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US4462222A Expired / Lapsed US ⏱️ 0.0 years remaining

Dilute solution producing system of absorption refrigerating apparatus

Assignee: Hitachi Ltd
•
Filing: 1982-12-10
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Granted: 1984-07-31
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Expires: 2002-12-10
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Abstract

Abstract A dilute solution producing system of an absorption refrigerating apparatus wherein spraying of a solution and absorption of a refrigerant gas into the solution take place in a plurality of stages to produce a solution of low concentration. A solution of high concentration is sprayed in a zone of cooling water of high temperature in an absorber and the refrigerant gas is absorbed into the sprayed solution to produce a solution of intermediate concentration, and the solution of intermediate concentration is sprayed in a zone of cooling water of low temperature and the refrigerant gas is absorbed into the sprayed solution to produce a dilute solution as desired.

Inventors

  • 👤 Shigeo Sugimoto
  • 👤 Ryohei Minowa
  • 👤 Kozi Sakai

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 11:56
CPC Classifications
F; F25; F25B; F25B15/00; F25B15/02; F25B15/06; Y; Y02; Y02A; Y02A30/00; Y02A30/27; Y02B; Y02B30/00; Y02B30/62

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 362 words
In an absorption refrigerating apparatus comprising: at least one generator having a heating source for heating a solution to generate a refrigerant in a gaseous state; a condenser for condensing said refrigerant in the gaseous state by cooling into a refrigerant in a liquid state; an evaporator causing the refrigerant in the liquid state to evaporate for performing cooling by utilizing the latent heat of evaporation; an absorber having a refrigerant in a gaseous state produced in said evaporator and a concentrated solution produced in said generator introduced therein to cause the refrigerant in the gaseous state to be absorbed into the concentrated solution to produce a dilute solution; a solution pump for feeding said dilute solution into said generator; and a heat exchanger for causing a heat exchange to take place between the solution flowing into said generator and the solution flowing out of the generator; wherein said absorber has a nest of cooling water tubes comprising a plurality of heat transfer tubes extending from one end of a shell to the other end thereof to allow cooling water to flow into said heat transfer tube through one end thereof and flow out of it through the other end thereof; a dilute solution producing system comprising: spray header means located above said nest of heat transfer tubes in said absorber and divided into a plurality of spray header sections extending in a longitudinal direction of the heat tranfer tubes, a first spray header section located nearest an outlet end of the cooling water being connected to a path of flow of the solution flowing out of said generator so as to spray the solution flowing out of the generator, the solution sprayed by said first spray header section absorbing a refrigerant in a gaseous state so as to produce a solution of intermediate concentration; and at least one solution spray pump for drawing by suction said solution intermediate concentration and feeding same into the next following spray header section, a solution sprayed by the spray header section located nearest an inlet end of the cooling water in the absorber absorbing a refrigerant in a gaseous state to produce a dilute solution.
Claim 2
Dependent Claim 362 words
In an absorption refrigerating apparatus comprising: at least one generator having a heating source for heating a solution to generate a refrigerant in a gaseous state; a condenser for condensing said refrigerant in the gaseous state by cooling into a refrigerant in a liquid state; an evaporator causing the refrigerant in the liquid state to evaporate for performing cooling by utilizing the latent heat of evaporation; an absorber having a refrigerant in a gaseous state produced in said evaporator and a concentrated solution produced in said generator introduced therein to cause the refrigerant in the gaseous state to be absorbed into the concentrated solution to produce a dilute solution; a solution pump for feeding said dilute solution into said generator; and a heat exchanger for causing a heat exchange to take place between the solution flowing into said generator and the solution flowing out of the generator; wherein said absorber has a nest of cooling water tubes comprising a plurality of heat transfer tubes extending from one end of a shell to the other end thereof to allow cooling water to flow into said heat transfer tube through one end thereof and flow out of it through the other end thereof; a dilute solution producing system comprising: spray header means located above said nest of heat transfer tubes in said absorber and divided into a plurality of spray header