Solar powered intermittent operation based continuous absorption system

Patent metadata

Field	Value
Publication number	US-9772128-B2
Application number	US-201414244424-A
Country	US
Kind code	B2
Filing date	Apr 3, 2014
Priority date	Apr 3, 2014
Publication date	Sep 26, 2017
Grant date	Sep 26, 2017

Abstract

An intermittent operation based continuous absorption system (IOBCAS) which supports cooling effect during the daytime without the use of a solution pump is provided. The IOBCAS may utilize an isochoric process for pressurization of the system and the system may include a plurality of generator-absorber units that intermittently operate in succession to provide a continuous refrigeration cooling effect during the daytime. The system of the present disclosure enables the plurality of generator-absorber units to switch between a generation, absorption, and heat recovery mode of operation to provide cooling effect during the daytime which a higher coefficient of performance compared with conventional intermittent system.

First claim

The invention claimed is:

1. An intermittent operation based continuous absorption system comprising:
a plurality of generator-absorber units, each of the plurality of generator-absorber units including a shell and a heat exchanger disposed within the shell;
a heat recovery circuit including a transfer pump to conduct heat recovery;
a solar collection circuit including a solar collector to collect solar thermal energy;
a heat rejection circuit including a heat rejection unit to reject heat; and
a generation circuit including a vapor-liquid heat exchanger unit and an evaporator to provide refrigeration to a cooling load,
wherein each of the heat exchangers of the plurality of generator-absorber units include an internal passage that is in selective fluid communication with the solar collection circuit, the heat rejection circuit, and the heat recovery circuit, and
wherein each of the shells of the plurality of generator-absorber units is in selective fluid communication with the generation circuit.

2. The absorption system of claim 1 , wherein each of the plurality of generator-absorber units include a first inlet valve connected to the solar collection circuit, a second inlet valve connected to the heat rejection circuit, a third inlet valve connected to the heat recovery circuit, and a fourth inlet valve connected to the generation circuit, and
wherein each of the plurality of generator-absorber units include a first outlet valve connected to the solar collection circuit, a second outlet valve connected to the heat rejection circuit, a third outlet valve connected to the heat recovery circuit, and a fourth outlet valve connected to the generation circuit.

3. The absorption system of claim 1 , wherein the generation circuit further includes a dephlegmator and a condenser.

4. The absorption system of claim 3 , wherein the dephlegmator is disposed upstream of the condenser in the generation circuit.

5. The absorption system of claim 1 , wherein the generation circuit further includes a throttling valve, and
wherein the vapor-liquid heat exchanger unit includes a heat exchanger to conduct sub-cooling of refrigerant by heat recovery before the refrigerant is conveyed to the evaporator of the generation circuit via the throttling valve.

6. The absorption system of claim 5 , wherein the vapor-liquid heat exchanger unit, the throttling valve, and the evaporator are disposed in sequential order in an upstream to downstream direction of the generation circuit.

7. The absorption system of claim 1 , wherein the plurality of generator-absorber units include a first generator-absorber unit, a second generator-absorber unit, a third generator-absorber unit, and a fourth generator-absorber unit.

8. A method of operating the absorption system of claim 7 , comprising:
partially pressurizing the first generator-absorber unit and partially depressurizing the third generator-absorber unit, in a first stage of operation, by fluidly connecting the heat exchanger of the first generator-absorber unit to the heat exchanger of the third generator-absorber unit via the heat recovery circuit;
completely pressurizing, in the first stage of operation, the second generator-absorber unit by fluidly connecting the heat exchanger of the second generator-absorber unit to the solar collector via the solar collection circuit;
completely depressurizing, in the first stage of operation, the fourth generator-absorber unit by fluidly connecting the heat exchanger of the fourth generator-absorber unit to the heat rejection unit via the heat rejection circuit; and
throttling refrigerant, in the first stage of operation, through a throttling valve of the generation circuit by fluidly connecting the shell of the fourth generator-absorber unit to the vapor-liquid heat exchanger unit via the generation circuit.

9. The method of operating the absorption system of claim 8 , further comprising:
partially pressurizing the fourth generator-absorber unit and partially depressurizing the second generator-absorber unit, in a second stage of operation, by fluidly connecting the heat exchanger of the second generator-absorber unit to the heat exchanger of the fourth generator-absorber unit via the heat recovery circuit;
completely pressurizing, in the second stage of operation, the first generator-absorber unit by fluidly connecting the heat exchanger of the first generator-absorber unit to the solar collector via the solar collection circuit;
completely depressurizing, in the second stage of operation, the third generator-absorber unit by fluidly connecting the heat exchanger of the third generator-absorber unit to the heat rejection unit via the heat rejection circuit; and
throttling refrigerant, in the second stage of operation, through the throttling valve of the generation circuit by fluidly connecting the shell of the third generator-absorber unit to the vapor-liquid heat exchanger unit via the generation circuit.

10. The method of operating the absorption system of claim 9 , further comprising:
partially pressurizing the third generator-absorber unit and partially depressurizing the first generator-absorber unit, in a third stage of operation, by fluidly connecting the heat exchanger of the first generator-absorber unit to the heat exchanger of the third generator-absorber unit via the heat recovery circuit;
completely pressurizing, in the third stage of operation, the fourth generator-absorber unit by fluidly connecting the heat exchanger of the fourth generator-absorber unit to the solar collector via the solar collection circuit;
completely depressurizing, in the third stage of operation, the second generator-absorber unit by fluidly connecting the heat exchanger of the second generator-absorber unit to the heat rejection unit via the heat rejection circuit; and
throttling refrigerant, in the third stage of operation, through the throttling valve of the generation circuit by fluidly connecting the shell of the second generator-absorber unit to the vapor-liquid heat exchanger unit via the generation circuit.

11. The method of operating the absorption system of claim 10 , further comprising:
partially pressurizing the second generator-absorber unit and partially depressurizing the fourth generator-absorber unit, in a fourth stage of operation, by fluidly connecting the heat exchanger of the second generator-absorber unit to the heat exchanger of the fourth generator-absorber unit via the heat recovery circuit;
completely pressurizing, in the fourth stage of operation, the third generator-absorber unit by fluidly connecting the heat exchanger of the third generator-absorber unit to the solar collector via the solar collection circuit;
completely depressurizing, in the fourth stage of operation, the first generator-absorber unit by fluidly connecting the heat exchanger of the first generator-absorber unit to the heat rejection unit via the heat rejection circuit; and
throttling refrigerant, in the fourth stage of operation, through the throttling valve of the generation circuit by fluidly connecting the shell of the first generator-absorber unit to the vapor-liquid heat exchanger unit via the generation circuit.

Assignees

• Univ King Fahd Pet & Minerals

Inventors

• Said Syed Ahmed Mohammad
• Siddiqui Muhammad Umar

Classifications

• F25B27/007 Primary

  in sorption type systems · CPC title

• F25B17/04

  with two or more boilers operating alternately · CPC title

• Y02B30/62

  Absorption based systems · CPC title

• Y02A30/27

  Relating to heating, ventilation or air conditioning [HVAC] technologies · CPC title

• F25B17/00

  Sorption machines, plants or systems, operating intermittently, e.g. absorption or adsorption type · CPC title