JPH0629568B2 - Power generation system - Google Patents
Power generation systemInfo
- Publication number
- JPH0629568B2 JPH0629568B2 JP24703686A JP24703686A JPH0629568B2 JP H0629568 B2 JPH0629568 B2 JP H0629568B2 JP 24703686 A JP24703686 A JP 24703686A JP 24703686 A JP24703686 A JP 24703686A JP H0629568 B2 JPH0629568 B2 JP H0629568B2
- Authority
- JP
- Japan
- Prior art keywords
- air
- tank
- turbine generator
- gas turbine
- power generation
- 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 - Lifetime
Links
- 238000010248 power generation Methods 0.000 title claims description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 36
- 239000010865 sewage Substances 0.000 claims description 18
- 238000010438 heat treatment Methods 0.000 claims description 15
- 238000002485 combustion reaction Methods 0.000 claims description 8
- 238000001816 cooling Methods 0.000 claims description 8
- 239000000446 fuel Substances 0.000 claims description 5
- 239000007789 gas Substances 0.000 description 51
- 238000005338 heat storage Methods 0.000 description 13
- 235000019645 odor Nutrition 0.000 description 6
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- 238000005273 aeration Methods 0.000 description 4
- 238000004065 wastewater treatment Methods 0.000 description 4
- 239000004576 sand Substances 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 230000001112 coagulating effect Effects 0.000 description 2
- 238000004332 deodorization Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000002828 fuel tank Substances 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 239000010840 domestic wastewater Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000010800 human waste Substances 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910017464 nitrogen compound Inorganic materials 0.000 description 1
- 150000002830 nitrogen compounds Chemical class 0.000 description 1
- 150000003018 phosphorus compounds Chemical class 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
- Activated Sludge Processes (AREA)
Description
【発明の詳細な説明】 〈産業上の利用分野〉 本発明は汚水処理と発電とを有機的に結合させると共
に、発電の際に発生する熱エネルギーを有効に利用する
ようにした発電システムに関する。DETAILED DESCRIPTION OF THE INVENTION <Industrial field of application> The present invention relates to a power generation system that organically combines sewage treatment and power generation and effectively uses thermal energy generated during power generation.
〈従来の技術とその問題点〉 体育館,映画館,演芸場,総合病院などの施設は大量の
電力を消費すると共に停電時の混乱や危険を回避する必
要があるところから予備あるいは非常用の自家発電装置
を備えている。これらの施設は住宅地の近辺あるいは繁
華街に建設されるところから、悪臭を発生する汚水処理
施設とは目的,性質を反対にしており、汚水処理施設は
住宅地の郊外に設置されるのが一般的である。<Conventional technology and its problems> Facilities such as gymnasiums, movie theaters, theaters, and general hospitals consume a large amount of power and need to avoid confusion and danger at the time of power outage, so that they can be used as spare or emergency homes. Equipped with a power generator. Since these facilities are constructed near residential areas or in downtown areas, they are opposite in purpose and nature to sewage treatment facilities that generate odors, and sewage treatment facilities are installed in the suburbs of residential areas. It is common.
従って、上記各種施設と汚水処理施設とはかけ離れた場
所に建設され、これらを有機的に結合した施設は未だ建
設されていないのが現状である。Therefore, it is the current situation that the above-mentioned various facilities and the wastewater treatment facility are constructed in a place far apart from each other, and the facility in which these are organically combined has not yet been constructed.
本発明は、汚水処理と発電とを有機的に結合させたもの
であり、特に汚水から発生する悪臭をなくし、しかも発
電の余剰エネルギーを各種施設に有効に利用し、これに
より各種施設と汚水処理施設とを一の建造物内に設ける
ようにした発電システムを提供することを目的としてい
る。INDUSTRIAL APPLICABILITY The present invention is an organic combination of wastewater treatment and power generation, in particular, it eliminates the offensive odor generated from wastewater, and effectively utilizes the surplus energy of power generation for various facilities. It is an object of the present invention to provide a power generation system in which facilities and facilities are provided in the same building.
