EP0805307A1 - Systeme et four de combustion - Google Patents

Systeme et four de combustion Download PDF

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Publication number
EP0805307A1
EP0805307A1 EP96938530A EP96938530A EP0805307A1 EP 0805307 A1 EP0805307 A1 EP 0805307A1 EP 96938530 A EP96938530 A EP 96938530A EP 96938530 A EP96938530 A EP 96938530A EP 0805307 A1 EP0805307 A1 EP 0805307A1
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EP
European Patent Office
Prior art keywords
combustion
furnace
temperature
incinerated
air
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Withdrawn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
EP96938530A
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German (de)
English (en)
Other versions
EP0805307A4 (fr
Inventor
Shigeru Saitoh
Noboru Kurita
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.)
Kurihara Kogyo Co Ltd
Original Assignee
Kurihara Kogyo 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 Kurihara Kogyo Co Ltd filed Critical Kurihara Kogyo Co Ltd
Publication of EP0805307A1 publication Critical patent/EP0805307A1/fr
Publication of EP0805307A4 publication Critical patent/EP0805307A4/fr
Withdrawn legal-status Critical Current

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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/50—Control or safety arrangements
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L17/00—Inducing draught; Tops for chimneys or ventilating shafts; Terminals for flues
    • F23L17/005—Inducing draught; Tops for chimneys or ventilating shafts; Terminals for flues using fans
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00—Pretreatment
    • F23G2201/10—Drying by heat
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2207/00—Control
    • F23G2207/10—Arrangement of sensing devices
    • F23G2207/101—Arrangement of sensing devices for temperature
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2207/00—Control
    • F23G2207/30—Oxidant supply
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2900/00—Special features of, or arrangements for incinerators
    • F23G2900/00001—Exhaust gas recirculation
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2900/00—Special features of, or arrangements for incinerators
    • F23G2900/55—Controlling; Monitoring or measuring
    • F23G2900/55009—Controlling stoker grate speed or vibrations for waste movement

