4.03.2022

Firing the TDI Downdraft Kiln Conversion

The following text has been updated from the second revision of the TDI Downdraft Kiln Conversion book published November 2023. The revised edition presents more detail on firings as included following. The Firing the TDI Kiln text is oriented towards a more novice potter transitioning to gas reduction firing with just a quick overview for experienced potters. The Evening-Out-the-Temperature process at the end of the firing is for anyone that doesn't already know this method and it is the same as is done in updraft kiln firings. 

The TDI Downdraft Kiln Conversion manual is available on amazon at: https://www.amazon.com/dp/B084DH88GH

The Facebook Group - TDI Downdraft Kiln Conversion: http://www.facebook.com/groups/4124895130900261/

Firing the TDI Kiln

By most standards, a 23”x27” (7 cubic feet) converted gas kiln is pretty small with approximately 5.5 cubic feet of pottery setting area. The 28”x27” (10 cubic feet) isn’t much bigger with about 8 cubic feet of setting area. The larger gas downdraft kilns found at ceramics schools and potteries can be three to four times larger. These larger kilns typically have firing times of 10 to 14 hours and they can be relatively reliable as far as reduction and temperature hot and cool spots. A lot of what can be read or studied about gas reduction firing is often from the perspective of these larger kiln types.

Several experienced potters who work in the large kiln environment expressed reservations about being able to fire a TDI kiln in 6 to 7 hours and achieve good results. TDI firings over the past 5 years have proved those opinions incorrect, but it is important to learn and understand why and how the firing process works so as to understand important sequences and elements. The temperatures of large kilns fired in school settings are usually ramped up much more slowly and then often have 6 to 8 hours after body reduction to the end of firing. What is important is to have a sufficient amount of time for glazes to develop their characters.

The small TDI kilns can get to 900°C/1,652°F in 2 hours after the initial candling. Cone 10 can be reached in another 2 to 3 hours after body reduction, especially in the two-burner 28” kilns. However, many glazes will simply not produce the results they are capable of in such a short time. A good plan is to allow at least 4 hours from the end of body reduction to Cone 10 going down. So, after the initial candling it is possible to have a 6 to 7 hour firing and have great glaze result. But there are also glazes that might be a lot more interesting after giving them 6 or more hours after body reduction to Cone 10 down.

Things to know or learn for the firing include tracking temperature rise rates, body reduction, glaze reduction, the concept of heat-work verses temperature, and the final process of evening out the kiln towards the end of the firing.

John Britt's book, The Complete Guide to High-Fire Glazes, has a good section on Kilns, Firing, and Safety and describes well the firing process. Search the internet for “Val Cushing High Fire Process”. Cushing has a lot of good resources and a simple firing method that produces great results. Britt shows an R1 (basic reduction) firing time of 8.5 hours with about 4 hours from the end of body reduction to the Cone 10 going down. Both are a little longer than the TDI firings but they also don’t increase in temperatures as fast initially and don’t increase as fast between body reduction and around Cone 7 when things are slowed down.

The TDI Kiln can be fired in both oxidation and reduction. For an oxidation firing, simply leave the flue exit dampened to about 8 inches. One downfall of straight oxidation firing is that, without a dampening process at the end (dampening causes reduction), the kiln temperatures top to bottom are going to be a cone or two different. Glazes will simply have to be placed accordingly. Though not always, a 28”x27” kiln will tend to fire more evenly simply as a result of the lower height to width ratio as compared to the 23”x27” kiln.

For reduction firing, the flue is dampened to control the draft and create the reduction atmosphere. The MR-750 burner has an adjustable plate that I set to an opening of 1/2 inch and do not change. In some kilns, the burner plates are closed down to restrict the primary air causing incomplete fuel combustion and the reduction atmosphere. Closing the burner plate is not necessary with the TDI Kiln as flue dampening provides more precise and repeatable control.

Basics Process

First, I’d like to present the basic process for more experienced gas-firing potters. Following is a more extensive discussion for those not as familiar.

On a following page are basic Cone 10 firing schedules for the 23” and 28” conversions. Your kiln may end up with slightly different numbers, but these should provide a good starting point. The following numbers were gleaned after 3 or 4 initial firings to get my numbers figured out on my newest 23” single-burner conversion and have proved pretty consistent in subsequent firings.

From the main firing start I plan on two hours to 900C/1652F, the beginning of body reduction. After candling, which may be from 15 to 30 minutes while I set up everything, I simply set the pressure to 1.3 PSI with the bricks 8” to 9” apart. My last firing of a 3/4 loaded kiln took two hours two minutes at this pressure setting. At first, the climb was around 800C/1440F per hour, then 430C/774F after 30 minutes, slowing to 252C/454F at 1 hour, and 96C173F at 1.5 hours. At 900C/1652F, I dampened down to 2 3/8” and set the pressure at 1.8 PSI. This gives me a miniscule climb and if it gets to 930C/1706F, I dampen another 1/16” or so to fully stall the kiln. After 45 minutes of body reduction, I open the dampener block up to 3.25” and set the PSI to 2.0 for the climb to Cone 7 or about 1230C/2245F.  

I plan for a 6.5 hour firing. With the two hours and 45 minutes through body reduction and a one hour time period from Cone 7 to Cone 10 trying to maintain around 60C/108F per hour climb, that leaves around 2.75 hours for the climb from around 930C/1706F to 1230C/2245F. This equates to an average climb of about 109C/196F per hour.

My target points (or when I change something) have become 1050C/1922F, 1150C/2102F, and 1230C/2245F. After 930C/1706F, the initial climb will be around 180C/324F per hour then degrade to around 80C/144F per hour close to 1050C/1922F, where I bump the PSI up to 2.1 and open the dampener to 3.5”. At 1150C/2102F I go to 2.2 PSI and 3.75” on the dampener. After about the 2.75 hours from 930C/1706F, the climb has slowed to about 60C/108F per hour. I open the dampener to 4” and log the temperature every 10 minutes or so and calculate the climb per hour. Usually, every 20 minutes I open the dampener 1/8” and it ends up at 4.5” after about an hour.

I then do an end-of-firing-evening-out process, which takes around 5 to 10 minutes. I start when Cone 10 is bending near the 2 o’clock position and finish when the Cone 10 is down. Before I added the deflector block, the evening out process was much longer and has significantly been reduced with minimal top to bottom temperature differences. I still like to do the evening out process just in case kiln packing has caused a void or stagnant spot, or some other cooler area.

That’s basically the firing. It is pretty simple once the PSI and dampening numbers have been figured out and firings have become very consistent and repeatable. It is different from firing the larger production gas kilns and I think this is due in large part to the thinner walls of the conversions, as compared to the larger kilns, and the resultant heat losses as the temperature increases.

Firing Elements

Cones

Because the kiln can be heated to 900C/1652F in about 2 hours, many have switched to using self-supporting cones rather than cone packs. I personally had several cone packs explode even after long drying times and low humidity conditions. I also use cone holders while using up the regular cones I already have. Self-supporting cones are also easy to place around the kiln as witness cones. I haven’t seen a difference in using regular cones verses self-supporting cones – in the photo below are self-supporting Cone 9, 10, and 11. 


Temperature, a Pyrometer, and Cone Placement

The placement of the pyrometer probe is usually in the middle section of the kiln and closer to the flue wall to keep away from where the burner gases are rising – it should not be near the flame for obvious reasons. Note that when packing ware it is very important to not have items to close to or blocking the probe otherwise the reading may not be accurate. The pyrometer reading can be used for most of the firing and is accurate enough for the body reduction phase and for calculating degrees per hour. For the end of the firing, I think the cones should be relied upon.

Initial Ware & Glazes

For the initial firings in a new TDI conversion, I suggest making a bunch of quick boring pots mostly around 6” to 8” tall, which will provide about 3 levels of ware. I try to have the kiln around 3/4ths filled. The kiln heats up faster for lighter loads and as a result, less propane pressure is required to get the same temperature per hour increases than in a heavily loaded kiln. So, 3/4 full is a good mid-point in establishing base propane pressure/flue-dampening numbers.  

The photo following is an initial test load on my 2021 TDI conversion. Mass-wise it is almost 3/4 full. I included some poor pots already fired just to provide some additional mass. 