sections extending in a longitudinal direction of the heat tranfer tubes, a first spray header section located nearest an outlet end of the cooling water being connected to a path of flow of the solution flowing out of said generator so as to spray the solution flowing out of the generator, the solution sprayed by said first spray header section absorbing a refrigerant in a gaseous state so as to produce a solution of intermediate concentration; and at least one solution spray pump for drawing by suction said solution intermediate concentration and feeding same into the next following spray header section, a solution sprayed by the spray header section located nearest an inlet end of the cooling water in the absorber absorbing a refrigerant in a gaseous state to produce a dilute solution.
Claim 3
Dependent Claim 55 words
A dilute solution producing system as claimed in claim 1, wherein said spray header means located above said nest of heat transfer tubes in the absorber is divided into a first spray header section located on the outlet end of the cooling water, and a second spray header section located on the inlet end thereof.
Claim 4
Dependent Claim 32 words
A dilute solution producing system as claimed in claim 2, wherein the area of said first spray header section contributing to spraying is smaller than that of said second spray header section.
Claim 5
Dependent Claim 73 words
A dilute solution producing system as claimed in claim 2, wherein said solution pump is connected to said second spray header section in such a manner that the refrigerant in the gaseous state is absorbed into the solution sprayed from the first spray header section to provide a solution of intermediate concentration, said solution of intermediate concentration being drawn by suction by the solution pump and sprayed from the second spray header section.
Claim 6
Dependent Claim 40 words
A dilute solution producing system as claimed in claim 3, wherein the ratio of the area of the first spray header section contributing to spraying to the area of the second spray header section contributing to spraying is about 38:62.
Claim 7
Dependent Claim 97 words
A dilute solution producing system as claimed in claim 1, wherein said refrigerating apparatus comprises a low temperature generator and a high temperature generator to effect heating of said low temperature generator by a refrigerant of a gaseous state produced by said high temperature generator, and wherein said absorber, solution pump, heat exchanger, low temperature generator and high temperature generator are connected together in such a manner that dilute solution produced by said absorber is fed by said solution pump through said heat exchanger into said low temperature and high temperature generators in parallel to each other.
Claim 8
Dependent Claim 55 words
A dilute solution producing system as claimed in claim 6, wherein said spray header means located above said nest of heat transfer tubes in the absorber is divided into a first spray header section located on the outlet end of the cooling water, and a second spray header section located on the inlet end thereof.
Claim 9
Dependent Claim 32 words
A dilute solution producing system as claimed in claim 7, wherein the area of said first spray header section contributing to spraying is smaller than that of said second spray header section.
Claim 10
Dependent Claim 73 words
A dilute solution producing system as claimed in claim 7, wherein said solution pump is connected to said second spray header section in such a manner that the refrigerant in the gaseous state is absorbed into the solution sprayed from the first spray header section to provide a solution of intermediate concentration, said solution of intermediate concentration being drawn by suction by the solution pump and sprayed from the second spray header section.
Claim 11
Dependent Claim 40 words
A dilute solution producing system as claimed in claim 8, wherein the ratio of the area of the first spray header section contributing to spraying to the area of the second spray header section contributing to spraying is about 38:62.
Claim 12
Dependent Claim 70 words
A dilute solution producing system as claimed in claim 8, further comprising an ejector interposed between the first spray header section and the heat exchanger, a line connected to said ejector at one end and to a discharge side of the solution pump at the other end to introduce a portion of the solution from the solution pump, and a valve mounted in said line midway between the opposite ends.

References Cited (Backward Citations)

US2430047A Cited
US2494972A Cited
US3124938A Cited
US3126720A Cited
US3299667A Cited
US4085595A Cited
JPS5339544A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-07-31 1988-01-30 1988-07-31 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-07-31 1992-01-30 1992-07-31 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-07-31 1996-01-30 1996-07-31 $7700.00 Window Closed / Lapsed

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