Definitions

  • the present invention relates to a control system for an incinerating furnace and an incinerating furnace using the same.
  • the furnace To accomplish the complete combustion, that is no residue carbon in the exhaust gas, and toxic substances such as dioxin, PCB or the like are completely decomposed during the incineration, it is desirable to operate the furnace under the condition such that the temperature of the combustion chamber is kept more than 1,200 °C, the retention time of the combustion gas is more than 2 seconds, and the oxygen concentration in the combustion chamber is more than 3%.
  • the retention time of the combustion gas the more complete combustion is accomplished, however the capacity of the furnace may be reduced. For example, if a volume load is 100,000 Kcal/m 3 hr, and in case the 3% of an oxygen concentration and 1,200 °C of the exhaust gas, the retention time becomes approximately 4 seconds which is considered to be within a reasonable condition.
  • the volume load is more than 200,000 Kcal/m 3 hr by increasing the charging rate of the materials to be incinerated, the retention time of the exhaust gas becomes too short to accomplish the complete combustion, consequently the residue carbon in the exhaust gas increases or the dioxin is not completely decomposed by combustion heat, furthermore, it is threatening that they remain in the exhaust gas and are emitted into the air.
  • an amount of air for combustion equals to the amount of primary air which is heated to high temperature by the high temperature exhaust gas through the heat exchanger and is forced into the furnace from the furnace bottom. That is, the amount of pressurized gas is dependent on the amount of intake air for combustion by an inducing fan, thereby the amount of pressurized gas and the temperature of the pressurized gas are influenced by the amount of intake air for combustion introduced by the inducing fan, consequently a full automatic combustion control is difficult in view of complexity of the system.
  • Japanese Patent Publication No. Kokoku Hei 3-79612 teaches an control system in which a blower inducing the exhaust gas in the incinerating furnace or the like is driven by an inverter, in which a motor and an inverter are not over-loaded although the automatic operation is carried out from the beginning of the operation, regardless of the temperature of the gas, therefore the objective is different from that of the present invention.
  • the invention disclosed in Japanese Patent Application Publication No. Hei 5-83811, is a method for controlling a furnace in which in case an automatic return of an inverter control circuit after a sudden power failure, a forced draft fan is restarted after detecting a restart of the inducing draft fan thereby preventing the combustion chamber being at positive pressure.
  • the objective of the disclosed invention is different from that of the present invention.
  • the present invention is a combustion control system which is characterized by a circulating system of supplying a high temperature air for vaporizing or gasfying moisture and volatile component in the materials to be incinerated or for primary combustion of the materials to be incinerated supplied from furnace bottom a hearth bed, and the circulating system is independent from an air intake system for combustion driven by an inducing draft fan.
  • An air intake rate for combustion by the inducing draft fan is automatically controlled in relation with a temperature of the furnace thereby a release of a combustion energy of the materials to be incinerated or a combustion load of the furnace is kept constant value.
  • an incinerating furnace which comprises an open type inlet or a closed type inlet for materials to be incinerated, an air inlet for inhaling air, a side wall extended from the air inlet, a combustion chamber having a lower side wall portion, a bottom of the furnace, and an auxiliary burner; a high-temperature zone provided in the upper area of the combustion chamber; an exhaust gas flow control damper and/or frequency controlled inducing draft fan provided in an exhaust pipe provided in the upper portion of the high temperature zone to continue to a flue; an outlet for a part of a high-temperature combustion exhaust gas provided in the upper portion of the combustion chamber; a conduit passage for a high temperature combustion circulating gas connected to the outlet; a high temperature combustion gas circulating fan connected to the conduit passage; a high temperature pressure gas sending inlet provided in the furnace bottom link to the conduit passage; an intake for a part of the air for combustion connected through a conduit passage, a flow control valve for a part of the air for combustion, and a conduit passage leading to the conduit passage for
  • Fig.1I is a schematic sectional view of an incinerating furnace according to the present invention
  • Fig. 2 is a schematic sectional view of another incinerating furnace according to the present invention
  • Fig. 3 is a schematic sectional view of a conventional incinerating furnace.
  • the present invention is a control system and an incinerating furnace for using the system, in which, in order to control the temperature of the furnace at a predetermined value, an air intake rate for combustion is automatically controlled, and at the same time, a charging rate of an subject to be incinerated (solid or fluid or both solid and fluid) into the furnace is also automatically controlled so that the air intake rate for combustion is kept at a predetermined specified rate.