〈問題点を解決するための手段〉 上記目的を達成するため本発明は、汚水処理槽を建造物
の地下部分に隔離し、汚水処理槽からの悪臭を高温で駆
動されるガスタービン発電機に供給するようにしたもの
である。すなわち本発明に係る発電システムは、汚水処
理槽を隔離するように建造物の地下部分に設けられ内部
が負圧に調整されてなる処理室と、処理室内の空気が燃
料燃焼用空気として供給されるガスタービン発電機と、
ガスタービン発電機の排ガスの潜熱から温水を得る熱交
換器と、熱交換器からの温水によって建造物の冷暖房を
行う冷暖房装置とを備えていることを特徴としている。<Means for Solving Problems> In order to achieve the above object, the present invention separates a sewage treatment tank into an underground part of a building, and a bad smell from the sewage treatment tank is applied to a gas turbine generator driven at high temperature. It is something that is supplied. That is, the power generation system according to the present invention is provided with a processing chamber which is provided in the underground part of the building so as to isolate the sewage treatment tank, and the inside of which is adjusted to a negative pressure, and the air in the processing chamber is supplied as air for fuel combustion. Gas turbine generator,
It is characterized by including a heat exchanger that obtains hot water from the latent heat of the exhaust gas of the gas turbine generator, and an air conditioner that cools and heats the building by the hot water from the heat exchanger.
〈実施例〉 以下、本発明を図面を参照して、さらに具体的に説明す
る。<Example> Hereinafter, the present invention will be described more specifically with reference to the drawings.
第1図は本発明の一実施例の概略断面図、第2図はその
地下部分の平面図、第3図は発電系統のブロック図であ
る。建造物1が住宅地あるいは繁華街に建造され、体育
館,映画館,演芸場等の各種施設を構成している。建造
物1は地上部分と地下部分とからなり、上記各種施設は
地上部分に設けられ、地下部分には汚水処理を行う処理
室2と発電を行う発電室3とが設けられている。処理室
2は周辺の住宅地,繁華街から排出されるし尿、生活排
水などを環境基準に合うように処理するものであり、各
種の汚水処理槽が配設されている。この汚水処理槽は、
沈砂槽4,曝気槽5,沈澱槽6,硝化槽7,脱窒槽8,
凝集沈澱槽9からなり、さらに流量調整槽,脱気槽,消
毒槽(いずれも図示せず)が中間に適宜、接続されてい
る。沈砂槽4は導入管10から流入する汚水中の土,
砂,紙等の異物を取り除き、曝気槽5はエアレーション
を行って曝気槽5に続く沈澱槽6で汚泥を沈澱させる。
硝化槽7では主にアンモニアの酸化分解を行い、脱窒槽
8では酸化窒素を還元除去し、これらにより汚水のBO
D,COD,SSの低減およびリン化合物や窒素化合物
の分解を行われ、環境基準値に適合した汚水は凝集沈澱
槽9を経て排出管11から河川等に放流される。なお、
このような一連の汚水処理槽は処理室2に複数列、配設
されて、汚水量が多くても適合することができるように
なっている。かかる処理室2は地上部分,発電室,その
他の部屋からコンクリート壁,ドアによって隔離されて
おり、さらに内部が負圧に維持されている。この負圧条
件は本実施例ではファン12によって維持されている。
すなわち、処理室2には送気ダクト13と吸気ダクト1
4とが汚水処理槽上方で対向配置されており、前記ファ
ン12は吸気ダクト14に取り付けられている。従っ
て、ファン12を駆動すると、吸気ダクト14によって
処理室2内が減圧状態となり、送気ダクト13から外気
が流入するが、この排出量と流入量とをバルブ15,1
6によって調整することにより負圧状態が得られる。こ
のように処理室2を建造物1の他の部屋から隔離し、な
おかつ処理室2内を負圧に維持することによって、処理
室2内の空気は吸気ダクト4を除く他の部屋から洩れる
ことがないと共に、処理室2のドアを開けても外気が流
入するだけの一方通行となるため、汚水処理槽から発生
する悪臭が外部、特に地上部分の各種施設、に洩れず不
快感を与えることがなくなる。FIG. 1 is a schematic sectional view of an embodiment of the present invention, FIG. 2 is a plan view of an underground portion thereof, and FIG. 3 is a block diagram of a power generation system. The building 1 is built in a residential area or a downtown area and constitutes various facilities such as a gymnasium, a movie theater, and a theater. The building 1 is composed of an above-ground portion and an underground portion, the above-mentioned various facilities are provided above the ground portion, and a treatment room 2 for treating wastewater and a power generation room 3 for generating electricity are provided in the underground portion. The treatment room 2 treats human waste, domestic wastewater, etc. discharged from surrounding residential areas and downtown areas so as to meet environmental standards, and is provided with various sewage treatment tanks. This sewage treatment tank is
Sand settling tank 4, aeration tank 5, settling tank 6, nitrification tank 7, denitrification tank 8,
It is composed of a coagulating sedimentation tank 9, and a flow rate adjusting tank, a deaeration tank, and a disinfection tank (none of which are shown) are appropriately connected in the middle. The sand settling tank 4 is the soil in the wastewater flowing from the introduction pipe 10,
Foreign substances such as sand and paper are removed, and the aeration tank 5 performs aeration to settle sludge in a settling tank 6 following the aeration tank 5.
