JPH05288327A - Energy recycling device - Google Patents

Energy recycling device

Info

Publication number
JPH05288327A
JPH05288327A JP4085677A JP8567792A JPH05288327A JP H05288327 A JPH05288327 A JP H05288327A JP 4085677 A JP4085677 A JP 4085677A JP 8567792 A JP8567792 A JP 8567792A JP H05288327 A JPH05288327 A JP H05288327A
Authority
JP
Japan
Prior art keywords
gas
steam
plant
discharged
tank
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.)
Withdrawn
Application number
JP4085677A
Other languages
Japanese (ja)
Inventor
Yoshihide Iijima
祥穎 飯島
Shunji Sudo
俊二 須藤
Masatomo Tsugawa
雅朋 津川
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.)
Kumagai Gumi Co Ltd
Original Assignee
Kumagai Gumi Co 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 Kumagai Gumi Co Ltd filed Critical Kumagai Gumi Co Ltd
Priority to JP4085677A priority Critical patent/JPH05288327A/en
Publication of JPH05288327A publication Critical patent/JPH05288327A/en
Withdrawn legal-status Critical Current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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

PURPOSE:To feed combustibles dusts as well as raw waste materials and sewage discharged from a city region to each of processing plants, recycle energy gener ated when each of the processing plants performs the processing to the city region, perform the energy recycling operation and make an effective utilization of it. CONSTITUTION:Digestive gas is generated with a digestive gas generating plant from the raw garbages and sewage muds discharged from city regions. Combustible dusts discharged from the city regions are ignited with a dust combustion boiler of a dust incineration and power generating plant so as to produce steam. The digestive gas is used for igniting dusts and as driving fuel for a gas turbine of a power generating plant. Combustion discharged gas from the gas turbine is injected and guided to an over-heater. The combustion discharging gas of high temperature of the gas turbine is fed out to the super heater, the steam from the dust incineration boiler is converted into an super heated steam and the steam turbine is driven by a super heated steam.

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、都市地域から排出され
るごみや下水を処理して得られるエネルギを、他のプラ
ントや都市地域へ還元するエネルギのリサイクル装置に
関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an energy recycling apparatus for returning energy obtained by treating refuse and sewage discharged from urban areas to other plants and urban areas.

【0002】[0002]

【従来の技術】都市地域から排出されるごみは、生ご
み、可燃ごみ、不燃ごみ等に大別でき、之等ごみを分別
収集して処理を行うことが多くなってきている。生ごみ
及び可燃ごみはごみ焼却プラントに運搬されて焼却され
ることが多く、この焼却炉の燃焼によりボイラーを沸か
し、ボイラーから発生する蒸気によって蒸気タービンを
回転させて発電機を駆動する。ここで、発生する蒸気温
度は、ボイラー熱交換部の高温腐食が懸念されるため3
00℃以下に制限され、発電される電力は小量となる。
この電力は、ごみ焼却プラント自体の運営に係るものに
使用されるほか、近時、プラントに近接して休養施設を
設け、この休養施設へ前記ごみ焼却プラントで発電した
電力を供給することも多くなっている。然るときは、ボ
イラーで沸かした熱湯を休養施設へ供給し、浴場等の給
湯に利用する。
2. Description of the Related Art Garbage discharged from urban areas can be roughly classified into raw garbage, combustible garbage, non-combustible garbage, etc., and it is becoming more common to dispose of such garbage separately for processing. Garbage and combustible waste are often transported to a refuse incineration plant for incineration, and a boiler is boiled by the combustion of this incinerator, and a steam turbine is rotated by steam generated from the boiler to drive a generator. Here, the generated steam temperature is 3 because the high temperature corrosion of the boiler heat exchange part is a concern.
The electric power generated is limited to less than 00 ° C and is small.
This electric power is used not only for the operation of the refuse incineration plant itself, but recently, a rest facility is established near the plant, and the power generated by the waste incineration plant is often supplied to this rest facility. Is becoming In that case, the hot water boiled by the boiler will be supplied to the rest facility and used for hot water supply at the bathhouse.

【0003】一方、都市地域の下水は下水処理プラント
へ集められ、下水処理水槽にて浄化されて河川又は海へ
放流される。
On the other hand, sewage in urban areas is collected in a sewage treatment plant, purified in a sewage treatment tank and discharged into a river or the sea.

【0004】[0004]

【発明が解決しようとする課題】従来のごみ焼却プラン
トで発生する蒸気は、熱交換部での高温腐食を懸念して
300℃程度に制限されており、高圧力・高過熱にする
ことができず、蒸気タービンの高効率運転は望めなかっ
た。そこで、ごみ焼却プラントで発生した蒸気により、
高効率な蒸気タービン駆動を図るために解決すべき技術
的課題が生じてくるのであり、本発明はこの課題を解決
することを目的とする。
The steam generated in the conventional refuse incineration plant is limited to about 300 ° C because of concern about high temperature corrosion in the heat exchange section, and high pressure and high overheat can be achieved. Therefore, high efficiency operation of the steam turbine could not be expected. Therefore, by the steam generated in the refuse incineration plant,
A technical problem to be solved in order to drive the steam turbine with high efficiency arises, and an object of the present invention is to solve this problem.

