JPH0124527Y2 - - Google Patents

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Publication number
JPH0124527Y2
JPH0124527Y2 JP1981040848U JP4084881U JPH0124527Y2 JP H0124527 Y2 JPH0124527 Y2 JP H0124527Y2 JP 1981040848 U JP1981040848 U JP 1981040848U JP 4084881 U JP4084881 U JP 4084881U JP H0124527 Y2 JPH0124527 Y2 JP H0124527Y2
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JP
Japan
Prior art keywords
heat
exhaust
pipe
air
hot water
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.)
Expired
Application number
JP1981040848U
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Japanese (ja)
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JPS57153969U (en
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Priority to JP1981040848U priority Critical patent/JPH0124527Y2/ja
Publication of JPS57153969U publication Critical patent/JPS57153969U/ja
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Expired legal-status Critical Current

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    • 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

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  • Other Air-Conditioning Systems (AREA)

Description

【考案の詳細な説明】 本考案は排熱利用システムに関する。[Detailed explanation of the idea] The present invention relates to an exhaust heat utilization system.

地下鉄の排熱量は莫大なものであるが、その綜
合排熱利用はあまりなされていない。
Although the amount of waste heat generated by subways is enormous, the total amount of waste heat is not utilized much.

本考案はこのような事情に鑑みて提案されたも
ので、地下鉄等の排熱利用システムを提供するこ
とを目的とし、分散した各地域に発生する比較的
低温空気の排熱をそれぞれ各地域で空気熱源ヒー
トポンプにより回収し、移送効率のよい液体媒体
に変換する複数の分散排熱回収部と、上記複数の
分散排熱回収部からの液体媒体を集めこれを水熱
源ヒートポンプ、排蒸気熱交換器、排気ガス熱交
換器により所定温度に加熱する集中排熱回収部と
を具えたことを特徴とする。
This invention was proposed in view of these circumstances, and aims to provide a waste heat utilization system for subways, etc., in which the waste heat of relatively low-temperature air generated in each dispersed area can be used in each region. A plurality of distributed waste heat recovery units collect the liquid medium using an air heat source heat pump and convert it into a liquid medium with high transfer efficiency, and a water heat source heat pump and a waste steam heat exchanger collect the liquid medium from the plurality of distributed waste heat recovery units. , and a centralized exhaust heat recovery section that heats the exhaust gas to a predetermined temperature using an exhaust gas heat exchanger.

本考案の一実施例を図面について説明すると、
第1図はその系統図である。
An embodiment of the present invention will be explained with reference to the drawings.
Figure 1 is its system diagram.

上図において、1は地下鉄線の駅舎、2は隣接
駅舎の中間地点に設けられ地下鉄内換気を行なう
排気塔、3は空気熱交換器、4は圧縮機、5は凝
縮機、6は圧縮機4を駆動する電動機、7,8,
9は冷媒連絡管、10,11は冷却水連絡管で3
〜11は協働して空気熱源ヒートポンプを構成
し、各空気熱源ヒートポンプで汲上げた熱は温水
状態で各排気塔2に付設され分配母管13、集中
移送管12を経て後記集中センターに送られる。
In the above diagram, 1 is a station building for the subway line, 2 is an exhaust tower installed at the midpoint between adjacent station buildings and provides ventilation in the subway, 3 is an air heat exchanger, 4 is a compressor, 5 is a condenser, and 6 is a compressor. Electric motor driving 4, 7, 8,
9 is a refrigerant communication pipe, 10 and 11 are cooling water communication pipes, and 3
~ 11 work together to form an air source heat pump, and the heat pumped up by each air source heat pump is attached to each exhaust tower 2 in the form of hot water, and is sent to the concentration center described later through the distribution main pipe 13 and the central transfer pipe 12. It will be done.

