Hybrid spray absorber

• US 20100175395A1
• Filed: 01/08/2010
• Published: 07/15/2010
• Est. Priority Date: 01/09/2009
• Status: Active Grant

• Current Assignee: Donald Charles Erickson
• Original Assignee: Donald Charles Erickson
• Inventors: Erickson, Donald Charles
• Granted Patent: US 8,800,318 B2
• Time in Patent Office: Days
• US Class Current: 62/101
• CPC Class Codes: F01K 25/065 with an absorption fluid remaining at least partly in the liquid state, e.g. water for ammonia F01K5/00 takes precedence
• 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 35/00 Boiler-absorbers, i.e. boilers usable for absorption or adsorption
• CPC Class Codes: Y02A 30/27 Relating to heating, ventilation or air conditioning [HVAC] technologies
• CPC Class Codes: Y02B 30/62 Absorption based systems

Abstract

A hybrid absorber is disclosed for a closed absorption cycle apparatus. The hybrid absorber is comprised of a non-adiabatic section plus an adiabatic spray section in that order, with absorbent solution and vapor supplied sequentially to them. The spray section preferably also includes a non-adiabatic spray cooler. Coolant is supplied to the non-adiabatic absorber and the cooler either in parallel or in series, countercurrently to the absorbent.

Claims

1. A hybrid absorber for a closed cycle absorption apparatus, comprised of:

a. a non-adiabatic absorption section;

b. an adiabatic spray absorption section that receives vapor and liquid from said non-adiabatic section; and

c. a recirculating liquid spray loop for said adiabatic section, comprised of a spray pump and a cooler.

2. The apparatus according to claim 1 wherein the absorbent liquid is aqueous ammonia, and the non-adiabatic absorber is a shell and coil configuration.

3. The apparatus according to claim 1 wherein the absorbent liquid is aqueous ammonia, and the non-adiabatic absorber is an air-cooled configuration comprised of fin tubes plus liquid injectors for injecting solution into each tube.

4. The apparatus according to claim 1 wherein the non-adiabatic absorber is a shell and tube configuration.

5. The apparatus according to claim 1 wherein the absorbent liquid is aqueous ammonia, and the non-adiabatic absorber is a wetted surface configuration comprised of tubes wetted on the outside by recirculated spray water plus liquid injectors for injecting solution into each tube.

6. The apparatus according to claim 1 wherein said spray pump also boosts the solution pump that pumps absorbent liquid to the desorber of said absorption apparatus.

7. The apparatus according to claim 1 wherein said spray pump also supplies cooling liquid to the rectifier of said absorption apparatus.

8. The apparatus according to claim 1 wherein said spray pump also supplies coolant to said non-adiabatic absorber and said cooler.

9. The apparatus according to claim 1 additionally comprised of a spray receiver for said solution that has separate suction pipes for the spray pump and the solution pump, plus a partition between the two suctions.

10. The apparatus according to claim 1 wherein said spray pump is also the solution pump that supplies absorbent liquid to the desorber.

11. The apparatus according to claim 1 wherein the absorbent is aqueous ammonia, and the absorber receives vapor from an ammonia expander that produces power.

12. The apparatus according to claim 1 wherein the absorbent is aqueous ammonia, and the absorber receives vapor from an ammonia evaporator that produces refrigeration.

13. The apparatus according to claim 1 wherein the absorbent is aqueous ammonia, and wherein useful heating is supplied by the heat rejected from said non-adiabatic absorber and said cooler.

14. A closed absorption cycle apparatus comprised of:

a. an absorber comprised of a non-adiabatic section followed by an adiabatic spray section, the latter including a spray pump and a cooler;

b. a desorber; and

c. a solution pump that circulates absorbent from said absorber to said desorber.

15. The apparatus according to claim 14 additionally comprised of a spray receiver for said absorbent that receives vapor and liquid from said non-adiabatic absorber;

supplies suction liquid to said spray pump; and

supplies separate suction liquid from under the spray nozzles to said solution pump

16. The apparatus according to claim 15 wherein said absorbent is aqueous LiBr, and additionally comprised of an evaporator and condenser.

17. The apparatus according to claim 15 wherein said absorbent is aqueous ammonia, and additionally comprised of an evaporator and condenser.

18. The apparatus according to claim 15 additionally comprised of an expander that is supplied high pressure vapor from said desorber and supplies low pressure vapor to said absorber, and wherein said absorbent is aqueous ammonia.

19. An absorption process for producing at least one of refrigeration, heat pumping, and power from a heat source, comprising:

a. desorbing vapor from an absorbent liquid with said heat source;

b. absorbing the vapor at lower pressure into the desorbed liquid in a multi-step process comprised of;

i. partially absorbing the vapor in a non-adiabatic absorber;

ii. absorbing the residual vapor in an adiabatic spray absorber; and

iii. recirculating and cooling the spray liquid.

20. The process according to claim 19 additionally comprising using aqueous ammonia as the absorbent.