【0005】[0005]

【課題を解決するための手段】本発明は上記目的を達成
するために提案されたものであり、都市地域から排出さ
れる生ごみを収集し、この生ごみを粉砕して貯留槽に蓄
え、下水処理水槽を備えた下水処理プラントから採取し
た汚泥を濃縮して前記貯留槽の生ごみとともに消化槽へ
投入し、該消化槽にて消化ガスを発生させる消化ガス発
生プラントを設け、都市地域から排出される可燃ごみを
収集し、この可燃ごみをごみ焼却ボイラーで燃焼して蒸
気を発生し、蒸気タービンを回転させて発電機を駆動す
るごみ焼却及び発電プラントを設け、前記ごみ焼却及び
発電プラントにガスタービンを設け、該ガスタービンの
駆動燃料に前記消化ガス発生プラントにて発生した消化
ガスを使用するとともに、該ガスタービンの燃焼排ガス
をごみ焼却ボイラーの外部に設けた過熱器に導出して前
記ごみ焼却ボイラーからの蒸気を過熱蒸気に変換し、こ
の過熱蒸気により蒸気タービンを駆動するようにしたこ
とを特徴とするエネルギのリサイクル装置を提供するも
のである。
The present invention has been proposed in order to achieve the above object, and collects garbage discharged from urban areas, crushes this garbage and stores it in a storage tank, Sludge collected from a sewage treatment plant equipped with a sewage treatment water tank is concentrated and put into a digestion tank together with the garbage of the storage tank, and a digestion gas generation plant for generating a digestion gas in the digestion tank is provided. We collect combustible waste that is discharged, burn this combustible waste in a waste incineration boiler to generate steam, and install a waste incineration and power generation plant that drives a generator by rotating a steam turbine. A gas turbine is installed in the gas turbine, and the digested gas generated in the digested gas generation plant is used as a driving fuel for the gas turbine, and the combustion exhaust gas of the gas turbine is incinerated by a refuse incineration boiler. An energy recycling device characterized in that the steam from the refuse incineration boiler is converted into superheated steam by being led to a superheater provided outside the steam turbine, and the steam turbine is driven by the superheated steam. Is.

【0006】[0006]

【作用】消化ガス発生プラントでは、下水処理プラント
から採取した汚泥を濃縮し、貯留槽の生ごみとともに消
化槽へ投入する。消化槽では醗酵作用により消化ガスが
発生し、この消化ガスをごみ焼却及び発電プラントへ送
る。ごみ焼却及び発電プラントでは、前記消化ガスを燃
料としてガスタービンを駆動し、高温の燃焼排ガスを過
熱器に導出する。該過熱器はボイラーからの蒸気を過熱
蒸気に変換し、蒸気タービンを駆動する。又、前記ガス
タービン及び蒸気タービンに夫々発電機を接続して大電
力の発電を行う。
[Function] In the digestion gas generation plant, the sludge collected from the sewage treatment plant is concentrated and put into the digestion tank together with the garbage in the storage tank. Digestion gas is generated in the digestion tank by the fermentation action, and this digestion gas is sent to the refuse incineration and power generation plant. In a refuse incineration and power generation plant, a gas turbine is driven by using the digested gas as fuel, and high temperature combustion exhaust gas is led to a superheater. The superheater converts steam from the boiler to superheated steam and drives a steam turbine. Further, a generator is connected to each of the gas turbine and the steam turbine to generate a large amount of electric power.

【0007】[0007]

【実施例】以下、本発明の一実施例を図面に従って詳述
する。図1はエネルギのリサイクル装置の全体を示した
ものであり、都市地域を中心にして各プラントが設けら
れている。都市地域から排出される生ごみは消化ガス発
生プラントへ送られ、可燃ごみはごみ焼却及び発電プラ
ントへ送られる。又、都市地域の下水は下水処理プラン
トで処理され、汚泥として前記消化ガス発生プラントへ
送られる。又、熱供給プラントでは熱ポンプとボイラに
より、蓄熱槽へ温水、熱源水、冷水を分別して蓄え、夫
々をエネルギとして都市地域へ供給するとともに、他の
プラントとの間で熱エネルギ交換を行う。海水淡水化プ
ラントでは、海水を蒸留して淡水化し、都市地域へ供給
する。
An embodiment of the present invention will be described in detail below with reference to the drawings. FIG. 1 shows the entire energy recycling apparatus, and each plant is provided mainly in an urban area. Garbage discharged from urban areas is sent to a digestion gas generation plant, and combustible waste is sent to a refuse incineration and power generation plant. The sewage in the urban area is treated in a sewage treatment plant and sent to the digestion gas generation plant as sludge. In the heat supply plant, hot water, heat source water, and cold water are separated and stored in a heat storage tank by a heat pump and a boiler, each of which is supplied as energy to a city area, and heat energy is exchanged with other plants. The seawater desalination plant distills seawater into desalination and supplies it to urban areas.