The nitrification tank 7 mainly oxidizes and decomposes ammonia, and the denitrification tank 8 reduces and removes nitric oxide.
D, COD, SS are reduced and phosphorus compounds and nitrogen compounds are decomposed, and sewage that conforms to the environmental standard value is discharged from a discharge pipe 11 to a river or the like through a coagulating sedimentation tank 9. In addition,
Such a series of sewage treatment tanks are arranged in a plurality of rows in the treatment chamber 2 so that even a large amount of sewage can be accommodated. The processing chamber 2 is separated from the above-ground portion, the power generation chamber, and other rooms by a concrete wall and a door, and the inside is maintained at a negative pressure. This negative pressure condition is maintained by the fan 12 in this embodiment.
That is, the air supply duct 13 and the intake duct 1 are provided in the processing chamber 2.
4 are opposed to each other above the sewage treatment tank, and the fan 12 is attached to the intake duct 14. Therefore, when the fan 12 is driven, the inside of the processing chamber 2 is depressurized by the intake duct 14, and the outside air flows in from the air supply duct 13, but the discharge amount and the inflow amount are determined by the valves 15 and 1.
A negative pressure state is obtained by adjusting with 6. By isolating the processing chamber 2 from the other rooms of the building 1 and maintaining the negative pressure in the processing chamber 2 in this way, the air in the processing chamber 2 leaks from the other rooms except the intake duct 4. In addition, since the outside air flows in only one way even if the door of the treatment room 2 is opened, the offensive odor generated from the sewage treatment tank does not leak to the outside, especially various facilities on the ground, and gives an unpleasant feeling. Disappears.
前記発電室3は処理室2と同様にコンクリート壁によっ
て隔離されており、内部には発電機17が設けられ、地
上部分に設けられた各種施設の照明器具,空調器などの
各種機器に電気を供給するようになっている。本発明に
おいて、この発電機17はガスタービン発電機が使用さ
れている。かかるガスタービン発電機17は航空機,船
舶等の駆動力となるジェットエンジンに発電装置が組み
込まれてなり、従来公知のものが使用できるため、その
詳細を省略するが、このガスタービン発電機17は80
0℃以上の高温で燃焼し、この高温度を利用して悪臭の
無臭化および熱エネルギーの有効利用を図っている。ま
ず、悪臭の無臭化は前記処理室2内の空気を吸気ダクト
14からガスタービン発電機17に導き、燃料燃焼用空
気として供給することにより行われる。又、熱エネルギ
ーの有効利用はガスタービン発電機17からの排ガスを
熱交換器18に導くことによって行われる。ここで、ガ
スタービン発電機17は駆動時に騒音を発生するが、こ
の騒音はガスターイン発電機17の高速の回転数から生
じる周波数の高い音波であるため、周囲のコンクリート
壁に容易に吸収されて外部に伝幡することがない。従っ
て、建造物9の各施設に騒音が達することがなく、騒音
障害が生じることがない。Like the processing chamber 2, the power generation chamber 3 is separated by a concrete wall, and a generator 17 is provided inside the power generation chamber 3 to supply electricity to various equipment such as lighting fixtures and air conditioners of various facilities provided on the ground. It is supposed to be supplied. In the present invention, the generator 17 is a gas turbine generator. The gas turbine generator 17 has a power generator built into a jet engine that serves as a driving force for an aircraft, a ship, etc., and a conventionally known one can be used. Therefore, details thereof will be omitted. 80
Combustion is performed at a high temperature of 0 ° C or higher, and by utilizing this high temperature, the odor is eliminated and the heat energy is effectively used. First, deodorization of a bad odor is performed by introducing the air in the processing chamber 2 from the intake duct 14 to the gas turbine generator 17 and supplying the air as fuel combustion air. Further, effective use of heat energy is performed by introducing exhaust gas from the gas turbine generator 17 to the heat exchanger 18. Here, the gas turbine generator 17 generates noise when it is driven, but since this noise is a high frequency sound wave generated from the high speed rotation of the gas turbine generator 17, it is easily absorbed by the surrounding concrete wall. It doesn't spread outside. Therefore, noise does not reach each facility of the building 9 and no noise trouble occurs.
