steel with reasonable accuracy, the same is not true of medium and high alloy steels. This is due to the presence of carbides forming and dissolving during the LPC process. During a boost step, the carbides formed increase the total amount of carbon into the surface. During the diffuse step, as the carbon that is in solid solution diffuses into the part, reducing the carbon in austenite, the carbides can dissolve to provide more carbon to the solid-state solution. If the carbides are not allowed to fully dissolve or shrink to a significantly small size before the next boost step begins, they will continue to grow. In order to properly predict the carbon profile of medium and high alloy steels, the carbide formation and dissolution must be considered. The heat treatment simulation software DANTE has implemented this feature.

The following is a case study for redesigning a LPC schedule of a ring gear using DANTE. The original LPC schedule, consisting of six boost-diffuse steps, was producing large amounts of carbides during the process. With large amounts of primary carbides in the case of the heat treated gear, rolling contact fatigue performance was decreased.

Image 1

Geometry and Model

Part: Ring Gear

  • Material: Ferrium C64
  • Outer Diameter: 5.5 inches
  • Inner Diameter: 4.5 inches
  • Height: 0.060 inches
  • Number of Teeth: 40

Model: Single Tooth

  • Cyclic Symmetry: Carbon boundary conditions
    act uniformly on all teeth
  • Number of Elements: 233,850 linear hexagonal
  • Number of Nodes: 245,055
  • Higher mesh density near surface to capture
    steep carbon gradients

 

LPC Experiments vs. Prediction

Image 2

  • Experimental data versus DANTE prediction for 3 LPC runs
  • LPC experiments conducted using a cylinder with a 4-inch OD and a 4-inch height made of Ferrium C64
  • 3 different boost-diffuse schedules executed
    • 6 boost-diffuse steps
    • All 3 schedules used the same first 11 steps
    • Final diffuse time increased for each run, with Run 1 having the shortest and Run 3 having the longest
  • LECO used to measure the carbon profile of the test coupons
  • DANTE model parameters for carbon diffusivity, carbide formation, and carbide dissolution fit from experimental data
    • Simulation matches experimental data reasonably well

 

Baseline (Original Carburizing Process)  Model Results

  • The case depth originally was designed for 0.75 mm (0.030 inch) on the flank of the tooth, with a carbon value of 0.3% resulting in a hardness value of 50 HRC for Ferrium C64 when tempered at 495°C (925°F).
  • The contour plot shows all carbon, the carbon in the austenite matrix and the carbon in primary carbide form, at the end of the process for the baseline model:
    • Areas above 0.011 carbon contain primary carbides
    • Tip contains a high amount of primary carbides
  • Line plot shows the predicted carbon in the austenite matrix (Carbon) and the carbon in primary carbide form (Carbon in Carbides) at the surface of the flank for the baseline model over the total time of the process.
    • Carbides present at a depth of 0.25 mm (0.010 inch)
    • Case depth ~0.35 mm deeper than required

Image 3

Image 4

 

 

 

 

 

 

 

  • Contour plot shows all carbon, the carbon in the austenite matrix and the carbon in primary carbide form, at the end of the 3rd boost and diffuse steps
  • Line plot shows the predicted carbon in the austenite matrix (Carbon) and the carbon in primary carbide form (Carbon in Carbides) at the surface of the flank for the baseline model over the total time of the process
    • Carbides formed during the first boost step continue to grow as the process progresses, indicated by the increasing carbon in carbide
    • Final diffuse not long enough to fully dissolve carbides

Image 5

Image 6

Image 7

Redesigned Carburizing Process Model Results

Image 8

  • To ensure the primary carbides dissolve completely before hardening, a new schedule was developed with the aim of reducing the carbon in primary carbide form:
    1. 3 boost-diffuse steps were removed, and the diffuse times increased substantially.
    2. An increase in diffuse time increased the schedule by approximately one-half hour, which is acceptable given the positive results.
  • The contour plot shows all carbon, the carbon in the austenite matrix, and the carbon in primary carbide form at the end of the process for the redesigned process model.
  • Line plot shows the carbon in the austenite matrix (Carbon) and the carbon in primary carbide form (Carbon in Carbide) from the surface of the flank towards the core for the redesigned model at the end of the process
  • Small carbides (negligible) at a depth of 0.1 mm (0.004 inch)