I use only a couple of glazes in the test firings on Laguna 900, a dark iron-rich clay that shows well the effects of reduction. They are known glazes that provide good feedback on both reduction and temperature. Two come from Digitalfire.com, the G2571A - Cone 10 Silky Dolomite Matte Base Glaze and the GR10-E Ravenscrag/Alberta Slips Celadon Green. The Dolomite Matt is a good indicator of temperature and will get nice and glossy at the high end of Cone 10. The Celadon Green is thicker than a traditional celadon with a deep forest green color and is a good indicator of the extent of reduction. Neither will run off the pot if it gets a bit too hot.

Stoney White or Mamo Whites show reduction by browning, especially when the coating is thin. Same for Shino glazes. For the most insightful first firings, glaze predominantly with known reduction reactive glazes with varying coating thicknesses. Making and bisquing enough bowls for around 3 consecutive firings will also help to remember firing details and gain confidence and knowledge.

Basically, what one should use are well-known simple glazes that provide a high degree of reliability. Dark clays are good as one can ascertain the level of body reduction being done.

Measuring Degree Change Per Hour, PSI, and Dampening

An important part of the initial firings is documenting what is happening. Many experienced potters have traditionally used the graph method of logging the firing. They create an X/Y axis line trace and the slope of the line tells them what they need to know about the firing. Britt uses it in his High Fire book and it provides a great representation of the firing and differences between firing types.

If you’re not a potter experienced in using graph logs, I suggest using the log similar to those presented following. It provides an easier way to interpret what is going on in each firing sequence and establish and record your base firing pressures and flue dampening sizes.

The time and temperature are the first items in the log. Obviously, temperature provides specific points in the firing. I consider the pyrometer fairly reliable for most of the firing including body reduction. For the final part, I use the pyrometer for an indication of degree per hour changes, but I 100% rely on the cones to let me know the firing has reached Cone 10. Pyrometers indicate temperature. Cones indicate “heat-work”, which is what you want to know. Research and understand “heat-work” if you’re not familiar with the concept.

Later, I will discuss some degree-per-hour guidelines for parts of the firing and also relate it to the ideal functioning of the cones. I use a calculator to figure degrees per hour. Record the difference in temperature and the number of minutes between readings. The calculation is:

Temperature Difference times 60, then that number divided by the number of minutes between readings.

So, if the kiln went from 1,234° to 1,249°, a difference of 15° in 17 minutes, then degree per hour change is:

15 times 60 = 900, then 900 divided by 17 = 53 degrees per hour

To keep track of what is going on without a lot of fuss, I typically set my mobile phone timer for 6 minutes and mark down the temperature. After 6 minutes, I mark down the new temperature and multiply the temperature difference over the 6 minutes times 10 and you get degrees per hour. Easy. For 3 minutes, multiply times 20. For 10 minutes, multiply times 6.

Without an accurate log of the firing numbers and conditions (PSI, dampening, & degree/hour change), it is difficult to establish baseline numbers that will make the firing outcomes consistent and repeatable. Firing is both science and art. The science is the knowledge and understanding of the baseline firing numbers. The art is the packing, visualization of the flame path, knowing the hot/cool/reduction areas, and the subtle tweaks during firing that produce the desired results.

Measuring propane gas pressure is easy – just get it right off of the 0-3 PSI gauge.

To measure the width of the flue dampening blocks, I leave a heavy metal ruler next to the soft-brick blocks as shown in the photo on the following page. I find this easier than holding a ruler to measure it. Recently, I forgot my ‘readers’ glasses (and was too lazy to go into the house and get them) and had the dampening blocks and extra inch and a half open from body reduction up to the end evening-out process. I simply made 1/4” or 1/2” adjustments per my schedule without actually noting the total dampening block distance. The kiln did fire faster than usual and I didn’t think about why this was happening. The result was the loss of a whole load of Shino glazed pots that showed no reduction effects. It is really important to properly measure the flue dampening. 


Judging Reduction

First, reduction is performed by dampening the flue opening restricting the draft. The round plate on the burner can be adjusted to lessen the airflow through the burner (primary air) but this method is not required and is also difficult to adjust with accurate repeatability – just leave it at 1/2” to 5/8” open. Adjustment of the flue dampener bricks is easy, measurable, and repeatable.

As previously mentioned, the firing numbers and schedule that I use and refer to herein are largely from the writings of Val Cushing and what Walford Campbell taught me and the clay and glazes I use are for Cone 10 firings. Others may use or teach different schedules and, like any gas kiln, other firing temperatures can be used for different clays and glazes.

The first reduction you will encounter is the body reduction (heavy reduction) at around 900C/1652F (~ Cone 010) with a maximum of 950C/1742F (~ Cone 08). By dampening the flue to a small opening, the kiln will stall out, meaning the temperature stops climbing, and might even begin dropping.

To test the amount of heavy reduction, make small 1/16” to 1/8” adjustments narrowing the dampener opening until you see smokey soot or see black soot accumulating on the inside of the exhaust hood. You might have to increase the gas pressure slightly to keep the kiln from falling below 900C/1652F. Soot is not good and means you dampened too much and are just wasting fuel, so open up the dampener a little and the kiln will be in heavy reduction. If then the temperature begins to climb too much and get near the maximum, lower the gas pressure very slightly to stabilize the temperature. Follow the tweaking procedures discussed later to maintain body reduction.

Since it may be too light out to see the reduction flame during body reduction, one method to verify reduction is to quickly open a dampener block 2 to 3 inches and the increase in draft flow will ignite reduction atmosphere in the flue and you’ll see a quick pop of reduction flame above the lid. Reduction verified, dampen back down to continue body reduction.

One other way of noticing reduction is that there will be an acrid smell. It is not a good indicator of how much reduction, just that reduction is present.

After the body reduction phase, there is the long climb to around cone 7, 1235C/2255F, which should then allow about a 1 hour slow 60C/108F per hour climb to cone 10. Reduction numbers during the long climb phase is usually medium to light depending on your glaze requirements. I typically use medium reduction, which works for the glazes I previously mentioned.

After the firing, judge the reduction and write the plan for the next firing. For dark clay bodies like the Laguna 900 I use, too little reduction results in the body having a light tan color. The heavier the reduction the more red/brown the clay color. Having some pots with tan colors and others with dark red/brown means that the reduction atmosphere was not evenly distributed and this can be caused by two factors. First, if dampening was not aggressive enough, the good reduction may only have been near where the flame was, with the bottom shelf typically having the least. Second, if there are spots in the kiln where the gas was not flowing due to the kiln packing or maybe a shelf being too close to the side wall creating a dead gas-flow pocket, there may be less reduction effects.

One glaze I use and recommend that is a good indicator of reduction is the Rhodes Stoney White matt. Thin areas of the glaze will turn the most brown with reduction and with thicker areas a yellowish white. From Rhode’s pdf’s available online, the Cone 10 recipe I use is: Dolomite 22.5, Custer Feldspar 48.9, Grolleg Kaolin 25.1, Whiting 3.5, and Zircopax 7.5. Specific gravity of around 140 and a 3 to 6 second dip makes for thin enough coats.

Cones can also show the effects of very strong reduction by having an uneven or blistered surface.

After about 3 or 4 firings, you should have some numbers that give repeatable results, or at least narrowing the range of possible PSI/Dampening numbers. For a recent TDI conversion, the firings went from way too little reduction, then way too much reduction, then just ok (a tad weak) reduction on third firing, which only required small tweaks with subsequent firings.

Tip: It is hard to see the reduction flame in broad daylight. Try and time the firing so the last 2 to 3 hours will be in darkness (if you don’t have a shed you can make dark). 3 hours in darkness means you will have 2 hours in ramp up to cone 7 and you will be able to see the reduction flame more clearly. It will grow in size and intensity as the kiln gets hotter. For the last hour, you will be able to maintain a nice reduction flame and have more confidence in the pressure/dampening tweaks.

Initial Firing Guide

The following sections have been written primarily for the more inexperienced gas-firing potter and it contains a lot of minutiae. Since I don’t know what people don’t know, I’ve tried to make it as comprehensive as possible without delving too far into areas that should probably be learned from books like Britt’s or Cushing’s PDF’s.