  • the following is an means for accomplishing the furnace control.
  • Means for keeping the temperature in the furnace at a specified value by automatically controlling the rate of inhaling air for combustion by an inducing draft fan are;
  • Fig. 1 is a side schematic sectional view of a furnace of a preferred embodiment of the present invention
  • Fig. 2 is a side schematic sectional view of another furnace of a preferred embodiment of the present invention
  • Fig. 3 is a schematic sectional view of a conventional incinerating furnace.
  • the incinerating furnace which is provided with an open-type inlet 2 for materials to be incinerated, a side wall 3 extending from the inlet 2 , and a conveyor 4 for transporting the materials to be incinerated, a combustion chamber 9 comprising a bottom 7 which includes the lower portion of the side wall 3, a hearth bed 6 having an inlet 5 for a part of a high-temperature gas E, an auxiliary burner 8 and so on, in which an materials to be incinerated is charged from the inlet 2 is incinerated by an air A charged from the inlet 2.
  • a high-temperature zone 10 is provided, and further, in the upper portion of the high-temperature zone 10 an exhaust pipe 1 1 is provided.
  • An exhaust gas A flows into the exhaust pipe 11 and flows into an exhaust gas flow control damper 12, a frequency controlled inducing draft fan 13 and then a flue 14.
  • a combustion gas outlet 15 for a part of the high-temperature combustion exhaust gas D is provided, whereby the part of the high-temperature combustion exhaust gas D is continuously flown from the combustion gas outlet 15 through a conduit passage 16, a flow control valve 17 for the high temperature gas, a conduit passage 18, a high-temperature circulating fan 19 and a conduit passage 20 to a inlet 21, and it is blown as a part of the high-temperature gas E from the inlet 21 through the flowing inlet 5 for the part of the high-temperature gas E, provided in the furnace bottom 7to the combustion chamber9.
  • an air inlet 22 for air B for combustion is provided, which is connected through a conduit passage 23, air for a combustion flow controlling valve 24 and a conduit passage 25 to the conduit passage 18 at a leading inlet 26.
  • the flow control valve 17 for the high-temperature gas can be omitted if unnecessary.
  • the air A for combustion enters into the incinerating furnace from the open-type material inlet 2 introduced by the inducing draft fan 13, in which the part of the air for combustion indicated as C directly enters into the combustion chamber 9 with the materials to be incinerated and is used for incineration.
  • the remainder of the air for combustion is mixed with the part of the high temperature combustion exhaust gas D at a predetermined rate controlled by each flow control valve, and is forced into the combustion chamber 9 as the predetermined high temperature pressurized gas E. That is, in view of gas flow system, the air for combustion is introduced from the open-type inlet 2, passing through the combustion chamber 9 and the combustion exhaust gas is emitted to the open air from the flue 14 which is an air supply system.
  • the other gas flow system is a high temperature gas circulating system in which the high-temperature gas circulates passing through the conduit passages 16, 18 and 20, the furnace bottom 7 and the combustion chamber 9.
  • a CPU (Central Processing Unit) 27 controls the amount of air for combustion flowing from the inlet 2 with the frequency controlled inducing draft fan 13 or the exhaust gas flow control damper 12 by detecting a T temperature inside the furnace of the high-temperature zone 10. Further, the CPU 27 controls the conveying rate of the materials to be incinerated conveyor 4 by detecting the frequency of electric power supplied to the inducing draft fan 13 or the opening degree of the flow control damper 12 in order that the amount of flowing air for combustion is to be the specified value.
  • Fig. 2 as well as Fig. I is an explanatory view of a system for circulating the high-temperature gas as another embodiment according to the present invention.
  • An incinerating furnace 28 has a closed-type materials to be incinerated guide inlet 29, a pusher apparatus 30 for the materials to be incinerated guide inlet 29, a side wall 31 extended from the pusher apparatus 30, a combustion chamber 36 including a furnace bottom 34 including a hearth bed 33 having an inlet 32 for a part of the high-temperature gas and an auxiliary burner 35, in which the materials to be incinerated is charged from the guide inlet 29 and is incinerated in the combustion chamber 36 with the air for combustion introduced from an inlet 53 through an inlet 50, an intake control valve 51, and a conduit passage 52.
  • the part of the air A at room temperature is sent to the inlet 53 as a combustible air through the conduit passage 52 into the combustion chamber 36 directly, and the remainder air B is sent through an outlet 54 disposed in the conduit passage 52, a conduit passage 55 extended from the outlet 54, a flow control valve 56 and a conduit passage 57 to an inlet 58 connected to the conduit passage 45, and further sent as the high-temperature pressurized gas E, being adjusted to be a specified temperature by mixing in the conduit passage 45 with a part of the high-temperature combustion exhaust gas D, into the combustion chamber 36.
