JP3400699B2 - Absorption chiller / heater using engine exhaust heat - Google Patents
Absorption chiller / heater using engine exhaust heatInfo
- Publication number
- JP3400699B2 JP3400699B2 JP35436397A JP35436397A JP3400699B2 JP 3400699 B2 JP3400699 B2 JP 3400699B2 JP 35436397 A JP35436397 A JP 35436397A JP 35436397 A JP35436397 A JP 35436397A JP 3400699 B2 JP3400699 B2 JP 3400699B2
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- hot water
- engine
- exhaust gas
- heat exchanger
- 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 - Fee Related
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
- Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
- Y02B30/625—Absorption based systems combined with heat or power generation [CHP], e.g. trigeneration
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は発電と冷暖房を同時
にできるコージェネレーションシステムに関し、特に吸
収冷温水機にエンジン排熱を回収して冷暖房に利用する
エンジン排熱利用吸収冷温水機に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cogeneration system capable of generating electricity and heating and cooling at the same time, and more particularly to an absorption chiller-heater utilizing engine exhaust heat for recovering engine exhaust heat in an absorption chiller-heater and utilizing it for cooling and heating.
【0002】[0002]
【従来の技術】従来の装置は、エンジンの排気ガスを高
温再生器に導入し、二重効用吸収サイクルを構成して熱
効率を高め、ジャケットからの温水は低温再生器に導入
し、一重効用吸収サイクルを構成し冷凍作用を行なって
いた。2. Description of the Related Art A conventional device introduces engine exhaust gas into a high-temperature regenerator to form a double-effect absorption cycle to improve thermal efficiency, and hot water from a jacket is introduced into a low-temperature regenerator to absorb a single-effect absorption. It constituted a cycle and performed a refrigerating action.
【0003】また他の装置として、エンジン排気ガスと
エンジンジャケット出口冷却温水とを熱交換させてエン
ジンの排熱を全て温水として熱回収し、一重効用低温水
吸収冷凍機を用いて冷水をつくるものがあった。As another device, the engine exhaust gas and the engine jacket outlet cooling hot water are heat-exchanged to recover all the exhaust heat of the engine as hot water, and cold water is produced using a single-effect low-temperature water absorption refrigerator. was there.
【0004】なお、この種の技術として関連するものに
特開平7−218017号公報が挙げられる。A related technique of this type is disclosed in Japanese Patent Laid-Open No. 7-218017.
【0005】[0005]
【発明が解決しようとする課題】上記装置は、エンジン
の排気ガスを熱効率の高い二重効用吸収サイクルで熱利
用するため、エンジンの排熱から取り出せる冷凍容量は
大きくなるが高温再生器を流出する排気ガスの温度が2
00℃程度になり、排熱の回収量が少なくなるという点
に関して配慮されていなかった。In the above apparatus, since the exhaust gas of the engine is utilized in the double-effect absorption cycle having high thermal efficiency, the refrigerating capacity that can be taken out from the exhaust heat of the engine is large, but it flows out from the high temperature regenerator. Exhaust gas temperature is 2
No consideration was given to the fact that the temperature was about 00 ° C and the amount of exhaust heat recovered was small.
【0006】また上記他の装置においても、エンジン排
気ガスと90℃程度の温水と熱交換させるため、排気ガ
スの出口温度を120℃程度になるまで熱回収できるの
で排熱回収量は多くなるが、吸収式冷凍機が一重効用サ
イクルとなり熱効率が低く、前記の冷凍機より冷凍容量
は少なくなるという点に関して配慮されていなかった。Also, in the other device described above, since the engine exhaust gas and the hot water of about 90 ° C. are heat-exchanged, heat can be recovered until the outlet temperature of the exhaust gas reaches about 120 ° C., but the amount of exhaust heat recovery increases. No consideration was given to the fact that the absorption refrigerator has a single-effect cycle and the thermal efficiency is low and the refrigerating capacity is smaller than that of the refrigerator.