Presented is a method for less experienced potters to learn the kiln and set up a firing schedule to produce some good and repeatable results. After, there is a section on evening out the kiln temperatures at the end of the firing. If you don’t like my schedules, it’s your kiln so do your own thing. And if you’re firing to a lower cone temperature, just modify the climb to the last hour for your pottery, the procedure is the same.

The purpose of the initial test firings is to get some base numbers. I want a set of base pressures and flue dampening sizes that correspond to specific sequences in the firing process. Once one gets the base numbers, the firings can be reliably repeated and the numbers more accurately altered when necessary. The specific sequences discussed for an initial Cone 10 reduction firing are:

  • Candling
  • Main firing start
  • Climb to body reduction
  • Clay Body reduction
  • Climb to around Cone 7 ~ 1235C/2255F
  • 60C/108F degree per hour climb to Cone 10 down

The sequences will produce a very basic firing and I am not worried about top to bottom temperature differences yet – most likely the differences will be around 1 cone.

At the end of the initial test firing process is evening-out the top to bottom temperatures, which is also a phase of moderate to strong reduction. After you get your base firing numbers and feel comfortable with controlling the kiln, you can delve into the art part and play with the evening-out process at the end, which adds time to the firing and also contributes to more interesting glaze results.

It is important to understand that the propane pressures and dampening can be different from one firing to another and yet Cone 10 going down can be achieved. A lower pressure and more open flue dampening can produce an expected temperature per hour climb rate yet create a more oxidizing type firing. This may produce little reduction and not be the desired outcome. Conversely, a higher propane pressure can be used with a smaller flue dampening opening, also leading to an expected temperature climb rate yet the firing might have too much reduction with bad glaze outcomes. We’re looking to determine the happy medium.

If you read the firing text following, it might become evident that in the firing process the temperature change rate per hour varies considerably, but what is important is that there is a certain allowable time period between certain target events. What I shoot for is a 2-hour timeframe from burner full on to body reduction. From the time the burners are turned on full after candling until body reduction, the initial temperature climb rate per hour is very high and then it slows down considerably by the time it gets to clay body reduction, or about 900C/1652F.

After the end of the 45 minute clay body reduction, the propane PSI is increased and the damper is opened up. There is initially a rise of around 180C/324F per hour then it degrades to around 80C/144F per hour, at which point I increase the PSI a tenth and open up the dampener 1/4”. Again, there is an initial steep rise in degrees per hour change that then degrades to a slower rise after a while. This process gets repeated several times and one can see that, looking at temperature climb per hour, there is a sawtooth shape to the climb rates verses time. In the beginning, because it is new and both the technique and numbers have to be learned, there will be a lot of these sawtooth adjustments. I think the process can be reduced to one PSI/dampening number from the main start to clay body reduction, and three adjustments after body reduction to Cone 7, which is the beginning of the last hour of a Cone 10 firing. Even though I have my numbers and am just sitting there for most of the firing, I still monitor the temperature change rate every 10 to 15 minutes just in case the ware load is causing a too fast climb or maybe a too slow climb and I have to make an adjustment.

The Story

Following, I will describe the 3rd firing of one of my initial test firings and what my goals/expectations were in each firing sequence. The kiln was a 23”x27” and the log of major PSI/dampening changes is shown following – I left off the many readings in between. The results were good and I think this can be used as a starting point for other 23”x27” TDI kilns. I hope that understanding this “story” might help you visualize your firings.

I do note that this recent conversion was of an Olympic Updraft that has 3” thick walls and no element grooves. As a result, it is more efficient and for the higher temperatures I added 0.2 PSI to my actual numbers. For a 2.5” thick kiln wall, it may require another tenth or so. This will be more obvious after judging the firing times/temperature climb rates and the amount of reduction, as described later.

Another tip would be to make a significant change to the numbers after the first firing, as I had done, either for more reduction or in the direction of less reduction. When the firing progresses from too much to too little, or vice versa, you can then pick numbers in between to hone in on the best ones. Ultimately, making significant changes will usually speed up the learning process since result differences will be greater.

The 23”x27” firing schedule below was adapted from the third test firing and is used in the text following. 


For the 28” kiln, I have included a rough schedule as shown below. The process and procedure is essentially the same as the 27” kiln text, just with different pressure and dampening numbers. The warmup was done with one burner only, then the second burner turned on.


Lighting Pilots and Burner

For safety, the lid should always be open when the pilot light is lit. First, check that the gas valve on the burner assembly is closed as well as the pilot light (pilot needle valve clockwise for closed).

Important: Ensure that the gas regulator knob is unscrewed to loose (counter-clockwise) so that there is no chance of applying over-pressure that may damage the 3 PSI pressure gauge when the gas is turned on.

Next, I open the valve on the tank in the water bucket, and only one propane tank at a time. Next, screw the pressure regulator knob in until the pressure gauge reads a slight movement, not more than 1/2 PSI.

With a grill lighter lit and near the pilot light, open the pilot light needle valve and adjust to get a flame about 1-1/2 to 2 1/2 inches long. The needle valve is very sensitive and takes a minute movement to get the right flame size. Since the 10’ hose has to fill with propane, it may take a long while for the pilot to fully light. As the propane fills the pipe it will begin to sputter a bit and then finally stay lit.

Gently open the burner value and the burner should light immediately – notice the pilot flame gets smaller. The pressure can be adjusted up or down slightly to have a small flame for candling warm-up. The flame may sputter a bit initially as air is purged from the hose line. Don’t leave it unattended for the first few minutes until a good steady flame is being produced.

If you have trouble lighting the burner and you feel that some propane has filled into the bottom of the kiln, shut things off and just wait a few minutes. Propane is heavier than air and will seep out the inlet hole and then the lighting procedure can be repeated.

After the PSI has been set for a small candling flame, an option is to turn the burner off and note the reading on the PSI gauge and the size of the pilot light. Record the PSI and and note how many turns the pilot value needs to off and back on and the flame size. This will be the burner lighting numbers for the firing.

If using a Baso safety valve and pilot light assembly, follow the directions for the valve and remember that it will also take a while to purge the hose of air and have the pilot light stay lit.

Another option mentioned later is to use a grill style piezo-electric lighter, which makes it easier to light both the pilot and the main burner.

Here is a setup and initial procedure checklist that can be copied and referred to.

Candling and Main Firing Start

The TDI kiln is capable of very fast initial climb rates that can have bad effects on wet glazes and cone packs due to moisture. Candling helps dry things out. Listed is a pressure of under 0.1 PSI. With the pilot light lit and making a large flame, I turn on the valve for the MR-750 burner and then reduce the pressure as much as possible and still have a bit of flame in the burner. It is generally not good to have a flame down inside the burner body, but if it is small, it won’t hurt anything over a short period. After the burner is lit, I close the lid, however, if there is a moisture concern, place a soft brick wedge under the kiln lid for about 15 minutes and then close the lid for another 15 to 30 minutes to dry things out, or longer if necessary. In the log above, I used about 0.1 PSI and after 35 minutes the temperature climbed to 210C/410F. I use cone holders and self-supporting cones rather than cone packs, so the fast rise wasn’t an issue.

To start the main firing, I turned the gas pressure up to 1.3 PSI and turned the pilot light off. Below red-hot, I don’t leave the kiln unattended just in case the wind blows the flame out or something else happens. For the 28” kiln, an initial pressure of around 1 PSI should be good. The flue dampening was set to 8” and not adjusted until body reduction.

Climb to Body Reduction

Generally, I plan for about 2 hours from main firing start to 900C/1652F and body reduction. I was at 210C/410F at the start, which is 690C/1242F from 900C/1652F. So, for a 2-hour timeframe, an average climb rate target of 345C/621F per hour would be work. After initially going to 1.3 PSI, the actual initial climb rate will seem very high but settles down after a while and doesn’t seem to hurt anything.

As shown in the log, my 1.3 PSI equated to 2.2 hours and an actual average climb rate of 320C/576F per hour. This was the third test firing of this kiln. For the first firing, I used 1 PSI and the rate slowed after a bit, so I kept increasing to 1.2 PSI and it took 2.5 hours to get to 900C/1652F. For the second firing I used 1.4 and got to body reduction in just under 2 hours.