  • an outlet 42 for a part of the high-temperature combustion gas is provided in the upper portion of the combustion chamber 36, thereby a part of the high-temperature combustion exhaust gas D is flown from the outlet 42 through a conduit passage 43 continued from the outlet 42, a flow control valve 44 for the part of the high-temperature combustion gas D, a conduit passage 45, a high-temperature circulating fan 46, and a conduit passage 47 in order, and further the part of the high-temperature combustion exhaust gas D and the air B for combustion are controlled to be at specified temperature by being mixed; and sent as a high-temperature circulating pressurized gas E into the combustion chamber 36 for incineration of the materials to be incinerated.
  • the flow control valve 44 for the part of the high-temperature combustion gas D can be omitted if unnecessary.
  • a high-temperature zone 37 is provided, and further, in the upper portion of the high-temperature zone 37, an exhaust pipe 38 is provided.
  • the combustion exhaust gas A flown into the exhaust pipe 38 is, briefly, emitted through an exhaust gas flow control damper 39, a frequency controlled inducing draft fan 40 and a flue 41 to the open air.
  • the air introduced from the inlet 50 for combustion is used for incineration of materials to be incinerated in the combustion chamber 36 and the high-temperature zone 37 and is emitted from the flue 41, and the high temperature exhaust gas circulates through the conduit passages 43, 45 and 47, the furnace bottom 34 and the combustion chamber 36.
  • a CPU 49 detects a temperature inside the high-temperature zone T and controls the amount of air intake rate for combustion with the aid of the frequency controlled inducing draft fan 40 or the flow control damper 39 to control the amount of air flown from the intake control valve 51 connected to the inlet 53 for the combustion air.
  • the CPU 49 controls the amount of the materials to be incinerated introduced into the combustion chamber which is conveyed from the guide inlet 29 by controlling-the frequency of the electric power supplied to the inducing draft fan 40 or the opening degree of the flow control damper 39 at a predetermined value.
  • the air intake control valve 51 should be operated depending on the pressure inside the furnace P whether to allow the air to flow from the inlet 50 to the combustion chamber 36 by detecting the pressure inside the furnace. And further, the rate of reaction of the temperature inside the furnace is slightly slower compared with the method illustrated in Fig. 1, because of a time-lag between the charge of the materials to be incinerated into the furnace and a start of combustion.
  • Fig. 3 is an explanatory view of a conventional incinerating furnace 59.
  • the incinerating furnace 59 has a guide inlet 61 for the materials to be incinerated, having a pusher inlet 60, a side wall 62 extended from the pusher inlet 60, a combustion chamber 67 including an auxiliary burner 66, a furnace bottom 65, including a hearth bed 64 having a high-temperature gas inlet 63 , and so on, in which the materials to be incinerated in the airtight state sent from the guide inlet 61 is incinerated in the combustion chamber 67.
  • a high-temperature zone 68 is provided in the upper portion of the combustion chamber.
  • an air intake 69 for combustion opened to the outside atmosphere is provided.
  • Air( A) introduced into the furnace from the intake 69 through a furnace pressure control valve 70 and air forcing draft fan 71, is heat exchanger at a heat exchanger 72, is passed through a conduit line 73 and a high-temperature forced draft air inlet 74 and is sent from the high-temperature gas inlet 63 of the furnace bottom 65 into the combustion chamber 67.
  • An exhaust pipe 75 is connected to the upper portion of the high temperature zone 68 of the furnace.
  • the combustion exhaust gas from the exhaust pipe 75 is emitted to the open air though a flow control damper 76, an inducing draft fan 77 and a flue 78.
  • a CPU (Central Processing Unit) 79 detects a temperature inside the furnace T of the high temperature zone 68, and controls an air intake rate from the intake 69 by controlling the frequency of the inducing draft fan 77 or controlling the opening degree of the flow control damper 76. Also, the CPU 79 automatically controls the amount of the materials to be incinerated which the pusher inlet 60 conveys into the furnace so that the amount of intake air for combustion which passes through the inducing draft fan 77 is to be at a predetermined value.
  • the control system of the present invention illustrated in Fig. 1 the high-temperature exhaust gas produced by incinerating the materials to be incinerated is circulated independently from the intake air for combustion introduced into the furnace from the outside atmosphere, thereby the moisture and the volatile component of the materials to be incinerated are vaporized or gasifyed and the primary combustion is executed. After that, a secondary combustion of the materials to be incinerated is carried out with the air introduced from the inlet 2.
  • the temperature of the furnace is directly controlled by the amount of air introduced by the inducing draft fan, and furthermore, it turned out that the rate of conveying the materials to be incinerated by the conveyor can be controlled with a high response rate to maintain the temperature at predetermined value, whereby the combustion temperature can be completely and automatically controlled within a deviation of ⁇ 50 °C by the CPU 27.
