Posted 27 November 2010 - 01:53 PM
Newtech:
You continue to be confused for a variety of reasons. One reason is that I was unable to make comments and notes on your PowerPoint sketch. That is why I always recommend that members use an Excel spreadsheet to make their sketches if they want comments and recommendations made on them. That is a quick and accurate way to exactly indicate where the comment is made and why.
Another reason seems to be because you don’t have the proper (or enough) learning in refrigeration thermodynamics. I have seen our Forums change recently and noted that the Personal Background feature was removed. This, in my opinion, is bad when dealing with students. I am unable to tell or know what level of learning or experience you have or where you are located. The more personal background I have, the better I can tailor my responses so that the member can better understand what I am trying to convey. From what you write I get the impression that you don’t have a thorough grasp of what is happening in a normal, conventional mechanical refrigeration cycle. Have you read and studied the Chiller Tutorial Workbook that I uploaded for you? Have you gone over the sample calculations I did? Did you study and understand what is shown in the process flow diagram I drew? Did you fully understand what is happening in each of the different components within the refrigeration cycle? Do you completely understand the concept of phase equilibria and the importance of distinguishing and establishing different fluid PHASES within the same system? Have you plotted your refrigeration system and cycle on the Mollier (or T-S) diagram?
If you haven’t done the above, then that could explain why you are having difficulties understanding what is happening. You return with additional (actually, the same questions – but with a different slant) queries and my responses are – again, in RED – as follows:
But Art the control valve before the evaporator is just a normal level control valve.
This is true. However, the type or make of the valve means nothing from a thermodynamic point of view. What is important is that the relatively higher pressure liquid refrigerant (which is saturated) enters the evaporator on demand by the liquid level in the same evaporator. Once it enters the evaporator, it is subjected to a lower pressure – which is part of the driving force that allowed it to enter. This action constitutes what is called in thermodynamics as an irreversible, adiabatic expansion (defined as a process where the enthalpy is held constant). If you use your Mollier Diagram (or T-S chart) you will see that the constant enthalpy expansion from 17.64 to 5.2 kg/cm2g will yield a R-22 mixture within the “dome” that defines the saturated liquid and vapor lines. The “normal level control valve” (the expansion valve) merely allows the HP R-22 to enter the evaporator; the action of the R-22 compressor is what is maintaining a constant, 5.5 kg/cm2 pressure in the evaporator. The valve does NOT CREATE refrigeration. It is the maintenance of the evaporator pressure by the compressor which allows for the fluid expansion to take place. The valve is merely a tool to maintain the constant liquid level. It is important that you tell me if you know and understand what I just stated. If you don’t, we can’t continue in trying to show you how mechanical refrigeration works from an engineering point of view.
In the tube side of the evaporator is glycol entering at 12.8 oC and is being cooled to 5.5 oC. So it means the heat from the glycol is being transfered to the liquid freon and it evaporates and cools the rest of the remaining liquid freon inside.
You are correct in stating that there is heat transferred from the glycol to the liquid Freon. HOWEVER, the evaporation of the Freon due to its receiving Latent Heat DOES NOT cause further cooling of the remaining Freon in the evaporator. As explained above, it is the compressor that causes the refrigeration cycle to operate due to its removal of the saturated vapor produced by the latent heat added by the glycol. REMEMBER: the evaporator has SATURATED Freon liquid and vapor, so the liquid Freon is subject to being vaporized by the addition of latent heat.
Lets say the glycol return back to the evaporator at about 5.5 oC, which means lesser heat or no is being transfered to the liquid freon. The freon inside should boil by it self as it has reach the boiling point for that pressure? Pressure drop, temperature will also drop, but the amount of heat energy inside is the same.
If the glycol enters at a temperature close to that of the liquid R-22, then the heat transferred will diminish or stop. When that happens, the compressor will suck less R-22 vapors (since there is less – or no - vapor being produced) in order to keep the vapor pressure in the evaporator at the set point of 5.2 kg/cm2g. You are producing less refrigeration because it is not required. The liquid Freon does not evaporate anymore. It just sits there – still in the saturated state – waiting to receive latent heat from the warm glycol. (You continue to worry me by not specifically identifying the state and phase of your fluids. If you are describing the SATURATED LIQUID Freon inside the evaporator, then state is as such. DO NOT describe it as “freon inside should boil”. This is probably one of the reasons for your confusion.
Alcohol evaporates and produce a cooling effect, just like it touches your skin, it takes heat from your skin and evaporates, thats why you feel cold.
Correct. This is the effect that you detect when you apply alcohol on your skin and the heat transfer mechanism that makes it work.
If a 45 oC alcohol poured on your skin, would you still feel the coolness or would you feel a 45 oC alcohol?
Yes, you would. Stop and apply the previous correct statement you made. Even though the alcohol is much warmer than your body and there can be no heat transferred from your body to the alcohol, the alcohol is still subject to Mr. Dalton’s Law. It will exert a vapor pressure to fulfill the need to have all the Partial Pressures equal to atmospheric. When that happens, the alcohol is vaporizing – because it is “expanding” (actually, vaporizing & cooling) into a vapor phase due the action of partial pressures. The dryer the atmospheric air is, the faster the evaporation – and the subsequent cooling of the film of alcohol remaining on the skin surface. It is the driving force of partial pressures that allows the alcohol to evaporate and cool. The moment all the liquid alcohol on the skin surface is evaporated, the cooling ceases and you have to apply more liquid in order to continue the effect. Note that once the alcohol starts to cool due to partial pressure evaporation, there will follow a normal heat transfer from your skin surface to the cooled liquid alcohol. This then raises the temperature of the residual alcohol and also raises the partial pressure of the alcohol – so the evaporation process continues (but only as long as the atmosphere can take the contributing partial pressure addition of alcohol vapors).
I think i am lost too deep, to be found back.
Don’t give up trying. If you do, you will force me to stop helping you.
As i do not understand 45 oC at 17 kg/cm2, pressure drop to 5.2 kg/cm2 it should vaporize immediately as it is 45 oC, at that low pressure its boiling is lower. But yet it has so much heat, so all of the liquid has enough energy to flash.
Read the above paragraph and tell me what fluid you are writing about. As I stated before, you are not writing clearly and therefore communicating very badly. Please correct this defect for your own good. If you are referring to the HP liquid R-22, then state so. I believe that you are and I have explained already what is happening in the “expansion” of this fluid. But I will repeat it again (because it such an important point): The HP R-22 liquid fluid entering the “expansion” valve is in the SATURATED state. If you locate it on a Mollier Diagram and follow it along its constant enthalpy line to a pressure of 5.3 kg/cm2g, you will discover that you are inside the phase “dome” of the diagram. This dome defines the CRITICAL POINT and the saturated liquid (left-hand side) and vapor (right-hand side) phases. You should already have been taught this material and should know how to employ it to find data and to make calculations.
I hope that the above detailed explanations help you understand and also to communicate accurately and correctly.