KR960024010A - Waste incineration method and apparatus - Google Patents

Waste incineration method and apparatus Download PDF

Info

Publication number
KR960024010A
KR960024010A KR1019950038192A KR19950038192A KR960024010A KR 960024010 A KR960024010 A KR 960024010A KR 1019950038192 A KR1019950038192 A KR 1019950038192A KR 19950038192 A KR19950038192 A KR 19950038192A KR 960024010 A KR960024010 A KR 960024010A
Authority
KR
South Korea
Prior art keywords
waste
incinerated
metering shaft
incineration
calorific value
Prior art date
Application number
KR1019950038192A
Other languages
Korean (ko)
Other versions
KR100416114B1 (en
Inventor
뒤벤도르퍼 피터
밀러드 존
쯔바이펠 마르틴
Original Assignee
한스 요트. 헤쩨르
아세아 브라운 보베리 매니지먼트 악티엔게젤샤프트
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 한스 요트. 헤쩨르, 아세아 브라운 보베리 매니지먼트 악티엔게젤샤프트 filed Critical 한스 요트. 헤쩨르
Publication of KR960024010A publication Critical patent/KR960024010A/en
Application granted granted Critical
Publication of KR100416114B1 publication Critical patent/KR100416114B1/en

Links

Classifications

    • 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
    • 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
    • F23G2207/00—Control
    • F23G2207/10—Arrangement of sensing devices
    • F23G2207/112—Arrangement of sensing devices for waste supply flowrate
    • 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
    • F23G2900/55—Controlling; Monitoring or measuring
    • F23G2900/55007—Sensors arranged in waste loading zone, e.g. feed hopper level
    • 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
    • F23G2900/55011—Detecting the properties of waste to be incinerated, e.g. heating value, density

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Incineration Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)
  • Gasification And Melting Of Waste (AREA)

Abstract

The waste burning method involves passing the waste (1) via a feed shaft (2) and an output slider (3) for burning on a burner (4) to which air is fed to maintain combustion. At least one parameter which influences the combustion is controlled according to the calorific value of the waste to be burnt. The calorific value, or a parameter defining it, is determined in the feed shaft using a microwave technique and the resulting measurement value stored in a process control unit (9). The process control unit controls the quantity of air and/or waste fed to the burner depending on the magnitude of the calorific value of the waste.

Description

폐기물 소각 방법 및 장치Waste incineration method and apparatus

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음Since this is an open matter, no full text was included.

제1도는 본 발명에 따른 폐기물 소각장치의 종단면도.1 is a longitudinal sectional view of a waste incineration apparatus according to the present invention.

Claims (16)