14は蒸発器、15は圧縮機、16は凝縮器、
17,18,19は冷媒配管で、14〜19は協
働して水熱源ヒートポンプを構成する。20は地
域より集中センターへの戻り管、21,27は温
水連絡管、28は地域への供給管、22はボイラ
ー、23はタービン、24は復水器、25は排ガ
ス熱交換器、26は煙突、29,30,31は蒸
気連絡管、32は燃料供給管、33,34は煙
道、35は各駅舎の空調用放熱設備、36,37
は温水連絡管である。
14 is an evaporator, 15 is a compressor, 16 is a condenser,
17, 18, and 19 are refrigerant pipes, and 14 to 19 cooperate to constitute a water heat source heat pump. 20 is a return pipe from the region to the central center, 21 and 27 are hot water communication pipes, 28 is a supply pipe to the region, 22 is a boiler, 23 is a turbine, 24 is a condenser, 25 is an exhaust gas heat exchanger, and 26 is a Chimneys, 29, 30, 31 steam communication pipes, 32 fuel supply pipes, 33, 34 flues, 35 air conditioning heat radiation equipment for each station building, 36, 37
is a hot water connection pipe.

このような装置において、駅舎、トンネル等に
分散する排気ガスを空気熱交換器3に内蔵された
誘引フアンにより誘引し、排気ガスと空気熱源ヒ
ートポンプの冷媒とが空気熱交換器3において熱
交換することにより排熱回収を行なう。
In such a device, exhaust gas dispersed in a station building, tunnel, etc. is induced by an induction fan built into the air heat exchanger 3, and the exhaust gas and the refrigerant of the air heat source heat pump exchange heat in the air heat exchanger 3. This allows waste heat to be recovered.

空気熱源ヒートポンプのサイクルは空気熱交換
器3で排気ガス顕熱により冷媒を加熱気化し、冷
媒連絡管7を経て、圧縮機4に至り冷却水により
凝縮、液化する行程よりなる。言いかえると空気
熱交換器3にて回収された熱量と圧縮に要した仕
事を加えた熱量に相当する分だけ冷却水の温度が
上昇することになる。
The cycle of the air source heat pump consists of a process in which the air heat exchanger 3 heats and vaporizes the refrigerant using the sensible heat of the exhaust gas, passes through the refrigerant communication pipe 7, reaches the compressor 4, and condenses and liquefies it with cooling water. In other words, the temperature of the cooling water increases by an amount corresponding to the amount of heat collected by the air heat exchanger 3 plus the work required for compression.

凝縮器5にて液化した冷媒は、冷媒連絡管9を
経て空気熱交換器3に至りサイクルが完結する。
The refrigerant liquefied in the condenser 5 reaches the air heat exchanger 3 via the refrigerant communication pipe 9, completing the cycle.

この空気熱源ヒートポンプは排気塔数と同数設
置され、通常駅舎数をNとすれば(N−1)台程
度となる。このことはガス状で分散した排熱を分
散地域で熱回収し移送効率のよい温水に媒体変換
し集中移送管12にて集中センターに集める。
The number of air source heat pumps is the same as the number of exhaust towers, and if N is the number of station buildings, the number of air source heat pumps is approximately (N-1). This means that the gaseous and dispersed waste heat is recovered in the dispersed areas, converted into a medium of hot water with good transfer efficiency, and collected in a centralized center through the central transfer pipe 12.

この冷却水は集中センター内に設けられた水熱
源ヒートポンプの蒸発器14の熱源になるとゝも
に、その温度レベルは30〜45℃で単なる暖房には
十分使用可能であるため集中移送管12より適
宜、温水連絡管36に分岐し、駅舎1等に設けら
れた空調機35にて暖房に利用し連結管37によ
り分配管13に戻す。
This cooling water becomes the heat source for the evaporator 14 of the water heat source heat pump installed in the central center, and since its temperature level is 30 to 45°C, which is sufficient for simple heating, it is transferred from the central transfer pipe 12. As appropriate, the hot water is branched into a hot water communication pipe 36, used for heating in an air conditioner 35 installed in the station building 1, etc., and returned to the distribution pipe 13 through a connecting pipe 37.