【0007】本発明は、エンジンの排気ガスを高温再生
器に導入し、二重効用吸収サイクルで熱利用を図り、冷
凍容量を増大させ且つ、排気ガスからの回収熱量を排気
ガスと温水を熱交換させる場合と同等以上にし、コージ
ェネレーションシステムの熱効率を最大にするエンジン
排熱利用吸収冷温水機を提供することを目的とする。The present invention introduces engine exhaust gas into a high temperature regenerator to utilize heat in a double-effect absorption cycle, increase refrigeration capacity, and recover the amount of heat recovered from the exhaust gas by heating the exhaust gas and hot water. It is an object of the present invention to provide an engine exhaust heat utilization absorption chiller-heater that maximizes the thermal efficiency of a cogeneration system by making it equal to or more than when replaced.
【0008】上記目的は、エンジンの排気ガスを利用す
る高温再生器、低温再生器、凝縮機、吸収器、低温熱交
換器、高温熱交換器を動作的に配管接続してなる吸収式
冷温水機と、排気ガスを前記高温再生器に導く排気ガス
導入手段とを備えるエンジン排熱利用吸収冷温水機にお
いて、前記高温再生器の排気ガス出口側に前記エンジン
を冷却したジャケット冷温水が排気ガスと熱交換する熱
交換器を、前記エンジンとこの熱交換器との間にこの熱
交換器を通らずにエンジンに温水を戻す温水戻り配管
を、熱交換器の温水下流側にこの熱交換器で熱交換して
温度の低下した温水を低温再生器を通らずにエンジンに
戻すバイパス配管をそれぞれ設け、前記温水戻り配管の
分岐部にジャケット温水温度調節器を設け、このジャケ
ット温水温度調節器の働きにより、前記熱交換器に流入
する温度低下を防ぎ、前記バイパス配管に温度調節手段
を設け、前記温度調節手段で前記低温再生器からエンジ
ンジャケットに還流する温水温度を一定に保持するよう
に制御することにより達成される。The above-mentioned object is an absorption type cold / hot water in which a high temperature regenerator, a low temperature regenerator, a condenser, an absorber, a low temperature heat exchanger and a high temperature heat exchanger which utilize exhaust gas of an engine are operatively connected by piping. Machine and an exhaust gas introduction means for introducing exhaust gas to the high-temperature regenerator, in an absorption chiller-heater using exhaust heat of the engine, jacket cold-hot water that cools the engine is exhaust gas on the exhaust gas outlet side of the high-temperature regenerator. A heat exchanger for exchanging heat with the engine, and a hot water return pipe for returning hot water to the engine without passing the heat exchanger between the engine and the heat exchanger, the heat exchanger being provided downstream of the heat exchanger with the hot water. Bypass pipes are provided for returning the hot water whose temperature has been lowered by heat exchange to the engine without passing through the low temperature regenerator.A jacket hot water temperature controller is provided at the branch of the hot water return pipe.
The hot water temperature controller works to flow into the heat exchanger.
Preventing temperature drop of the temperature adjusting means in the bypass pipe provided, engine from the low temperature generator in said temperature regulating means
So that the temperature of the hot water flowing back to the jacket is kept constant
It is achieved by controlling the.
【0009】[0009]
【0010】[0010]
【0011】排気ガスと温水の熱交換器の温水出口側よ
り吸収冷温水機をバイパスしてエンジンのジャケットに
温水が還流する配管を設け、温水温度が下がり過ぎない
ように制御する装置を設けることにより排気ガスと温水
の熱交換器のガス側伝熱面の温度を排気ガスの結露温度
以上に保持する。A pipe for returning hot water to the engine jacket is provided by bypassing the absorption chiller / heater from the hot water outlet side of the heat exchanger of exhaust gas and hot water, and a device for controlling the hot water temperature not to fall too low is provided. Thus, the temperature of the heat transfer surface on the gas side of the heat exchanger of the exhaust gas and the hot water is maintained above the dew condensation temperature of the exhaust gas.
【0012】[0012]
【発明の実施の形態】図1は本発明の実施例を示す。FIG. 1 shows an embodiment of the present invention.