소각될 폐기물이 계량샤프트(2)와 피이더 슬라이드(3)로 이송되고, 소각을 지속하기 위해 공기가 화격자(4)에 공급되며, 소각에 영향을 미치는 하나 이상의 파라미터가 소각될 폐기물의 발열량의 함수로서 제어되는 폐기물 소각 방법에 있어서, 소각될 폐기물(1)의 발열량이나 발열량을 결정하는 측정변수가 미리 상기 계량샤프트(2)에서 결정되고, 여기서 결정된 측정치가 폐기물(1)이 소각되는 동안 발열량의 크기의 함수로서 상기 화격자(4)에 공급되는 공기의 양 및/ 또는 상기 화격자(4)에 공급되는 폐기물의 양을 조절류는 공정제어기(9)에 저장되는 것을 특징으로 하는 폐기물 소각방법.The waste to be incinerated is transferred to the metering shaft (2) and the feeder slide (3), air is supplied to the grate (4) to continue incineration, and one or more parameters affecting the incineration of the calorific value of the waste to be incinerated In the waste incineration method controlled as a function, a measurement variable for determining the calorific value or calorific value of the waste 1 to be incinerated is determined in advance in the metering shaft 2, wherein the determined value is the calorific value while the waste 1 is incinerated. The amount of air supplied to the grate (4) and / or the amount of waste supplied to the grate (4) as a function of the size of the control flow is stored in the process controller (9). 제1항에 있어서, 소각될 폐기물(1)이 상기 화격자(4)에 공급되기 전에 그의 발열량이 소정의 시간에 결정되는 것을 특징으로 하는 폐기물 소각방법.2. Method according to claim 1, characterized in that the calorific value of the waste (1) to be incinerated is determined at a predetermined time before it is supplied to the grate (4). 제1항 또는 제2항에 있어서, 상기 폐기물(1)의 발열량이 규정된 크기를 가진 상기 계량샤프트(2)의 측정부(5)안에서 소각되기 30분 전에 결정되는 것을 특징으로 하는 폐기물 소각방법.The waste incineration method according to claim 1 or 2, characterized in that the calorific value of the waste (1) is determined 30 minutes before incineration in the measuring section (5) of the metering shaft (2) having a prescribed size. . 재3항에 있어서, 상기 마이크로파가 상기 계량샤프트(2)의 이송방향에 대해 수직으로 상기 측정부(5)안에 전송되고, 이들 마이크로파의 신호감쇠 및/ 또는 상변환을 측정하여 소각될 폐기물(1)의 발열량을 결정하는 것을 특징으로 하는 폐기물 소각방법.The waste (1) according to claim 3, wherein said microwaves are transmitted in said measuring section 5 perpendicular to the conveying direction of said metering shaft (2), and the signals to be incinerated by measuring the signal attenuation and / or phase Waste incineration method, characterized in that for determining the calorific value. 제3항 또는 제4항에 있어서, 상기 마이크로파는 상기 측정부(5)의 한쪽 내벽으로부터 대향하는 벽으로 상기 계량샤프트(2)의 이송방향에 대해 수직으로 전송되어, 거기서 수신되며, 상기 마이크로파가 폐기물(1)을 통과하는 경우, 수신된 마이크로파의 신호감쇠와 상변환으로부터 폐기물의 함수량을 결정하고, 결정된 측정치를 상기 공정제어기(9)에 저장하는 것을 특징으로 하는 폐기물 소각방법.The microwave according to claim 3 or 4, wherein the microwave is transmitted perpendicularly to the conveying direction of the metering shaft (2) from one inner wall of the measuring section (5) to an opposing wall and received therein. When passing through the waste (1), the waste water incineration method characterized in that the water content of the waste is determined from the received signal attenuation and phase transformation of the microwave, and the determined measurement is stored in the process controller (9). 