水熱源ヒートポンプのサイクルは蒸発器14に
おいて冷却水により加熱された冷媒を気化し、冷
媒連絡管17を経て圧縮機15に至り所定圧力ま
で圧縮し、冷媒連絡管18を経て凝縮器16に至
りこゝで地域よりリターンした温水により冷却し
液化凝縮する行程よりなる。言いかえると分散地
域で空気熱源ヒートポンプにて排熱回収し更にヒ
ートアツプした熱量の合計と圧縮に要した仕事を
加えた熱量に相当する分だけ地域よりの戻り管2
0を経てリターンした温水の温度を昇温すること
になる。
The water source heat pump cycle consists of vaporizing the refrigerant heated by cooling water in the evaporator 14, passing through the refrigerant connecting pipe 17 to the compressor 15, compressing it to a predetermined pressure, and passing through the refrigerant connecting pipe 18 to the condenser 16. It consists of a process in which it is cooled and liquefied and condensed using hot water returned from the area. In other words, the return pipe 2 from the area corresponds to the total amount of heat that is recovered by the air source heat pump in the distributed area and further heated up, plus the work required for compression.
The temperature of the hot water returned after passing through 0 will be increased.

凝縮器16にて液化した冷媒は冷媒連絡管19
を経て蒸発器14に至りサイクルは完結する。
The refrigerant liquefied in the condenser 16 is transferred to the refrigerant communication pipe 19.
The cycle is completed through the evaporator 14.

また、凝縮器16にて加熱された温水は、温水
連絡管21を経て熱交換器24に入り、こゝでタ
ービン23の排気によつて加熱され、更に温水連
絡管27を経て排気ガス熱交換器25に至りボイ
ラ排ガスによつて加熱昇温し地域供給管28によ
り地域へサプライされる。
The hot water heated in the condenser 16 enters the heat exchanger 24 via the hot water communication pipe 21, where it is heated by the exhaust gas of the turbine 23, and further passes through the hot water communication pipe 27 for exhaust gas heat exchange. The water reaches the boiler 25, is heated and heated by boiler exhaust gas, and is supplied to the region through the regional supply pipe 28.

一方、圧縮機15を駆動するタービン系では、
ボイラー22において燃料供給管32に供給され
た、燃料の燃焼により蒸気の発生が行なわれ、蒸
気は蒸気連絡管29を経てタービン23にて圧縮
機15を駆動し、蒸気連絡管30を経て復水器2
4にて凝縮し更に連絡管31によりボイラー22
に戻る。
On the other hand, in the turbine system that drives the compressor 15,
Steam is generated by combustion of the fuel supplied to the fuel supply pipe 32 in the boiler 22, and the steam passes through the steam communication pipe 29, drives the compressor 15 in the turbine 23, and is condensed through the steam communication pipe 30. Vessel 2
4 and further condensed through the connecting pipe 31 to the boiler 22.
Return to

またボイラー22の排気ガスは煙道33を経て
排気ガス熱交換器25に至り温水との熱交換後煙
道34より煙突26を経由して大気へ放出され
る。
Further, the exhaust gas from the boiler 22 passes through the flue 33 to the exhaust gas heat exchanger 25, exchanges heat with hot water, and is then discharged from the flue 34 to the atmosphere via the chimney 26.

本考案によれば、 地下鉄、駅舎間の各排気塔など分散形排熱源
に1次空気熱源ヒートポンプを分散配置し温水
状態にて熱回収を図ることにより次の効果が奏
せられる。
According to the present invention, the following effects can be achieved by distributing primary air heat source heat pumps to distributed exhaust heat sources such as subways and exhaust towers between station buildings and recovering heat in a hot water state.

(1) 排気をダクト等で集約して熱回収する場合
に比し経済的にかつ熱ロスの小さいものにで
きる。
(1) It is more economical and has less heat loss than the case where exhaust gas is concentrated in a duct or the like and heat is recovered.

(2) 1次空気熱源ヒートポンプより集中移送管
にて集中センターへ導かれる過程における温
水温度は30〜45℃程度となるが、駅舎暖房等
ではこの程度の温度で十分であるため、この
集中移送管よりの分岐で、駅舎暖房等をまか
なうことにより分散形負荷への供給対応も経
済的に実施できる。
(2) The temperature of the hot water during the process of being led from the primary air heat source heat pump to the central center via the central transfer pipe is approximately 30 to 45°C, but this temperature is sufficient for station building heating, etc. By branching from the pipe and providing station building heating, etc., it is also possible to economically supply distributed loads.