【0008】図2は都市地域を示し、各家庭から排出さ
れるごみは、ステラークによって生ごみと可燃ごみを分
別収集し、生ごみは消化ガス発生プラントへ運搬され、
可燃ごみはごみ焼却及び発電プラントへ運搬される。都
市地域の下水は、地下の下水管を経て下水処理プラント
へ送られる。そして、前述した熱供給プラントの蓄熱槽
からパイプラインを経て冷水(約4℃)を受水し、事務
所等のビル冷房設備に使用し、使用後の冷水(約12
℃)をパイプラインを経て熱供給プラントの蓄熱槽へ戻
す。又、パイプラインを経て該蓄熱槽から温水(約50
℃)を受水し、ビル暖房設備に使用する。使用後の温水
(約45℃)はパイプラインを経て熱供給プラントの蓄
熱槽へ戻す。更に、パイプラインを経て該蓄熱槽の熱源
水(約12〜25℃)を受水し、集合住宅等の熱ポンプ
装置に使用する。熱ポンプ装置では前記熱源水(約12
〜25℃)を吸熱源として暖房及び給湯を行う。使用後
の熱源水(約12〜50℃)はパイプラインを経て熱供
給プラントの蓄熱槽へ戻す。
[0008] Fig. 2 shows an urban area. The garbage discharged from each household is separated and collected by Stellak as raw garbage and combustible garbage, and the raw garbage is transported to a digestion gas generation plant.
Combustible waste is incinerated and transported to the power plant. Sewage in urban areas is sent to a sewage treatment plant via an underground sewage pipe. Then, cold water (about 4 ° C.) is received from the heat storage tank of the heat supply plant described above through the pipeline, and is used for building cooling equipment such as offices.
℃) is returned to the heat storage tank of the heat supply plant via the pipeline. In addition, hot water (about 50
℃) is received and used for building heating equipment. The used hot water (about 45 ° C) is returned to the heat storage tank of the heat supply plant through the pipeline. Further, the heat source water (about 12 to 25 ° C.) of the heat storage tank is received through a pipeline and used for a heat pump device such as an apartment house. In the heat pump device, the heat source water (about 12
(~ 25 ° C) is used as a heat absorption source for heating and hot water supply. The used heat source water (about 12 to 50 ° C.) is returned to the heat storage tank of the heat supply plant through the pipeline.

【0009】一方、海水淡水化プラントで淡水化された
造水はパイプラインを経て集合住宅等の給水設備に使用
される。又、ごみ焼却及び発電プラントで発電された電
気は、配電線を経て都市地域へ送電される。図3は消化
ガス発生プラントを示し、前記都市地域から排出される
生ごみを収集し、選別粉砕して貯留槽11に蓄えてゼリ
ー状に変化させる。又、下水処理プラントで採取される
汚泥のうち、初沈汚泥は円形放射流式の濃縮槽12で濃
縮し、終沈の余剰汚泥は汚泥スクリーン13で雑物を除
去した後に、横形スクリューコンベア式の濃縮機14で
濃縮する。
On the other hand, the desalinated water desalinated in the seawater desalination plant is used for water supply equipment such as an apartment house through a pipeline. In addition, the electricity generated by the refuse incineration and power generation plants is transmitted to the urban area through distribution lines. FIG. 3 shows a digestion gas generation plant in which raw garbage discharged from the urban area is collected, sorted and crushed, and stored in the storage tank 11 to be changed into jelly. Of the sludge collected at the sewage treatment plant, the first settling sludge is concentrated in the circular radial flow type thickening tank 12, and the surplus sludge at the final settling is removed by a sludge screen 13 to remove foreign matters, and then a horizontal screw conveyor type sludge is used. It concentrates with the concentrator 14 of.

【0010】之等濃縮汚泥は前記貯留槽に蓄えたゼリー
状の生ごみとともに、一次消化槽15へ投入される。こ
の一次消化槽15内では、投入された汚泥等が攪拌ポン
プ16により攪拌されながら醗酵し、メタン等の消化ガ
スを発生する。前記濃縮汚泥は一次消化槽15へ投入さ
れる前に汚泥熱交換器17を通過するが、ここには熱供
給プラントの蓄熱槽からパイプラインを経て温水(約5
0℃)が送られており、濃縮汚泥が暖められて一次消化
槽15へ投入後の醗酵作用を助成する。汚泥熱交換器1
7で使用した後の温水(約45℃)は、パイプラインを
経て再び熱供給プラントの蓄熱槽に戻される。尚、符号
18は攪拌ブロワーであり、一次消化槽15の内底部に
圧縮ガスを噴射し、この噴射ガスの上昇流により汚泥の
消化を促進させる。
The concentrated sludge is put into the primary digestion tank 15 together with the jelly-like food waste stored in the storage tank. In the primary digestion tank 15, the fed sludge and the like are fermented while being stirred by the stirring pump 16 to generate digestive gas such as methane. The concentrated sludge passes through the sludge heat exchanger 17 before being fed to the primary digestion tank 15, where hot water (about 5
(0 ° C.) is sent, the concentrated sludge is warmed, and the fermentation action after being added to the primary digestion tank 15 is assisted. Sludge heat exchanger 1
The hot water (about 45 ° C.) used in 7 is returned to the heat storage tank of the heat supply plant again through the pipeline. Reference numeral 18 is a stirring blower, which injects a compressed gas to the inner bottom portion of the primary digestion tank 15 and promotes digestion of sludge by the upward flow of the injection gas.