제3항 또는 제4항에 있어서, 상기 측정부(5)의 한쪽 내벽으로부터 대향하는 벽으로 상기 계량샤프트(2)의 이송방향에 대해 수직으로 전송되고, 폐기물에 대해 반사된 상기 마이크로파의 신호변화를 측정하여 이들 폐기물의 함수량을 결정하고, 결정된 측정치를 상기 공정제어기(9)에 저장하는 것을 특징으로 하는 폐기물 소각방법.The signal change of the microwave according to claim 3 or 4, which is transmitted perpendicularly to the conveying direction of the metering shaft 2 from one inner wall of the measuring section 5 to an opposite wall and reflected on the waste. To determine the water content of these wastes, and store the determined measurements in the process controller (9). 제3항 또는 제4항에 있어서, 하나 이상의 수직의 마이크로파가 폐기물(1)의 함수량을 결정하기 위해 상기 측정부(5) 내부의 대향하는 두벽(2A,2B)사이에서 발생되고, 그리고 신호감쇠 및/ 또는 상변환으로부터 소각 될 폐기물(1)의 함수량을 결정하고 또한 측정치를 상기 공정제어기(9)에 저장하는 것을 특징으로 하는 폐기물 소각방법.The method according to claim 3 or 4, wherein at least one vertical microwave is generated between the opposing head walls 2A, 2B inside the measuring section 5 to determine the water content of the waste 1, and the signal attenuation. And / or to determine the water content of the waste (1) to be incinerated from phase conversion and to store the measurements in the process controller (9). 제1항 또는 제2항에 있어서, 상기 송, 수신되는 마이크로파 신호를 소각될 폐기물(1)의 함수량을 결정하기 위해 계산장치(8)에 전달하고, 이 게산장치(8)를 사용하여 체크된 폐기물(1)의 함수량을 송, 수신된 마이크로파 신호사이의 차이로부터 계산하고, 상기 공정제어기(9)에 이에 대한 정보신호를 보내는 것을 특징으로 하는 폐기물 소각방법.The method according to claim 1 or 2, wherein the transmitted and received microwave signal is transmitted to a calculating device (8) to determine the water content of the waste (1) to be incinerated, and checked using the calculating device (8). The waste incineration method, characterized in that the water content of the waste (1) is calculated from the difference between the transmitted and received microwave signals, and an information signal is sent to the process controller (9). 제3항에 있어서, 소각될 폐기물의 전기저항을 상기 측정부(5)내에서 상기 계량샤프트(2)의 이송방향에 대해 수직으로 측정하고, 소각될 폐기물(1)의 발열량을 결정하기 위해 전기저항을 계산하는 것을 특징으로 하는 폐기물 소각방법.The method of claim 3, wherein the electrical resistance of the waste to be incinerated is measured perpendicularly to the conveying direction of the metering shaft 2 in the measuring unit 5, and the electricity is determined to determine the calorific value of the waste 1 to be incinerated. Waste incineration method characterized by calculating the resistance. 제1항 또는 재2항에 있어서, 소각될 폐기물(1)의 발열량 뿐만 아니라, 폐기물의 유량 및/또는 무게도 상기 계량샤프트에서 결정하고, 공정제어기에서 계산하는 것을 특징으로 하는 폐기물 소각방법.The waste incineration method according to claim 1 or 2, characterized in that not only the calorific value of the waste (1) to be incinerated, but also the flow rate and / or weight of the waste are determined in the weighing shaft and calculated by a process controller. 