【0013】図1において、1は蒸発器、2は吸収器、
3は凝縮器、4は低温再生器、5は高温再生器、6は低
温熱交換器、7は高温熱交換器、8は冷媒ポンプ、9は
溶液ポンプ、10は排気ガス・温水熱交換器、11は排
気ガス管、12はジャケット冷却温水配管、13は温水
3方弁、14は温水温度調節器、15は温水ポンプ、1
6はエンジン、17は発電機、18は温水バイパス配
管、19は冷温水、20は冷却水、21はジャケット冷
却温水温度調節器である。In FIG. 1, 1 is an evaporator, 2 is an absorber,
3 is a condenser, 4 is a low temperature regenerator, 5 is a high temperature regenerator, 6 is a low temperature heat exchanger, 7 is a high temperature heat exchanger, 8 is a refrigerant pump, 9 is a solution pump, 10 is an exhaust gas / hot water heat exchanger. , 11 is an exhaust gas pipe, 12 is a jacket cooling hot water pipe, 13 is a hot water three-way valve, 14 is a hot water temperature controller, 15 is a hot water pump, 1
6 is an engine, 17 is a generator, 18 is hot water bypass piping, 19 is cold / hot water, 20 is cooling water, and 21 is a jacket cooling hot water temperature controller.
【0014】エンジン16の排気ガスは排気ガス管11
を通り高温再生器5に導入され、吸収器2より送られて
きた稀溶液を加熱し、溶液より冷媒蒸気(水蒸気)を発
生させ溶液を濃縮する。高温再生器5で発生した冷媒蒸
気は低温再生器4に導かれ、吸収器2より送られてきた
稀溶液を加熱し、冷媒蒸気を発生させて溶液を濃縮す
る、所謂二重効用吸収サイクルを形成し、吸収サイクル
の熱効率を高め冷凍能力を増大させる働きをする。Exhaust gas from the engine 16 is exhaust gas pipe 11
The diluted solution introduced into the high temperature regenerator 5 through the absorber is heated and the refrigerant solution (water vapor) is generated from the solution to concentrate the solution. The refrigerant vapor generated in the high temperature regenerator 5 is guided to the low temperature regenerator 4 to heat the dilute solution sent from the absorber 2 to generate refrigerant vapor and concentrate the solution, a so-called double-effect absorption cycle. It acts to increase the thermal efficiency of the absorption cycle and increase the refrigeration capacity.
【0015】エンジン16の排気ガスを高温再生器5に
導入した場合、上記の通り吸収サイクルの熱効率が高く
なり冷凍容量が増えるが高温再生器内の溶液温度が15
0〜160℃になるため、排気ガスの出口温度は200
℃程度止りであり、エンジン16の燃料に都市ガス等良
質なものを使用している場合には更に熱回収可能であ
る。When the exhaust gas of the engine 16 is introduced into the high temperature regenerator 5, the thermal efficiency of the absorption cycle is increased and the refrigeration capacity is increased as described above, but the solution temperature in the high temperature regenerator is 15%.
Since the temperature is 0 to 160 ° C, the exhaust gas outlet temperature is 200
The temperature is only about 0 ° C., and when a high quality gas such as city gas is used as the fuel for the engine 16, the heat can be further recovered.