So, it appears that 1.3 to 1.4 PSI will be a good baseline pressure going forward. I can set this pressure and probably not have to make any adjustments until 900C/1652F body reduction. After the first hour, I will still monitor the climb rate every 20 minutes or so just to make sure.

For the 28” kiln, an initial pressure of around 1.0 to 1.3 PSI should be good.

Body Reduction

Body reduction is a period of heavy reduction affecting the clay body, which is done before the glaze melts and seals off the clay. Recommended times are around 30 to 60 minutes and I generally maintain it for 45 minutes. The range of acceptable temperatures is about 900C1652F to not above 950C/1742F. Potters also use Cone 011 and 010 as indicators to begin body reduction.

The objective is to stall out the kiln and then maintain a temperature for around 45 minutes. I don’t mind a slight creep and find that I like to keep the temps around 910C to 920C or 1670F to 1690F.

There are two concurrent ways a kiln will stall. First, if the fuel is increased too much, there will not be enough oxygen for a complete burn relative to the draft/airflow and the temperature can stop increasing and even decrease. The second way is to close down the dampeners restricting the draft/airflow with the result that there will not be enough airflow relative to the amount of fuel and the incomplete burn causes the kiln to stall. Both of these methods are used at the same time – dampening and increased propane pressure.

For the initial firing, dampen first to around 2” to 2 1/4” and wait a few seconds for things to begin to happen. Then increase the gas pressure slightly to stop the temperature from dropping. Increase again if needed.

For my first test firing, I kept the gas pressure at 1.2 PSI and closed the flue opening to 1 3/4”, stalling the kiln. There wasn’t enough fuel going in and the body reduction was poor for most of the ware.

For the second firing, I chose 2.2 PSI and a dampening of 1 7/8” stalled the kiln. Unfortunately, there was too much fuel and the reduction was way too heavy. The clay over-reduced and did not look as good.

For the third firing, I settled on 1.8 PSI and a 2 5/16” flue dampening stalling the kiln. The body reduction was really good and towards the end of the 45 minutes I had let it creep up a bit to about 939C/1722F.

Even when you find the pressure/dampening size that stalls the kiln and produces the results you want, there will still be a bit of tweaking during the 45 minutes. I leave the pressure at 1.8 PSI and make very small changes to the dampening opening. A dampening brick adjustment of 1/16” can make the temps rise or fall and so it requires constant attention. Sometimes I get it pretty perfect and just sit as the temperature stays almost constant or very slowly rises over 45 minutes staying within the range.

Have some fun with learning this, like letting it climb slowly to 930C/1706F and then close the dampener slightly and bring it back down to 915C/1679F, and then hold with slight dampening block tweaks. This is good practice of the process and patience that will be used in later firings when you are doing the same thing in order to even out the top to bottom kiln temperatures at the end of the firing. It is a lot less stressful to learn it here than at the end of the firing when you are also trying to watch the cones go down.

For the 28” kiln, a pressure of around 2.0 PSI should be good. Just dampen down to stall the kiln out and tweak to hold the temperature. Observe the results and make changes accordingly.

Climb to Around Cone 7 ~ 1235C/2255F

The objective here is to find the pressure and dampening settings that will bring up the temperature from body reduction to around Cone 7, or ~1235C/2255F. During this sequence, there should generally be light to medium reduction and the timeframe should be about 2 1/2 to 3 hours. The timeframe and desired reduction may change later commensurate with your glaze requirements but for initial firings, one is just trying to learn baseline numbers.

The log shows the pressure going from 2.0 to 2.2 PSI and the dampening from 2 5/16” to 3 1/4”. I usually just open up the dampening, leaving the pressure where it is, and observe and write down the results. Then adjust the pressure to keep the reduction/temperature rise going. Several adjustments will likely be required.

Since I want to go from around 950C to 1235C/1742F to 2255F over 2 1/2 to 3 hours, an average climb rate of about 100C/180F per hour is indicated (285C divided by 2.75 hours = 104C per hour rate). What actually happens is that the initial climb rates will be much higher, around 140C to 160C/252F to 288F and then it will slow down to around 50C to 60C/90F to 108F when the temps are close to Cone 7 - 1235C/2255F.

During this sequence, I keep an eye on the per hour climb rate with more frequent observations the closer it gets to Cone 7. I adjusted the dampener opening, making it larger by small increments and waited for something to happen. After about 45 minutes, a 6-minute check showed that the temperature climb rate had dropped to about 108C/194F per hour. So, I increased the gas pressure to 2.1 and opening the dampener 1/4” to 3 1/2” and the climb rate popped up to about 135C/243F per hour. It had been slowly dropping in climb rate per hour for a while (I was taking temperature measurements every 6 minutes), but I was patient and waited until it was pretty low and then made the adjustment.

About 40 minutes later, it had slowed down to 70C/126F and I opened the dampener another 1/4” to 3 3/4” and also increased the pressure to 2.2 PSI. This increased the rate to about 100C/180F per hour. About an hour later, it slowed again to about 40C/72F per hour so I opened the dampener to 4”. Being at approximately the Cone 7 temperature, the rate after a 6-minute test was about 60C/108F per hour, which was good.

Being the third firing, I had some baseline number ideas and so there was much less tweaking than in the first two firings. In the third firing, I made 3 pressure changes and 4 dampener changes in the after body-reduction sequence. By comparison, in the first firing I made 3 pressure changes and 7 dampener adjustments, both wider and smaller. In the second firing, I made 1 pressure adjustment and 6 dampener adjustments (and had too little reduction).

It is best to adjust only one thing at a time and then wait for something to happen, verified by a 3 or 6 minute temperature rate per hour check. The initial firings will have more adjustments. After a firing, look at the log and pick some incremental pressure settings and their related dampening sizes that you think might be good and mark them for use as a baseline in the next firing. If they are off slightly, then adjust next time as you hone in on the best baseline settings.

Judging these results and for the next firing in the after body-reduction to Cone 7 sequence, I would plan on using 2.1 PSI then probably 2.3 PSI as my two changes, with 3 or 4 dampener size changes – 3 1/4”, 3 3/4”, and then 4 1/8”.

60C/108F Degree Per Hour Climb to Cone 10 Down

As mentioned, for the initial test firings, I think the best thing to do is to try and keep a 60C/108F rate to the end of the firing and to not worry yet about the full-on process for evening out the top to bottom kiln temps. From Cone 7 - 1235C/2255F it should take about an hour for Cone 10 to go down. Note the witness cones on each shelf and there might be a large difference in top to bottom, or the middle might be hotter as a result of the deflector block size. For now, record all of this information on the kiln log.

For the third test firing, I continued with 2.2 PSI. The dampener was at 4” at the Cone 7 temperature point. I did 6-minute temperature rate calculations and when, after about 17 minutes it had slowed to around a 40C/72F per hour climb again, I opened up the dampener 1/8” and increased the PSI to 2.3. The climb slowed again at about 7:06 PM, and I opened dampener up 1/8” to 4 1/4”. At 7:22 PM Cone 10 was down and I shut off the kiln. So there were lots of 6 and 12-minute calculations written down but not shown in the previous sample log.

A goal in the initial test fire sequences is to have light to moderate reduction. During the top to bottom evening out procedure, detailed later, the reduction will be moderate to strong, so getting the numbers for light to moderate reduction here works. In order to see reduction (assuming one is not using an oxygen probe), it is better to finish the firing at night, as previously mentioned. My small shed’s doors are open during the firing so I time the last 1 to 2 hours of firing to be at dusk to dark outside.

As should be noted by this point, reduction is adjusted by dampening the flue and there is a relationship between the temperature rise and dampening. So, if one wants more reduction, the block may be dampened a small increment. But then the kiln temperature does not rise as fast as you want, so the gas pressure must be increased. Initially, one will tend to make larger adjustments but once you gain confidence, you’ll notice that you make fewer adjustments. And, that the adjustments are more related – the dampening increment is not quite as much knowing that you will probably be increasing the gas pressure. 

The first photo following is from the third test firing being discussed and shows light to medium reduction near the end of the firing – the reduction flame is there but not too large or bright. Something like this is what you want for the initial test firings. The second photo following is moderate to heavy reduction, also near the end of firing, with a larger brighter and more ragged flame.


