Solid adsorbent heat pump system

• US 4,610,148 A
• Filed: 05/03/1985
• Issued: 09/09/1986
• Est. Priority Date: 05/03/1985
• Status: Expired due to Fees

• Current Assignee: Wave Air Corporation
• Original Assignee: Samuel V. Shelton
• Inventors: Shelton, Samuel V.
• Primary Examiner(s): SOLLECITO, JOHN M
• Application Number:
  US06/729,921
• Time in Patent Office: 494 Days
• Field of Search: 62/101, 62/106, 62/480, 62/115, 62/118
• US Class Current: 62/480
• CPC Class Codes: F25B 17/083 with two or more boiler-sorbers operating alternately
• CPC Class Codes: Y02A 30/27 Relating to heating, ventilation or air conditioning [HVAC] technologies
• CPC Class Codes: Y02B 30/00 Energy efficient heating, ventilation or air conditioning [HVAC]
• CPC Class Codes: Y02B 30/62 Absorption based systems

Abstract

A heat pump system with a pair of solid adsorbent beds connected to a heat pump loop and a reversible heat transfer loop. The heat pump loop has a heater connected between one end of the beds and a cooling heat exchanger connects the other end of the beds so that a heat transfer fluid flowing around the heat transfer loop heats one bed and cools the other with the flow being reversed to cycle the beds and drive the heat pump loop.

Claims

1. A method of operating a heat pump system between an upper operating temperature and a lower operating temperature comprising two solid adsorbent beds connected to the condenser and evaporator in a heat pump circuit so that desorbed refrigerant can flow from the bed by being heated into the condenser and refrigerant from the evaporator can flow into the bed being cooled comprising the steps of:

(a) placing a separate heat exchanger in a heat transfer relationship with each bed and connecting the heat exchangers in series with each other in a closed fluid loop so that heat transfer fluid flows around the closed loop serially through the heat exchangers;

(b) heating the heat transfer fluid passing between one of the ends of the beds to the upper operating temperature;

(c) cooling the heat transfer fluid passing between the other ends of the beds to the lower operating temperature;

(d) circulating the heat transfer fluid around the closed fluid loop serially through the heat exchangers so that the heat transfer fluid passes generally lengthwise of both beds where the circulation rate of the heat transfer fluid is such that the heated heat transfer fluid passing into the end of the bed heats the solid adsorbent bed from an initial cool bed temperature in the vicinity of the lower operating temperature while the bed cools the heat transfer fluid from the upper operating temperature down to about the initial cool bed temperature in a distance less than the length of the bed and with the cooled heat transfer fluid passing into the end of the other bed cooling the solid adsorbent bed from an initial hot bed temperature in the vicinity of the upper operating temperature while the bed heats the heat transfer fluid from the lower operating temperature up to about the initial hot bed temperature in a distance less than the length of the bed;

(e) when the exit temperature of the heat transfer fluid passing out of either of the beds shifts from the initial temperature of that bed by a prescribed amount less than about fifty percent (50%) of the difference between the initial bed temperature and inlet fluid temperature in step (b), changing the circulation of the heat transfer fluid so that the heated heat transfer fluid passes through the cooled bed and the cooled heat transfer fluid passes through the heated bed; and

(f) when the exit temperature of the heat transfer fluid passing out of either of the beds shifts from the initial temperature of that bed by said prescribed amount in step (c), changing the circulation of the heat transfer fluid to step (b) to cycle the beds between the upper and lower operating temperatures.

2. The method of claim 1 wherein the heat transfer fluid is serially circulated through the beds in a first direction lengthwise of the beds during step (b) and in the opposite direction during step (c).

3. The method of claim 1 wherein the initial bed temperature of each of the beds during heating is the temperature to which the bed is raised from the lower operating temperature by pressurizing the bed from evaporator pressure to condenser pressure and the initial bed temperature of each of the beds during cooling is the temperature to which the bed is lowered from the upper operating temperature by depressurizing the bed from condenser pressure to evaporator pressure.

4. The method of claim 1 further including the step of configuring the beds and heat exchangers so that the correlation parameter of the fluid Peclet number of the fluid passing through each bed divided by one plus the thermal conductance ratio of the solid adsorbent bed with the heat transfer fluid passing through the bed is greater than one and less than the bed Biot number.