계량샤프트(2)와 소각될 양의 폐기물(1)의 소각을 위해 설치된 화격자(4)로 이송하기 위해 상기 계량샤프트(2)의 하부에 설치된 피이더 슬라이드(30)를 구비하고, 소각을 지속하기 위해 공기가 화격자에 공급되는 폐기물 소각장치에 있어서, 하나 이상의 측정기(6)가 폐기물(1)의 발열량을 결정하기 위해 계량샤프트(2)안에설치되어, 하나 이상의 계산장치(8,16)에 연결되고, 이계산장치의 출력신호가 화격자(4)에 공급되는 공기 및/ 또는 피이더 슬라이드(3)를 제어하기 위해 설치된 공정제어기(9)에 보내지는 것을 특징으로 하는 폐기물 소각장치.A feeder slide 30 is provided at the bottom of the metering shaft 2 for transport to the metering shaft 2 and the grate 4 installed for incineration of the amount of waste 1 to be incinerated, and continues incineration. In a waste incineration device in which air is supplied to the grate for the purpose, at least one measuring device (6) is installed in the weighing shaft (2) to determine the calorific value of the waste (1), and at least one calculating device (8, 16). Connected, and the output signal of the calculating device is sent to a process controller (9) installed for controlling the air and / or feeder slides (3) supplied to the grate (4). 제11항에 있어서, 상기 측정기(6)는 상기 계량샤프트(2)의 측정부(5)에 설치되고, 상기 계산장치(8)에 연결되는 마이크로파 송신기, 마이크로파 수신기, 조합된 마이크로파 송/수신 모듈을 가지며, 상기 계산장치(8)의 출력신호가 상기 공정제어기(9)에 보내지는 것을 특징으로 하는 폐기물 소각장치.12. The microwave transmitter / receiver module according to claim 11, wherein the measuring device (6) is installed in the measuring unit (5) of the metering shaft (2) and is connected to the calculating device (8). And an output signal of the calculating device (8) is sent to the process controller (9). 제11항 또는 제12항에 있어서, 네 개 이상의 마이크로파 송/수신 모듈(6a,6b,6c,6d와 6a′, 6b′,6c′,6d′)이 두 평면 (α,β)에 각각 설치되며, 이들 평면중 한 평면은 다른 평면위에 있으며, 두 평면 모두 상기 계량 샤프트(2)의 이송방향에 수직으로 형성되는 것을 특징으로 하는 폐기물 소각장치.The method according to claim 11 or 12, wherein four or more microwave transmit / receive modules 6a, 6b, 6c, 6d and 6a ', 6b', 6c ', 6d' are installed in two planes (α, β), respectively. Wherein one of these planes is on the other plane, both planes being formed perpendicular to the conveying direction of the metering shaft (2). 제11항에 있어서, 두 개의 판상 전극(13,14)이 상기 계량샤프트(2)의 대향하는 벽의 내측에 설치되고, 상기 전극이 상기 벽들로부터 전기적으로 절연되고, 계량샤프트(2)에 위치한 폐기물을 통과한 전류를 기록하는 전류측정기로 구성되는 전압원(16)에 연결되는 것을 특징으로 하는 폐기물 소각장치.12. The device according to claim 11, wherein two plate electrodes (13, 14) are installed inside the opposing wall of the metering shaft (2), and the electrode is electrically insulated from the walls and located on the metering shaft (2). Waste incineration device, characterized in that connected to a voltage source (16) consisting of a current meter for recording the current passing through the waste. 제11항 또는 제12항에 있어서, 폐기물(1)의 무게를 기록하는 수단이 상기 계량샤프트(2)에 설치되는 것을 특징으로 하는 폐기물 소각장치.The waste incineration device according to claim 11 or 12, wherein means for recording the weight of the waste (1) is provided on the metering shaft (2). 제11항 또는 제12항에 있어서, 상기 계량샤프트(2)에 있는 폐기물의 유량을 기록하는 수단(18,19)이 상기 계량샤프트(2)에 설치되는 것을 특징으로 하는 폐기물 소각장치.13. A waste incineration device according to claim 11 or 12, characterized in that means (18,19) for recording the flow rate of the waste in the metering shaft (2) are provided in the metering shaft (2). ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019950038192A 1994-12-22 1995-10-30 Method and apparatus for the incineration of waste materials KR100416114B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DEP4445954.8 1994-12-22
DE4445954A DE4445954A1 (en) 1994-12-22 1994-12-22 Waste incineration process

