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Metalworking (rec.crafts.metalworking) Discuss various aspects of working with metal, such as machining, welding, metal joining, screwing, casting, hardening/tempering, blacksmithing/forging, spinning and hammer work, sheet metal work. |
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#201
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SCFM vs. CFM, also air flow/pressure across a regulator
Don Foreman writes:
It might be interesting to put a thermocouple on a regulator, wrap the lot in thermal insulation, run it for a while and see what happens. Did you ever pop open the overpressure relief valve, and let it run for a few minutes to bleed a full tank? No thermocouple needed to feel that result. |
#202
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SCFM vs. CFM, also air flow/pressure across a regulator
Ted Edwards writes:
P=V x I x Cos(angle) P=V x I x abs(Cos(angle)) ? |
#203
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SCFM vs. CFM, also air flow/pressure across a regulator
Gary Coffman writes:
Now try it without the regulator. You can't do it as many times, because energy stored in the tank has been *wasted* at each fill, ie the pressure in the cylinder and tank equalize each time you open the fill valve even though that's more energy than you *need* to lift the weight one foot, and that excess energy is lost when you vent the cylinder. This is a clear case where the *absence* of a regulator wastes energy. It is in fact the *usual* case. You are correct that with-the-regulator beats without-the-regulator, but compressing-the-air-to-50-psi-to-start-with beats them both, which is to say, if mechanical efficiency is the figure of merit, then a regulator on a high-pressure supply is wasteful compared to an unregulated source at the application pressure. |
#204
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SCFM vs. CFM, also air flow/pressure across a regulator
Gary Coffman writes:
Therefore, the heat in the regulator *is* directly proportional to the regulator temperature. The system in view consists of the regulator and the air, not just the regulator. If the air expands, this system can decrease in temperature while gaining heat. And furthermore, the air flow can segregate the heat and temperatures, so some parts of the system get colder and some hotter (in temperature). |
#205
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SCFM vs. CFM, also air flow/pressure across a regulator
Gary Coffman writes:
A *rate* is a measure of how quickly *something* else is converted, moved, or otherwise transferred past an observation point. It is that *something else*, in this case energy, which does the moving. You say that a "rate" is "not an actual thing that moves". By your logic, then "energy" is not a thing either, it is just a rate at which molecules pass by at some density. When you get down to the philosophical underpinnings, a "thing" in physics is just whatever you can measure, which is to say, something sensible in any quantitative manner, whether by direct human sense or via intermediate instruments. Do you believe in electrons, or in holes, or both, or what? |
#206
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SCFM vs. CFM, also air flow/pressure across a regulator
Gary Coffman writes:
Power doesn't dissipate. Hitler had power, and was dissipated. I hereby invoke Godwin's Law to close this thread. |
#207
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SCFM vs. CFM, also air flow/pressure across a regulator
Gary Coffman writes:
dissipationless dynamic resistance Get a patent on that. |
#208
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SCFM vs. CFM, also air flow/pressure across a regulator
In article , Richard J Kinch
says... I'll agree to this as your definitional retreat. "Defintional Retreat?" That's where the terms and phrases used have a precise meaning, in accordance with accepted principles of science. I can live with that. Jim ================================================== please reply to: JRR(zero) at yktvmv (dot) vnet (dot) ibm (dot) com ================================================== |
#209
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SCFM vs. CFM, also air flow/pressure across a regulator
In article , Richard J Kinch
says... Temperature and heat content are not always related. In an ideal gas, they are. Another definitional retreat - or simply the contents of an introductory textbook? I'll let you make the call on that. Jim ================================================== please reply to: JRR(zero) at yktvmv (dot) vnet (dot) ibm (dot) com ================================================== |
#211
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SCFM vs. CFM, also air flow/pressure across a regulator
"Gary Coffman" wrote in message
... dissipationless dynamic resistance of a vacuum tube, So why do my plates glow when they are overbiased? Do you recommend I grab onto a 6L6 for more than 30 seconds? Tim -- "That's for the courts to decide." - Homer Simpson Website @ http://webpages.charter.net/dawill/tmoranwms |
#212
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SCFM vs. CFM, also air flow/pressure across a regulator
On Tue, 06 Jan 2004 03:24:22 -0600, Richard J Kinch