【0016】高温再生器5を流出した排気ガスをエンジ
ン16のジャケット冷却温水と熱交換する排気ガス・温
水熱交換器10に導入し、排気ガスより更に熱回収し、
排気ガス温度を約120℃にして排出させる。このよう
に高温再生器5の排気ガス出口に排気ガス・温水熱交換
器10を取り付けることにより、エンジン出口の約50
0〜600℃の排気ガスを約200℃まで高温再生器5
で二重効用サイクルで熱利用し、200℃から120℃
までは温水として熱回収し一重効用サイクルで熱利用す
ることでエンジン16の排熱回収量の増大と冷凍容量の
増大が図れる。エンジン16のジャケット冷却温水はエ
ンジン入口温度が80〜83℃、エンジン出口温度が8
5〜90℃と低いため、吸収冷温水機に利用する場合、
吸収冷温水機の伝熱面積を大きくしないと熱が伝わら
ず、大型の吸収冷温水機が必要である。また、この時の
温水と溶液の平均温度差は約8〜10℃にとられてい
る。このようなジャケット冷却温水を排気ガスで更に加
熱すると2〜3℃高くなって冷温水機の低温再生器4に
供給できるため、温水と溶液の平均温度差が1〜2℃多
くなり、吸収冷温水機の伝熱面積を約2割少なくでき、
冷温水機の小型化が図れる。The exhaust gas flowing out of the high temperature regenerator 5 is introduced into the exhaust gas / hot water heat exchanger 10 for exchanging heat with the jacket cooling hot water of the engine 16, and the heat is further recovered from the exhaust gas,
The exhaust gas temperature is set to about 120 ° C. and the gas is discharged. By mounting the exhaust gas / hot water heat exchanger 10 on the exhaust gas outlet of the high temperature regenerator 5 as described above, about 50
Exhaust gas of 0-600 ℃ up to about 200 ℃ High temperature regenerator 5
Utilizing heat in a double-effect cycle at 200 ℃ to 120 ℃
By recovering the heat as hot water and utilizing the heat in the single-effect cycle, it is possible to increase the exhaust heat recovery amount of the engine 16 and increase the refrigeration capacity. The jacket cooling hot water of the engine 16 has an engine inlet temperature of 80 to 83 ° C and an engine outlet temperature of 8
Since it is as low as 5 to 90 ° C, when it is used in an absorption chiller / heater,
Unless the heat transfer area of the absorption chiller-heater is large, heat cannot be transferred and a large-scale absorption chiller-heater is required. The average temperature difference between the hot water and the solution at this time is set to about 8 to 10 ° C. If such jacket cooling hot water is further heated by the exhaust gas, the temperature rises by 2 to 3 ° C and can be supplied to the low temperature regenerator 4 of the cold / hot water machine, so that the average temperature difference between the hot water and the solution increases by 1 to 2 ° C, and the absorption cold temperature is increased. The heat transfer area of the water machine can be reduced by about 20%,
The chiller / heater can be downsized.
【0017】エンジン16の排気ガスは水分と炭酸ガス
を多く含み、排気ガスを60℃程度まで冷やすと排気ガ
ス中の水分が凝縮し伝熱面に水滴となって付着する。こ
の水滴に排気ガス中の炭酸ガスがとけ込み炭酸水とな
り、熱交換器の伝熱面を激しく腐蝕する。従って排気ガ
スの熱交換器の伝熱面の温度を水分が凝縮しないような
温度に保持しなければならない。一方、冷温水機の溶液
温度は冷凍負荷が下がったり、冷却水温度が下がると低
温再生器の溶液温度が大幅に下がる特性があり、溶液と
熱交換する温水温度も大幅に下がることになる。このよ
うな場合、エンジンのジャケット側はジャケット温水温
度調節器21が働き、温水温度の大幅な低下は起きない
が、この反作用で排気ガス・温水熱交換器側の温水温度
の温度が下がりやすくなる。The exhaust gas of the engine 16 contains a large amount of moisture and carbon dioxide gas, and when the exhaust gas is cooled to about 60 ° C., the moisture in the exhaust gas condenses and adheres to the heat transfer surface as water droplets. The carbon dioxide gas in the exhaust gas melts into the water droplets to become carbonated water, and the heat transfer surface of the heat exchanger is severely corroded. Therefore, the temperature of the heat transfer surface of the exhaust gas heat exchanger must be maintained at a temperature at which water does not condense. On the other hand, the solution temperature of the cold / hot water machine has a characteristic that the solution temperature of the low-temperature regenerator is significantly lowered when the refrigeration load is lowered or the cooling water temperature is lowered, and the hot water temperature for heat exchange with the solution is also greatly lowered. In such a case, the jacket hot water temperature controller 21 works on the jacket side of the engine and the hot water temperature does not drop significantly, but this reaction tends to lower the hot water temperature on the exhaust gas / hot water heat exchanger side. .