  • the control system illustrated in Fig. 2 the high-temperature exhaust gas produced by incinerating the materials to be incinerated is circulated independently from the intake air for combustion introduced from the outside atmosphere, thereby the moisture and the volatile component of the materials to be incinerated are vaporized or gasifyed and the primary combustion is executed. After that, a secondary combustion of the materials to be incinerated is carried out.
  • the temperature of the furnace is directly controlled by the amount of air introduced by the inducing draft fan 40, and furthermore, it turned out that the rate of conveying the materials to be incinerated by the pusher 30 can be controlled to maintain the temperature at predetermined value, whereby the combustion temperature can be controlled within a deviation of ⁇ 100 °C by the CPU 49.
  • the response is slower compared with the control system used in the embodiment 1 illustrated in Fig. 1.
  • control factors of the system are related each other with complexity, in some cased the control system has some drawback that not only the delay of the response of the system but a rather big temperature deviation ( ⁇ 100 °C) and the full automatic control can not be accomplished.
  • the furnace illustrated in Fig. 1 having the hearth bed area of 0.4 m 2 is used.
  • the inducing fan having a capacity of 300 mm Aq. and 3,000 Nm 3 /hr at a rated input power of 50 Hz is used.
  • An air intake rate is controlled by an inverter control system, the control value is 25 Hz.
  • Waste of 2,000 Kcal/kg of an average low level calorific value is introduced into the furnace by the conveyer and the furnace temperature is controlled at 1200 °C.
  • the incineration is executed steadily with a waste charging rate of approximately 220 kg/hr.
  • the air intake rate for combustion is measured of about 1,000 Nm 3 /hr.
  • the maximum air intake rate for combustion is approximately 1,300 Nm 3 /hr. After that, the frequency of the inverter gradually falls to 25 Hz in 20 minutes and become steady. During the steady state combustion, an automatic charging rate of the materials to be incinerated is approximately 70 kg/hr.
  • the high-temperature circulating gas blown up from the furnace bottom is independently controlled and operated continuously at a temperature of 350 °C and approximately 1,200 Nm 3 /hr of circulating velocity.
  • the control system is designed to automatically start ignition of the auxiliary burner if the temperature in the furnace falls below 1,150 °C, to supplement the shortage of the total calorific value in the furnace, however, during the operation, no use of the auxiliary burner is observed.
  • the pressure control valve 51 is operated by the CPU 49. Similar to the embodiment 1, the temperature of the high-temperature circulating gas blown up from the furnace bottom is 350 °C and the velocity of the circulating gas is 1,200 Nm 3 /hr at all times.
  • the operation condition is likewise the embodiment 1.
  • the materials to be incinerated is changed to waste having 6,000 Kcal/kg of an average low level calorific value, whereupon, 30 minutes later, the frequency of the inverter reached to 50 Hz, the temperature in the furnace reaches to 1,400 °C at maximum, and the air intake rate rises up to approximately 1,600 Nm 3 /hr.
  • the pushing rate of materials to be incinerated by the pusher 60 is constantly reduced with the operation of the CPU 79, to 30kg/hr at minimum. Consequently the temperature in the furnace falls to 1,150 °C which was below the predetermined acceptable level, so that the auxiliary burner 66 automatically starts burning temporarily.
  • the temperature in the furnace still falls down 1,100 °C, but after a while it is reversed to rise. increased. After that, at a deviation of ⁇ 150 °C, it fluctuates for a while and becomes stable one and a half hours later. After being in the stable state, a pushing rate of materials to be incinerated is approximately 70 kg/hr, the temperature in the furnace is 1,200 °C, and the amount of air intake (air intake rate) for combustion is approximately 1,000 Nm 3 /hr.
  • the temperature of the high-temperature pressurized gas forced from the inlet 63 falls down to 180 °C at minimum, and the intake rate of the high-temperature pressurized gas fluctuates greatly between a maximum of 1,600 Nm 3 /hr and a minimum of 600 Nm 3 /hr.
  • tbe CPU 79 controls the furnace pressure control valve 70.
  • the pressure inside the furnace of both embodiment 2 and comparative example 1 are controlled to be minus 10 mm Aq.
  • the inventors of the present invention invented the process and the equipment in which the high temperature gas for combustion blown up from the furnace bottom is circulated independently from the air for combustion thereby the fall automatic control system of the continuous incineration furnace is accomplished. Further, the temperature inside the furnace is uniquely determined by controlling the air intake rate for combustion introduced by the inducing draft fan. Not only the temperature inside the furnace is controlled between the predetermined temperature range but also the retention time of the exhaust gas is automatically controlled between the predetermined range by the simultaneous control of combustion calorific value of the materials to be incinerated and the air intake rate for combustion with the frequency controlled inducing fan.
EP96938530A 1995-11-24 1996-11-22 Systeme et four de combustion Withdrawn EP0805307A4 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP327910/95 1995-11-24
JP7327910A JP2712017B2 (ja) 1995-11-24 1995-11-24 燃焼系システム及び燃焼炉
PCT/JP1996/003437 WO1997019295A1 (fr) 1995-11-24 1996-11-22 Systeme et four de combustion