wrote: Don Foreman writes: I've always thought of temperature as proportional to heat content in joules or calories times specific heat of the material holding it. If that were always true, you couldn't have air conditioning, or an ice cold drink. You're right. I was thinking only of the metal in the regulator when we said "the regulator gets cold". However, if the regulator is colder than ambient then it is not dissipating energy as heat. (If anything it's recovering some heat from the environment, some of which was put there at the compressor during compression.) If the regulator isn't losing energy to the environment in the form of heat, then all energy coming in with the high pressure gas must be going out with the lower-pressure gas -- so where's the loss in the regulator? |
#213
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SCFM vs. CFM, also air flow/pressure across a regulator
On Tue, 06 Jan 2004 04:04:40 -0600, Richard J Kinch
wrote: Gary Coffman writes: Now try it without the regulator. You can't do it as many times, because energy stored in the tank has been *wasted* at each fill, ie the pressure in the cylinder and tank equalize each time you open the fill valve even though that's more energy than you *need* to lift the weight one foot, and that excess energy is lost when you vent the cylinder. This is a clear case where the *absence* of a regulator wastes energy. It is in fact the *usual* case. You are correct that with-the-regulator beats without-the-regulator, but compressing-the-air-to-50-psi-to-start-with beats them both, which is to say, if mechanical efficiency is the figure of merit, then a regulator on a high-pressure supply is wasteful compared to an unregulated source at the application pressure. Yes, at the system level. It still has NOT been shown how any energy remains in the regulator, or leaves it other than in the downstream airflow, if the regulator doesn't get warmer. If energy out = energy in, then there's no net loss at the regulator. We've looked at other parts of the system and thought we accounted for the energy and so inferred or deduced that there must be loss in the regulator, but we've all failed to show how any energy leaves the regulator other than in the gas going to the point of use. Geez, my regulator is only 2 feet from me. Hope it ain't emitting Xrays! |
#214
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SCFM vs. CFM, also air flow/pressure across a regulator
Don Foreman writes:
If energy out = energy in, then there's no net loss at the regulator. Sez who? The "loss" is in the conversion of some of the useful-energy-in into waste-heat-out and entropy-out. Whether this waste heat stays in the regulator to raise its temperature, versus being carried downstream, doesn't change the fact that the regulator directly caused the waste. Remember that part of the loss is also in the form of work performed on the ambient atmosphere, not heat. |
#215
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SCFM vs. CFM, also air flow/pressure across a regulator
On Thu, 08 Jan 2004 01:13:24 -0600, Richard J Kinch
wrote: Don Foreman writes: If energy out = energy in, then there's no net loss at the regulator. Sez who? The "loss" is in the conversion of some of the useful-energy-in into waste-heat-out and entropy-out. Whether this waste heat stays in the regulator to raise its temperature, versus being carried downstream, doesn't change the fact that the regulator directly caused the waste. Remember that part of the loss is also in the form of work performed on the ambient atmosphere, not heat. What waste? Heat is still energy. If the downstream air is colder than ambient then heat is not lost by conduction or radiation to ambient, so that energy is still in the downstream gas. Maybe we're getting closer to understanding, though. We've agreed that a certain amount (mass) of air is compressed, and some heat is lost in that process. Compression to higher pressure results in more work being converted to heat (usually lost) at the compressor or in the reservoir as that air cools by conduction to ambient -- and perhaps a little radiation as well. But what about after that, as in from just before the regulator to point of exhaust? I think that was the original question. Adding heat from the regulator to the air downstream of the compressor will raise it's temperature above what it would otherwise be, hence it's volume at regulated pressure, so less high-pressure air will be required per unit volume of air at regulated pressure. However, air exhausting to atmosphere from the point of use will carry heat with it, the amount of heat depending on it's temperature. The warmer the exhaust gas is (even if below ambient temp), the more heat (hence energy) is lost by that route. Maybe *that's* where the thus-far unaccounted-for energy goes. I'll admit to being a bit disappointed that you, with your impressive academic credentials, didn't clear this up many messages ago. It was said somewhere along the line that I am incredibly stubborn. That's true. I don't care a bit about "winning the argument" or "being the one that's right" but I'm admittedly stubborn as hell about persisting until I understand and continuing to question "expert exhortations" until I understand. I have the greatest respect for those who will teach and share, am not a bit impressed with wizards who may know but can't or won't help others to know and understand as well. Perhaps my age is showing? |
#216
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SCFM vs. CFM, also air flow/pressure across a regulator