Publications (2)

Publication Number Publication Date
KR960024010A true KR960024010A (en) 1996-07-20
KR100416114B1 KR100416114B1 (en) 2004-04-21

Family

ID=6536698

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019950038192A KR100416114B1 (en) 1994-12-22 1995-10-30 Method and apparatus for the incineration of waste materials

Country Status (9)

Country Link
EP (1) EP0718553B1 (en)
JP (1) JPH08219428A (en)
KR (1) KR100416114B1 (en)
AT (1) ATE185187T1 (en)
DE (2) DE4445954A1 (en)
DK (1) DK0718553T3 (en)
ES (1) ES2139873T3 (en)
NO (1) NO305338B1 (en)
TW (1) TW301699B (en)

Families Citing this family (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19706606A1 (en) * 1997-02-20 1998-08-27 Babcock Anlagen Gmbh Process for controlling the temperature in thermal waste treatment plants and waste treatment plant
DE19917572A1 (en) 1999-04-19 2000-10-26 Abb Alstom Power Ch Ag Method for automatically setting the combustion of a waste incineration plant
DE19919222C1 (en) * 1999-04-28 2001-01-11 Orfeus Comb Engineering Gmbh Method for controlling the combustion of fuel with a variable calorific value
NL1014515C2 (en) * 1999-06-04 2000-12-06 Tno Determining system for process parameters relating to thermal process e.g. waste incineration, has computer which determines percentages and combustion heat of carbon dioxide, oxygen and water based on its mole
AU2001241269A1 (en) * 2000-02-28 2001-09-12 Nederlandse Organisatie Voor Toegepast- Natuurwetenschappelijk Onderzoek Tno System for continuous thermal combustion of matter, such as waste matter
US6499412B2 (en) * 2000-09-15 2002-12-31 Rohm And Haas Company Method of firebox temperature control for achieving carbon monoxide emission compliance in industrial furnaces with minimal energy consumption
KR100434650B1 (en) * 2000-12-22 2004-06-07 현대중공업 주식회사 Automatic Combustion Control System for Stoker Type Refuse Incinerator
IL160527A0 (en) * 2001-09-25 2004-07-25 Hoffmann La Roche Enzymatic process for the preparation of substituted 2-amino-3 (2-aminophenylsulfanyl)-propionic acid
DE10327471B3 (en) * 2003-06-18 2005-04-07 Sar Elektronic Gmbh Method and device for controlling the fire performance of incinerators
DE10330376B4 (en) * 2003-07-04 2007-09-13 Pfister Gmbh Method and device for continuous, gravimetric dosing of flowable goods for combustion plants
ATE504784T1 (en) 2004-11-02 2011-04-15 Ae & E Inova Ag WASTE FLOW LIMIT REGULATION
DE102010031528B4 (en) * 2010-07-19 2013-04-25 Klaus Seeger System for determining an energy content of a solid fuel and use of the system
IT1402556B1 (en) * 2010-11-08 2013-09-13 Amsa S P A Societa Per Azioni Con Socio Unico LOADING AND COMBUSTION CONTROL SYSTEM, FOR WASTE COMBUSTION SYSTEMS.
EP2543997B1 (en) 2011-07-07 2014-08-13 Mantex AB Method and apparatus for the estimation of the heat value
WO2013107509A1 (en) * 2012-01-18 2013-07-25 Heinrich Unland System for determining an energy content of a fuel
AU2013402760B2 (en) 2013-10-11 2018-11-08 Mantex IP AB Method and apparatus for estimation of heat value using dual energy X-ray transmission measurements and X-ray fluorescence measurements
KR101436067B1 (en) * 2014-04-08 2014-09-12 (주)씨엠환경에너지 Incinerator Containing Combustion Control Methode Using Exhaust GAS
JP6685506B2 (en) * 2016-03-30 2020-04-22 Ｊｆｅエンジニアリング株式会社 Waste incinerator
JP6624451B2 (en) * 2016-03-30 2019-12-25 Ｊｆｅエンジニアリング株式会社 Waste treatment furnace equipment
DE102017120222B3 (en) 2017-09-01 2018-11-29 Technische Universität Dresden Method and system for predicting a fuel composition in the thermal utilization of waste
JP2019178845A (en) * 2018-03-30 2019-10-17 Ｊｆｅエンジニアリング株式会社 Waste moisture percentage measuring apparatus, stoker-type waste incinerator, waste moisture percentage measuring method, and waste incineration method
JP2019178846A (en) * 2018-03-30 2019-10-17 Ｊｆｅエンジニアリング株式会社 Waste moisture percentage measuring apparatus, stoker-type waste incinerator, waste moisture percentage measuring method, and waste incineration method
JP2019178847A (en) * 2018-03-30 2019-10-17 Ｊｆｅエンジニアリング株式会社 Waste moisture percentage measuring apparatus, stoker-type waste incinerator, waste moisture percentage measuring method, and waste incineration method
JP2019178844A (en) * 2018-03-30 2019-10-17 Ｊｆｅエンジニアリング株式会社 Waste moisture percentage measuring apparatus, stoker-type waste incinerator, waste moisture percentage measuring method, and waste incineration method
WO2021033636A1 (en) * 2019-08-20 2021-02-25 日本たばこ産業株式会社 Production method and production device for cylindrical heating-type smoking article
JP6998485B1 (en) * 2021-06-29 2022-01-18 三菱重工環境・化学エンジニアリング株式会社 Incinerator equipment control device

