Intermittent absorption refrigeration system with an ejector

Patent metadata

Field	Value
Publication number	US-9441863-B2
Application number	US-201414259100-A
Country	US
Kind code	B2
Filing date	Apr 22, 2014
Priority date	Apr 22, 2014
Publication date	Sep 13, 2016
Grant date	Sep 13, 2016

Abstract

The intermittent absorption refrigeration system with an ejector includes a generator/absorber unit, a solar collector unit, a dephlegmator, a condenser unit, a first evaporator, and valves to control the flow of aqua-ammonia coolant through the system, as in a conventional intermittent absorption refrigeration system. However, the present system also includes an ejector disposed between the dephlegmator and the condenser, and also a second evaporator disposed in a feedback loop between the first evaporator and the ejector, together with appropriate valves to control coolant flow through the feedback loop. The utilization of the ejector and the feedback loop in the intermittent system allows the intermittent system to produce a cooling effect during the daytime, as well as during the nighttime, which increases the coefficient of performance of the intermittent system.

First claim

We claim:

1. An intermittent absorption refrigeration system with an ejector, comprising:
a primary refrigerant loop having:
a combination generator/absorber unit having a generator heat exchanger and an absorber heat exchanger;
a dephlegmator connected to the combination generator/absorber unit;
the ejector selectively connected to the dephlegmator;
a condenser unit connected to a diffuser;
a first evaporator unit selectively connected to the condenser and selectively connected to the combination generator/absorber unit;
a solar collector unit selectively connected to the generator heat exchanger of the combination generator/absorber unit; and
aqua-ammonia coolant circulating between the combination generator/absorber unit, the dephlegmator, the condenser unit, and the first evaporator unit so that the combination generator/absorber unit, the dephlegmator, the condenser unit, the first evaporator unit, the solar collector unit and the aqua-ammonia coolant define a solar-powered intermittent absorption system operable to generate liquid ammonia refrigerant for storage in the first evaporator unit in daytime and to produce a refrigerant effect in the first evaporator unit and absorb the refrigerant in the combination generator/absorber unit at nighttime; and
a refrigerant feedback loop having:
a second evaporator unit;
a first conduit disposed between the first evaporator unit and the second evaporator unit;
a ball valve and a throttling valve disposed in series in the first conduit between the evaporator units, the ball valve and the throttling valve being selectively openable in the daytime to produce a refrigerant effect in the second evaporator unit;

a second conduit disposed between the second evaporator and the ejector; and
a feedback valve disposed in the second conduit, the feedback valve being selectively openable in the daytime to feed the liquid ammonia refrigerant back to the ejector for flow to the condenser and the first evaporator unit;

whereby the intermittent absorption refrigeration system is operable to produce a refrigerant effect during both the daytime and the nighttime.

2. The intermittent absorption refrigeration system with an ejector of claim 1 , wherein the dephlegmator unit is located above the generator/absorber unit.

3. A method of producing refrigerant effects in an intermittent absorption refrigeration system during both daytime and nighttime, comprising the steps of:
during the daytime, pressurizing a combination generator/absorber unit while blocking flow of coolant through an absorber heat exchanger in the combination generator/absorber unit in order to heat a cold, strong aqua-ammonia solution in the combination generator/absorber unit, generating aqua-ammonia vapor;
rectifying the aqua-ammonia vapor in a dephlegmator to produce pure ammonia vapor, water being condensed from the aqua ammonia vapor and returned to the combination generator/absorber unit;
flowing the pure ammonia vapor through an ejector and into a condenser unit;
condensing the ammonia vapor to form liquid ammonia;
storing the liquid ammonia in a first evaporator unit during the daytime;
drawing a portion of the liquid ammonia from the first evaporator unit into a second evaporator unit;
producing a refrigeration effect drawn off by a heat exchanger in the second evaporator unit during the daytime, thereby forming saturated ammonia vapor in the second evaporator unit;
inducting the saturated ammonia vapor from the second evaporator unit into the ejector;
mixing the saturated ammonia vapor from the second evaporator unit with the pure ammonia vapor from the dephlegmator in the ejector, whereby a portion of the liquid ammonia is continuously cycled through a feedback loop comprising the ejector, the condenser unit, the first evaporator unit and the second evaporator unit to produce refrigerant effects during the daytime;
at nighttime, depressurizing the combination generator/absorber unit while isolating the feedback loop from the combination generator/absorber unit and the dephlegmator;
after depressurizing the combination generator/absorber unit, opening a ball valve and a throttling valve between the first evaporator unit and the combination generator/absorber unit, thereby reducing pressure and producing a refrigerant effect in the first evaporator unit during the nighttime by evaporation of the stored liquid ammonia, producing ammonia vapor;
throttling the ammonia vapor through the throttling valve into the combination generator/absorber unit; and
absorbing the ammonia vapor in the aqua-ammonia solution in the combination generator/absorber unit during the nighttime.

4. The method of producing refrigerant effects according to claim 3 , wherein said step of pressurizing the combination generator/absorber unit comprises the steps of:
opening valves in conduits connecting a solar collection unit to a generator heat exchanger in the combination generator/absorber unit to apply heat to the aqua-ammonia solution; and
closing valves connecting a coolant to the absorber heat exchanger in the combination generator/absorber unit to prevent cooling the aqua-ammonia solution during pressurization.

5. The method of producing refrigerant effects according to claim 4 , wherein said step of pressurizing the combination generator/absorber unit comprises the steps of:
closing the valves in the conduits connecting the solar collection unit to the generator heat exchanger in the combination generator/absorber unit;
opening the valves connecting the coolant to the absorber heat exchanger in the combination generator/absorber unit to cool the aqua-ammonia solution during depressurization; and
keeping the ball valve and the throttling valve between the first evaporator unit and the combination generator/absorber unit closed during depressurization of the combination generator/absorber unit.

Assignees

• Univ King Fahd Pet & Minerals

Inventors

• Said Syed A M
• Siddiqui Muhammad Umar

Classifications

• F25B17/02 Primary

  the absorbent or adsorbent being a liquid, e.g. brine (F25B17/10 takes precedence) · CPC title

• F25B27/007

  in sorption type systems · CPC title

• F25B41/00

  Fluid-circulation arrangements · CPC title

• Y02B30/62

  Absorption based systems · CPC title

• Y02A30/27

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