Process for producing cold and/or heat by use of an absorption cycle with carbon dioxide as working fluid

• US 4,433,554 A
• Filed: 07/16/1982
• Issued: 02/28/1984
• Est. Priority Date: 07/16/1982
• Status: Expired due to Fees

• Current Assignee: Institut Francais Du Petrole, Interamerican Zinc, Inc.
• Original Assignee: Institut Francais Du Petrole
• Inventors: Rojey, Alexandre, Cheron, Jacques
• Primary Examiner(s): King, Lloyd L.
• Application Number:
  US06/399,158
• Time in Patent Office: 592 Days
• Field of Search: 62/101, 62/112, 62/476, 252/67
• US Class Current: 62/112
• CPC Class Codes: C09K 5/047 for absorption-type refrigeration systems
• CPC Class Codes: F25B 15/12 with resorber F25B15/004, F25B15/006, F25B15/008, F25B15/14 take precedence
• CPC Class Codes: F25B 29/006 of the sorption type system
• CPC Class Codes: Y02A 30/27 Relating to heating, ventilation or air conditioning [HVAC] technologies
• CPC Class Codes: Y02B 30/62 Absorption based systems
• CPC Class Codes: Y02P 20/10 Process efficiency

Abstract

Process for producing cold and/or heat, making use of an absorption cycle and wherein carbon dioxide is the working fluid, comprising the steps of:

(a) heating a solution L₁ of carbon dioxide in a liquid solvent so as to obtain a carbon dioxide gaseous phase G₁ and a desorbed liquid phase S₁,

(b) dissolving said gaseous phase in a liquid solvent S₂ therefor while removing the evolved heat,

(c) heating under reduced pressure the solution obtained in step b so as to desorb a carbon dioxide phase G₂ therefrom and form a desorbed liquid phase S₃,

(d) admixing S₁ and G₂ at the pressure level of G₂ while removing heat and increasing the pressure of the resulting solution L₃ to the pressure of L₁ and recycling it at least partially to step a, and

(e) recycling at least a portion of S₃ to step b after recompression to the pressure level of G₁, in order to reconstitute S₂.

Claims

1. A process for producing cold and/or heat, making use of an absorption cycle, characterized by the steps of:

(a) subjecting a solution (L1) of carbon dioxide in a liquid phase comprising a solvent for carbon dioxide to heating, under at least partial carbon dioxide desorption conditions, so as to form a gaseous phase (G1) of carbon dioxide and a desorbed liquid phase (S1), and separating the phase (G1) from the phase (S1),

(b) admixing the gaseous phase (G1) with a liquid phase (S2) comprising a solvent for carbon dioxide and removing the heat evolved, so as to dissolve at least a portion of the gaseous phase (G1) into the solvent liquid phase (S2) and to obtain a solution (L2) of carbon dioxide in the solvent liquid phase (S2),

(c) decreasing the pressure of solution (L2) and subjecting said solution to heating, under conditions of at least partial desorption of carbon dioxide, so as to form a gaseous phase (G2) of carbon dioxide and a desorbed liquid phase (S3), and separating the phase (G2) from the phase (S3),

(d) decreasing the pressure of the desorbed liquid phase (S1) substantially to the pressure level of phase (G2) and admixing the phase (S1) with the phase (G2) while removing the evolved heat, so as to obtain a solution (L3) of the phase (G2) in the phase (S1),

(e) increasing the pressure level of solution (L3) substantially to the pressure level of solution (L1) and then feeding back at least a portion of solution (L3), after recompression, to step (a) so as to reconstitute at least a portion of solution (L1), and

(f) increasing the pressure level of the desorbed liquid phase (S3) substantially to the pressure level of the gaseous phase (G1) and then feeding back at least a portion of the liquid phase (S3), after recompression, to step (b) so as to reconstitute at least a portion of the liquid phase (S2).

2. A process according to claim 1, wherein the solution (L2) produced in step (b), before proceeding to step (c), is subjected to a heat exchange with the liquid phase (S3) or (S2).

3. A process according to claim 1, wherein the solution (L3) or (L1) is subjected to a heat exchange with the liquid phase (S1) discharged from step (a).

4. A process according to claim 1, wherein the solvent of carbon dioxide is the same in step (a) and in step (b).

5. A process according to claim 1, wherein the solution (L3) of step (d) directly communicates with the desorbed liquid phase (S3) of step (c) so as to maintain substantially constant the levels of the solution (S3) and of the liquid phase (S3).

6. A process according to claim 3, wherein the heat exchange of solution (L3) or (L1) with the liquid phase (S1) is effected after the latter has been subjected to a pressure decrease in step (d) and has been admixed with at least a portion of the gaseous phase (G2).

7. A process according to claim 1, wherein the solution (L2) is subjected, before being transferred to step (c), to a heat exchange with the liquid phase (S3), said exchange being effected before subjecting the liquid phase (S3) to a pressure increase in step (f), said heat exchange resulting in the formation of a gaseous phase (G3) of carbon dioxide from the liquid phase (S3), and wherein said gaseous phase (G3) is separated from the residual liquid phase (S3), the so-separated gaseous phase (G3) is admixed with the liquid phase (S1) previously subjected to the pressure decrease in step (d) and the residual liquid phase (S3) is then subjected to a pressure increase in step (f).

8. A process according to claim 7, wherein the product obtained by admixing the separated gaseous phase (G3) with the liquid phase (S1) is subjected thereafter to the heat exchange with the solution (L3) or (L1).

9. A process according to claim 8, wherein at least a portion of the gaseous phase (G2) is admixed with the gaseous phase (G3) before said heat exchange.