Method and apparatus for transferring energy in an absorption heating and cooling system

• US 4,152,901 A
• Filed: 12/21/1976
• Issued: 05/08/1979
• Est. Priority Date: 12/30/1975
• Status: Expired due to Term

• Current Assignee: ABet CARL Munters
• Original Assignee: ABet CARL Munters
• Inventors: Munters, Carl G.
• Primary Examiner(s): King, Lloyd L.
• Application Number:
  US05/752,730
• Time in Patent Office: 868 Days
• Field of Search: 62/107, 62/112, 62/480, 62/494, 62/495, 62/79
• US Class Current: 62/112
• CPC Class Codes: B01D 61/025 Reverse osmosis; Hyperfiltration
• CPC Class Codes: B01D 61/026 comprising multiple reverse osmosis steps
• CPC Class Codes: F25B 15/14 using osmosis F25B15/004, F25B15/006, F25B15/008 take precedence
• CPC Class Codes: F25B 29/006 of the sorption type system
• CPC Class Codes: F25B 30/04 of the sorption type

Abstract

A method and apparatus for transferring energy in an absorption system according to the heat pump principle to improve the cycle efficiency thereof, in which the selected working medium is vaporized in an evaporator by heat exchange with heat source of ambient pressure and passed into a sorption station where it is brought into contact with an absorbent solution with consequent release of heat of absorption and heat of condensation. The mixture of absorbent solution and absorbed working medium is passed from the sorption station into a pressurized separating station, where the absorbent is separated from the working medium by diffusing the mixture under pressure through a semi-permeable membrane defining a zone of relatively high pressure and a zone of relatively low pressure higher than the ambient pressure, the concentrated absorbent solution being collected in the high pressure zone and the solution of working medium being received in the low pressure zone by virtue of the resultant reverse osmotic flow. The dilute solution of working medium is passed to the evaporator upon being depressurized, while the concentrated absorbent solution, upon being reduced to the ambient pressure, is passed into the sorption station.

Claims

1. In a closed absorption system based on the heat pump principle, in which a solution of working medium is vaporized in an evaporator by heat exchange with an energy source and the vaporized solution is passed into an absorber where it is brought into contact with an absorbent solution, the heat of condensation being removed from the absorber for use to condition an enclosure, the improvement comprising:

(a) a pressure sealed separation means having a high pressure and a low pressure zone;

(b) a semi-permeable membrane defining said high pressure zone and said low pressure zone;

(c) means for passing a mixture of absorbent solution and working medium into said separator means;

(d) means for pressurizing said mixture effective to separate and collect a concentrated solution of absorbent in said high pressure zone and the working medium solution in said low pressure zone by reverse osmotic flow through said semi-permeable membrane;

(e) energy transfer means between said high pressure zone and said absorber to depressurize said concentrated absorbent solution;

(f) means for passing said pressurized concentrated absorbent solution through said energy transfer means into said absorber;

(g) expansion means connected to said evaporator; and

(h) means for passing said separated working solution through said expansion means to said evaporator.

2. The absorption system according to claim 1, in which a heat exchanger is located in the absorber for picking up the heat of condensation and connected to an energy transfer appliance located in an enclosure to be conditioned.

3. The absorption system according to claim 1, in which the energy transfer means for depressurizing the concentrated absorbent solution comprises turbine means.

4. The absorption system according to claim 3, comprising pump means located between the absorber and the separation means for pressurizing the mixture of absorbent solution and absorbed working medium.

5. The absorption system according to claim 4, in which said turbine means are effective to actuate said pump means.

6. The absorption system according to claim 2, in which the separating means comprise a plurality of units each comprising a semi-permeable membrane and interconnected in a closed circuit to carry out the concentration of the mixture of absorbent solution and working medium in successive steps.