【0011】而して、該一次消化槽15にて発生した消
化ガスはガスタンク19に貯蔵され、後述するごみ焼却
及び発電プラントのガスタービンへ供給される。又、一
次消化槽15で消化ガスを発生した汚泥は二次消化槽2
0へ送られ、ここで汚泥の脱気処理を施した後、薬品混
和槽21及びベルトプレス22を経て脱水ケーキが生成
され、ごみ焼却及び発電プラントのごみ焼却ボイラーへ
運搬される。尚、ごみ焼却及び発電プラントで発電され
た電気は消化ガス発生プラント内の各施設へ電力供給さ
れ、電気の一部を都市地域へ送電する。
The digestion gas generated in the primary digestion tank 15 is stored in the gas tank 19 and supplied to the gas turbine of the refuse incineration and power generation plant described later. In addition, the sludge that generated digestion gas in the primary digestion tank 15 is the secondary digestion tank 2
0, where the sludge is degassed, then a dehydrated cake is produced through the chemical mixing tank 21 and the belt press 22 and transported to the refuse incineration boiler and the refuse incineration boiler of the power plant. The electricity generated by the refuse incineration and power generation plant is supplied to each facility in the digestion gas generation plant, and a part of the electricity is transmitted to the city area.

【0012】図4は、下水処理プラントを示し、都市地
域からの下水は下水管を経て下水処理装置23へ送られ
る。この下水処理装置23にて下水の汚泥を沈澱させ、
更に、濾過工程を経て下水処理水槽24へ貯水する。下
水処理装置23で採取した汚泥は、初沈汚泥と終沈の余
剰汚泥とに区別され、夫々が消化ガス発生プラントへ送
られる。
FIG. 4 shows a sewage treatment plant, and sewage from an urban area is sent to a sewage treatment device 23 via a sewage pipe. Sewage sludge is settled by this sewage treatment device 23,
Further, the water is stored in the sewage treatment water tank 24 through a filtration step. The sludge collected by the sewage treatment apparatus 23 is divided into first settled sludge and surplus settled sludge, and each is sent to a digestion gas generation plant.

【0013】一方、下水処理水槽24の下水処理水はポ
ンプPにより汲み上げられ、パイプラインを経て冷却水
(15〜25℃)としてごみ焼却及び発電プラントの復
水器、並びに熱供給プラントの熱ポンプへ送られる。そ
して、上記各プラントから往還してきた下水処理水(3
0〜40℃)は下水処理水槽24へ戻る。そして、該下
水処理水槽では河川水を取り込むとともに、浄化した下
水処理水を河川又は海へ放流する。
On the other hand, the sewage treatment water of the sewage treatment water tank 24 is pumped up by a pump P and passed through a pipeline as cooling water (15 to 25 ° C.) as a waste incinerator and a condenser of a power generation plant, and a heat pump of a heat supply plant. Sent to. Then, the treated sewage (3
(0 to 40 ° C.) is returned to the sewage treatment water tank 24. Then, in the sewage treatment tank, the river water is taken in and the purified sewage treatment water is discharged to the river or the sea.

【0014】図5はごみ焼却及び発電プラントを示し、
都市地域から排出される可燃ごみを収集し、前記消化ガ
ス発生プラントで生成される脱水ケーキとともに可燃ご
みをごみ焼却ボイラー25で燃焼する。該ごみ焼却ボイ
ラー25で発生した蒸気は、過熱器26でもう一度過熱
されてから蒸気溜27へ導出される。一方、消化ガス発
生プラントで発生した消化ガスはガスタービン28の駆
動燃料に使用され、該ガスタービン28が駆動されると
発電機29が回転して発電する。該ガスタービン28の
燃焼排ガスの温度は約500〜550℃と高温であり、
この燃焼排ガスを前記過熱器26の中へ通過させれば、
ごみ焼却ボイラー25で発生した蒸気の温度が過熱蒸気
(約400℃)となって蒸気溜27へ導出される。
FIG. 5 shows a refuse incineration and power plant,
Combustible waste discharged from urban areas is collected, and the combustible waste is burned in the waste incineration boiler 25 together with the dehydrated cake produced in the digestion gas generation plant. The steam generated in the refuse incineration boiler 25 is once again superheated by the superheater 26, and then is discharged to the steam reservoir 27. On the other hand, the digestion gas generated in the digestion gas generation plant is used as the driving fuel for the gas turbine 28, and when the gas turbine 28 is driven, the generator 29 rotates to generate electricity. The temperature of the combustion exhaust gas of the gas turbine 28 is as high as about 500 to 550 ° C.,
If this combustion exhaust gas is passed into the superheater 26,
The temperature of the steam generated in the refuse incineration boiler 25 becomes superheated steam (about 400 ° C.) and is discharged to the steam reservoir 27.

【0015】従って、極めて高温の過熱蒸気により蒸気
タービン30が駆動されるため、蒸気タービン30の熱
効率が著しく向上する。蒸気タービン30の駆動により
発電機31が回転して発電し、太陽光発電装置32によ
って発電された電気及び前記ガスタービン28によって
発電された電気とともに他の各プラントへ電気が送電さ
れ、その一部はごみ焼却及び発電プラント内の各施設へ
電力供給される。
Therefore, since the steam turbine 30 is driven by the superheated steam of extremely high temperature, the thermal efficiency of the steam turbine 30 is significantly improved. The generator 31 rotates by driving the steam turbine 30 to generate electric power, and the electric power generated by the solar power generation device 32 and the electric power generated by the gas turbine 28 are transmitted to each of the other plants, part of which is transmitted. Electric power is supplied to each facility in the refuse incineration and power plant.