【0018】上記の防止策として排気ガス・温水熱交換
器10の出口温水を温水バイパス配管18、温水三方弁
13を介してエンジンジャケット側に還流させ、エンジ
ンジャケットに還流する温水温度を一定に保持するよう
に温度調節器14で三方弁13を開閉し、低温熱交換器
4をバイパスさせる。このように制御することにより排
気ガス・温水熱交換器10の伝熱面温度を排気ガスの水
分が凝縮する温度以上に保持することができるので、排
気ガス・温水熱交換器10の腐蝕を防止でき、長期間安
定した運転が可能となる。As a measure for preventing the above, the outlet hot water of the exhaust gas / hot water heat exchanger 10 is returned to the engine jacket side via the hot water bypass pipe 18 and the hot water three-way valve 13, and the temperature of the hot water returned to the engine jacket is kept constant. As described above, the temperature controller 14 opens and closes the three-way valve 13 to bypass the low temperature heat exchanger 4. By controlling in this way, the heat transfer surface temperature of the exhaust gas / hot water heat exchanger 10 can be maintained at a temperature higher than the temperature at which the water content of the exhaust gas condenses, so that the corrosion of the exhaust gas / hot water heat exchanger 10 is prevented. This enables stable operation over a long period of time.
【0019】[0019]
【発明の効果】本発明によれば、エンジンの排気ガスの
熱を効率良く、且つ、回収熱量も最大限にできるため冷
凍容量が大幅に増加する。又、排気ガスの通過する伝熱
面の温度を排気ガスの水分が凝縮する温度以上に保持出
来るので熱交換器の寿命が長くなり長期間安定した運転
ができる。According to the present invention, the heat of the exhaust gas of the engine can be efficiently provided and the amount of recovered heat can be maximized, so that the refrigerating capacity is significantly increased. Further, since the temperature of the heat transfer surface through which the exhaust gas passes can be maintained above the temperature at which the water content of the exhaust gas condenses, the life of the heat exchanger is extended and stable operation can be performed for a long period of time.
【図1】本発明の実施例の系統図。FIG. 1 is a system diagram of an embodiment of the present invention.
1…蒸発器、2…吸収器、3…凝縮器、4…低温再生
器、5…高温再生器、6…低温熱交換器、7…高温熱交
換器、8…冷媒ポンプ、9…溶液ポンプ、10…排気ガ
ス・温水熱交換器、11…排気ガス管、12…ジャケッ
ト冷却温水配管、13…温水3方弁、14…温水温度調
節器、15…温水ポンプ、16…エンジン17…発電
機、18…温水バイパス配管、19…冷温水、20…冷
却水、21…ジャケット温水温度調節器。1 ... Evaporator, 2 ... Absorber, 3 ... Condenser, 4 ... Low temperature regenerator, 5 ... High temperature regenerator, 6 ... Low temperature heat exchanger, 7 ... High temperature heat exchanger, 8 ... Refrigerant pump, 9 ... Solution pump 10 ... Exhaust gas / hot water heat exchanger, 11 ... Exhaust gas pipe, 12 ... Jacket cooling hot water pipe, 13 ... Hot water three-way valve, 14 ... Hot water temperature controller, 15 ... Hot water pump, 16 ... Engine 17 ... Generator , 18 ... Hot water bypass piping, 19 ... Cold / hot water, 20 ... Cooling water, 21 ... Jacket hot water temperature controller.