次に、前記発電システムを第3図により説明する。同図
において、19は燃料タンク,20は煙突,21は蓄熱
槽,22は冷暖房装置,23は給湯槽である。ガスター
ビン発電機17からの排ガスのガス路24は前記熱交換
器18に接続される第1のガス路25と煙突20に接続
される第2のガス路26とに分岐され、前記第1のガス
路25は熱交換器18を出た後、第2のガス路26に接
続されている。各ガス路25,26にはバルブ27,2
8が配設されてガス路の開閉および流量調整が行われる
ようになっており、これによりガスタービン発電機17
からの排ガスは主に、第1のガス路25から熱交換器1
8に導かれるが、第2のガス路26から直接、煙突20
に導かれて大気中に放出することも可能となっている。
ガスタービン発電機17には燃料タンク19から重油な
どの燃料が供給されると共に、燃料燃焼用の空気が処理
室2から供給される。かかる処理室2の空気内には各種
汚水処理槽から発生した硫化水素,フェノール,メルカ
プタン,アンモニア等の悪臭気体が含有されており、ガ
スタービン発電機17内で800℃以上の高温に曝され
ることにより、これらが分解して悪臭化される。このよ
うな悪臭気体を無臭化する方法として、従来では活性炭
吸着,酸化還元処理あるいは地中へ導き、地中内の細菌
による分解等が行われているが、大量の悪臭気体を発生
する汚水処理施設へ適用するには操作が面倒で、高価と
なるばかりでなく、完全な無臭化ができないものであっ
た。又、上記のような悪臭気体は温度耐性が高く、ディ
ーゼルエンジンなどが発生する燃焼熱では熱分解ができ
ない。本発明におけるガスタービン発電機17はジェッ
トエンジンから800〜850℃の高温の燃焼熱が発生
し、この高温下に曝されるため悪臭気体は容易に分解さ
れて無臭化される。又、ジェットエンジンの駆動には大
量の空気が必要であるが、この空気が全て処理室2から
供給されるため汚水処理槽から悪臭気体が大量に発生し
ても完全な悪臭化が可能となっている。29は三方弁3
0を介して煙突20に接続された分岐管であり、処理室
2からの空気を煙突20に直接に導くように作用する。
この分岐管29は処理室2内の空気に悪臭気体が大量に
含有されておらず、周囲に悪臭を感じさせない場合に使
用されて煙突20から直接、大気放出を行い、ガスター
ビン発電機17へ空気供給を行わない。これにより、悪
臭気体によってガスタービン発電機17が犯されること
がなく、延命化が可能となっている。Next, the power generation system will be described with reference to FIG. In the figure, 19 is a fuel tank, 20 is a chimney, 21 is a heat storage tank, 22 is an air conditioner, and 23 is a hot water supply tank. The gas passage 24 of the exhaust gas from the gas turbine generator 17 is branched into a first gas passage 25 connected to the heat exchanger 18 and a second gas passage 26 connected to the chimney 20, and the first gas passage 25 is connected to the first gas passage 25. After exiting the heat exchanger 18, the gas passage 25 is connected to the second gas passage 26. Valves 27 and 2 are provided in each gas passage 25 and 26.
