JPH09137927A - Power generation amount control equipment in waste treatment system having power generation equipment - Google Patents

Power generation amount control equipment in waste treatment system having power generation equipment

Info

Publication number
JPH09137927A
JPH09137927A JP7294581A JP29458195A JPH09137927A JP H09137927 A JPH09137927 A JP H09137927A JP 7294581 A JP7294581 A JP 7294581A JP 29458195 A JP29458195 A JP 29458195A JP H09137927 A JPH09137927 A JP H09137927A
Authority
JP
Japan
Prior art keywords
power generation
waste
supplied
thermal decomposition
amount
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Withdrawn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
JP7294581A
Other languages
Japanese (ja)
Inventor
Hiroaki Harada
裕昭 原田
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.)
Mitsui Engineering and Shipbuilding Co Ltd
Original Assignee
Mitsui Engineering and Shipbuilding 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 Mitsui Engineering and Shipbuilding Co Ltd filed Critical Mitsui Engineering and Shipbuilding Co Ltd
Priority to JP7294581A priority Critical patent/JPH09137927A/en
Publication of JPH09137927A publication Critical patent/JPH09137927A/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Withdrawn legal-status Critical Current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
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/12Heat utilisation in combustion or incineration of waste
    • 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
    • Y02E50/10Biofuels, e.g. bio-diesel

Abstract

PROBLEM TO BE SOLVED: To regulate the amount of supply of waste and thereby to make the amount of power generation constant in the equipment which generates electric power by utilizing exhaust heat of a waste treatment system. SOLUTION: This power generation equipment so constructed that waste D is charged in a thermal decomposition reactor 2 by a charging device 1 and subjected to thermal decomposition and thereby dry distillation gas G1 and a thermal decomposition residue (z) constituted mainly of nonvolatile components are produced, that the dry distillation gas G1 and the thermal decomposition residue are separated from each other and the latter is supplied to a separating device 13 to be separated into combustive components (n) and non-combustive components (fn) and that the combustive components (n) and the dry distillation gas G1 are supplied to a combustor 11 and steam S obtained by supplying combustion gas from the combustor 11 to an exhaust heat boiler 17 is supplied to a steam turbine 21 driving a generator 20, is provided. A detector 22 detecting the amount of power generation is provided for the generator 20 and the aforesaid charging device 1 is controlled by a signal from the detector 22 so as to control the amount of the waste D charged in the thermal decomposition reactor 2.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は発電装置を有する廃
棄物処理装置における発電量制御装置、より詳しくは廃
棄物を熱分解して熱分解生成物を生成させ、これを燃焼
器で燃焼させて得られた燃焼ガスを排熱ボイラに供給
し、この排熱ボイラで発生した蒸気を利用して発電する
ようにした発電装置を有する廃棄物処理装置における発
電量制御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 a power generation amount control device in a waste treatment device having a power generation device, and more specifically to thermal decomposition of waste to generate a thermal decomposition product, which is combusted in a combustor. The present invention relates to a power generation amount control device in a waste treatment device having a power generation device configured to supply the obtained combustion gas to an exhaust heat boiler and use the steam generated in the exhaust heat boiler to generate electric power.

【0002】[0002]

【従来の技術】都市ごみなどの一般廃棄物や廃プラスチ
ックなどの可燃物を含む産業廃棄物の処理装置の一つと
して廃棄物を投入装置により熱分解反応器に入れ、大気
圧下の低酸雰囲気中にて加熱して熱分解し、乾留ガスと
主として不揮発性分からなる熱分解残留物とを生成し、
さらに、この熱分解残留物を冷却した後、分離装置に導
き、この分離装置において例えば金属や陶器、砂利、コ
ンクリート等のガレキよりなる不燃焼成分と燃焼成分と
に分離する。
2. Description of the Related Art Waste is put into a thermal decomposition reactor by an input device as one of the treatment devices for general waste such as municipal solid waste and industrial waste containing combustible substances such as waste plastic, and low acid under atmospheric pressure is used. Pyrolysis is performed by heating in an atmosphere to produce a dry distillation gas and a pyrolysis residue mainly composed of non-volatile components,
Further, after the thermal decomposition residue is cooled, it is led to a separating device, and in this separating device, it is separated into non-combustible components and burning components such as rubble of metal, pottery, gravel, concrete and the like.

