JPH08296922A - Cogeneration type absorption refrigerating machine - Google Patents

Cogeneration type absorption refrigerating machine

Info

Publication number
JPH08296922A
JPH08296922A JP7103597A JP10359795A JPH08296922A JP H08296922 A JPH08296922 A JP H08296922A JP 7103597 A JP7103597 A JP 7103597A JP 10359795 A JP10359795 A JP 10359795A JP H08296922 A JPH08296922 A JP H08296922A
Authority
JP
Japan
Prior art keywords
cooling water
pressure regenerator
heat
low pressure
power generating
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP7103597A
Other languages
Japanese (ja)
Inventor
Makoto Fujiwara
誠 藤原
Kanji Otake
幹治 大武
Masayoshi Toyofuku
正嘉 豊福
Akira Fukushima
亮 福島
Akihiro Kawada
章広 川田
Kenzo Inoue
健三 井上
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP7103597A priority Critical patent/JPH08296922A/en
Publication of JPH08296922A publication Critical patent/JPH08296922A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y02A30/274Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems
    • Y02B30/625Absorption based systems combined with heat or power generation [CHP], e.g. trigeneration

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Abstract

PURPOSE: To enable effective recovery of a holding heat quantity of cooling water of power generating equipment which has been abandoned heretofore and to enhance a refrigerating capacity by a method wherein the cooling water discharged from the power generating equipment is led to a low pressure regenerator and circulated and the heat of the cooling water is used as a heat source of the low pressure regenerator. CONSTITUTION: A cogeneration type absorption regrigerating machine 205 is equipped with a high pressure regenerator 301, a low pressure regenerator 303, an absorber 304, a condenser 305 and an evaporator 306. The heat of exhaust gas 202 coming out from power generating equipment 201 such as a gas engine is used as a heat source of the high pressure regenerator 301 of the absorption refrigerating machine 205 and thereby regeneration of an LiBr solution 302 is conducted. In this case, cooling water 206 discharged from the power generating equipment 201 is led to the low pressure regenerator 303 so that a holding heat quantity of the cooling water be recovered, and the cooling water is used also for regeneration of the LiBr solution 302 herein. Thereby the holding heat quantity of the cooling water is recovered effectively and the refrigerating capacity of the absorption refrigerating machine is improved in a large degree by the same quantity of power generation.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明はコージェネ型吸収冷凍機
に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cogeneration type absorption refrigerator.

【0002】[0002]

【従来の技術】図2は従来のコージェネ型吸収冷凍機の
第1の例の系統図である。図において201は発電装
置、202は同発電装置から排出される排ガス、203
は同排ガスを利用した排ガスボイラ、204は同排ガス
ボイラから生成される蒸気、205は同蒸気を利用する
吸収冷凍機、206は前記発電装置へ循環させる冷却
水、207は同冷却水を冷却する冷却器である。
2. Description of the Related Art FIG. 2 is a system diagram of a first example of a conventional cogeneration type absorption refrigerator. In the figure, 201 is a power generator, 202 is exhaust gas discharged from the power generator, 203
Is an exhaust gas boiler using the same exhaust gas, 204 is steam generated from the same exhaust gas boiler, 205 is an absorption refrigerator using the same steam, 206 is cooling water circulated to the power generator, and 207 is cooling the same cooling water. It is a cooler.

【0003】上記装置は、発電装置201から出る排ガ
ス202を排ガスボイラ203に導き一旦蒸気204を
発生させ、この蒸気で吸収冷凍機205を駆動し冷水を
発生させる方式のものである。
The above-mentioned device is a system in which exhaust gas 202 emitted from a power generator 201 is guided to an exhaust gas boiler 203 to temporarily generate steam 204, and this steam drives an absorption refrigerator 205 to generate cold water.

【0004】図3は従来のコージェネ型吸収冷凍機の第
2の例の系統図である。本装置は排ガス202を直接吸
収冷凍機205に導き吸収冷凍機を駆動させる方式のも
のであり、第1の例と比べると、排ガスボイラ203が
省略され、蒸気204の発生が行われていない。
FIG. 3 is a system diagram of a second example of a conventional cogeneration type absorption refrigerator. This device is of a type that directly guides the exhaust gas 202 to the absorption refrigeration machine 205 and drives the absorption refrigeration machine. Compared to the first example, the exhaust gas boiler 203 is omitted and steam 204 is not generated.

【0005】[0005]

【発明が解決しようとする課題】上記従来の方式では、
排ガスの保有する熱量は回収出来るが冷却水206が保
有する熱量は207の冷却器で外部に無駄にすてられて
おり、この熱量はガスエンジン等からなる発電装置20
1に投入される熱量の約1/3程度にも達する。このた
め有効エネルギーの回収効率が改善できない欠点を持っ
ていた。
SUMMARY OF THE INVENTION In the above conventional method,
Although the heat quantity of the exhaust gas can be recovered, the heat quantity of the cooling water 206 is wasted to the outside by the cooler 207, and this heat quantity is generated by the power generator 20 including a gas engine or the like.
It reaches about 1/3 of the heat input to 1. Therefore, it has a drawback that the recovery efficiency of effective energy cannot be improved.