On Tue, 06 Jan 2004 04:31:22 -0600, Richard J Kinch wrote:
Gary Coffman writes: dissipationless dynamic resistance Get a patent on that. Lee DeForest beat me to it by about 100 years. Gary |
#217
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SCFM vs. CFM, also air flow/pressure across a regulator
On Tue, 6 Jan 2004 10:21:33 -0500, Ned Simmons wrote:
In article , says... This is a clear case where the *absence* of a regulator wastes energy. It is in fact the *usual* case. This is like saying there is no loss in a shunt regulator because it can be used to supply the proper voltage to a device that may self destruct or draw excessive current in the absence of the regulator. (Just had to work in an electrical analogy.) No! It is not even remotely similar. A shunt regulator accepts *every bit of energy the source is capable of supplying* at any given moment, passes part of it to the load, and converts the rest of it to heat in the shunt resistance. All right. Yet another bad electrical analogy. I oughta know better by now. An air regulator valves *just enough* energy from the tank to satisfy the load at any given moment. No more. The rest *remains in the tank*. Then please respond to my previous post and explain how you're going to determine whether the water removed from a reservoir, or the air released from a pressurized tank, was used to do mechanical work, or simply released to the environment. If you're correct it will be possible to tell without looking beyond the boundaries of the reservoir or tank. If I'm correct, and I am, you have to *look* downstream to see whether the water or air released was usefully employed. There's no way to determine that from inside the tank. Fortunately, a regulator is a feedback device, it does "look" downstream to see what the load demand is, and adjusts itself to just supply that demand. In other words, it looks at the downstream pressure and adjusts the flow just enough to maintain the pressure at the set value. It lets no more air through than is required to supply the energy the load demands. Gary |
#218
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SCFM vs. CFM, also air flow/pressure across a regulator
On Tue, 6 Jan 2004 15:01:54 -0600, "Tim Williams" wrote:
"Gary Coffman" wrote in message .. . dissipationless dynamic resistance of a vacuum tube, So why do my plates glow when they are overbiased? Do you recommend I grab onto a 6L6 for more than 30 seconds? Tim I can't lay my hands on my receiving tube manual at the moment, but I do have an RCA transmitting tube manual at hand so I'll use the 813 as my example. It has a filament voltage of 10 volts at 5 amps. So this converts electrical energy to heat at the rate of 50 watts. That makes the tube envelope hot, but is not part of the tube's dynamic resistance. It is a parasitic loss, necessary for a vacuum tube's operation, but not part of the energy flow it is controlling. Note that a transistor wouldn't have this loss, nor does an air regulator. Static plate voltage is 2250 volts, and static plate current is 50 mA. So the static plate resistance is 2250/0.05 = 45,000 ohms, and energy is dissipated at the plate at a rate of 112.5 watts. This is due to the kinetic impact of electrons on the plate. Again, this is necessary to the tube's operation, but isn't part of the energy it is controlling. A transistor would have a similar static collector current and collector dissipation, but an air regulator would not. The dynamic resistance is 8,800 ohms, and the energy controlled, but not dissipated, by that dynamic resistance is at a rate of 573.75 watts. None of that is consumed by the tube. The dynamic resistance of a tube is the slope of the load line drawn on the characteristic curves of the tube. It exists because of the throttling effect of grid voltage on plate current. An air regulator has a similar load line, or lossless dynamic resistance, controlled by the feedback to the regulator diaphragm and pintle valve. Gary |
#219
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SCFM vs. CFM, also air flow/pressure across a regulator
On Tue, 06 Jan 2004 04:04:40 -0600, Richard J Kinch wrote:
Gary Coffman writes: Now try it without the regulator. You can't do it as many times, because energy stored in the tank has been *wasted* at each fill, ie the pressure in the cylinder and tank equalize each time you open the fill valve even though that's more energy than you *need* to lift the weight one foot, and that excess energy is lost when you vent the cylinder. This is a clear case where the *absence* of a regulator wastes energy. It is in fact the *usual* case. You are correct that with-the-regulator beats without-the-regulator, but compressing-the-air-to-50-psi-to-start-with beats them both, which is to say, if mechanical efficiency is the figure of merit, then a regulator on a high-pressure supply is wasteful compared to an unregulated source at the application pressure. It isn't the regulator which is wasteful. The energy loss is in the compressor you're asking to pump to a higher tank pressure. And no surprise, it is the compressor which gets hot as it does so. *That's* where the energy loss in your scenario occurs, not in the regulator. The regulator itself has nearly zero loss, as my example of drawing down a filled tank to supply a load shows. Gary |
#220
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SCFM vs. CFM, also air flow/pressure across a regulator
In article , Gary Coffman says...