【0003】そしてこの燃焼成分を粉砕し、この粉砕さ
れた燃焼成分と前記した乾留ガスとを燃焼器である溶融
炉に導き、この溶融炉で燃焼させ、生じた燃焼灰を溶融
スラグとなし、この溶融スラグを排出して冷却固化させ
るとともに溶融炉の燃焼ガスを排熱ボイラに供給して蒸
気を発生させ、この蒸気で蒸気タービンを駆動して発電
機を駆動するようにした廃棄物処理装置が既に提案され
ている(例えば特開平1-49816号)。
Then, this combustion component is pulverized, and the pulverized combustion component and the above-mentioned carbonization gas are introduced into a melting furnace which is a combustor and burned in this melting furnace, and the generated combustion ash is made into molten slag, A waste treatment device that discharges this molten slag to cool and solidify it, and also supplies combustion gas from the melting furnace to an exhaust heat boiler to generate steam, which drives a steam turbine to drive a generator. Has already been proposed (for example, JP-A-1-49816).

【0004】[0004]

【発明が解決しようとする課題】ところでこのような排
熱ボイラと発電機を併設して排気の熱を回収するように
した廃棄物処理装置においては、廃棄物の性状、具体的
には廃棄物の含水率や可燃物の種類と含有率等により溶
融炉から発生する燃焼ガスの温度が変化し、そのため排
熱ボイラで発生する蒸気も温度及びその量が変化する。
By the way, in a waste treatment apparatus in which such an exhaust heat boiler and a generator are provided side by side to recover heat of exhaust gas, the nature of the waste, specifically, the waste The temperature of the combustion gas generated from the melting furnace changes depending on the water content and the type and content of combustible substances, and therefore the temperature and amount of steam generated in the exhaust heat boiler also change.

【0005】その結果として発電機の発電量が変化する
こととなる。この発電量のバラツキはこの電力を利用す
る負荷側の機器類の運転は好ましくない。特にこの発電
機が売電を目的とする発電所に設置される場は、この発
電量のバラツキは大きな問題となる。
As a result, the amount of power generated by the generator changes. Due to this variation in the amount of power generation, it is not preferable to operate the equipment on the load side that uses this power. Especially when this generator is installed in a power plant for the purpose of selling power, this variation in the amount of power generation is a serious problem.

【0006】[0006]

【課題を解決するための手段】本発明は前記したような
問題点を解決するためになされたものであって、廃棄物
を投入装置により熱分解反応器に投入し、該熱分解反応
器内における前記廃棄物を加熱して熱分解し、乾留ガス
と主として不揮発性成分よりなる熱分解残留物とを生成
し、該乾留ガスと熱分解残留物とを分離し、熱分解残留
物を分離装置に供給して燃焼成分と不燃焼成分とに分離
し、燃焼成分と前記乾留ガスとを燃焼器に供給し、該燃
焼器からの燃焼ガスを排熱ボイラに供給し、該排熱ボイ
ラで得られた蒸気を発電機を駆動する蒸気タービンへ供
給するようにした発電装置を有する廃棄物処理装置にお
いて、前記発電機に発電量を検出する検知器を設け、該
検知器からの信号により前記投入装置を制御して熱分解
反応器への廃棄物投入量を制御するようにした発電装置
を有する廃棄物処理装置における発電量制御装置を提供
するものである。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, in which waste is put into a thermal decomposition reactor by an input device, and the inside of the thermal decomposition reactor is charged. In the above, the waste is heated to be thermally decomposed to generate a dry distillation gas and a thermal decomposition residue mainly composed of a non-volatile component, the dry distillation gas and the thermal decomposition residue are separated, and the thermal decomposition residue is separated. Is supplied to a combustor to separate it into a combustion component and a non-combustion component, the combustion component and the carbonized gas are supplied to a combustor, and the combustion gas from the combustor is supplied to an exhaust heat boiler, which is obtained by the exhaust heat boiler. In a waste treatment device having a power generator configured to supply the generated steam to a steam turbine that drives a generator, the generator is provided with a detector for detecting the amount of power generation, and the injection is performed by a signal from the detector. Waste to the pyrolysis reactor by controlling the equipment There is provided a power generation control device of the waste processing apparatus having a power generator so as to control the Iriryou.