【0016】蒸気タービン30の後段には復水器33を
設けてあり、前記下水処理プラントの下水処理水を往還
させて復水器33を冷却する。このため、復水器33内
の蒸気圧力が急速に低下し、水に戻って復水タンク34
及び35へ送られるので、蒸気タービン30の入口と出
口との圧力差が大となって熱効率が増大する。そして、
蒸気タービン30から抽気した蒸気で吸収冷凍機36を
稼働し、熱供給プラントの蓄熱槽から冷水(約12℃前
後)を導入し、該吸収冷凍機36で低温の冷水(約7〜
8℃)を造って熱供給プラントの熱ポンプへ導出する。
更に、蒸気タービン30で余剰となった抽気蒸気を熱供
給プラントのボイラーへ導出する。
A condenser 33 is provided at the subsequent stage of the steam turbine 30 to return the sewage treatment water of the sewage treatment plant to cool the condenser 33. For this reason, the steam pressure in the condenser 33 is rapidly reduced, returning to water and returning to the condensate tank 34.
And 35, the pressure difference between the inlet and the outlet of the steam turbine 30 becomes large and the thermal efficiency increases. And
The absorption refrigerator 36 is operated by the steam extracted from the steam turbine 30, cold water (about 12 ° C.) is introduced from the heat storage tank of the heat supply plant, and the absorption refrigerator 36 cools cold water (about 7 to
8 ° C) is produced and led to the heat pump of the heat supply plant.
Further, the excess extracted steam in the steam turbine 30 is led to the boiler of the heat supply plant.

【0017】前記ガスタービン28の燃焼排ガスは、過
熱器26を通過して排ガスボイラー37で蒸気を生成
し、この蒸気とごみ焼却ボイラー25で生成した蒸気と
を合流させる。更に、該燃焼排ガスは排ガス熱交換器3
8へ送られ、復水タンク34の水を加熱した後に外部へ
排出される。排ガス熱交換器38で加熱された温水は前
記蒸気タービンから抽気した温水とともに脱気器39へ
送られ、ここから、ごみ焼却ボイラー25及び排ガスボ
イラー37へ送られて、再度蒸気に変換する。
The combustion exhaust gas of the gas turbine 28 passes through the superheater 26 to generate steam in the exhaust gas boiler 37, and the steam and the steam generated in the refuse incineration boiler 25 join together. Further, the combustion exhaust gas is used as the exhaust gas heat exchanger 3
The water in the condensate tank 34 is heated and then discharged to the outside. The hot water heated in the exhaust gas heat exchanger 38 is sent to the deaerator 39 together with the hot water extracted from the steam turbine, and from there, sent to the refuse incineration boiler 25 and the exhaust gas boiler 37 to be converted into steam again.

【0018】図6は熱供給プラントを示し、製氷用の熱
ポンプ40及び冷水用の熱ポンプ41を設けてあり、夫
々の熱交換器42及び43と前記下水処理プラントの下
水処理水槽24との間をパイプラインで接続する。そし
て、このパイプラインから下水処理水(約15〜20
℃)を導入して熱ポンプ40及び41の吸熱源とし、熱
交換処理後の下水処理水を排熱源として下水処理プラン
トの下水処理水槽24へ戻す。熱ポンプ40が駆動され
ると蓄熱槽44の氷槽44a内の直膨コイル45へ冷媒
が往還し、氷槽44a内の水が氷水になる。熱ポンプ4
0の排熱は前記熱交換器42によって行われるが、蓄熱
槽44の熱源水槽44cからの循環水にも排熱する。
FIG. 6 shows a heat supply plant, in which a heat pump 40 for ice making and a heat pump 41 for cold water are provided, and the heat exchangers 42 and 43 are connected to the sewage treatment tank 24 of the sewage treatment plant. Connect between them with a pipeline. And from this pipeline, treated sewage water (about 15-20
(.Degree. C.) is introduced as an endothermic source of the heat pumps 40 and 41, and the sewage treated water after the heat exchange treatment is returned to the sewage treatment tank 24 of the sewage treatment plant as an exhaust heat source. When the heat pump 40 is driven, the refrigerant goes back and forth to the direct expansion coil 45 in the ice tank 44a of the heat storage tank 44, and the water in the ice tank 44a becomes ice water. Heat pump 4
Although the exhaust heat of 0 is performed by the heat exchanger 42, it is also exhausted to the circulating water from the heat source water tank 44c of the heat storage tank 44.