As with the prior Climb to Cone 7 sequence, in the first few firings there might be lots of tweaking to try and keep a steady rate increase and the kiln may stall a few times. This is fine, you are both learning how to tweak and control the kiln and also recording and figuring out the baseline numbers to use later.

Besides it taking about an hour for Cone 10 to go down in this sequence, two other things can happen. One, the temperature can increase too fast and even exceed the Cone 10 temperatures listed in the Orton cone charts. Just dampen down a bit and the rise can be stalled or even lowered, and then wait for Cone 10 to fall. Second, it might take longer than one hour and you find yourself doing a lot of large and small tweaking with the dampener block and even stalling it out at slightly near or above the Orton cone temperature as indicated by the pyrometer. This is ok too and will actually serve to even out the top to bottom temperatures. Record and note the PSI and dampener opening numbers that you think made the increase more stable and closer to a 60C/108F per hour climb rate.

After a few firings, you may notice the temperature is within a few degrees of the same reading when the cone bend shows you’re finished. For example, the self-supporting cone 10 chart shows 1285C and I consistently get 1273C to 1278C on the pyrometer, so I know I’m close but still use the cone going down as the primary indication.

When Cone 10 goes down, the propane gets shut off. The dampening blocks are moved to completely cover the flue exit. A soft brick piece about 1/2 inch thick is placed on top of the burner to somewhat block off the burner port, and it also protects the copper pilot from radiating heat. Now, it’s just a matter of waiting a day or so for a kiln opening.

Again, the purpose of these initial firings is to find the pressure and flue dampener setting that provide acceptable sequence times and results for the candling, climb to body reduction, body reduction, climb to around Cone 7, and then climb to Cone 10 down. Eventually you will have baseline numbers that will give you a relaxed and repeatable firing for the 6 hours or so to get to a Cone 7 ~ 1235C/2255F temperature. A lightly loaded kiln may require less PSI and slightly smaller dampener opening than the baseline otherwise the firing may be too fast. Conversely, a heavily loaded kiln may require more heat energy and slightly higher PSI and larger dampener settings in order to get to Cone 7 in 6 hours. Use your clay and glaze results to determine whether sufficient reduction is occurring. 

Once you have more confidence in you firing abilities or have the firing pressure and dampener changes down to something that looks like the log previously shown, you can move on to the next section and begin with evening-out-the-temperatures process.

To help with recording and comparing firings, there is a sheet on the last page that can be copied. It has items most important to the firing outcomes and should provide a visual path to setting up pressure/dampening numbers to get the firing process under your control. I assume that reduction will be done, so I note temperature climbs to body reduction, which just helps plan times for light or heavy kiln loads. Kiln loads will greatly affect the time of the firing, so if one is looking for that two-hour climb to body reduction with a heavy loaded kiln, the gas pressures may be significantly higher. Yet, the body reduction PSI and dampening will likely be about the same.

The Climb to Last Hour numbers entry is just to set the initial PSI/dampening to get the climb going, also affected by ware load. During the last hour to whatever cone temperature that may be, I think following the Orten Cone temp rise per hour listing seems to work well. The Last Hour Sequence numbers entry is also just to set the initial PSI/dampening.

Evening-Out-the-Temperature Process

Evening-out-the-temperatures is basically just a process whereby the gas pressure is reduced slightly and then the dampener opening is reduced to the point that the kiln stalls. The goal is to have a very slow or no climb rate. Even though the temperature is held almost constant, the heat work continues, which is what makes the cone go down and ware mature. The back pressure caused by the over-dampening helps even out the temperatures in the kiln.

Walford Campbell has an end-of-firing method he learned firing gas updraft kilns in his pottery in Jamaica. Walford studied ceramics at Derby Lonsdale University, Derbyshire, England. On returning to Jamaica, he joined the faculty of the Edna Manley College of the Visual and Performing Arts in Kingston and also started his own very successful pottery. His procedure is used as follows.

Firing cone 10 reduction and after the 900C/1652F body reduction period, he brings the temperature up at 2.0 to 2.5 PSI (for his 28”x32” kiln) until Cone 7 falls. The gas is then reduced to 1.5 PSI and the flue dampening is reduced to the point that the kiln stalls. From there to Cone 10 going down, he opens the dampening slightly and maintains a very slow rise in temperature. The rise might be only 30C to 40C/54F to 72F per hour.

In order to keep the temperature slowly rising, the dampening blocks require constant attention and tweaking. Small adjustments can make for surprising large changes in the temperature rise of the kiln, or it might start going down in temperature. What does happen is that the top to bottom temperatures in the kiln are evening out and when Cone 10 is falling he shuts off the kiln and closes the flue dampening blocks. The temperature on the pyrometer is not relevant and only the cones are used to judge the firing (look at the Orton cone chart for Self-Supporting cones and slow, medium, and fast rates and the difference in temperature indications). This process can take an hour but sometimes it goes on for longer, especially when the kiln is heavily loaded.

I do the evening out process slightly different in that I wait until Cone 10 begins to bend. For the 23”x27” kiln, I drop the pressure from 2.1 PSI to about 1.8 PSI and reduce dampening to about 2.5”, and the kiln stalls. The dampening block is then opened up about 1/8” and I wait to see what the climb rate is. I’ll do 3 and 6-minute rise rate checks and tweak the block accordingly. Adjustments can often be as little as 1/16”. The indicated temperature is not relevant to the actual Cone 10 going down, yet it still shows a target climb rate since, in this process, the final temperature might be in the 1260C to 1280C/2300F to 2340F range. If it does climb to around 1280C/2400F in my kiln, I will stall it out there and then wait for Cone 10 to drop.

Your kiln might have different numbers and it is important to remember that the pressure and dampening numbers will range from a low pressure/dampening that will stall the kiln with almost no reduction (in oxidation) to a higher pressure/dampening that will produce high reduction. What you’re looking for is a pressure/dampening that creates a nice light to moderate reduction, as evidenced by the flame and, of course, the final glaze results.

There are other resources for the evening out process. Florian Gadsby makes interesting YouTube videos and in this one, “Packing a Kiln Load of Pottery and Gas Firing in Reduction” at 10 minutes, he is firing his Rohde KG-340 kiln, which has an interior flue made of thin refractory material like the TDI flue wall and 4 bottom vertical burners. Take aways from this are that after heavy reduction, the dampener is only slightly opened to get a climb rate of around 85C/153F per hour until about an hour to the end at which time it goes down to 50C/90F per hour. It takes 4.5 hours from after heavy reduction to finish and the constant reduction and strong dampening is what evens out the kiln so he gets about a 1/2 cone difference (seen from cones in his other video). He also does a crash cool down to 1000C/1800F, which he says makes the colors brighter, then he closes it up for a slow cool. The strong dampening and slow per hour climb rate at the end even out the top to bottom temps.

Perry Brown, from the TDI Downdraft Kiln Conversion group on Facebook posted: I am working on a TDI conversion right now, but the kiln I have been using for several years is a small Olympic updraft. I have found that the keys to even firing are patience (i.e., not bringing the temperature too quickly) and actually letting the temperature rise stall a couple of times during the firing (i.e., holding at, for example, 1300 deg and 2000 deg for about 30 min each) to let the temperature even out bottom to top.

If this whole evening-out explanation seems overly simplistic and somewhat anticlimactic given the previous hype, well it is. Once the baseline numbers of the firing are established and the tweaking process is learned, the evening-out is not difficult, but it does require patience.

To finish, below is a photo of Walford’s 23”x27” and the 28”x32” kilns towards the end of the double firing and showing nice reduction flames. Good luck and have fun! 