【0007】そして投入装置がスクリューフィーダであ
るときは、そのスクリューの回転数を制御することによ
り廃熱分解反応器への廃棄物投入量が調整される。かか
る発電装置を有する廃棄物処理装置における発電量制御
装置によれば、廃棄物の性状により変化する発電量は、
廃棄物の投入量を調整することによりほぼ一定に保つこ
とができ、負荷側の機器類の負担を軽くすることができ
る。
When the feeding device is a screw feeder, the amount of waste fed to the waste pyrolysis reactor is adjusted by controlling the rotation speed of the screw. According to the power generation amount control device in the waste treatment device having such a power generation device, the power generation amount that changes depending on the property of the waste is
By adjusting the input amount of waste, it can be kept almost constant, and the load on the load side equipment can be reduced.

【0008】[0008]

【発明の実施の形態】以下、図面を参照して本発明によ
る発電機を有する廃棄物処理装置における発電量制御装
置の一実施の形態を説明する。1は廃棄物Dを熱分解反
応器2内へ投入する投入装置であって、この投入装置1
はケーシング3内にスクリュー軸に取付けられたスクリ
ュー4を配置したスクリューフィーダ5と、このスクリ
ュー4を回転させるモータの如き駆動装置6とで構成さ
れている。そしてこの駆動装置6は後述する信号V1
より制御されるようになっている。
BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of a power generation amount control device in a waste treatment device having a generator according to the present invention will be described below with reference to the drawings. Reference numeral 1 denotes a charging device for charging the waste D into the thermal decomposition reactor 2.
Is composed of a screw feeder 5 in which a screw 4 attached to a screw shaft is arranged in a casing 3, and a drive device 6 such as a motor for rotating the screw 4. The driving device 6 is controlled by a signal V 1 described later.

【0009】熱分解反応器2として通常は横型回転式ド
ラムが用いられ、図示しないシール機構によりシールさ
れるとともに燃焼ガスの通路の最終段階に設けた誘引送
風機8により内部は誘引され大気圧下、即ち負圧の状態
で運転している。そしてこの熱分解反応器2は熱交換器
9からラインL1 を経て供給される加熱空気aにより 3
00℃〜600℃に、通常は 450℃程度に加熱され、供給さ
れた廃棄物Dは熱分解され、乾留ガスG1 と主として不
揮発性の熱分解残留物zとが生成される。
A horizontal rotary drum is usually used as the thermal decomposition reactor 2, which is sealed by a sealing mechanism (not shown) and the inside of which is attracted by an induction blower 8 provided at the final stage of the passage of the combustion gas under atmospheric pressure. That is, it is operating in a negative pressure state. Then, the thermal decomposition reactor 2 is heated by the heated air a supplied from the heat exchanger 9 through the line L 1.
The waste D supplied is heated to 00 ° C. to 600 ° C., usually to about 450 ° C., and the supplied waste D is pyrolyzed to produce a dry distillation gas G 1 and mainly a non-volatile pyrolysis residue z.