【0019】又、熱ポンプ41が駆動されると、前記ご
み焼却及び発電プラントの吸収冷凍機36から送られる
冷水(7〜8℃)を、熱ポンプ41の蒸発器へ導出して
更に冷却し、この冷水を蓄熱槽44の冷水槽44bへ戻
すとともに、熱源水槽44cにも冷水を戻す。冷水槽4
4bの冷水の一部と熱源水槽44cの熱源水の一部(約
12℃の冷水)は、再びごみ焼却及び発電プラントの吸
収冷凍機36へ送られ、該吸収冷凍機36によって低温
の冷水(約7〜8℃)が造られる。上記工程を繰り返す
ことによって低温度の冷水が段階的に生成され、冷水槽
44b内の温度を約4〜12℃に安定させる。又、熱ポ
ンプ41の排熱は前記熱交換器43によって行われる
が、蓄熱槽44の温水槽44dからの循環水にも排熱す
る。
When the heat pump 41 is driven, the cold water (7 to 8 ° C.) sent from the absorption chiller 36 of the refuse incineration and power generation plant is led to the evaporator of the heat pump 41 for further cooling. The cold water is returned to the cold water tank 44b of the heat storage tank 44 and is also returned to the heat source water tank 44c. Cold water tank 4
Part of the cold water of 4b and part of the heat source water of the heat source water tank 44c (cold water of about 12 ° C.) are sent again to the refuse incinerator and the absorption refrigerator 36 of the power generation plant, and the absorption refrigerator 36 cools the low temperature cold water ( About 7-8 ° C) is produced. By repeating the above process, low-temperature cold water is generated stepwise, and the temperature in the cold water tank 44b is stabilized at about 4 to 12 ° C. The heat of the heat pump 41 is exhausted by the heat exchanger 43, but is also exhausted to the circulating water from the hot water tank 44d of the heat storage tank 44.

【0020】一方、ごみ焼却及び発電プラントの蒸気タ
ービン30で余剰となった抽気蒸気は熱供給プラントの
ボイラー46へ導入され、この抽気蒸気を熱交換器47
で温水に変え、該温水を蓄熱槽44の温水槽44dへ貯
水する。従って、前述した熱ポンプ41からの循環水と
も相俟って、温水槽44d内の温度は約45〜50℃に
安定する。又、熱交換器47から熱源水槽44cにも温
水を供給し、この温水と前記熱ポンプ40の循環水並び
に熱ポンプ41からの冷水とが混和して、熱源水槽44
c内の温度は約12〜25℃に安定する。
On the other hand, the excess extracted steam in the steam turbine 30 of the refuse incineration and power generation plant is introduced into the boiler 46 of the heat supply plant, and the extracted steam is exchanged with the heat exchanger 47.
Is changed to hot water, and the hot water is stored in the hot water tank 44d of the heat storage tank 44. Therefore, in combination with the circulating water from the heat pump 41 described above, the temperature in the hot water tank 44d is stabilized at about 45 to 50 ° C. Further, hot water is also supplied from the heat exchanger 47 to the heat source water tank 44c, and this hot water is mixed with the circulating water of the heat pump 40 and the cold water from the heat pump 41 to form the heat source water tank 44c.
The temperature in c stabilizes at about 12-25 ° C.

【0021】而して、蓄熱槽44の氷槽44aの氷水及
び冷水槽44bの冷水は四方切替弁48を通過して合流
し、この冷水(約4℃)はパイプラインを経て都市地域
の事務所等のビル冷房設備へ供給される。そして、ビル
冷房設備で使用後の冷水(約12℃)はパイプラインを
経て、再び冷水槽44bに戻される。又、蓄熱槽44の
熱源水槽44cの熱源水(約12〜25℃)はパイプラ
インを経て集合住宅等の熱ポンプ装置へ供給される。そ
して、該熱ポンプ装置で使用後の熱源水(約12〜50
℃)はパイプラインを経て、再び熱源水槽44cに戻さ
れる。
Thus, the ice water in the ice tank 44a of the heat storage tank 44 and the cold water in the cold water tank 44b merge through the four-way switching valve 48, and this cold water (about 4 ° C.) passes through the pipeline to work in the urban area. It is supplied to the building cooling facilities such as offices. Then, the cold water (about 12 ° C.) after being used in the building cooling equipment is returned to the cold water tank 44b again through the pipeline. Further, the heat source water (about 12 to 25 ° C.) in the heat source water tank 44c of the heat storage tank 44 is supplied to a heat pump device such as an apartment house through a pipeline. Then, the heat source water (about 12 to 50) after being used in the heat pump device.
(° C) is returned to the heat source water tank 44c again through the pipeline.

【0022】更に、蓄熱槽44の温水槽44dの温水
(約50℃)は、パイプラインを経て都市地域の事務所
等のビル暖房設備へ供給される。そして、ビル暖房設備
で使用後の温水(約45℃)はパイプラインを経て、再
び温水槽44dに戻される。又、該温水槽44dの温水
(約50℃)の一部は、パイプラインを経て消化ガス発
生プラントへ供給され、前述したように、汚泥熱交換器
17で濃縮汚泥を加温して醗酵作用を助成する。そし
て、消化ガス発生プラントで使用後の温水(約45℃)
はパイプラインを経て、再び温水槽44dに戻される。
Further, the hot water (about 50 ° C.) in the hot water tank 44d of the heat storage tank 44 is supplied to the building heating equipment such as offices in urban areas through the pipeline. Then, the hot water (about 45 ° C.) after being used in the building heating equipment is returned to the hot water tank 44d again through the pipeline. Further, a part of the hot water (about 50 ° C.) in the hot water tank 44d is supplied to the digestion gas generating plant through the pipeline, and as described above, the sludge heat exchanger 17 heats the concentrated sludge to ferment the sludge. Subsidize. And hot water (about 45 ° C) after use in the digestion gas generation plant
Is returned to the hot water tank 44d again through the pipeline.