Publications (2)

Publication Number Publication Date
EP0805307A1 true EP0805307A1 (fr) 1997-11-05
EP0805307A4 EP0805307A4 (fr) 1999-12-01

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EP96938530A Withdrawn EP0805307A4 (fr) 1995-11-24 1996-11-22 Systeme et four de combustion

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Country Link
EP (1) EP0805307A4 (fr)
JP (1) JP2712017B2 (fr)
KR (1) KR100216426B1 (fr)
WO (1) WO1997019295A1 (fr)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2253959A1 (es) * 2002-12-20 2006-06-01 Vai Pomini S.R.L. Unidad para el tratamiento de productos ceramicos y sistema que comprende dicha unidad.
EP1726876A1 (fr) * 2005-05-27 2006-11-29 Takuma Co., Ltd. Méthode améliorée pour la combustion des déchets solides
DE102006005464B3 (de) * 2006-02-07 2007-07-05 Forschungszentrum Karlsruhe Gmbh Verfahren zur primärseitigen Stickoxidminderung in einem zweistufigen Verbrennungsprozess
TWI424134B (zh) * 2010-09-24 2014-01-21 China Steel Corp Method of controlling the oxygen content of combustion furnace over / under - oxygen combustion state and combustion exhaust gas
CN106594747A (zh) * 2017-01-26 2017-04-26 严志谋 改进的无害化垃圾焚烧炉

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Publication number Priority date Publication date Assignee Title
JP5358234B2 (ja) * 2009-03-23 2013-12-04 三菱重工環境・化学エンジニアリング株式会社 ストーカ式焼却炉及びその運転方法
KR101986133B1 (ko) * 2018-06-26 2019-09-30 에이엠나노텍 주식회사 왕겨 연소산화장치

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US4838183A (en) * 1988-02-11 1989-06-13 Morse Boulger, Inc. Apparatus and method for incinerating heterogeneous materials
WO1990009552A1 (fr) * 1989-02-14 1990-08-23 L. & C. Steinmüller Gmbh Procede et dispositif pour mesurer le rayonnement emis en au moins deux points separes dans l'espace dans un processus de combustion et pour reguler ce dernier en fonction du rayonnement mesure
EP0480047A1 (fr) * 1990-03-27 1992-04-15 Nkk Corporation Procede de regulation de la combustion dans un incinerateur a lit fluidise
WO1995014194A1 (fr) * 1993-11-17 1995-05-26 Shigeru Saitoh Procede et appareil d'elimination de cendres residuelles d'incineration

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US4495872A (en) * 1981-08-28 1985-01-29 Kabushiki Kaisha Takuma Incinerator and method of reducing NOx emissions
DE3402787A1 (de) * 1984-01-27 1986-01-02 Wilhelm & Sander GmbH, 3418 Uslar Heizkessel fuer manuelle und/oder automatische beschickung von festen brennstoffen sowie regeleinrichtung zur regelung der heizleistung des heizkessels
US4838183A (en) * 1988-02-11 1989-06-13 Morse Boulger, Inc. Apparatus and method for incinerating heterogeneous materials
WO1990009552A1 (fr) * 1989-02-14 1990-08-23 L. & C. Steinmüller Gmbh Procede et dispositif pour mesurer le rayonnement emis en au moins deux points separes dans l'espace dans un processus de combustion et pour reguler ce dernier en fonction du rayonnement mesure
EP0480047A1 (fr) * 1990-03-27 1992-04-15 Nkk Corporation Procede de regulation de la combustion dans un incinerateur a lit fluidise
WO1995014194A1 (fr) * 1993-11-17 1995-05-26 Shigeru Saitoh Procede et appareil d'elimination de cendres residuelles d'incineration

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Title
See also references of WO9719295A1 *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2253959A1 (es) * 2002-12-20 2006-06-01 Vai Pomini S.R.L. Unidad para el tratamiento de productos ceramicos y sistema que comprende dicha unidad.
EP1726876A1 (fr) * 2005-05-27 2006-11-29 Takuma Co., Ltd. Méthode améliorée pour la combustion des déchets solides
DE102006005464B3 (de) * 2006-02-07 2007-07-05 Forschungszentrum Karlsruhe Gmbh Verfahren zur primärseitigen Stickoxidminderung in einem zweistufigen Verbrennungsprozess
US8544394B2 (en) 2006-02-07 2013-10-01 Forschungszentrum Karlsruhe Gmbh Method for reducing nitrogen oxide on the primary side in a two-stage combustion process
TWI424134B (zh) * 2010-09-24 2014-01-21 China Steel Corp Method of controlling the oxygen content of combustion furnace over / under - oxygen combustion state and combustion exhaust gas
CN106594747A (zh) * 2017-01-26 2017-04-26 严志谋 改进的无害化垃圾焚烧炉
CN106594747B (zh) * 2017-01-26 2018-06-15 严志谋 改进的无害化垃圾焚烧炉

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EP0805307A4 (fr) 1999-12-01
WO1997019295A1 (fr) 1997-05-29
JPH09145035A (ja) 1997-06-06
KR970028062A (ko) 1997-06-24
JP2712017B2 (ja) 1998-02-10
KR100216426B1 (ko) 1999-08-16

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