Refrigeration apparatus and method

• US 5,873,260 A
• Filed: 04/02/1997
• Issued: 02/23/1999
• Est. Priority Date: 04/02/1997
• Status: Expired due to Fees

• Current Assignee: Harold L. Jackson
• Original Assignee: Harold L. Jackson
• Inventors: Rosener, Joseph Jr., Linhardt, Hans D.
• Primary Examiner(s): DOERRLER, WILLIAM CHARLES
• Application Number:
  US08/832,478
• Time in Patent Office: 692 Days
• Field of Search: 62/101, 62/476, 62/497
• US Class Current: 62/497
• CPC Class Codes: B01D 61/362 Pervaporation
• CPC Class Codes: F25B 15/02 without inert gas F25B15/004, F25B15/006, F25B15/008, F25B15/12, F25B15/14, F25B15/16 take precedence
• CPC Class Codes: F25B 15/04 the refrigerant being ammonia evaporated from aqueous solution F25B15/025 takes precedence
• CPC Class Codes: F25B 33/00 Boilers; Analysers; Rectifiers boiler-absorbers F25B35/00

Abstract

A refrigeration cycle combines a concentrated absorbent liquid and a refrigerant in its vapor phase at low pressure in an absorber which provides, as an output, a liquid-rich refrigerant in solution with the absorbent liquid. The pressure of the absorbent/refrigerant solution is increased and the pressurized solution is supplied to a pervaporation membrane separator which provides as one output stream a vapor-rich refrigerant and as another output stream a concentrated liquid absorbent. The liquid-rich refrigerant output stream is condensed and subsequently expanded to a low pressure into an evaporator where it evaporates extracting heat from the spaced to be cooled. The concentrated liquid absorbent output stream from the separator is reduced in pressure and recombined in the absorber with the low pressure refrigerant vapor exiting the evaporator.

Claims

1. A refrigeration cycle using as a working fluid a refrigerant and a concentrated liquid absorbent comprising:

a) combining the concentrated absorbent liquid and the refrigerant substantially in its vapor phase at low pressure in an absorber while extracting heat to provide a liquid-rich refrigerant in solution with the absorbent liquid;

b) increasing the pressure of the absorbent/refrigerant solution;

c) separating the refrigerant from the absorbent liquid in a pervaporation selective membrane separator which provides as one output a vapor-rich refrigerant and as another output a concentrated absorbent liquid;

d) condensing the vapor output of the membrane separator to provide a liquid-rich refrigerant in a first condenser;

e) expanding the liquid-rich refrigerant from a high to a low pressure into an evaporator where it is evaporated at low temperature and pressure with heat added to provide a substantially vaporized low pressure refrigerant;

f) reducing the pressure of the concentrated absorbent liquid from the membrane separator to substantially equalize the pressure between the absorbent liquid and the low pressure substantially vaporized refrigerant; and

g) returning the low pressure concentrated absorbent liquid and the substantially vaporized refrigerant to the absorber in repetition of the cycle.

2. The refrigeration cycle of claim 1 wherein the refrigerant is ammonia and the absorbent is water.

3. The refrigeration cycle of claim 2 wherein the expansion operation of the refrigerant from the first to the lower pressure is provided by an expansion valve.

4. The refrigeration cycle of claim 3 wherein the expansion operation of the refrigerant from the first to the lower pressure is provided by an expansion turbine.

5. The refrigeration cycle of claim 3 wherein the pressure of the substantially vaporized refrigerant input to the absorber is less than 50 psia.

6. The refrigeration cycle of claim 1 further including exchanging heat between the concentrated absorbent liquid output from the membrane separator and the pressurized absorbent/refrigerant solution.

7. The refrigeration cycle of claim 6 further including increasing the pressure of the vaporized refrigerant vapor prior to its return to the absorber.

8. The refrigeration cycle of claim 7 further including:

removing heat from the vapor-rich refrigerant exiting said pervaporation membrane separator (hereinafter the "first separator"), separating additional refrigerant from the absorbent in a second pervaporation membrane separator having as one output an enriched vapor refrigerant and as another output concentrated absorbent liquid;

supplying the vapor output of the second membrane separator to the condenser and then to the evaporator; and

recombining the concentrated absorbent liquid from the second membrane separator with the absorbent/refrigerant solution entering the first membrane separator.

9. The refrigeration cycle of claim 8 further including exchanging heat between the vapor-rich refrigerant output stream from the first separator and the pressurized absorbent/refrigerant solution.

10. The refrigeration cycle of claim 5 wherein the pressure of the absorbent/refrigerant solution entering the membrane separator is within the range of about 250 to 400 psia.