(3) 1次空気熱源ヒートポンプにより得られる
温水温度は季節変動等による負荷変動にかゝ
わりなくほゞ一定供給でき第2次の高温度落
差運転を行なう水熱源ヒートポンプの外乱要
素を軽減でき安定運転に寄与する。
(3) The hot water temperature obtained by the primary air heat source heat pump can be supplied at an almost constant level regardless of load fluctuations due to seasonal fluctuations, etc., and the disturbance elements of the water heat source heat pump, which performs secondary high temperature drop operation, can be reduced and stable operation can be achieved. Contribute to

2次水熱源ヒートポンプシステムにおいて背
圧タービン駆動としその復水器をヒートポンプ
凝縮器出口側に設置することにより次の効果が
奏せられる。
In the secondary water heat source heat pump system, the following effects can be achieved by driving the back pressure turbine and installing the condenser on the outlet side of the heat pump condenser.

(1) 集中地域熱供給における供給温水温度は
100〜150℃前後となるがヒートポンプサイク
ルは逆カルノーサイクルでありその高温側温
度によつて成積系数(汲み上げ熱量/所要動
力の比)は異なる。
(1) The temperature of hot water supplied in centralized district heat supply is
The temperature is around 100 to 150°C, but the heat pump cycle is a reverse Carnot cycle, and the system number (ratio of pumped heat/required power) differs depending on the high temperature side.

凝縮器出口側に背圧タービン復水器を配置
することによりヒートポンプサイクル高温側
温度を低くゝすることができサイクル効率を
高められる。
By arranging the back pressure turbine condenser on the condenser outlet side, the temperature on the high temperature side of the heat pump cycle can be lowered and cycle efficiency can be increased.

(2) 背圧タービンサイクルの排熱を全て利用熱
量に廻すことができる。
(2) All of the exhaust heat from the back pressure turbine cycle can be converted into usable heat.

(3) ヒートポンプサイクルの作動流体にフレオ
ン系を利用した場合通常110〜120℃前後より
熱分解を生じ機器の腐食等問題となつてくる
が、所要供給温度に対し背圧タービン復水器
によりヒートポンプ出口温水温度を安全域に
挿えることができる。
(3) When a Freon system is used as the working fluid for a heat pump cycle, thermal decomposition occurs at around 110 to 120°C, causing problems such as equipment corrosion. The outlet hot water temperature can be kept within a safe range.

本方式によるシステム全体とし従来の集中地
域熱供給設備に対し次の効果が奏せられる。
The overall system of this method has the following effects compared to conventional centralized district heat supply equipment.

従来のボイラーを利用して高温水を製造する
方式のものに対しボイラーへの供給エネルギを
1.0とすると利用可能な高温水エネルギはボイ
ラー効率に依存し1.0以下になるとゝもに発生
する蒸気等の持つエクセルギ効率は著しく悪く
なる。
Compared to the conventional method that uses a boiler to produce high-temperature water, the energy supplied to the boiler is reduced.
If it is 1.0, the usable high-temperature water energy will depend on the boiler efficiency, and if it is less than 1.0, the exergy efficiency of the steam generated will deteriorate significantly.

しかしながら、本方式による場合、従来の熱
利用率以上に排熱のヒートポンプ作用による回
収が行われ総合の利用可能熱量は1.2程度まで
すなわち、入力エネルギに対し約2割増しの熱
量が得られることになる。
However, in the case of this method, the heat pump action of the exhaust heat is recovered at a higher rate than the conventional heat utilization rate, and the total available heat amount is about 1.2, which means that about 20% more heat can be obtained than the input energy. .