【0010】そしてこの乾留ガスG1 と熱分解残留物z
とは熱分解反応器2に併設した排出装置10により分離さ
れ、乾留ガスG1 はラインL2 を経て燃焼器を構成して
いる溶融炉11のバーナ12に供給される。一方、熱分解残
留物zは冷却装置を有する分離装置13に供給される。こ
の分離装置13は、例えば5mm、2mm、1mm程度の複数段
の篩からなる分級手段を有しており、熱分解残留物z中
に存在する主として粗大な不燃焼成分fn(金属やガレ
キなど)が分離除去される。
The dry distillation gas G 1 and the thermal decomposition residue z
Are separated by a discharge device 10 provided in the pyrolysis reactor 2 and the dry distillation gas G 1 is supplied to a burner 12 of a melting furnace 11 constituting a combustor via a line L 2 . On the other hand, the thermal decomposition residue z is supplied to the separation device 13 having a cooling device. The separating device 13 has a classifying means composed of a plurality of stages of sieves of, for example, 5 mm, 2 mm, and 1 mm, and is mainly a coarse non-combustible component fn (metal, rubble, etc.) present in the thermal decomposition residue z. Are separated and removed.

【0011】そしてこの分離装置13で分離された比較的
微細な粒子よりなる熱分解残留物は主として燃焼成分n
であり、その燃焼成分nを粉砕機14により、好ましくは
1mm以下の微粉よりなる燃焼成分n′とされ、この燃焼
成分n′がラインL3 から直接に又は図示しない貯蔵装
置を経て溶融炉11のバーナ12に供給される。そしてライ
ンL2 から供給された乾留ガスG1 と、ラインL3 から
供給された燃焼成分n′と:送風機15によりラインL4
から供給された燃焼用空気kとは、この溶融炉11内で約
1300℃の高温で燃焼され、このとき生じた燃焼灰は溶融
スラグsとなって水槽16中に落下し冷却固化する。この
冷却固化されたスラグsは例えば舗装材等の建材として
利用される。
The thermal decomposition residue composed of relatively fine particles separated by the separator 13 is mainly a combustion component n.
, And the by a pulverizer 14 to the fuel constituent n, preferably 'is a, the combustion component n' combustion components n which consists of the following fine 1mm melting furnace 11 through the storage device is not directly or illustrated from the line L 3 Is supplied to the burner 12. Then, the dry distillation gas G 1 supplied from the line L 2 and the combustion component n ′ supplied from the line L 3 : the line L 4 by the blower 15
The combustion air k supplied from the
Combustion is performed at a high temperature of 1300 ° C., and combustion ash generated at this time becomes molten slag s and falls into the water tank 16 to be cooled and solidified. The cooled and solidified slag s is used as a building material such as a paving material.

【0012】溶融炉11内の燃焼ガスG2 はラインL5
経由して熱交換器9、排熱ボイラ17及び集塵装置18a,
18bを順次経由して熱回収及び除塵処理され、比較的低
温のクリーンな燃焼ガスG3 となって誘引送風機8によ
り誘引され、煙突19から大気中に放出される。集塵装置
18bの出口側に接続されたラインL6 は、燃焼ガスG3
の一部を分離装置13、具体的には分離装置13中に組込ま
れた冷却装置に供給するためのラインである。
The combustion gas G 2 in the melting furnace 11 passes through the line L 5 and the heat exchanger 9, the exhaust heat boiler 17 and the dust collector 18a,
18b are successively heat recovery and dust removal via, they are attracted by the attractant blower 8 relatively a low temperature clean combustion gas G 3, and is discharged from the chimney 19 into the atmosphere. Dust collector
The line L 6 connected to the outlet side of 18b is the combustion gas G 3
Is a line for supplying a part of this to the separating device 13, specifically, the cooling device incorporated in the separating device 13.