フロントページの続き (72)発明者 矢澤 國雄 東京都港区芝浦三丁目4番1号 株式会 社 エヌ・ティ・ティファシリティーズ 内 (72)発明者 福光 超 東京都港区芝浦三丁目4番1号 株式会 社 エヌ・ティ・ティファシリティーズ 内 (72)発明者 清川 浩二 東京都港区芝浦三丁目4番1号 株式会 社 エヌ・ティ・ティファシリティーズ 内 (56)参考文献 特開 平7−218019(JP,A) 特開 平8−233391(JP,A) (58)調査した分野(Int.Cl.7,DB名) F25B 27/02 F25B 15/00 303 Front Page Continuation (72) Inventor Kunio Yazawa 3-4-1, Shibaura, Minato-ku, Tokyo Inside NTT FACILITIES CORPORATION (72) Inventor Fukumitsu 3-4-1, Shibaura, Minato-ku, Tokyo Incorporated in NTT Facilities (72) Inventor Koji Kiyokawa 3-4-1, Shibaura, Minato-ku, Tokyo Incorporated in NTT Facilities (56) Reference JP-A-7-218019 ( JP, A) JP-A-8-233391 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) F25B 27/02 F25B 15/00 303
Claims (2)
器、低温再生器、凝縮機、吸収器、低温熱交換器、高温
熱交換器を動作的に配管接続してなる吸収式冷温水機
と、排気ガスを前記高温再生器に導く排気ガス導入手段
とを備えるエンジン排熱利用吸収冷温水機において、前
記高温再生器の排気ガス出口側に前記エンジンを冷却し
たジャケット冷温水が排気ガスと熱交換する熱交換器
を、前記エンジンとこの熱交換器との間にこの熱交換器
を通らずにエンジンに温水を戻す温水戻り配管を、熱交
換器の温水下流側にこの熱交換器で熱交換して温度の低
下した温水を低温再生器を通らずにエンジンに戻すバイ
パス配管をそれぞれ設け、前記温水戻り配管の分岐部に
ジャケット温水温度調節器を設け、このジャケット温水
温度調節器の働きにより、前記熱交換器に流入する温度
低下を防ぎ、前記バイパス配管に温度調節手段を設け、
前記温度調節手段で前記低温再生器からエンジンジャケ
ットに還流する温水温度を一定に保持するように制御す
ることを特徴とするエンジン排熱利用吸収冷温水機。Claims: 1. An absorption chiller-heater which uses an engine exhaust gas to operatively connect a high temperature regenerator, a low temperature regenerator, a condenser, an absorber, a low temperature heat exchanger, and a high temperature heat exchanger. In an absorption chiller-heater using engine exhaust heat, which comprises exhaust gas introduction means for guiding exhaust gas to the high-temperature regenerator, the jacket chilled water that has cooled the engine is exhausted from the exhaust gas and heat to the exhaust gas outlet side of the high-temperature regenerator. The heat exchanger to be exchanged, between the engine and this heat exchanger, the hot water return pipe that returns hot water to the engine without passing through this heat exchanger Bypass pipes are provided to return the hot water whose temperature has been lowered to the engine without passing through the low temperature regenerator, and to the branch part of the hot water return pipe.
This jacket hot water is equipped with a jacket hot water temperature controller.
The temperature flowing into the heat exchanger due to the function of the temperature controller
Prevent deterioration, a temperature adjusting means provided in the bypass pipe,
From the low temperature regenerator to the engine jacket by the temperature control means.
An absorption chiller-heater using exhaust heat from an engine, which is controlled to keep the temperature of the hot water flowing back to the tank constant .
側伝熱面の温度を排気ガスの結露温度以上に制御するこ
とを特徴とする請求項1に記載のエンジン排熱利用吸収
冷温水機。2. A pre-Symbol temperature adjustment means, the engine waste heat utilization according to claim 1, characterized in that to control the temperature of the gas-side heat transfer surface of the heat exchanger above condensation temperature of the exhaust gas Absorption chiller / heater.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP35436397A JP3400699B2 (en) | 1997-12-24 | 1997-12-24 | Absorption chiller / heater using engine exhaust heat |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP35436397A JP3400699B2 (en) | 1997-12-24 | 1997-12-24 | Absorption chiller / heater using engine exhaust heat |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH11182973A JPH11182973A (en) | 1999-07-06 |
JP3400699B2 true JP3400699B2 (en) | 2003-04-28 |
Family
ID=18437057
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP35436397A Expired - Fee Related JP3400699B2 (en) | 1997-12-24 | 1997-12-24 | Absorption chiller / heater using engine exhaust heat |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3400699B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106352591B (en) * | 2016-05-30 | 2020-01-31 | 李华玉 | Combined heat and power system |
-
1997
- 1997-12-24 JP JP35436397A patent/JP3400699B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH11182973A (en) | 1999-07-06 |
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