7.02.2018

Gas Kiln Conversion - Downdraft

November 2023 - A second revision of the TDI Downdraft Kiln Conversion book has been uploaded and published and is available at the same Amazon link previously provided. The book presents clarifications of previous text and enhancements and ideas from many people, including from the Facebook group. A major revision was to the Firing the TDI kiln sections. Oval kiln conversion is discussed as well as more detail relative to the optional or alternative parts. New text not included in other prior blogposts is included in this short blogpost: 

October 2023 - A new blogpost with details of the current design features with some helpful information has been added: http://www.sebastianmarkblog.com/2023/10/tdi-downdraft-kiln-conversion-further.html

April 2022 - This updated blogpost presents Firing the TDI Conversion section from the new 2023 book revision. It details the methods for the initial test firings, judging reduction, and also the Evening-Out-the-Temperatures process at the end of the firing:

January 2021- The Facebook Group TDI Downdraft Kiln Conversion has been created to provide a place to share information including building the conversion, firing schedules, and pottery results. www.facebook.com/groups/4124895130900261/

February 2020 – I appreciate the many people have given me feedback relative to the post or questions with their conversion. From this communication, I’ve realized that I assumed a level of understanding and construction ability above many people and have not adequately explained to all how to get it done using tools typically owned. To remedy this, I have put together a conversion book that explains the process in more detail, shows why specific items are important and how to measure them, and current sources for tools and components.

The TDI Downdraft Kiln Conversion book is available on amazon at: https://www.amazon.com/dp/B084DH88GH

Thanks, and if you have any questions, I can still be contacted at borissquare@gmail.com


2018 - GAS DOWNDRAFT KILN CONVERSION
The following details gas downdraft conversions of two kiln sizes – a 23” by 27” and a large 28” by 32”. The goal was to fire cone 10 reduction. The design is relatively inexpensive and easy to construct from commercially available parts. Simplicity of both design and use was a major objective. Both kilns fired very well and excellent reduction and repeatability were obtained. Photos, firing schedules, and pressure/flue size settings are provided following. Specific components/methodology were employed and using different burners or dimensions may not produce the same results requiring recalculation of the inlet and flue sizes. I would also suggest reading and understanding the entire process before doing a conversion.

The photo below of the 28”x32” conversion essentially provides the design. The 28”x32” was an Olympic gas updraft and thus had smooth walls. The 23”x27” was a Skutt electric and had the element grooves.


Theory
There is a tremendous amount of information available concerning kiln designs. There are also numerous examples of kiln electric to gas conversions in both text and video. Through research, I noted that there were some very insightful comments in website documents written by Marc Ward with Ward Burner Systems. Marc also provides equipment including drilled orifices in case you don’t want to buy a #50 bit and drill yourself.

Ward wrote “Draft is the life's breath of a gas fired kiln”. Most of the kiln construction and conversion problems, even from documents written in the 60’s and 70’s, related to issues with draft. Kilns are constructed and then flue sizes and external flue piping are rebuilt and tweaked until the kiln maybe works. Numerous books and articles detail flue/chimney heights and size calculations, and many seem to be providing a flue of around three times the draw length of the kiln, including the exit length. The draft is created by the ducted rising hot air, so the higher the chimney the more suction/pull. From a simplicity standpoint, the attached exterior chimney adds both expense and difficulty to the construction process.

Many electric to gas kiln conversions have been built with an interior flue made with firebrick. Three issues with this design are the amount of space the bricks and flue take up, the added difficulty in building and cementing the bricks, and the oft-requirement of additional flues added to the top of the kiln to increase the draft/suction.

Discovering a German design that uses cordierite shelf material for the flue provided the success for our small kiln conversions. The beauty of the German design is that the thin shelves become super-heated, providing energy to the exiting gases creating a better draft. The shelves also speed up the conversion process. Once all of the parts were obtained and readied, the 28”x32” kiln conversion took about two hours.

Another important consideration is the ratio of primary air to secondary air for the burner. The burner hole drilled in the bottom shelf is 3.5”, which provides for an adequate ratio of primary to secondary air relative to this specific design and the draft it produces. With the flue undampened, the kiln will fire in complete oxidation.

In order to have even temperatures between the bottom and top of the kiln, there is a consistency of past designs/descriptions of having close to a 1 to 1 ratio between the width (or depth) and height of the kiln. The width/depth is related to the path of the flowing gas/heat from the burners up, around, and down to the flue entrance. For the 23”x27” electric to gas conversion, the flue entrance is 2” high and 2” kiln posts are used to support the ¾” bottom shelf, yielding an interior of approximately 23” by 24” tall. Also using 2” posts and flue opening for the 28”x32” downdraft conversion, the interior measures approximately 28” by 29” tall.

Conversion
The flue wall is made from square kiln shelves and the conversion utilizes the inexpensive MR-750 Venturi Burners. The brass orifice that comes with the MR-750 is drilled to #38 (0.1015”) and is too large. Order new ones from Ward Burners and have them drill them with a #50 drill bit (0.07”). Or, if you have a #50 bit, order “Brass Spud Orifice #70 Drill Blank Starter Hole” from www.thebbqdepot.com - $3.14 each.

In order to ensure controlled and consistent firings, an adjustable pressure regulator was used along with a decent quality pressure gauge. The 0-30 psi pressure regulator was purchased from a local grill/propane company and the brand was Marshall Excelsior, made in the US. The pressure gauge was average quality 0-15 psi. A standard 12 foot (¼” Inside Diameter) propane hose was used and can be purchased with 3/8” flare fittings attached. The hose does not have to be high pressure so any ¼” ID rubber hose can be used and grill companies can make them with the flare fittings attached.

A propane tank fitting is attached to the pressure regulator input and the gauge is T’d in directly to the output, rather than placing the pressure gauge at the other end near the burner. Due to the slight flow restriction of the 12’ hose, the pressure readings will be higher and thus allow for a more sensitive adjustment during firing. It’s also easier to set pressures at the regulator.

Following are dimensions of the two conversions. Since shelves and kilns vary, the dimensions may change slightly.



23x27 Specs


A – Flue to inside burner wall
16.25”
B – Flue width
13.5”
C – Flue depth
2.125”
D – Flue flat dimension
7.5”
Flue Area
22.3 Sq. In.
E – Center hole for single burner

F – Burner hole diameter
3.5”
Burner hole total area
9.6 Sq. In.
Flue shelf size
2@ 16” square x 3/4”
G – space between burner and burner wall/kiln wall
Approx. 1/4”

28x32 Specs

A – Flue to inside burner wall
21.25”
B – Flue width
17.25”
C – Flue depth
2.875”
D – Flue flat dimension
7.5”
Flue Area
35.6 Sq. In.
E – Burner/hole center distance
6.5”
F – Burner hole diameter
3.5”
Burner hole total area
19.2 Sq. In.
Flue shelf size
2@ 20” Square x 1/2"
G – space between burner and burner wall/kiln wall
Approx. 1/4"

In both kilns, the flue wall was placed on a small 2 inch post. Thus, the flue opening for the 28x32 was B-17.25” times 2” or 34.5 square inches, less 1 square inch for the small post, yielding 33.5 square inches.

Photos 15 and 16 show the 28x32 burner assembly, which must be made first. The MR-750’s are screwed into the iron pipe fittings. The MR-750 has ½” NPT threads and ½” NPT pipe and fittings were used. Required are: 4-elbows; 2- gas cock valves; 2-‘T’s; 2-6” length threaded pipe; 2-1” pipe; 3-2” pipe; ½” NPT to 3/8” male flare (for 12’ hose connection); needle valve and adapter fittings to get it into the steel pipe ‘T’; ¼” copper tubing; and, the copper tube T. Thread seal was also used on the pipe threads. Note that the burner photos show a cap over the hose flare fitting, used to keep dirt out.

After the burner assembly is made, an accurate measurement of the distance between the burners can be done, then the holes in the kiln bottom can be drilled with the 3.5” hole saw. A pilot hole was drilled first as the hole saw was not deep enough for a single cut on one side. For the 23x27 kiln, one burner is used and an ‘L’ shaped burn assembly can be made to make it stable. Later, to position and secure the burners, several daubs of Liquid Nails Construction Adhesive were used. Due to the height of the kiln stand, a ½” shelf was placed under the 28x32 kiln burner assembly to get a ½” space from the burner to the kiln bottom. The shelf was glued to the floor. Liquid Nails is very hardy (and easy to use) yet can be cut apart with a razor knife if it needed for repositioning, etc.

Drill burner holes in kiln bottom and position on stand.

Photo 1 shows the placement of the first shelf and the groove cut in the soft bricks on the 28x32. Start by marking and sawing on the bottom kiln section first. To establish and mark the groove position, a ½” wide 20” wood piece was placed on the top of the bottom kiln section (or use a ruler) and squared up by getting a constant C dimension. The actual flue shelf/wall can also be placed on the kiln wall to mark the groove. Note that the shelf may be recessed slightly into the groove.

