Latest correspondence with Lloyd Tanner
Hi folks,
This post includes my latest correspondence to, and reply from, Lloyd Tanner. Please note that, in his reply, Lloyd is giving details concerning his newer friction roller design, which can feed several pieces of wood simultaneously. With the new design, Lloyd has increased the operating temperature and pressure to 700 degrees @ 300 psi. The new design features a horizontal roller that is 10 inches in diameter, and 36 inches long (full width of trough). It is interesting to note that the amount of water contained in each "drop" is said to be 1/2 teaspoon, which is roughly 2.5 milliliters. As pointed out in my correspondence to Lloyd, a normal droplet of water is about .025 milliliters, and would be just 1/100 of Lloyd's controlled water drop amount. Thus, his water drop is actually a metered amount rather than a natural drip. From Lloyd's description, it would appear that these metered amounts are dropped at 4 inch intervals along the length of the water distribution rail in a linearly progressive manner, from one end of the rail to the other.
My correspondence to Lloyd:
Sent: Sat 12/06/08 4:50 AM
Hi Lloyd,
Thought you might be interested to know that we are currently at over 9,000 views by people interested in your friction heater, and many are interested in building replications. I think that I have been able to answer most questions to the satisfaction of inquirers, but lately the topic of discussion has focused on steam production as related to your original vertical rotor design. Specifically, people are asking about the volume of steam per minute that is created over a period of time that would determine an average output volume of sustainability. This knowledge, of course, would enable us to determine what size steam engine might be realistically feasible. For example, let's consider the 10 horsepower Green Steam Engine. It has two cylinders, each with a 3.125 inch bore and a 1.125 inch stroke. The displacement of each cylinder is equal to Pi times 2.4414 (the cylinder radius squared) times 1.125, or 8.632ci (cubic inches). Thus the total displacement per revolution is 2 times 8.632, or 17.264. Converted to liters, that would equal 0.28 liter per revolution. Theoretically, then, a 5 hp engine's displacement would be half that amount (0.14 liter), and that of a 2 hp engine would be 0.056 liter. If you require 1 hp to drive the rotor shaft, you would appear to have 1 reserve horsepower left over to perform other work (such as driving an electric generator) if you are using a 2 hp steam engine. You have said that the rotor shaft speed needs to be about 1800 rpm. At 1800 rpm, we would require a volume of steam equal to 1800 x 0.056, or about 100 lpm (liters per minute) to operate a 2 hp steam engine. One drop of distilled water is equal to about .025ml volume. Exploded to steam, at a factor of 1600 to 1, that drop has a volume of 40ml. Thus, it would require 25 exploded drops to equal roughly 1 liter of volume, or 2500 drops per minute to produce 100 lpm of steam, and that equates to about 42 drops per second. Of course the steam would also have to remain at a fairly constant and adequate pressure for a sustained period of time. Operating a 2 hp Green Steam Engine at 1800 rpm would require a pressure of about 50 psi.
I know that you have done some testing at various steam pressures and temperatures. Do you have any test data that you could share with us? Absent any actual output volume measurements, I can compute the steam production volume if I know 4 factors:
1. The sustained psi pressure of the steam.
2. The sustained temperature of the steam.
3. The time period of the sustained test (should be perhaps 10 minutes or more).
4. The amount of water that is fully converted to steam during the test period. I would actually suggest timing the period required to fully convert 1 kilogram of water (1 liter) to steam at a sustained temperature and 50 psi pressure.
Any such data that you can supply will be greatly appreciated, as has all the information that you have so generously shared with us.
Best wishes to you during this Holiday season, and always,
Rick
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Lloyd's reply:
From: LKTanner Sent:Fri 12/12/08 5:44 PM
Hi Rick - Thank you for your email of last Saturday, December 6, 2008. Please forgive me for the delay in getting back to you. I may have told you before that I don't know how to use a computer so I have to have my wife do all of my replies and she has been busy with therapy with her new knee. I really appreciate your interest in this project and want to thank you again for all of your input, time and comments.
In answer to your questions - I am not very educated and therefore I answer these to what I know from my own testing. If you have a 10" diameter roller turning at 1700 r.p.m. or more, I have gotten the floor of the pressure vessel to 700 degrees with 10 lbs. of friction pressure against the friction roller.
I have reached 300 lbs. of pressure in my pressure vessel and have sustained 300 lbs. of pressure by letting the water in and carefully regulating the 1/2 teaspoonful drop of water falling to the floor of the pressure vessel. NOTE: My roller is 3' long and my drops start at one end and drip 4" apart the length of the roller. By the time the drops start at the far end again, the floor of the pressure vessel's first 4'' is back from 500 degrees to 700 degrees - you lose 200 degrees when the drop hits the first 4". The steam in the pressure vessel rises up into the pressure dome and that's where you discharge your steam to run whatever you want to run. If you want more heat, you increase the friction pressure against the friction roller. My water reservoir holds 20 gallons and never runs empty. It feeds my pressure vessel. My water hopper holds 5 gallons and takes about 1/2 hour to empty. It refills in less than 5 minutes.
Note that your water bar [water distribution rail] should be 1" above the floor of the pressure vessel.
We saw an article on CNN the other night about an engineer named Peter Jansson at Rowan University (Glassboro, NJ) who is working with a
gentleman's formula where he adds salt water to a chemical to use as fuel. We continue to be in touch with Rowan and they are very excited about my concept as well.
Best wishes for the holidays to you and your family!