8 is arranged to open and close the gas passage and adjust the flow rate, whereby the gas turbine generator 17
Exhaust gas from the heat exchanger 1 mainly flows from the first gas passage 25.
8, but directly from the second gas path 26 to the chimney 20.
It is also possible to be released into the atmosphere by being guided by.
Fuel such as heavy oil is supplied to the gas turbine generator 17 from the fuel tank 19, and air for fuel combustion is supplied from the processing chamber 2. The air in the processing chamber 2 contains malodorous gases such as hydrogen sulfide, phenol, mercaptan, and ammonia generated from various wastewater treatment tanks, and is exposed to a high temperature of 800 ° C. or higher in the gas turbine generator 17. As a result, these are decomposed and turned into malodor. As a method for deodorizing such malodorous gas, conventionally, adsorption of activated carbon, redox treatment, or introduction into the ground and decomposition by bacteria in the ground are performed, but treatment of sewage that generates a large amount of malodorous gas Not only was the operation cumbersome and expensive to apply to facilities, but it was also impossible to completely eliminate odor. Further, the above malodorous gas has high temperature resistance and cannot be thermally decomposed by the combustion heat generated by a diesel engine or the like. In the gas turbine generator 17 of the present invention, a jet engine generates high-temperature combustion heat of 800 to 850 ° C., and since it is exposed to this high temperature, the malodorous gas is easily decomposed and deodorized. Further, a large amount of air is required to drive the jet engine, but since all this air is supplied from the processing chamber 2, even if a large amount of malodorous gas is generated from the sewage treatment tank, complete malodorization is possible. ing. 29 is a three-way valve 3
It is a branch pipe connected to the chimney 20 via 0, and acts so as to guide the air from the processing chamber 2 directly to the chimney 20.
This branch pipe 29 is used when a large amount of malodorous gas is not contained in the air in the processing chamber 2 and does not cause a bad smell in the surroundings, so that the air is directly emitted from the chimney 20 to the gas turbine generator 17. Do not supply air. As a result, the gas turbine generator 17 is not violated by the malodorous gas and the life can be extended.
前記熱交換器18はガスタービン発電機17からの排ガ
スが導かれ、排ガスの潜熱によって水を加熱する。この
加熱は約80〜85℃の温度の高温水と高温水よりも低
温(約55〜65℃)の蓄熱水を得る2段階で行われ
る。図中、30は高温水が循環する高温循環路であり、
熱交換器18の高温部18aと給湯槽23と冷暖房装置
22とを高温水が循環するように接続する。又、31は
蓄熱水が循環する蓄熱循環路であり、熱交換器18の蓄
熱部18bと蓄熱槽21との間を蓄熱水が循環するよう
に接続する。ここで熱交換器18は従来、公知のものが
使用できるが、第4図を例として説明する。この熱交換
器18は内部が大気圧以下の減圧状態に維持される減圧
蒸気室32内に複数の煙管33が挿通されると共に、減
圧蒸気室32の上部には各循環路30および31と接続
される熱交換管34,35が挿通されて構成されてい
る。又、減圧蒸気室32内には熱媒水36が貯留されて
おり、煙管33にガスタービン発電機17からの高温の
排ガスが流入すると、熱媒水36が熱を吸収して蒸気と
なり、熱交換管34,35をそれぞれ所定温度に加熱し
て熱交換を行う。従って、高温の排ガスは低温となって
煙突20から排出され、排ガスの潜熱は水の熱エネルギ
ーに変換され、以下に述べる熱エネルギーの有効利用が
行われる。まず、高温水は高温循環路30から給湯槽2
3および冷暖房装置22に導かれる。給湯槽23は建造
物1に配管された水道,シャワー設備,風呂等に高温水
を供給する。一方、建造物1には使用目的に応じた各ホ
ール37が形成されており、各ホール37には冷暖房を
行う空調器38が設けられている。前記冷暖房装置22
は、例えばヒートポンプが使用され、高温水によって各
空調器38を駆動する。従って、熱交換器18からの高
温水によって給湯および冷暖房が行われるから、これら
の駆動のため電源が不要となり、電力の節約が可能とな
る。次に、蓄熱槽21に貯留されている蓄熱水は管路3
9によって建造物1の床暖房に適用される。このため建
造物1の床下には蓄熱水が流通する複数本のパイプライ
ン40が配管されており、ポンプ(図示せず)等によっ
てパイプライン40に蓄熱水が供給されると床全体が高
温に加温され、床暖房が行われる。これにより、排ガス
の潜熱が床暖房に利用されるから熱エネルギーの有効利
用が可能となっている。かかる床暖房は暖空気を強制的
に室内に送る空調暖房と異なり、空気流による騒音が生
じない。従って、騒音障害のない暖房ができるから建造
物1がコンサートホール,会議場等の騒音が気になる施
設の場合に、特に有効となっている。又、高温水よりも
蓄熱水の収量が多いところから蓄熱槽21の貯水量を多
くして、温水プール等に温水を供給することも可能であ