Image 9

  • Easily removed with finish grinding operation
  • Contour plot shows all carbon, the carbon in the austenite matrix and the carbon in primary carbide form, at the end of the 2nd boost and diffuse steps for the redesigned process
    • Primary carbides are nearly fully dissolved, even in the tip (carbon is higher, but it is not in carbide form), at the end of the diffuse step

Image 10

Image 11

 

 

 

 

 

 

 

  • Line plot shows the predicted carbon in the austenite matrix (Carbon) and the carbon in primary carbide form (Carbon in Carbides) at the surface of the flank for the redesigned model over the total time of the process
    • Carbides are nearly fully dissolved after each diffuse step

 

Image 12

Summary

  1. The heat treatment simulation software DANTE model parameters for carbon diffusivity, carbide formation, and carbide dissociation fit from experimental data.
    • Any steel alloy and LPC equipment can be fit to the DANTE carburizing model.
  2. The software successfully predicted the results of a low-pressure carburizing process that was resulting in poor part performance during rolling contact fatigue:
    • Model showed that large primary carbides exist at a depth of 0.25 mm (0.010 inch).
    • Model showed that the carbides do not have time to dissolve during the boost steps.
  3. The software was used to successfully redesign the boost-diffuse schedule to improve rolling contact fatigue performance:
    • Model showed that small primary carbides (negligible) exist at a depth of 0.1 mm (0.004 inch).
    • Model showed that the carbides nearly fully dissolve during the diffuse steps.
    • Small carbides were removed during the finish grinding operation.
    • Rolling contact fatigue performance improved due to the absence of primary carbides near the surface.
  4. Additionally, the software is not limited to Ferrium C64 with respect to primary carbide formation during LPC:
    • Continually updating the material database with carbide behavior for different alloys
    • Continually validating the model with experiments

 

About the Author: Justin Sims is a lead engineer at DANTE Solutions. For more information, contact Justin at DANTE Solutions

All images were provided by DANTE Solutions.

 

Case Study: The Low-Pressure Carburizing Process Improvement for a Ring Gear Read More »

Heat Treatment of a Large H13 Liner is a Success

HTD Size-PR Logo

Bob Hill
President
Solar Atmospheres of Western PA

Lake Park Tool and Machine, located in Youngstown Ohio, produced a massive H13 liner which Solar Atmospheres of Western PA (SAWPA)recently heat treated. The liner measured over 100” OAL and weighed a total of 16,000 pounds. The liner was turned on Lake Park’s new large capacity lathe with 34” max diameter and 200” max length.

This H13 liner was heat treated in, what SAWPA says is, "the fastest cooling large vacuum furnace in the industry." Solar Manufacturing, sister company to SAWPA, recently completed this 10 bar vacuum furnace several months ago. It is equipped with a hot zone measuring 48” wide x 108” OAL. Additionally, the furnace has a 600 HP blower motor for increased cooling power. The critical cooling rate, to obtain optimum properties for H13 hot worked tool steel, was achieved in the as-quenched hardness of HRC 54-55. The part was then double tempered to the customer’s specification of HRC 46 to 48.

"This large rapid cooling vacuum furnace provides us continued diversification to our vacuum heat treating repertoire and capabilities. We’re proud of this partnership with Lake Park Tool and Machine and to assist our customers in vacuum heat treating one of the largest air hardening dies that I have personally heat treated over my 40 year career,” stated Bob Hill, president of Solar Atmospheres.

 

(photo source: Solar Atmospheres)

 

 

 

 

 

 

 

Heat Treatment of a Large H13 Liner is a Success Read More »

Leading Tooling Manufacturer Purchases Furnace to Aid the Medical Industry

HTD Size-PR Logo

Top Loading Furnace
(Source: Lucifer Furnaces)

A leading tooling manufacturer recently received a top loading furnace for the production of dies. This is the second furnace that is being used by the manufacturer in order to produce dies to cut fabric in the making of N95 masks for the medical industry.

The Warrington, Pennsylvania based supplier, Lucifer Furnaces, noted that the model has a chamber size of 48” H x 18” W x 18” L and heats to 2300°F. The supplier also detailed how the furnace design provides uniform heating.

(photo source: Obi Onyeador at unsplash.com)

 

 

 

 

 

 

 

 

Leading Tooling Manufacturer Purchases Furnace to Aid the Medical Industry Read More »