【0013】溶融炉11の燃焼ガスG2 によって加熱され
る排熱ボイラ17により発生した蒸気Sは発電機20を駆動
する蒸気タービン21に供給され、この発電機20により得
られた電力は図示しない負荷側の機器等に供給される。
22は発電機20の発電量を検知する検知器であって、この
検知器22の信号V2 は演算装置23に入力されるようにな
っている。この演算装置23は記憶装置24、比較器25等の
機器で構成され、あらかじめ要求される所定の発電量が
記憶装置24に入力され、その信号V3 と検知器22からの
信号V2 とがこの比較器25に入力され、許容範囲外の発
電量となった場合は制御信号V1 が作成され、この制御
信号V1により前記したスクリューフィーダ5の駆動装
置6を制御することにより、熱分解反応器2への廃棄物
Dの投入量を調整するよう構成されている。
The steam S generated by the exhaust heat boiler 17 heated by the combustion gas G 2 of the melting furnace 11 is supplied to the steam turbine 21 which drives the generator 20, and the electric power obtained by the generator 20 is not shown. It is supplied to equipment on the load side.
A detector 22 detects the amount of power generated by the generator 20, and the signal V 2 from the detector 22 is input to the arithmetic unit 23. The arithmetic unit 23 is composed of devices such as a storage device 24 and a comparator 25, and a predetermined power generation amount required in advance is input to the storage device 24, and its signal V 3 and the signal V 2 from the detector 22 are input. When the amount of power generation is input to the comparator 25 and the power generation amount is out of the allowable range, a control signal V 1 is generated, and the control device V 1 controls the driving device 6 of the screw feeder 5 to perform thermal decomposition. It is configured to adjust the input amount of the waste D to the reactor 2.

【0014】なお、予め熱分解反応器2に投入される廃
棄物Dの性状を検知する手段を併用することにより、よ
り効果的な発電量の制御が可能となる。
It is possible to control the amount of power generation more effectively by using a means for detecting the property of the waste D which is previously charged into the thermal decomposition reactor 2.

【0015】[0015]

【発明の効果】以上の説明から明らかなように、本発明
による発電装置を有する廃棄物処理装置における発電量
制御装置によれば、熱分解反応器へ投入される廃棄物の
量を調整することにより発電機での発電量をほぼ一定に
保つことができる。その結果、この発電機からの電力を
利用する負荷側の機器制御が簡単となる。特にこの発電
機が売電を目的とした発電所に配置される場合はその効
果は大となる。
As is apparent from the above description, according to the power generation amount control device in the waste treatment device having the power generation device according to the present invention, the amount of waste to be put into the thermal decomposition reactor can be adjusted. This makes it possible to keep the amount of power generated by the generator almost constant. As a result, the device control on the load side using the electric power from this generator becomes simple. Especially when this generator is installed in a power plant for the purpose of selling power, the effect is great.

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

【図1】本発明による発電装置を有する廃棄物処理装置
における発電量制御装置を示す系統図である。
FIG. 1 is a system diagram showing a power generation amount control device in a waste treatment device having a power generation device according to the present invention.

【符号の説明】[Explanation of symbols]

1 投入装置 2 熱分解反応器 3 ケーシング 4 スクリュー 5 スクリューフィーダ 6 駆動装置 8 誘引送風機 9 熱交換器 10 排出装置 11 溶融炉 12 バーナ 13 分離装置 14 粉砕機 15 送風機 16 水槽 17 排熱ボイラ 18a,18b 集塵装置 19 煙突 20 発電機 21 蒸気タービン 22 検知器 23 演算装置 24 記憶装置 25 比較器 1 Input Device 2 Pyrolysis Reactor 3 Casing 4 Screw 5 Screw Feeder 6 Drive Device 8 Induction Blower 9 Heat Exchanger 10 Discharge Device 11 Melting Furnace 12 Burner 13 Separator 14 Crusher 15 Blower 16 Water Tank 17 Exhaust Heat Boiler 18a, 18b Dust collector 19 Chimney 20 Generator 21 Steam turbine 22 Detector 23 Computing device 24 Storage device 25 Comparator