【0006】本発明は上記従来技術の欠点を解消し、冷
却水の保有熱量を有効に回収して、同一発電量で吸収冷
凍機の冷凍能力を向上させようとするものである。
The present invention is intended to solve the above-mentioned drawbacks of the prior art, to effectively recover the heat quantity of the cooling water, and to improve the refrigerating capacity of the absorption refrigerator with the same amount of power generation.

【0007】[0007]

【課題を解決するための手段】本発明は上記課題を解決
したものであって、高圧再生器と低圧再生器を備え、発
電装置から排出された排ガスの熱を上記高圧再生器の熱
源として用いるコージェネ型吸収冷凍機において、上記
発電装置から排出された冷却水を上記低圧再生器に導い
て循環させ同冷却水の熱を同低圧再生器の熱源として用
いることを特徴とするコージェネ型吸収冷凍機に関する
ものである。
SUMMARY OF THE INVENTION The present invention has been made to solve the above problems and comprises a high pressure regenerator and a low pressure regenerator, and uses the heat of exhaust gas discharged from a power generator as a heat source for the high pressure regenerator. In a cogeneration-type absorption refrigerator, the cooling water discharged from the power generator is guided to the low-pressure regenerator and circulated, and the heat of the cooling water is used as a heat source of the low-pressure regenerator. It is about.

【0008】[0008]

【作用】従来、発電装置と冷却器との間を循環していた
冷却水の系を吸収冷凍機の低圧再生器へ延長し、発電装
置の冷却水排出側で冷却水に保有されている熱を用いて
溶液(LiBr溶液)の再生用熱源として用いる。
The system of cooling water, which has conventionally circulated between the power generator and the cooler, is extended to the low-pressure regenerator of the absorption refrigerator, and the heat retained in the cooling water on the cooling water discharge side of the power generator is extended. Is used as a heat source for regenerating the solution (LiBr solution).

【0009】[0009]

【実施例】図1は本発明の一実施例に係るコージェネ型
吸収冷凍機の系統図である。図において、201は発電
装置、202は排ガス、206は冷却水、一点鎖線で囲
んである205は吸収冷凍機である。301〜306は
吸収冷凍機205を構成する要素であり、301は高圧
再生器、302は循環するLiBr溶液、303は低圧
再生器、304は吸収器、305は凝縮器、306は蒸
発器である。
FIG. 1 is a system diagram of a cogeneration type absorption refrigerator according to an embodiment of the present invention. In the figure, 201 is a power generator, 202 is exhaust gas, 206 is cooling water, and 205 surrounded by an alternate long and short dash line is an absorption refrigerator. Reference numerals 301 to 306 are elements constituting the absorption refrigerator 205, 301 is a high pressure regenerator, 302 is a circulating LiBr solution, 303 is a low pressure regenerator, 304 is an absorber, 305 is a condenser, and 306 is an evaporator. .

【0010】本装置では、ガスエンジン等の発電装置2
01で発生した排ガス202を吸収冷凍機205の高圧
再生器301に導き、LiBr溶液302の再生に利用
するとともに、冷却水206を低圧再生器303に導
き、ここでもまたLiBr溶液302の再生に利用す
る。ここで吸収冷凍機205の他の構成機器(吸収器3
04、凝縮器305、蒸発器306)は従来のものと同
じ役割を果たす。
In this device, a power generator 2 such as a gas engine is used.
The exhaust gas 202 generated in 01 is guided to the high pressure regenerator 301 of the absorption refrigerator 205 and used for regeneration of the LiBr solution 302, and the cooling water 206 is also guided to the low pressure regenerator 303, and again used for regeneration of the LiBr solution 302. To do. Here, other components of the absorption refrigerator 205 (absorber 3
04, condenser 305, evaporator 306) play the same role as conventional ones.

【0011】尚、図1はいわゆる二重効用型のパラレル
フロー方式に本発明を適用した場合の系統図であるが、
一重効用型でも一つの再生器に排ガスと冷却水の熱源を
投入することにより同様の効果が得られる。また、溶液
の流し方の異なるシリーズフロー方式、リバースフロー
方式においても同様である。
FIG. 1 is a system diagram when the present invention is applied to a so-called double-effect parallel flow system.
Even in the single-effect type, the same effect can be obtained by introducing the heat source of exhaust gas and cooling water into one regenerator. The same applies to the series flow system and the reverse flow system in which the flow of the solution is different.