5. The method of claim 4 wherein the step of configurating the beds further includes configuring the beds and heat exchangers so that the correlation parameter is substantially equal to the square root of the Biot number.

6. The method of claim 1 further including the step of individually adjusting the volumetric flow rate of the heat transfer fluid flowing through each of said beds so that the exit temperature of the heat transfer fluid passing out of both beds shifts from the initial temperature of that bed by the prescribed amount in about the same length of time.

7. A heat pump system comprising:

a pair of solid adsorbent beds;

a heat pump circuit connected to said solid adsorbent beds so that said heat pump circuit is driven in response to the heating and cooling of said beds;

a heat transfer fluid;

a pair of bed heat exchange means, one of said bed heat exchange means operatively associated with each of said beds so that the heat transfer fluid passing through each of said heat exchange means passes lengthwise of said bed associated therewith in a single pass and each of said heat exchange means having opposed ends;

heating means adapted to heat said heat exchange fluid to a prescribed upper operating temperature connecting one of the ends of both of said bed heat exchange means;

cooling means adapted to cool said heat exchange fluid to a prescribed lower operating temperature connecting the other of the ends of both of said bed heat exchange means so that said heat transfer fluid can flow serially from said heating means, through one of said bed heat exchange means, through said cooling means, through the other of said bed heat exchange means and back to said heating means to define a heat transfer circuit;

circulation means for alternatively circulating said heat transfer fluid in one direction around the heat transfer circuit so that one of said beds is cooled while the other of said beds is heated, and in the alternate direction around the heat transfer circuit so that said other of said beds is cooled while said one of said beds is heated where the circulation rate of the heat transfer fluid is such that the heated heat transfer fluid passing into the end of one of said heat exchange means heats said solid adsorbent bed associated therewith from an initial cool bed temperature in the vicinity of the lower operating temperature while said bed cools the heat transfer fluid from the upper operating temperature down to about the initial cool bed temperature in a distance less than the length of said bed and with the cooled heat transfer fluid passing into the end of the other of said heat exchanger means cooling said solid adsorbent bed associated therewith from an initial hot bed temperature in the vicinity of the upper operating temperature while said bed heats the heat transfer fluid from the lower operating temperature up to about the initial hot bed temperature in a distance less than the length of the bed in order for heat exchanged between said heat transfer fluid and each of said beds to generate a thermal wave in the temperature profiles lengthwise of said beds moving through each of said beds; and

control means operatively associated with said heat transfer fluid passing out of said beds and with said circulation means to cause said circulation means to reverse the circulation direction of said heat transfer fluid around said heat transfer circuit when either of the thermal wave reaches that end of said bed from which said heat transfer fluid exits.

8. The heat pump system of claim 7 wherein each of said bed heat exchange means is constructed and arranged so that the correlation parameter of the fluid Peclet number of said heat transfer fluid passing through each of said bed heat exchange means divided by one plus the thermal conductance ratio of said solid adsorbent bed with said heat transfer fluid is greater than one and less than the bed Biot number.

9. The heat pump system of claim 8 wherein each of said bed heat exchange means is constructed and arranged so that said correlation parameters is about the same value as the square root of said bed Biot number.

10. The heat pump system of claim 8 wherein said control means is constructed and arranged to reverse the circulation direction of said heat transfer fluid in said heat transfer circuit when the temperature of said heat transfer fluid exiting either of said beds changes a prescribed amount less than about fifty percent (50%) of the difference between the temperature of said bed when said heat transfer fluid circulation direction was last reversed and the temperature of the heat transfer fluid entering the bed.

11. The heat pump system of claim 7 further including by-pass means connecting the common point between one of said bed heat exchange means and said cooling means with the common point between the other of said bed heat exchange means and said heating means;

and connecting the common point between the other of said bed heat exchange means and said cooling means with the common point between one of said bed heat exchange means and said heating means, said control means operatively connected to said by-pass means to cause said by-pass means to adjust the flow of said heat transfer fluid through said bed heat exchange means so that the thermal waves reach the ends of both of said beds from which said heat transfer fluid exits at about the same time.