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 投入装置により熱分解反応器に廃棄物を
投入し、この廃棄物を加熱して熱分解し、乾留ガスと主
として不揮発性成分よりなる熱分解残留物とを生成し、
該乾留ガスと熱分解残留物とを分離し、熱分解残留物を
分離装置に供給して燃焼成分と不燃焼成分とに分離し、
燃焼成分と前記乾留ガスとを燃焼器に供給し、該燃焼器
からの燃焼ガスを排熱ボイラに供給し、該排熱ボイラで
得られた蒸気を発電機を駆動する蒸気タービンへ供給す
るようにした発電装置を有する廃棄物処理装置におい
て、 前記発電機に発電量を検出する検知器に設け、該検知器
からの信号により前記投入装置を制御して熱分解反応器
への廃棄物投入量を制御するようにしたことを特徴とす
る発電装置を有する廃棄物処理装置の発電量制御装置。
1. A waste is charged into a pyrolysis reactor by an input device, and the waste is heated and pyrolyzed to produce a dry distillation gas and a pyrolysis residue mainly composed of a non-volatile component,
The dry distillation gas and the pyrolysis residue are separated, and the pyrolysis residue is supplied to a separation device to separate into a combustion component and a non-combustion component,
A combustion component and the carbonized gas are supplied to a combustor, the combustion gas from the combustor is supplied to an exhaust heat boiler, and the steam obtained by the exhaust heat boiler is supplied to a steam turbine that drives a generator. In the waste treatment device having the power generator described above, a detector for detecting the amount of power generation in the generator is provided, and the input device is controlled by a signal from the detector to input the amount of waste into the thermal decomposition reactor. A power generation amount control device for a waste treatment device having a power generation device.
【請求項2】 投入装置を、ケーシング内にスクリュー
を配置してなるスクリューフィーダと前記スクリューを
駆動する駆動装置とより構成し、検出器の信号により前
記駆動装置を制御し、前記スクリューの回転数を調整す
るようにした請求項1記載の発電装置を有する廃棄物処
理装置における発電量制御装置。
2. The feeding device comprises a screw feeder having a screw arranged in a casing and a driving device for driving the screw, and the driving device is controlled by a signal from a detector to rotate the screw. A power generation amount control device in a waste treatment device having the power generation device according to claim 1, wherein the power generation amount control device is adjusted.
JP7294581A 1995-11-13 1995-11-13 Power generation amount control equipment in waste treatment system having power generation equipment Withdrawn JPH09137927A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7294581A JPH09137927A (en) 1995-11-13 1995-11-13 Power generation amount control equipment in waste treatment system having power generation equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7294581A JPH09137927A (en) 1995-11-13 1995-11-13 Power generation amount control equipment in waste treatment system having power generation equipment

Publications (1)

Publication Number Publication Date
JPH09137927A true JPH09137927A (en) 1997-05-27

Family

ID=17809640

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7294581A Withdrawn JPH09137927A (en) 1995-11-13 1995-11-13 Power generation amount control equipment in waste treatment system having power generation equipment

Country Status (1)

Country Link
JP (1) JPH09137927A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103742918A (en) * 2013-12-05 2014-04-23 谢华原 Waste incineration treatment process
WO2015155565A1 (en) * 2014-04-07 2015-10-15 Babcock & Wilcox Vølund A/S Regulation of incineration in dependence of fluctuations in the price on electricity
CN106773922A (en) * 2016-12-01 2017-05-31 河北工业大学 A kind of control system of low-quality waste heat recovery generating device
WO2018107805A1 (en) * 2016-12-12 2018-06-21 大连理工大学 Organic matter self-energized pyrolysis and combustion periodic reaction device and method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103742918A (en) * 2013-12-05 2014-04-23 谢华原 Waste incineration treatment process
WO2015155565A1 (en) * 2014-04-07 2015-10-15 Babcock & Wilcox Vølund A/S Regulation of incineration in dependence of fluctuations in the price on electricity
CN106773922A (en) * 2016-12-01 2017-05-31 河北工业大学 A kind of control system of low-quality waste heat recovery generating device
CN106773922B (en) * 2016-12-01 2019-04-23 河北工业大学 A kind of control system of low-quality waste heat recovery generating device
WO2018107805A1 (en) * 2016-12-12 2018-06-21 大连理工大学 Organic matter self-energized pyrolysis and combustion periodic reaction device and method
US11020702B2 (en) * 2016-12-12 2021-06-01 Dalian University Of Technology Simultaneous reaction system and method for organic material pyrolysis and combustion

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Effective date: 20030204