る。The heat exchanger 18 receives the exhaust gas from the gas turbine generator 17, and heats water by the latent heat of the exhaust gas. This heating is performed in two stages to obtain high temperature water having a temperature of about 80 to 85 ° C. and heat storage water having a lower temperature (about 55 to 65 ° C.) than the high temperature water. In the figure, 30 is a high temperature circulation path through which high temperature water circulates,
The high temperature part 18a of the heat exchanger 18, the hot water supply tank 23, and the cooling / heating device 22 are connected so that high temperature water circulates. Reference numeral 31 is a heat storage circulation path through which the heat storage water circulates, and is connected between the heat storage portion 18b of the heat exchanger 18 and the heat storage tank 21 so that the heat storage water circulates. Here, as the heat exchanger 18, a conventionally known one can be used, but the heat exchanger 18 will be described by taking FIG. 4 as an example. In this heat exchanger 18, a plurality of smoke pipes 33 are inserted into a depressurized steam chamber 32 whose inside is maintained at a depressurized state below atmospheric pressure. The heat exchange pipes 34 and 35 are inserted and configured. Further, the heat transfer water 36 is stored in the reduced pressure steam chamber 32, and when the high-temperature exhaust gas from the gas turbine generator 17 flows into the smoke pipe 33, the heat transfer water 36 absorbs the heat and becomes steam, The exchange tubes 34 and 35 are heated to a predetermined temperature to perform heat exchange. Therefore, the high-temperature exhaust gas becomes a low temperature and is discharged from the chimney 20, the latent heat of the exhaust gas is converted into the thermal energy of water, and the thermal energy described below is effectively used. First, the high temperature water is supplied from the high temperature circuit 30 to the hot water supply tank 2
3 and the heating and cooling device 22. The hot water supply tank 23 supplies high-temperature water to the water supply, the shower equipment, the bath, etc., which are piped to the building 1. On the other hand, the building 1 is formed with each hole 37 according to the purpose of use, and each hole 37 is provided with an air conditioner 38 for cooling and heating. The air conditioner 22
For example, a heat pump is used, and each air conditioner 38 is driven by hot water. Therefore, hot water from the heat exchanger 18 is used for hot water supply and cooling / heating, so that no power supply is required to drive them, and power can be saved. Next, the heat storage water stored in the heat storage tank 21 is stored in the pipeline 3
9 applies to floor heating of Building 1. Therefore, under the floor of the building 1, a plurality of pipelines 40 through which the stored heat flows are laid, and when the stored water is supplied to the pipeline 40 by a pump (not shown) or the like, the entire floor becomes hot. It is heated and the floor is heated. As a result, the latent heat of the exhaust gas is used for floor heating, which enables effective use of heat energy. Such floor heating does not generate noise due to air flow unlike air conditioning and heating in which warm air is forcibly sent into the room. Therefore, it is particularly effective in the case where the building 1 is a facility such as a concert hall or a conference hall where noise is a concern because heating without noise interference is possible. It is also possible to supply hot water to a hot water pool or the like by increasing the amount of water stored in the heat storage tank 21 because the yield of the heat storage water is higher than that of the high temperature water.