Get a patent on that. Lee DeForest beat me to it by about 100 years. LOL Almost exactly 100 years. Not that *he* understood anything about that. I take it you've seen or read "empire of the air?" Jim ================================================== please reply to: JRR(zero) at yktvmv (dot) vnet (dot) ibm (dot) com ================================================== |
#221
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SCFM vs. CFM, also air flow/pressure across a regulator
On Tue, 06 Jan 2004 03:42:57 -0600, Richard J Kinch
wrote: Ted Edwards writes: After all, they are concerend with an upper linmit on the order of 20 or so KW. A few tens or hundreds of watts is a long way below full scale. I always thought they could track a night light. They run at incredibly slow rpms. We have some HOA customers with a meter pedestal and a meter feeding a 4-zone irrigation timer - figure a watt or two to run the timer, and 2 or 3 watts when there's a solenoid valve open. 30 years later, and the watthour meter reads 0000014. Watt-hour meters can record infintessimally small currents like that over the long term, but you can't see it to use the information in the short term. If the disk turns 1 degree... -- Bruce -- -- Bruce L. Bergman, Woodland Hills (Los Angeles) CA - Desktop Electrician for Westend Electric - CA726700 5737 Kanan Rd. #359, Agoura CA 91301 (818) 889-9545 Spamtrapped address: Remove the python and the invalid, and use a net. |
#222
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SCFM vs. CFM, also air flow/pressure across a regulator
Don Foreman writes:
What waste? Heat is still energy. If the downstream air is colder than ambient then heat is not lost by conduction or radiation to ambient, so that energy is still in the downstream gas. The point of the dispute was whether overcompressing and then regulating back down to application pressure was more/less/equally efficient compared to just compressing to application pressure (or just above). In short, are regulators inherently "lossy". Yes, air regulators are inherently lossy. The answer is, all other things being equal, overcompressing/regulating-down is always *less* efficient, in a degree increasing with the degree of overcompression and down-regulating. This is not to say that practical considerations won't make the inefficiency necessary. For example, you may have only one supply pipe across a building going to a variety of tools, and you therefore need to transmit the pressure for the highest-pressure tool. Or your pipes may be too small to transmit enough air at lower pressure. Or you may need very close regulation of the application pressure and widely varying delivery volumes. If I may risk another analogy, compressing and transmitting air at excess pressure (above what is needed for the application) is *not* an efficiency measure like boosting voltage up and down for long-distance electric power transmission. Maybe we're getting closer to understanding, though. We've agreed that a certain amount (mass) of air is compressed, and some heat is lost in that process. Compression to higher pressure results in more work being converted to heat (usually lost) at the compressor or in the reservoir as that air cools by conduction to ambient -- and perhaps a little radiation as well. But what about after that, as in from just before the regulator to point of exhaust? I think that was the original question. Yes, that was the original question. But the answer is, regulators are lossy, even if you assume the compressor is 100 percent efficient and lossless. |
#223
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SCFM vs. CFM, also air flow/pressure across a regulator
Gary Coffman writes:
It exists because of the throttling effect of grid voltage on plate current. An air regulator has a similar load line, or lossless dynamic resistance, controlled by the feedback to the regulator diaphragm and pintle valve. I know what you mean by dynamic resistance (at 47 today, mine was the last electrical engineering class in 1975 to study vacuum tube circuit design). But I don't follow the lossless. Forget the vacuum tube details like filament power. Assume they are perfect valves. Electronic charge is conserved in the device, so the current-in equals current-out. But voltage-out is less than voltage-in (definition of a regulator or valve). Thus power-out (voltage times current) is less than power-in, and the difference is the inherent loss. "Resistance" is force, ergo work, ergo loss. Doesn't matter if it is "dynamic" or not, or if it is charge or air flowing. |
#224
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SCFM vs. CFM, also air flow/pressure across a regulator
Gary Coffman writes:
It isn't the regulator which is wasteful. The energy loss is in the compressor you're asking to pump to a higher tank pressure. And no surprise, it is the compressor which gets hot as it does so. *That's* where the energy loss in your scenario occurs, not in the regulator. No. The compressor can be assumed perfect. THE MAXIMUM ATTAINABLE WORK DOWNSTREAM OF A RESTRICTION IS NECESSARILY LESS THAN UPSTREAM OF THAT RESTRICTION. The operating principle of a conventional regulator is a restriction. It is just a valve with a feedback arrangement on the handle Restrictions are lossy. Otherwise we'd be using the thinnest possible air hoses instead of paying for big ones. The regulator itself has nearly zero loss, as my example of drawing down a filled tank to supply a load shows. I've lost track of who is exhibiting what. But this waving of hands with Boyle's law and energy being P*V is flawed analysis. It shouldn't even take analysis. It should be obvious, anything that impedes the flow of compressed air has got to be robbing power. |
#225
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SCFM vs. CFM, also air flow/pressure across a regulator
In article , Richard J Kinch
says... It should be obvious, anything that impedes the flow of compressed air has got to be robbing power. This is fundamentally incorrect. An orifice that restricts flow does not disipate power. Consider an expansion valve in a refrigeration system. Your approach also fails at one end point, where the restriction prevents only a tiny bit of flow, almost none. YOu sould say this is the *lossiest* case - but it isn't. If you insist on approaching the issue with an incorrect view like this, you would never be able to model the real world behavior of these devices. Jim ================================================== please reply to: JRR(zero) at yktvmv (dot) vnet (dot) ibm (dot) com ================================================== |
#226
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SCFM vs. CFM, also air flow/pressure across a regulator
In article , Richard J Kinch
says... Yes, that was the original question. But the answer is, regulators are lossy, even if you assume the compressor is 100 percent efficient and lossless. The process you describe (compressing to a higher pressure and then regulating down to the point of use) may be less efficient, overall. But the statement 'regulators are lossy' is incomplete and inaccurate in light of the overall system you describe. There is no dissipation in the regulator itself. Jim ================================================== please reply to: JRR(zero) at yktvmv (dot) vnet (dot) ibm (dot) com ================================================== |
#227
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SCFM vs. CFM, also air flow/pressure across a regulator
jim rozen writes:
An orifice that restricts flow does not disipate power. You make a clear statement of what is obviously false, for any plain meaning of "dissipate power". The maximum attainable work from a compressed air source, being drawn through a close restriction, is less than the maximum work attainable drawn through a more open restriction. That difference is the loss of power directly attributable to the difference in restriction. This is true whether one presumes isothermal or adiabadic conditions, or for any ambient pressure, etc. It seems hopeless to correct your misunderstanding. Nevertheless, I presume you try not to pinch your air hoses, even though you believe restricting flow doesn't "dissipate power". |
#228
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SCFM vs. CFM, also air flow/pressure across a regulator
jim rozen writes:
There is no dissipation in the regulator itself. I hope this isn't a quibble over what "dissipation" means. There is a loss of power attributable to the regulator, as a measure of the input versus the output pressure and mass flow. The body of the regulator itself need not gain the waste heat. |
#229
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SCFM vs. CFM, also air flow/pressure across a regulator
Richard J Kinch wrote:
Gary Coffman writes: It isn't the regulator which is wasteful. The energy loss is in the compressor you're asking to pump to a higher tank pressure. And no surprise, it is the compressor which gets hot as it does so. *That's* where the energy loss in your scenario occurs, not in the regulator. No. The compressor can be assumed perfect. THE MAXIMUM ATTAINABLE WORK DOWNSTREAM OF A RESTRICTION IS NECESSARILY LESS THAN UPSTREAM OF THAT RESTRICTION. The operating principle of a conventional regulator is a restriction. It is just a valve with a feedback arrangement on the handle Restrictions are lossy. Otherwise we'd be using the thinnest possible air hoses instead of paying for big ones. The regulator itself has nearly zero loss, as my example of drawing down a filled tank to supply a load shows. I've lost track of who is exhibiting