11. A process for cooling or heating comprising:

a) combining a refrigerant substantially in its vaporized form at a low pressure with a concentrated absorbing liquid while extracting heat to provide a resulting dilute solution of liquid-rich refrigerant and absorbing liquid;

b) pumping the absorbent/refrigerant solution to a higher pressure;

c) passing the pressurized absorbent/refrigerant solution through a pervaporation membrane separator to separate the solution into two streams, one stream comprising primarily a vapor-rich refrigerant and the other stream comprising a concentrated absorbent liquid;

d) substantially condensing the vapor output from the membrane separator to provide a liquid-rich refrigerant;

e) passing the liquid-rich refrigerant stream through an expansion element to reduce the pressure and temperature thereof;

f) passing the liquid-rich refrigerant through an evaporator while adding heat to allow a substantial portion of the refrigerant to vaporize;

g) adjusting the pressure of the vaporized refrigerant from the evaporator and the concentrated liquid absorbent from the membrane to substantially the same pressure; and

h) repeating steps a-g above.

12. The process of claim 11 further including the steps of:

(i) passing the liquid-rich refrigerant from step d through an additional pervaporation membrane separator to separate the liquid into an enriched vapor-rich refrigerant as one stream and an additional concentrated absorbent liquid as another stream;

(j) condensing the enriched vapor-rich refrigerant stream;

(k) continuing step e with the enriched liquid refrigerant stream; and

(l) recombining the additional concentrated absorbent liquid with the absorbent/refrigerant solution prior to step b.

13. The process of claim 12 further including the step of:

(m) compressing the vapor refrigerant output stream from the evaporator.

14. The process of claim 13 further including the step of:

(n) exchanging heat between the output concentrated absorbent liquid stream from the membrane separator with the pressurized absorbent/refrigerant solution.

15. The process of claim 14 further including the step of:

(o) exchanging heat between the pressurized absorbent/refrigerant solution and vapor-rich refrigerant from the first pervaporation membrane separator.

16. In a refrigeration system for extracting energy in the form of heat from a desired space by utilizing as a working fluid a refrigerant in solution with an absorbent, the combination comprising:

a first pervaporation membrane separator for separating an absorbent/refrigerant solution into two streams, one stream comprising primarily refrigerant in its vapor state and the other stream comprising a concentrated liquid absorbent/refrigerant solution;

a condenser in fluid communication with the membrane assembly for condensing the refrigerant vapor stream into substantially a liquid;

a pressure reducer in fluid communication with the condenser for reducing the temperature of the liquid refrigerant stream output of the condenser by expanding it to a lower temperature;

an evaporator in fluid communication with the pressure reducer and said space to be cooled for transferring energy from said space to substantially evaporate the refrigerant;

an absorber for recombining the vaporized refrigerant from the evaporator and the concentrated absorbent/refrigerant solution from the membrane separator;

pressure regulating means connected between the absorber, the membrane separator and the evaporator for substantially equalizing the pressures of the concentrated absorbent/refrigerant solution and the vapor refrigerant entering the absorber; and

a pump in fluid communication with the absorber and the membrane separator for supplying the recombined refrigerant and absorbent from the absorber to the membrane separator under pressure.

17. The system of claim 16 further including a second pervaporation membrane connected in series between the refrigerant output of the first membrane separator and the condenser.

18. The system of claim 17 further including a compressor connector in series between the evaporator and the absorber.

19. A refrigeration cycle using as a working fluid a solution of refrigerant and an absorbent dissolvable in the refrigerant comprising:

a) separating a portion of liquid-rich refrigerant from an absorbent/refrigerant solution in a first pervaporation membrane separator at a first pressure, the membrane separator assembly providing as one output stream a vapor comprising primarily the refrigerant and as another output stream a liquid comprising primarily the absorbent solution;

b) condensing the vapor stream from the separator into a liquid-rich refrigerant;

c) expanding the liquid-rich refrigerant stream from the condenser to a low pressure into an evaporator where it is evaporated at low temperature with heat added to provide a substantially low pressure vapor;

d) adjusting the pressure of the vaporized refrigerant to substantially a second pressure;

e) adjusting the pressure of the concentrated absorbent/refrigerant solution from the separator to substantially said second pressure;

f) combining the concentrated absorbent/refrigerant solution and the substantially vaporized refrigerant in an absorber at said second pressure while extracting heat to provide a liquid-rich refrigerant in solution with the absorbent;

f) increasing the pressure of the solution to the first pressure; and

g) returning the pressurized solution to the separator.

20. The cycle of claim 19 further including a second membrane for separating additional absorbent from the refrigerant-rich vapor exiting the first membrane separator.