Lloyd L. Tanner
Hi folks,
This post includes my latest correspondence to, and reply from, Lloyd Tanner. Please note that, in his reply, Lloyd is giving details concerning his newer friction roller design, which can feed several pieces of wood simultaneously. With the new design, Lloyd has increased the operating temperature and pressure to 700 degrees @ 300 psi. The new design features a horizontal roller that is 10 inches in diameter, and 36 inches long (full width of trough). It is interesting to note that the amount of water contained in each "drop" is said to be 1/2 teaspoon, which is roughly 2.5 milliliters. As pointed out in my correspondence to Lloyd, a normal droplet of water is about .025 milliliters, and would be just 1/100 of Lloyd's controlled water drop amount. Thus, his water drop is actually a metered amount rather than a natural drip. From Lloyd's description, it would appear that these metered amounts are dropped at 4 inch intervals along the length of the water distribution rail in a linearly progressive manner, from one end of the rail to the other.
My correspondence to Lloyd:
Sent: Sat 12/06/08 4:50 AM
Hi Lloyd,
Thought you might be interested to know that we are currently at over 9,000 views by people interested in your friction heater, and many are interested in building replications. I think that I have been able to answer most questions to the satisfaction of inquirers, but lately the topic of discussion has focused on steam production as related to your original vertical rotor design. Specifically, people are asking about the volume of steam per minute that is created over a period of time that would determine an average output volume of sustainability. This knowledge, of course, would enable us to determine what size steam engine might be realistically feasible. For example, let's consider the 10 horsepower Green Steam Engine. It has two cylinders, each with a 3.125 inch bore and a 1.125 inch stroke. The displacement of each cylinder is equal to Pi times 2.4414 (the cylinder radius squared) times 1.125, or 8.632ci (cubic inches). Thus the total displacement per revolution is 2 times 8.632, or 17.264. Converted to liters, that would equal 0.28 liter per revolution. Theoretically, then, a 5 hp engine's displacement would be half that amount (0.14 liter), and that of a 2 hp engine would be 0.056 liter. If you require 1 hp to drive the rotor shaft, you would appear to have 1 reserve horsepower left over to perform other work (such as driving an electric generator) if you are using a 2 hp steam engine. You have said that the rotor shaft speed needs to be about 1800 rpm. At 1800 rpm, we would require a volume of steam equal to 1800 x 0.056, or about 100 lpm (liters per minute) to operate a 2 hp steam engine. One drop of distilled water is equal to about .025ml volume. Exploded to steam, at a factor of 1600 to 1, that drop has a volume of 40ml. Thus, it would require 25 exploded drops to equal roughly 1 liter of volume, or 2500 drops per minute to produce 100 lpm of steam, and that equates to about 42 drops per second. Of course the steam would also have to remain at a fairly constant and adequate pressure for a sustained period of time. Operating a 2 hp Green Steam Engine at 1800 rpm would require a pressure of about 50 psi.
I know that you have done some testing at various steam pressures and temperatures. Do you have any test data that you could share with us? Absent any actual output volume measurements, I can compute the steam production volume if I know 4 factors:
1. The sustained psi pressure of the steam.
2. The sustained temperature of the steam.
3. The time period of the sustained test (should be perhaps 10 minutes or more).
4. The amount of water that is fully converted to steam during the test period. I would actually suggest timing the period required to fully convert 1 kilogram of water (1 liter) to steam at a sustained temperature and 50 psi pressure.
Any such data that you can supply will be greatly appreciated, as has all the information that you have so generously shared with us.
Best wishes to you during this Holiday season, and always,
Rick
------------------------------------------------------------------
Lloyd's reply:
From: LKTanner Sent:Fri 12/12/08 5:44 PM
Hi Rick - Thank you for your email of last Saturday, December 6, 2008. Please forgive me for the delay in getting back to you. I may have told you before that I don't know how to use a computer so I have to have my wife do all of my replies and she has been busy with therapy with her new knee. I really appreciate your interest in this project and want to thank you again for all of your input, time and comments.
In answer to your questions - I am not very educated and therefore I answer these to what I know from my own testing. If you have a 10" diameter roller turning at 1700 r.p.m. or more, I have gotten the floor of the pressure vessel to 700 degrees with 10 lbs. of friction pressure against the friction roller.
I have reached 300 lbs. of pressure in my pressure vessel and have sustained 300 lbs. of pressure by letting the water in and carefully regulating the 1/2 teaspoonful drop of water falling to the floor of the pressure vessel. NOTE: My roller is 3' long and my drops start at one end and drip 4" apart the length of the roller. By the time the drops start at the far end again, the floor of the pressure vessel's first 4'' is back from 500 degrees to 700 degrees - you lose 200 degrees when the drop hits the first 4". The steam in the pressure vessel rises up into the pressure dome and that's where you discharge your steam to run whatever you want to run. If you want more heat, you increase the friction pressure against the friction roller. My water reservoir holds 20 gallons and never runs empty. It feeds my pressure vessel. My water hopper holds 5 gallons and takes about 1/2 hour to empty. It refills in less than 5 minutes.
Note that your water bar [water distribution rail] should be 1" above the floor of the pressure vessel.
We saw an article on CNN the other night about an engineer named Peter Jansson at Rowan University (Glassboro, NJ) who is working with a
gentleman's formula where he adds salt water to a chemical to use as fuel. We continue to be in touch with Rowan and they are very excited about my concept as well.
Best wishes for the holidays to you and your family!
Lloyd L. Tanner
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