Two lines are needed, inside the flue and outside. Measure from inside and outside of the wood piece, or the actual shelf, to the center kiln brick corners – ends of dimension D (inside kiln). Mark the lines on the bottom kiln section bricks and using a stiff saw, eyeball a square cut. The shelf width was 20 inches and the width of the grove was lightly wider.

Carefully stack and align/secure another kiln section. Measure, mark and cut, and repeat until all sections are cut. Afterwards, use a piece of coarse sandpaper attached to the edge of a board to smooth out the cut (Photo 20).

Photos 2, 3, and 4 shows the placement of the flue wall shelf pieces. Using twisted or straight pieces of Nichrome kiln wire about 1.5” long and a pair of needle-nose pliers, push the wire against the flue wall and into the brick, with approximately 3/8” sticking out and holding the flue in place.

I then jammed some ceramic fiber into the space on the side of the wall, first wetting it in a soupy refractory cement. The ceramic fiber helps holds the wall in place and seals it. After the bottom flue wall is in place, the top wall can be held in place and marked for cutting. Photo 5 shows the top wall piece, which was about 10” tall. The 10” cut off piece was then used as the burner wall (Photos 11 & 15). A standard cheap tile saw was used to easily cut the shelf.

Install the top flue wall the same as the bottom. A very small amount of cement was placed between the wall pieces and a small amount of fiber was used as the cut was not perfect (Photos 6 & 7).

Photos 9 and 10 show the placement of the bottom 2” shelf posts and also soft brick pieces cut to 2” tall that are used as baffles. The baffles make the exiting gases return from the burner side of the kiln and helps produce more even temperatures over the bottom shelf. The un-baffles areas were approximately 8” to 9” wide so as not to constrict the exit gas flow, providing around 16 square inches per side.

Photo 11 shows the 26” diameter by 3/4” shelf cut to fit the kiln. The cuts were based on the shelf being slight off center towards the flue as shown so as to have the gases exit through the unbaffled areas under the shelf. As shown, the space along the edge of the shelf provided an area of approximately 16 square inches per side for exiting gases. Cuts to the shelf were made with the tile saw.

Photo 11 also shows a soft brick baffle between the burners measuring 1” wide and around 5 inches tall. This keeps the 10” burner wall shelf piece from inadvertently leaning into the burners.

Photos 12 and 13 show the exit hole though the top. Note that it is to the side – this is the strongest place to put it but care must still be taken when opening the kiln lid to not overstress the bricks around the opening. The cut is carefully made with a flat saw and marked by measuring the flue on the top kiln section. Since the 28x32 was originally an updraft kiln, the round center exit hole in the lid was filled with cemented and pinned soft brick.

Photos 26 to 32 show the 23x27 electric to gas conversion. Missing from Photo 31 were soft brick baffles placed similar to the 28x32 to control exiting gases.


Firing Schedule
The attempted/ideal firing schedules were based on information from Val Cushing, John Britt, and Walford Campbell, and were tweaked for the two kilns. Initial issues encountered were too fast a warm-up and very fast firings. The too fast warm-up once caused a top cone pack to explode. There did not appear to be any adverse effects from the fast firings, however, Δ10 reduction firing in 4 hours just seemed too short a time. For both kilns, a firing time of approximately 7 hours appeared reasonable and included a 30 to 45 minute initial warm-up.

Noted about the firings is that the adjustable burner plate on the MR-750 burners was kept at around 5/8 to 3/4 of an inch throughout the firing. Reduction was made solely by restricting the exit flue, as shown in Photo 25. Soft bricks were used for dampening and in the following schedules the flue dampener opening is the distance between the bricks. It was found with both kilns that the flue area was larger than it needed to be. Both kilns will fire cleanly in oxidation dampened to around 9 inches. For the 28x32, this means that the flue has an excess area of approximately 9 square inches, equivalent to moving the flue wall around ½ inch, adding ½ inch to the kiln area. However, changing the flue dimensions may affect the firing – it would require experimentation.

As mentioned, the regulator in our conversions connects to a 12’ hose with a ¼ inside diameter. Varying the length or diameter will change the pressure verses flow characteristics and so the pressures will have to be found by experimenting. The valves on the burners are turn full on during the firing and gas flow is controlled by pressure only. When pressures are adjusted, tapping a fingernail lightly on the gauge is required to get an accurate reading.

The pilot light system is simple and is made from ¼” copper tubing, crimped at the top and drilled with a 1/16” hole. It works to light the burners. The 28x32 is warmed up with one burner and the pilot light was blown out and had to be relit to start the second burner. The pilot gas is shut off once the burners are running. We do not leave the kilns unattended during firing and no thus Baso safety system was employed.

Reduction commences at 900C and the kiln is stalled for 45 to 60 minutes with a constant temperature target of around 925C and not to exceed 950C. The gas pressures and flue dampener openings may have to be tweaked for your kiln and very small dampener changes can stall or increase kiln temps. A balance between gas and dampening will be found. No black smoke or soot is made during reduction. The appearance of soot shows over-reduction settings. Soot is carbon – reduction happens with unburnt fuel and carbon monoxide gas.

After the heavy reduction, the flue dampener is opened up and the temperature is allowed to increase quickly up to about 100C lower than the Δ10 temperature. The dampener settings listed following provide for a continued light to moderate reduction during this climb. Nearing the end of the firing, cones and color are used to affirm that the temperatures are relatively even from the top to bottom of the kiln. The top has always been slightly hotter than the bottom and ware is placed accordingly.

Photos 35 and 36 show some kiln packing. In Photo 35, the shelves were staggered vertically and placed toward the sidewalls causing the flame to zig-zag down though the shelves making for even temperatures. Photo 36 had taller bottles and pieces that made for a more abstract placing, but also had good firing results. One must try to visualize the flame going vertically to the top and flowing over the ware and through the shelves. For example, a shelf placed against the side wall and over a shelf also placed against the side wall will create a ‘dead’ spot near the wall that could experience lower temperatures. For the 28x32 kiln, 24” half round shelves were used with approximately 1” cut off the sides for fit – as shown in Photo 38.

Photos 22 and 33 show the propane bottles used. Bottles are placed in a tub and a small trickle of water is sufficient to keep the gas from freezing up causing pressure/flow loss.

Photos 23, 24 and 34 show the stove pipes used to exit gases from the building. The pyramid-shaped hood directly above the kiln was made from 24” wide sheet metal roofing panels and pop riveted together. 6-inch steel stove pipe was used to connect to outside the building.

Photo 37 was included as it shows a small shelf placed to block wind gusts during a windy firing day.

The following schedules are based on firings and can set up guidelines as a starting point. The primary objectives are an initial slow to moderate warm up, then fast climb to 900C, 45 to 60 minutes in heavy reduction, moderate reduction to 1182C, 60C per hour climb to 1282C with possible requirement to even out temps by dampening. The hotter the kiln gets above 950C, the slower the increase per hour if nothing is adjusted. Small changes in gas pressure and dampener opening size can have large effects in temperature rise or stall. Keep a log to learn the kiln.



At the end of the firing, the flue is completely closed off and a thin soft brick piece is placed over the burner providing somewhat of a block for the burner inlet. 

For questions or your comments/improvements, I can be contacted at borissquare@gmail.com


Photos

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10.15.2014

The Art of Flight: A Journey in Tibet

Wow, haven't posted in two years, not that anyone was reading this. It was, after all, a tool to optimize my studio website. But since I don't have television and I don't feel like practicing yoga, dobro guitar, archery, study paragliding manual, read, clean, or much of anything else I need to do, I'll mess with this.



This is about a trip I took to Tibet over a few days November 2012. Preview is limited - click HERE.

"The Art of Flight is about a journey to Tibet that resulted in an exploration into the higher levels of meditation and yoga. It is a personal flight manual that may lead to the extraordinary experience of semi-weightlessness, and will lead to a refinement of both body and mind. If your life is an experience you don't want to miss, then maybe it's time to understand yourself and the power of flight."

Ok, what's next...

6.16.2012

Copyrights

As soon as you create your work, a copyright is created. When a photographer clicks the shutter, they have a copyright in the image. A copyright exists as soon as the creator’s (non-copyrightable) idea is expressed in a medium that can be viewed.