what. But this waving of hands with Boyle's law and energy being P*V is flawed analysis. It shouldn't even take analysis. It should be obvious, anything that impedes the flow of compressed air has got to be robbing power. The velocity and turbulence downstream of the orifice is essentially wasted. That's a lot of kinetic energy that is doing no useful work. However, all this discussion of where the heat/energy is lost has little to do with using air to do mechanical work. Compressor inefficiency is also not really the issue. If we set Pressure*Volume equal to some constant, it takes more work, even with an ideal compressor, as P goes up and V goes down. A system that reverses that downstream wastes all of that extra work. I'm saying work because even an ideal compressor piston will have to exert a greater force when filling a tank that is at a higher pressure. That is not waste heat or bypassed air, just an unavoidable fact. |
#230
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SCFM vs. CFM, also air flow/pressure across a regulator
In article , Richard J Kinch
says... I hope this isn't a quibble over what "dissipation" means. It's not a quibble. This is not a simple question, and gaining a good understanding of the principles in operation require rigorous use of terms. Jim ================================================== please reply to: JRR(zero) at yktvmv (dot) vnet (dot) ibm (dot) com ================================================== |
#231
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SCFM vs. CFM, also air flow/pressure across a regulator
In article , Richard J Kinch
says... Nevertheless, I presume you try not to pinch your air hoses, even though you believe restricting flow doesn't "dissipate power". Read the previous comments about series regulators. Then go back and read them again. The reason that one employs hoses or pipes large enough to carry the flow is *not* to avoid thermal losses. It's to ensure that full pressure is available at the point of use. To reiterate what has been said a dozen times befo Any energy not used remains in the reservoir, behind the restriction. Jim ================================================== please reply to: JRR(zero) at yktvmv (dot) vnet (dot) ibm (dot) com ================================================== |
#232
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SCFM vs. CFM, also air flow/pressure across a regulator
I have a bunch of tube manuals in three or four arms reach -
I suspect the glowing plates on the 6L6 is a Beam tube. I suspect the Screen voltage is a bit high or the Grid voltage is a bit in the positive direction (should be negative DC and modulate that.) If the Grid is near zero and you drive over into the + side - the Grid pre-accelerates boiling electrons gathering on the hot cathode - IIRC thorium enhanced book still in shelf. When the grid pre-accelerates - the screen post accelerates as it should, but at a higher current density now - due to the assist. The plate physically gets smacked with electrons. Normal amount and the plates can keep their cool. To much and they get hot or melt a hole. I don't recommend anyone touch any hot tube if it is half the length of a cig lighter. More than that, and the wattage can far exceed the capacity of your skin to self cool. a.k.a. burn. I myself use 5881's two matched pair to drive my Mono output transformer. :-) Martin Gary Coffman wrote: On Tue, 6 Jan 2004 15:01:54 -0600, "Tim Williams" wrote: "Gary Coffman" wrote in message . .. dissipationless dynamic resistance of a vacuum tube, So why do my plates glow when they are overbiased? Do you recommend I grab onto a 6L6 for more than 30 seconds? Tim I can't lay my hands on my receiving tube manual at the moment, but I do have an RCA transmitting tube manual at hand so I'll use the 813 as my example. It has a filament voltage of 10 volts at 5 amps. So this converts electrical energy to heat at the rate of 50 watts. That makes the tube envelope hot, but is not part of the tube's dynamic resistance. It is a parasitic loss, necessary for a vacuum tube's operation, but not part of the energy flow it is controlling. Note that a transistor wouldn't have this loss, nor does an air regulator. Static plate voltage is 2250 volts, and static plate current is 50 mA. So the static plate resistance is 2250/0.05 = 45,000 ohms, and energy is dissipated at the plate at a rate of 112.5 watts. This is due to the kinetic impact of electrons on the plate. Again, this is necessary to the tube's operation, but isn't part of the energy it is controlling. A transistor would have a similar static collector current and collector dissipation, but an air regulator would not. The dynamic resistance is 8,800 ohms, and the energy controlled, but not dissipated, by that dynamic resistance is at a rate of 573.75 watts. None of that is consumed by the tube. The dynamic resistance of a tube is the slope of the load line drawn on the characteristic curves of the tube. It exists because of the throttling effect of grid voltage on plate current. An air regulator has a similar load line, or lossless dynamic resistance, controlled by the feedback to the regulator diaphragm and pintle valve. Gary -- Martin Eastburn, Barbara Eastburn @ home at Lion's Lair with our computer NRA LOH, NRA Life NRA Second Amendment Task Force Charter Founder |