なお、本発明においては種々変更が可能でる。処理室を
負圧にする手段としてポンプによって処理室内の空気を
吸い出してもよい。又、熱交換器では高温水だけを得て
冷暖房するようにしてもよい。この場合には蓄熱槽は不
要となると共に、より高温の温水が得られるから、冷暖
房の熱効率が向上する。さらには給湯槽を省いてもよ
い。Various modifications can be made in the present invention. The air in the processing chamber may be sucked by a pump as a means for making the processing chamber negative pressure. Further, in the heat exchanger, only high temperature water may be obtained for cooling and heating. In this case, the heat storage tank is not required and hotter hot water is obtained, so that the thermal efficiency of cooling and heating is improved. Furthermore, the hot water supply tank may be omitted.
〈発明の効果〉 以上のとおり本発明によれば、発電装置にガスタービン
発電機を使用すると共に、ガスタービン発電機の燃焼用
空気として汚水処理槽からの空気を供給して無臭化を図
ったから、体育館,映画館などの各種施設と汚水処理施
設とを一の建造物内に設けることができる。又、ガスタ
ービン発電機の余剰エネルギーを各種施設の暖房等に利
用したから熱エネルギーの節約も可能となる。<Effects of the Invention> As described above, according to the present invention, the gas turbine generator is used as the power generator, and the air from the sewage treatment tank is supplied as combustion air for the gas turbine generator to achieve deodorization. Various facilities such as a gymnasium, a movie theater, and a sewage treatment facility can be provided in one building. In addition, since the surplus energy of the gas turbine generator is used for heating various facilities, it is possible to save heat energy.
第1図は本発明の一実施例の概略断面図、第2図は地下
部分の平面図、第3図は発電系統のブロック図、第4図
は熱交換器の一例の断面図である。 1……建造物、2……処理室、3……発電室、 4,5,6,7,8,9……汚水処理槽、 12……ファン、13……送気ダクト、 14……吸気ダクト、17……ガスタービン発電機、 18……熱交換器、20……煙突、21……蓄熱槽、 22……冷暖房装置、23……給湯槽、 30,31……循環路、40……パイプライン。1 is a schematic sectional view of an embodiment of the present invention, FIG. 2 is a plan view of an underground portion, FIG. 3 is a block diagram of a power generation system, and FIG. 4 is a sectional view of an example of a heat exchanger. 1 ... Building, 2 ... Treatment room, 3 ... Power generation room, 4, 5, 6, 7, 8, 9 ... Wastewater treatment tank, 12 ... Fan, 13 ... Air supply duct, 14 ... Intake duct, 17 ... Gas turbine generator, 18 ... Heat exchanger, 20 ... Chimney, 21 ... Heat storage tank, 22 ... Air conditioner, 23 ... Hot water tank, 30, 31 ... Circulation path, 40 ……pipeline.
Claims (1)
部分に設けられ内部が負圧に調整されてなる処理室と、
処理室内の空気が燃料燃焼用空気として供給されるガス
タービン発電機と、ガスタービン発電機からの排ガスの
潜熱から温水を得る熱交換器と、熱交換器からの温水に
よって前記建造物の冷暖房を行う冷暖房装置とを備えて
なることを特徴とする発電システム。1. A treatment chamber which is provided in an underground portion of a building so as to isolate a sewage treatment tank and whose inside is adjusted to a negative pressure,
A gas turbine generator in which air in the processing chamber is supplied as air for fuel combustion, a heat exchanger for obtaining hot water from latent heat of exhaust gas from the gas turbine generator, and heating and cooling of the building by hot water from the heat exchanger. A power generation system, comprising: a cooling and heating device for performing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24703686A JPH0629568B2 (en) | 1986-10-17 | 1986-10-17 | Power generation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24703686A JPH0629568B2 (en) | 1986-10-17 | 1986-10-17 | Power generation system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63100233A JPS63100233A (en) | 1988-05-02 |
| JPH0629568B2 true JPH0629568B2 (en) | 1994-04-20 |
Family
ID=17157457
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24703686A Expired - Lifetime JPH0629568B2 (en) | 1986-10-17 | 1986-10-17 | Power generation system |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0629568B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5116703A (en) * | 1989-12-15 | 1992-05-26 | Xerox Corporation | Functional hybrid compounds and thin films by sol-gel process |
-
1986
- 1986-10-17 JP JP24703686A patent/JPH0629568B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63100233A (en) | 1988-05-02 |
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