【0012】[0012]

【発明の効果】本発明のコージェネ型吸収冷凍機におい
ては、上記発電装置から排出された冷却水を上記低圧再
生器に導いて循環させ同冷却水の熱を同低圧再生器の熱
源として用いるので、従来捨てられていた発電装置の冷
却水の保有熱量を有効に回収することが可能となり、同
一の発電量、即ち同一の燃料消費量で吸収冷凍機での冷
凍能力を60〜90%増大させることが可能となる。
In the cogeneration type absorption refrigerator of the present invention, the cooling water discharged from the power generator is guided to the low pressure regenerator and circulated, and the heat of the cooling water is used as the heat source of the low pressure regenerator. It becomes possible to effectively recover the heat quantity of the cooling water of the power generator, which was conventionally discarded, and increase the refrigerating capacity of the absorption refrigerator by 60 to 90% with the same power generation amount, that is, the same fuel consumption amount. It becomes possible.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の一実施例に係るコージェネ型吸収冷凍
機の系統図。
FIG. 1 is a system diagram of a cogeneration type absorption refrigerator according to an embodiment of the present invention.

【図2】従来のコージェネ型吸収冷凍機の第1の例の系
統図。
FIG. 2 is a system diagram of a first example of a conventional cogeneration type absorption refrigerator.

【図3】従来のコージェネ型吸収冷凍機の第2の例の系
統図。
FIG. 3 is a system diagram of a second example of a conventional cogeneration type absorption refrigerator.

【符号の説明】[Explanation of symbols]

201 発電装置 202 排ガス 205 吸収冷凍機 206 冷却水 301 高圧再生器 302 LiBr溶液 303 低圧再生器 304 吸収器 305 凝縮器 306 蒸発器 201 Power generator 202 Exhaust gas 205 Absorption refrigerator 206 Cooling water 301 High pressure regenerator 302 LiBr solution 303 Low pressure regenerator 304 Absorber 305 Condenser 306 Evaporator

───────────────────────────────────────────────────── フロントページの続き (72)発明者 福島 亮 兵庫県高砂市荒井町新浜二丁目1番1号 三菱重工業株式会社高砂研究所内 (72)発明者 川田 章広 兵庫県高砂市荒井町新浜二丁目1番1号 三菱重工業株式会社高砂製作所内 (72)発明者 井上 健三 兵庫県高砂市荒井町新浜2丁目8番19号 高菱エンジニアリング株式会社内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Ryo Fukushima 1-1-1, Niihama, Arai-cho, Takasago-shi, Hyogo Mitsubishi Heavy Industries Ltd. Takasago Research Institute (72) Inventor Akihiro Kawada 2-1-1, Niihama, Arai-cho, Takasago-shi, Hyogo No. 1 Mitsubishi Heavy Industries, Ltd. Takasago Plant (72) Inventor Kenzo Inoue 2-8-19, Niihama, Arai-cho, Takasago, Hyogo Prefecture Takahishi Engineering Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 高圧再生器と低圧再生器を備え、発電装
置から排出された排ガスの熱を上記高圧再生器の熱源と
して用いるコージェネ型吸収冷凍機において、上記発電
装置から排出された冷却水を上記低圧再生器に導いて循
環させ同冷却水の熱を同低圧再生器の熱源として用いる
ことを特徴とするコージェネ型吸収冷凍機。
1. A cogeneration-type absorption refrigerating machine comprising a high-pressure regenerator and a low-pressure regenerator, wherein heat of exhaust gas discharged from the power generator is used as a heat source of the high-pressure regenerator, and cooling water discharged from the power generator is A cogeneration-type absorption refrigerating machine, characterized in that the heat of the cooling water is guided to the low-pressure regenerator and circulated to use the heat of the cooling water as a heat source of the low-pressure regenerator.
JP7103597A 1995-04-27 1995-04-27 Cogeneration type absorption refrigerating machine Pending JPH08296922A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7103597A JPH08296922A (en) 1995-04-27 1995-04-27 Cogeneration type absorption refrigerating machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7103597A JPH08296922A (en) 1995-04-27 1995-04-27 Cogeneration type absorption refrigerating machine

Publications (1)

Publication Number Publication Date
JPH08296922A true JPH08296922A (en) 1996-11-12

Family

ID=14358180

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7103597A Pending JPH08296922A (en) 1995-04-27 1995-04-27 Cogeneration type absorption refrigerating machine

Country Status (1)

Country Link
JP (1) JPH08296922A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106568226A (en) * 2016-11-13 2017-04-19 浙江大学 Low-grade thermal-driven cold and electricity combined supply system and application method thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106568226A (en) * 2016-11-13 2017-04-19 浙江大学 Low-grade thermal-driven cold and electricity combined supply system and application method thereof
CN106568226B (en) * 2016-11-13 2019-01-29 浙江大学 A kind of the combined cooling and power system and its application method of low-grade heat driving

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Effective date: 20020402