#233
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SCFM vs. CFM, also air flow/pressure across a regulator
"Martin H. Eastburn" wrote in message
... If the Grid is near zero and you drive over into the + side - the Grid pre-accelerates boiling electrons gathering on the hot cathode - IIRC thorium enhanced book still in shelf. 811 is an example of a directly heated thoriated tungsten cathode; 6L6 uses an indirectly heated unipotential oxide coated cathode. Also, red plates are simply too much dissipation, on a 6L6 at say, 400V screen and plate, you'll get glowing around oh, -20Vg. I don't recommend anyone touch any hot tube if it is half the length of a cig lighter. More than that, and the wattage can far exceed the capacity of your skin to self cool. a.k.a. burn. And that rule of thumb (and fingers, and hands, and anything else that might contact a hot tube doesn't apply at all to Hept'AU7: http://webpages.charter.net/dawill/I...tAU7_Front.jpg For all that size, weight and heat it only puts out 7W. But that's plenty (unless I'm listening to Metallica, anyway). :-) Tim -- "That's for the courts to decide." - Homer Simpson Website @ http://webpages.charter.net/dawill/tmoranwms |
#234
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SCFM vs. CFM, also air flow/pressure across a regulator
jim rozen writes:
To reiterate what has been said a dozen times befo Any energy not used remains in the reservoir, behind the restriction. Let me show the absurdity of this, one more time. Say we operate a compressed air system at some specific requirement of a given mass flow and pressure (forget the "cfm" canard for now and just specify it mass flow). The mass flow of air is the same everywhere in the output circuit, starting with what leaves the compressor/reservoir, which then goes into the regulator, and then out of the regulator. The pressure drops across the regulator, the volume of a unit of gas mass expands, but the mass flow is still the same everywhere. This is just conservation of mass, aka Kirchoff's law. You say the reservoir can be kept at an excess pressure, then regulated down, and the energy output from the reservoir is the same in either case, the difference "not used remains in the reservoir". But the *mass flow* at the reservoir is *equal* in either case, while the reservoir output pressure is different. Thus the energy flow out of the reservoir is higher with the regulator, and lower without. The difference is being wasted by the regulator. This difference does not "stay in the reservoir", it has gone into the output. You don't even need to know any equations for how energy relates to mass and pressure, just that energy in compressed air is an increasing function of both mass and pressure. This should all be clear enough with simple mechanical intuition. No need for quantitative thermodynamic analysis. |
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SCFM vs. CFM, also air flow/pressure across a regulator
In article , Richard J Kinch
says... No need for quantitative thermodynamic analysis. As I said before, you cannot understand compressible gas flow in systems, using electrical analogies. I will go out on a further limb and suggest that one cannot understand the same subject, with a mechanical analogy either. It's not the same. It doesn't *work*. This is why thermodynamics was invented. Jim ================================================== please reply to: JRR(zero) at yktvmv (dot) vnet (dot) ibm (dot) com ================================================== |
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SCFM vs. CFM, also air flow/pressure across a regulator
jim rozen wrote:
As I said before, you cannot understand compressible gas flow in systems, using electrical analogies. Hi Jim, Mass flow isn't an analogy - its the real thing, and conservation of mass is real. Mass into the system must equal mass out. There is no way around that. The rocket engine folks use mass flow all the time. Mass flow is normally used with gasses (except of course in compressor specifications!), volume flow with liquids. Thinking of mass flow as current (its the same in all parts of a series circuit), and pressure as voltage, the electrical analogy works reasonably well (although the ideal fluid resistor is nonlinear). Fitch |