【0023】図7は海水淡水化プラントを示し、海水を
ポンプPによって海水蒸留装置49に汲み上げる。前記
ごみ焼却及び発電プラントから熱供給プラントへ導出さ
れた抽気蒸気の一部は、この海水淡水化プラントの海水
蒸留装置49にも導入される。該海水蒸留装置49で
は、前記抽気蒸気によって海水を蒸発させた後に凝縮
し、海水を淡水化して造水タンク50に貯水する。造水
された淡水は、ポンプPによりパイプラインを経て都市
地域へ供給され、集合住宅等の給水設備に使用される。
FIG. 7 shows a seawater desalination plant in which seawater is pumped by a pump P to a seawater distillation apparatus 49. A part of the extracted steam discharged from the refuse incineration and power generation plant to the heat supply plant is also introduced to the seawater distillation apparatus 49 of this seawater desalination plant. In the seawater distillation device 49, the extracted steam is used to evaporate the seawater and then condense it to desalinate it and store it in the fresh water tank 50. The fresh water produced is supplied to the city area through the pipeline by the pump P and used for water supply facilities such as apartment houses.

【0024】尚、本発明は、本発明の精神を逸脱しない
限り種々の改変を為すことができ、そして、本発明が該
改変されたものに及ぶことは当然である。
The present invention can be variously modified without departing from the spirit of the present invention, and it goes without saying that the present invention covers the modified ones.

【0025】[0025]

【発明の効果】本発明は上記一実施例に詳述したよう
に、都市地域から回収した生ごみや下水汚泥を醗酵させ
て消化ガスを生成し、この消化ガスをガスタービンの駆
動燃料に使用する。従って、ガスタービンの駆動コスト
が低減されるとともに、高温の燃焼排ガスを加熱器に導
出してボイラーからの蒸気を過熱蒸気に変換することが
可能となる。この過熱蒸気によって蒸気タービンを駆動
すれば、蒸気タービンの熱効率が著しく増大し、発電能
力も向上する。
INDUSTRIAL APPLICABILITY As described in detail in the above one embodiment, the present invention ferments raw garbage and sewage sludge collected from urban areas to produce digestive gas, which is used as a driving fuel for a gas turbine. To do. Therefore, the driving cost of the gas turbine can be reduced, and the high temperature combustion exhaust gas can be led to the heater to convert the steam from the boiler into superheated steam. When the steam turbine is driven by this superheated steam, the thermal efficiency of the steam turbine is significantly increased and the power generation capacity is also improved.

【0026】斯くして、一つのプラントで発生したエネ
ルギを他のプラントへ供給できるとともに、都市地域へ
エネルギを還元してエネルギの有効利用を図ることが可
能となる。
Thus, the energy generated in one plant can be supplied to another plant, and the energy can be returned to the urban area for effective use.

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

【図1】エネルギのリサイクル装置全体の概念を示すブ
ロック図。
FIG. 1 is a block diagram showing the concept of the entire energy recycling apparatus.

【図2】都市地域を示す解説図。[Figure 2] Explanatory diagram showing urban areas.

【図3】消化ガス発生プラントを示す解説図。FIG. 3 is an explanatory diagram showing a digestion gas generation plant.

【図4】下水処理プラントを示す解説図。FIG. 4 is an explanatory diagram showing a sewage treatment plant.

【図5】ごみ焼却及び発電プラントを示す解説図。FIG. 5 is an explanatory diagram showing a refuse incineration and power generation plant.

【図6】熱供給プラントを示す解説図。FIG. 6 is an explanatory diagram showing a heat supply plant.

【図7】海水淡水化プラントを示す解説図。FIG. 7 is an explanatory diagram showing a seawater desalination plant.

【符号の説明】[Explanation of symbols]

11 貯留槽 15 一次消化槽 23 下水処理装置 24 下水処理水槽 25 ごみ焼却ボイラー 26 過熱器 28 ガスタービン 29,31 発電機 30 蒸気タービン 11 Storage Tank 15 Primary Digestion Tank 23 Sewage Treatment Equipment 24 Sewage Treatment Water Tank 25 Waste Incineration Boiler 26 Superheater 28 Gas Turbine 29, 31 Generator 30 Steam Turbine

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 F02C 6/00 E 7910−3G F22B 1/18 G 7526−3L F23G 5/02 E 7815−3K 5/46 Z 7815−3K ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 5 Identification number Office reference number FI technical display location F02C 6/00 E 7910-3G F22B 1/18 G 7526-3L F23G 5/02 E 7815-3K 5 / 46 Z 7815-3K