A copyright is intangible intellectual property. It’s something that a person or corporation can have ownership of and can transfer ownership of to another person or corporation, but has no physical substance.

Generally speaking, no one has the right to copy your creation in any way in any medium without your permission. It is illegal for any unauthorized person or company to scan, copy, duplicate, manipulate, alter, etc. your work without your permission. And, the law specifically gives creators the right to copy, reproduce, distribute, display and create derivative uses of their work.

Registration is Protection: Although all work is copyrighted at the moment of creation, not all work is protected equally. If a registered work is later infringed, the creator/owner can recover actual damages (the fee that would normally have been paid for the use), as well as Statutory (Punitive) Damages (up to $150,000 for each infringement) and legal fees. A work that is infringed and has not been registered, can only generate the Actual Damages. This means that, in most cases, the cost of the suit far exceeds the recoverable moneys. If you expect to file a suit most attorneys won’t speak to you unless they know you’ve registered your images.

The one exception to the above is work that has been infringed within 90 days of first publication. In this case, it is still possible to register and have access to Statutory Damages and Legal Fees. If you are in this position, you need to register immediately.

The Copyright Act grants five rights to a copyright owner:
   the right to reproduce the copyrighted work;
   the right to prepare derivative works based upon the work;
   the right to distribute copies of the work to the public;
   the right to perform the copyrighted work publicly; and
   the right to display the copyrighted work publicly.


Workflow: Since registration of unpublished work affords the most protection, it is the most desirable. You can wait to submit/register until a specific work is about to be published. If you work on projects that have long lead times, this may mean infrequent submissions. If your work gets published more often, you may want to work the registration procedure into your normal image creation or digital darkroom workflow. Additionally, the image deposited to the US Copyright Office should be made in such a medium that it will still be viewable during the term of the copyright, which, for independent creators, extends to 70 years after the creator’s death.

The files in a registration are required to be uniquely named. Choose something that identifies the files, in case you had to dig up a single file for litigation - it’s a lot harder looking through lists of files named DCS_1045.jpg. It also makes it easier to prove that the image in question was actually part of the registration collection. Duplicate names in the owner’s other files or copyright registrations may cause problems.

Is it better to register the original capture or the post processed file? What if you increase the color saturation, contrast, crop the file, make it black and white, and so on? You can register files as basically captured, with minimal work, like exposure correction in Lightroom’s Quick Develop. The variations of the original are protected with what is known as the ‘right of derivatives’. You own the copyright to derivatives of your image. But, if you really work a file a lot - it couldn’t hurt to register it also.

And, just because a registered work is accepted by the Library of Congress, it does not mean that the copyright registration cannot be challenged in court. In fact, if a significant amount of money is on the line, a challenge is not uncommon. Any falsification or factual error in the registration could potentially invalidate the registration. You must expect that participants in a copyright case will look hard at all information on the form, including the publication dates. Make sure that you are registering the earliest possible publication of the photo.

Another tip - imbed copyright and owners information in metadata for electronically transferred files.

Myths and Questions:
“If it doesn’t have a copyright notice, it’s not copyrighted.” This was true in the past, but today almost all major nations follow the Berne Copyright Convention. For example, in the USA, almost everything created privately and originally after April 1, 1989 is copyrighted and protected whether it has a notice or not. By default, you should assume that other people’s works are copyrighted and may not be copied unless you know otherwise. There are some old works that lost protection without notice, but you should not risk using them unless you know for sure.

It is true that a notice strengthens the protection, by warning people, and by allowing one to get more and different damages, but it is not necessary. If it looks copyrighted, you should assume it is. You may not scan pictures from magazines and post them to the net, and if you come upon something unknown, you shouldn’t post that either.

The correct form for a notice is: “Copyright [dates] by [creator /owner]”

You can use C in a circle © instead of “Copyright” but “(C)” has never been given legal force. The phrase “All Rights Reserved” used to be required in some nations but is now not legally needed most places.

“If I don’t charge for it, it’s not a violation.”
False. Whether you charge can affect the damages awarded in court, but that’s main difference under the law. It’s still a violation if you give it away - and there can still be serious damages if you hurt the commercial value of the property. If the work has no commercial value, the violation is mostly technical and is unlikely to result in legal action. Fair use determinations do sometimes depend on the involvement of money.


“If it’s posted to the Internet or Usenet, it’s in the public domain.”
False. Nothing modern and creative is in the public domain anymore unless the owner explicitly puts it in the public domain. Explicitly, as in you have a note from the creator/owner saying, “I grant this to the public domain”, or words very much like them. Some argue that posting to Usenet implicitly grants permission to everybody to copy the posting within fairly wide bounds, and others feel that Usenet is an automatic store and forward network where all the thousands of copies made are done at the command (rather than the consent) of the poster. This is a matter of some debate, but even if the former is true (and in this writer’s opinion we should all pray it isn’t true) it simply would suggest posters are implicitly granting permissions “for the sort of copying one might expect when one posts to Usenet” and in no case is this a placement of material into the public domain. It is important to remember that when it comes to the law, computers never make copies, only human beings make copies. Computers are given commands, not permission. Only people can be given permission. Furthermore it is very difficult for an implicit license to supersede an explicitly stated license that the copier was aware of. Note that all this assumes the poster had the right to post the item in the first place. If the poster didn’t, then all the copies are pirated, and no implied license or theoretical reduction of the copyright can take place.


Note that granting something to the public domain (PD) is a complete abandonment of all rights. You can’t make something “PD for non-commercial use.” If your work is granted PD, other people can even modify one byte and put their name on it. You might want to look into Creative Commons style licenses if you want to grant wide rights.

“My posting was just fair use!” The “fair use” exemption to (U.S.) copyright law was created to allow things such as commentary, parody, news reporting, research and education about copyrighted works without the permission of the creator. This is vital so that copyright law doesn’t block your freedom to express your own works - only the ability to appropriate other people’s. Intent and damage to the commercial value of the work are important considerations.

“If you don’t defend your copyright you lose it.” False. Copyright is effectively never lost these days, unless explicitly given away. While copyright law makes it technically illegal to reproduce almost any new creative work (other than under fair use) without permission, if the work is unregistered and has no real commercial value, it gets very little protection. The creator/owner in this case can sue for an injunction against the publication or infringing user and may win actual damages from a violation, and possibly court costs. Actual damages means actual money potentially lost by the creator/owner due to publication or use, plus any money gained by the defendant. But if a work has no commercial value, the actual damages will likely be zero.

In Summary
These days, almost all images are copyrighted the moment they are created in a material form, and no copyright notice is required.


Copyright is still violated whether you charged money or not, only damages are affected by that.

Postings to the net are not granted to the public domain, and don’t grant you any permission to do further copying except perhaps the sort of copying the poster might have expected in the ordinary flow of the net.

Fair use is a complex doctrine meant to allow certain valuable social purposes.

Copyright is not lost because you don’t defend it; that’s a concept from trademark law.

Work derived from copyrighted works is a copyright violation.

Copyright law is mostly civil law where the special rights of criminal defendants you hear so much about don’t apply. Watch out, however, as new laws are moving copyright violation into the criminal realm.

Don’t rationalize that you are helping the copyright holder; often it’s not that hard to ask permission.
Posting E-mail is technically a violation, but revealing facts from E-mail you got isn’t, and for almost all typical E-mail, nobody could wring any damages from you for posting it. The law doesn’t do much to protect works with no commercial value.

The eCO (Electronic Copyright Office) system
As far as the paper VA form (Visual Arts form), it is being phased out. If you have any VA short forms you can still use them or you can still request them to be mailed to you from the copyright office.


There is a problem with the number of files you can register - if you are registering a very large number of images. There is an upload time limit of 30 minutes, not a size limit. So after 30 minutes, the upload will time-out. But what you can do is fill out all the info on the electronic form, make the payment of $35, and then printout a mailing sheet and mail in your images on a CD, along with a printout of the filenames.

The effective date of your registration will be the date they receive your CD, which the Copyright Office calls the “deposit.” If you do mail in a CD, get a delivery confirmation or return receipt to confirm the date they received your image deposit.

http://www.copyright.gov/