要するに本考案によれば、分散した各地域に発
生する比較的低温空気の排熱をそれぞれ各地域で
空気熱源ヒートポンプにより回収し、移送効率の
よい液体媒体に変換する複数の分散排熱回収部
と、上記複数の分散排熱回収部からの液体媒体を
集めこれを水熱源ヒートポンプ、排蒸気熱交換
器、排気ガス熱交換器により所定温度に加熱する
集中排熱回収部とを具えたことにより、経済的な
地下鉄等の排熱利用システムを得るから、本考案
は産業上極めて有益なものである。
In short, according to the present invention, a plurality of distributed waste heat recovery sections are used to collect the waste heat of relatively low-temperature air generated in each dispersed region using an air heat source heat pump in each region, and convert it into a liquid medium with high transfer efficiency. , by comprising a centralized exhaust heat recovery unit that collects the liquid medium from the plurality of distributed exhaust heat recovery units and heats it to a predetermined temperature using a water heat source heat pump, an exhaust steam heat exchanger, and an exhaust gas heat exchanger, The present invention is extremely useful industrially because it provides an economical waste heat utilization system for subways and the like.

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

第1図は本考案の一実施例を示す系統図であ
る。 1……駅舎、2……排気塔、3……空気熱交換
器、4……圧縮機、5……凝縮器、6……電動
機、7,8,9……冷媒連絡管、10,11……
冷却水連絡管、13……分配母管、14……蒸発
器、15……圧縮機、16……凝縮機、17,1
8,19……冷媒配管、20……戻り管、21…
…温水連絡管、22……ボイラー、23……ター
ビン、24……復水器、25……排ガス熱交換
器、26……煙突、27……温水連絡管、28…
…供給管、29,30,31……蒸気連絡管、3
2……燃料供給管、33,34……煙道、35…
…空調用放熱設備、36,37……温水連絡管。
FIG. 1 is a system diagram showing an embodiment of the present invention. 1... Station building, 2... Exhaust tower, 3... Air heat exchanger, 4... Compressor, 5... Condenser, 6... Electric motor, 7, 8, 9... Refrigerant communication pipe, 10, 11 ……
Cooling water communication pipe, 13... Distribution main pipe, 14... Evaporator, 15... Compressor, 16... Condenser, 17, 1
8, 19... Refrigerant piping, 20... Return pipe, 21...
... Hot water communication pipe, 22 ... Boiler, 23 ... Turbine, 24 ... Condenser, 25 ... Exhaust gas heat exchanger, 26 ... Chimney, 27 ... Hot water communication pipe, 28 ...
... Supply pipe, 29, 30, 31 ... Steam communication pipe, 3
2... Fuel supply pipe, 33, 34... Flue, 35...
...Radiation equipment for air conditioning, 36, 37...Hot water connection pipe.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 分散した各地域に発生する比較的低温空気の排
熱をそれぞれ各地域で空気熱源ヒートポンプによ
り回収し、移送効率のよい液体媒体に変換する複
数の分散排熱回収部と、上記複数の分散排熱回収
部からの液体媒体を集めこれを水熱源ヒートポン
プ、排蒸気熱交換器、排気ガス熱交換器により所
定温度に加熱する集中排熱回収部とを具えたこと
を特徴とする排熱利用システム。
A plurality of distributed waste heat recovery sections that collect the waste heat of relatively low-temperature air generated in each dispersed region using an air heat source heat pump in each region and convert it into a liquid medium with good transfer efficiency, and a plurality of distributed waste heat An exhaust heat utilization system characterized by comprising a centralized exhaust heat recovery section that collects a liquid medium from a recovery section and heats it to a predetermined temperature using a water heat source heat pump, an exhaust steam heat exchanger, and an exhaust gas heat exchanger.
JP1981040848U 1981-03-25 1981-03-25 Expired JPH0124527Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1981040848U JPH0124527Y2 (en) 1981-03-25 1981-03-25

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1981040848U JPH0124527Y2 (en) 1981-03-25 1981-03-25

Publications (2)

Publication Number Publication Date
JPS57153969U JPS57153969U (en) 1982-09-27
JPH0124527Y2 true JPH0124527Y2 (en) 1989-07-25

Family

ID=29837948

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1981040848U Expired JPH0124527Y2 (en) 1981-03-25 1981-03-25

Country Status (1)

Country Link
JP (1) JPH0124527Y2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5114679U (en) * 1974-07-18 1976-02-03

Also Published As

Publication number Publication date
JPS57153969U (en) 1982-09-27

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