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 都市地域から排出される生ごみを収集
し、この生ごみを粉砕して貯留槽に蓄え、下水処理水槽
を備えた下水処理プラントから採取した汚泥を濃縮して
前記貯留槽の生ごみとともに消化槽へ投入し、該消化槽
にて消化ガスを発生させる消化ガス発生プラントを設
け、都市地域から排出される可燃ごみを収集し、この可
燃ごみをごみ焼却ボイラーで燃焼して蒸気を発生し、蒸
気タービンを回転させて発電機を駆動するごみ焼却及び
発電プラントを設け、前記ごみ焼却及び発電プラントに
ガスタービンを設け、該ガスタービンの駆動燃料に前記
消化ガス発生プラントにて発生した消化ガスを使用する
とともに、該ガスタービンの燃焼排ガスをごみ焼却ボイ
ラーの外部に設けた過熱器に導出して前記ごみ焼却ボイ
ラーからの蒸気を過熱蒸気に変換し、この過熱蒸気によ
り蒸気タービンを駆動するようにしたことを特徴とする
エネルギのリサイクル装置。
1. Collecting food waste discharged from an urban area, crushing this food waste and storing it in a storage tank, concentrating sludge collected from a sewage treatment plant equipped with a sewage treatment water tank, A digestive gas generation plant that puts garbage into the digestion tank and generates digestion gas in the digestion tank is installed to collect combustible waste discharged from urban areas, and burn the combustible waste in a refuse incineration boiler to generate steam. Is installed, a waste incineration and power generation plant that drives a generator by rotating a steam turbine is installed, a gas turbine is installed in the waste incineration and power generation plant, and the digestion gas generation plant is used as driving fuel for the gas turbine. In addition to using the digested gas, the exhaust gas from the gas turbine is discharged to a superheater provided outside the refuse incineration boiler to superheat the steam from the refuse incineration boiler. An energy recycling device that converts the air into a steam and drives the steam turbine with this superheated steam.
JP4085677A 1992-04-07 1992-04-07 Energy recycling device Withdrawn JPH05288327A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4085677A JPH05288327A (en) 1992-04-07 1992-04-07 Energy recycling device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4085677A JPH05288327A (en) 1992-04-07 1992-04-07 Energy recycling device

Publications (1)

Publication Number Publication Date
JPH05288327A true JPH05288327A (en) 1993-11-02

Family

ID=13865470

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4085677A Withdrawn JPH05288327A (en) 1992-04-07 1992-04-07 Energy recycling device

Country Status (1)

Country Link
JP (1) JPH05288327A (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0709622A1 (en) 1994-10-25 1996-05-01 Hitachi, Ltd. Waste incineration heat conversion system
WO2001011289A1 (en) * 1999-08-06 2001-02-15 Maejima, Fumio Multi-function treating device
JP2002276387A (en) * 2001-03-15 2002-09-25 Mitsui Eng & Shipbuild Co Ltd Biomass generation system and biomass generation method using it
JP2002310419A (en) * 2001-04-12 2002-10-23 Meidensha Corp Thermal decomposition facility by gas engine power generation facility using digestive gas
JP2003083085A (en) * 2001-09-07 2003-03-19 Tsukishima Kikai Co Ltd Method and facility for obtaining electric power and heat energy from digested gas
JP2004066094A (en) * 2002-08-06 2004-03-04 Kawasaki Heavy Ind Ltd Treatment method in sewage disposal plant for garbage disposer waste water
JP2005270778A (en) * 2004-03-24 2005-10-06 Ebara Corp Digestion gas utilizing method and digestion gas utilizing apparatus
JP2006144633A (en) * 2004-11-18 2006-06-08 Tokyo Metropolitan Sewerage Service Corp System and method for incinerating disposal objects
JP2006167705A (en) * 2004-11-22 2006-06-29 Tsukishima Kikai Co Ltd Biomass treatment method in sewage treatment plant
JP2008253963A (en) * 2007-04-09 2008-10-23 Kawasaki Plant Systems Ltd Treating method and treatment facility of waste and sewage
JP2019141769A (en) * 2018-02-19 2019-08-29 三菱日立パワーシステムズ株式会社 Plant, biomass fuel manufacturing system, biomass power generation facility, plant operating method, and biomass fuel manufacturing method

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0709622A1 (en) 1994-10-25 1996-05-01 Hitachi, Ltd. Waste incineration heat conversion system
WO2001011289A1 (en) * 1999-08-06 2001-02-15 Maejima, Fumio Multi-function treating device
JP4598976B2 (en) * 2001-03-15 2010-12-15 三井造船株式会社 Biomass power generation system and biomass power generation method using the same
JP2002276387A (en) * 2001-03-15 2002-09-25 Mitsui Eng & Shipbuild Co Ltd Biomass generation system and biomass generation method using it
JP2002310419A (en) * 2001-04-12 2002-10-23 Meidensha Corp Thermal decomposition facility by gas engine power generation facility using digestive gas
JP2003083085A (en) * 2001-09-07 2003-03-19 Tsukishima Kikai Co Ltd Method and facility for obtaining electric power and heat energy from digested gas
JP2004066094A (en) * 2002-08-06 2004-03-04 Kawasaki Heavy Ind Ltd Treatment method in sewage disposal plant for garbage disposer waste water
JP2005270778A (en) * 2004-03-24 2005-10-06 Ebara Corp Digestion gas utilizing method and digestion gas utilizing apparatus
JP2006144633A (en) * 2004-11-18 2006-06-08 Tokyo Metropolitan Sewerage Service Corp System and method for incinerating disposal objects
JP4707370B2 (en) * 2004-11-18 2011-06-22 東京都下水道サービス株式会社 Processed object incineration system and processable object incineration method
JP2006167705A (en) * 2004-11-22 2006-06-29 Tsukishima Kikai Co Ltd Biomass treatment method in sewage treatment plant
JP2008253963A (en) * 2007-04-09 2008-10-23 Kawasaki Plant Systems Ltd Treating method and treatment facility of waste and sewage
JP2019141769A (en) * 2018-02-19 2019-08-29 三菱日立パワーシステムズ株式会社 Plant, biomass fuel manufacturing system, biomass power generation facility, plant operating method, and biomass fuel manufacturing method

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