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SCFM vs. CFM, also air flow/pressure across a regulator
On Fri, 09 Jan 2004 16:24:31 -0600, Richard J Kinch
wrote: Don Foreman writes: What waste? Heat is still energy. If the downstream air is colder than ambient then heat is not lost by conduction or radiation to ambient, so that energy is still in the downstream gas. The point of the dispute was whether overcompressing and then regulating back down to application pressure was more/less/equally efficient compared to just compressing to application pressure (or just above). In short, are regulators inherently "lossy". Yes, air regulators are inherently lossy. The answer is, all other things being equal, overcompressing/regulating-down is always *less* efficient, in a degree increasing with the degree of overcompression and down-regulating. This is not to say that practical considerations won't make the inefficiency necessary. For example, you may have only one supply pipe across a building going to a variety of tools, and you therefore need to transmit the pressure for the highest-pressure tool. Or your pipes may be too small to transmit enough air at lower pressure. Or you may need very close regulation of the application pressure and widely varying delivery volumes. If I may risk another analogy, compressing and transmitting air at excess pressure (above what is needed for the application) is *not* an efficiency measure like boosting voltage up and down for long-distance electric power transmission. Maybe we're getting closer to understanding, though. We've agreed that a certain amount (mass) of air is compressed, and some heat is lost in that process. Compression to higher pressure results in more work being converted to heat (usually lost) at the compressor or in the reservoir as that air cools by conduction to ambient -- and perhaps a little radiation as well. But what about after that, as in from just before the regulator to point of exhaust? I think that was the original question. Yes, that was the original question. But the answer is, regulators are lossy, even if you assume the compressor is 100 percent efficient and lossless. Answer offered is an assertion still dodging the question of where claimed lost energy might go. This is not a response worthy of an annointed scholar. |
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SCFM vs. CFM, also air flow/pressure across a regulator
"Don Foreman" wrote in message
news Answer offered is an assertion still dodging the question of where claimed lost energy might go. This is not a response worthy of an annointed scholar. Well certainly you have power (err...that's not energy...so just go integrate will ya?) dissipated in the compressor as it compresses the air, and you likewise have a cooling at the regulator... the power lost in turbulence (and moving the whatever downstream from it, that is, any mechanical work, such as a tool, or blowing along more air if it's an open leak) is where the actual power flows from input (mechanical compression) to output. That seems obvious enough to me. Tim -- "That's for the courts to decide." - Homer Simpson Website @ http://webpages.charter.net/dawill/tmoranwms |
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SCFM vs. CFM, also air flow/pressure across a regulator
jim rozen writes:
No need for quantitative thermodynamic analysis. As I said before, you cannot understand compressible gas flow in systems, using electrical analogies. I will go out on a further limb and suggest that one cannot understand the same subject, with a mechanical analogy either. It's not the same. It doesn't *work*. This is why thermodynamics was invented. My simple qualitative analysis (consisting of mass conservation plus energy being an increasing function of increasing mass and/or pressure) fully disproves your assertions. Thermodynamics is fine, I can do thermo, but it is more than needed, difficult to display in ASCII, and elaborate enough to provide perpertual-motion theorists (like you are starting to sound like) with endless quibbling points. |
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SCFM vs. CFM, also air flow/pressure across a regulator
Don Foreman writes:
Yes, that was the original question. But the answer is, regulators are lossy, even if you assume the compressor is 100 percent efficient and lossless. Answer offered is an assertion still dodging the question of where claimed lost energy might go. The "assertion" I have fully analyzed several times now. I am not gonna repeat that. No dodging. I offered four destinations for the missing energy: friction at the orifice, sonic noise, turbulence downstream, work done on the atmosphere by the expansion. Depending on the regulator design, the proportion of each will vary. |
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