Family Cites Families (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56141541A (en) * 1980-04-07 1981-11-05 Yamatake Honeywell Co Ltd Calorific value measuring device
JPS58195707A (en) * 1982-05-11 1983-11-15 Kawasaki Heavy Ind Ltd Combustion control method for refuse incinerator
DE3537945A1 (en) * 1985-10-25 1987-04-30 Babcock Anlagen Ag Method for combustion of waste
ES2031563T3 (en) 1987-10-24 1992-12-16 Kurt-Henry Dipl.-Ing. Mindermann PROCEDURE TO GOVERN THE COMBUSTION OF FUEL WITH VERY FLUCTING HEAT POWER.
IT1226691B (en) * 1987-11-27 1991-02-04 Enichem Anic Spa Refuse derived fuel
DE3825931A1 (en) 1988-07-29 1990-02-01 Martin Umwelt & Energietech METHOD AND DEVICE FOR CONTROLLING THE FIRING POWER OF COMBUSTION PLANTS
DE3904272C3 (en) * 1989-02-14 1998-01-08 Steinmueller Gmbh L & C Method for detecting the radiation emanating from at least two spatially separate locations of at least one combustion zone on a grate and device for detecting such radiation
CA2072122A1 (en) * 1989-10-30 1991-05-01 Ulrich Bonne Microbridge-based combustion control
EP0439645A1 (en) * 1990-01-30 1991-08-07 Officine Metalmeccaniche Nova S.P.A. Method for the controlled feeding of thermal destruction plants for urban and/or special refuse, and the plant for implementing the method
WO1991014915A1 (en) * 1990-03-27 1991-10-03 Nkk Corporation Method of controlling combustion in fluidized bed incinerator
JPH0659293B2 (en) * 1990-04-27 1994-08-10 川崎重工業株式会社 Medical waste treatment method and device
DE4028486A1 (en) * 1990-09-09 1992-05-27 Mindermann Kurt Henry Refuse incineration process control - is optimised w.r.t. variability of time taken to compress slack or compacted material entering process chamber
DE4106225C2 (en) * 1991-02-23 1993-12-16 Arndt Dipl Ing Goeller Sensor for determining the moisture of coarse and fine-grained bulk goods or fine-grained bulk goods with coarse-grained components in online operation
DE4215997C2 (en) * 1992-05-13 1995-09-07 Noell Abfall & Energietech Process for regulating the amount of waste or the layer of waste on combustion grates
DE4220149C2 (en) * 1992-06-19 2002-06-13 Steinmueller Gmbh L & C Method for regulating the combustion of waste on a grate of a furnace and device for carrying out the method
US5397551A (en) * 1992-07-09 1995-03-14 Daesung Industrial Co., Ltd. Incinerator
SG47890A1 (en) * 1993-04-20 1998-04-17 Martin Umwelt & Energietech Method for burning fuels particularly for incinerating garbage

Also Published As

Publication number Publication date
DE4445954A1 (en) 1996-06-27
JPH08219428A (en) 1996-08-30
EP0718553B1 (en) 1999-09-29
ATE185187T1 (en) 1999-10-15
NO305338B1 (en) 1999-05-10
DE59506948D1 (en) 1999-11-04
EP0718553A1 (en) 1996-06-26
DK0718553T3 (en) 2000-04-10
NO955178L (en) 1996-06-24
TW301699B (en) 1997-04-01
ES2139873T3 (en) 2000-02-16
KR100416114B1 (en) 2004-04-21
NO955178D0 (en) 1995-12-20

Similar Documents

Publication Publication Date Title
KR960024010A (en) Waste incineration method and apparatus
US4330260A (en) Method and apparatus for regulating the combustion in a furnace
US3412699A (en) Fuel feeding apparatus
US4663507A (en) Method and apparatus for reduction of fly ash carbon by microwave
AU589523B2 (en) Method and apparatus for controlling the density of a foam
US3813927A (en) Moisture transducer
EP0519178A1 (en) Combustion control method of refuse incinerator
JPS56141541A (en) Calorific value measuring device
FR2626673B1 (en) METHOD AND DEVICE FOR MEASURING THE HEAT POWER OF A VEHICLE BY A FUEL CURRENT
PT955499E (en) REGULATION PROCEDURE OF COMBUSTION CAPACITY IN INCINERATION INSTALLATIONS
JPS5773773A (en) Method for warranting quality of copy of copier
US4533258A (en) Method of determining the content of combustibles in the end products of fuel combustion and apparatus realizing said method
JP5076207B2 (en) Method and apparatus for continuously weighing flowable materials for burner systems
GB2036290A (en) Fuel sampling system
JP2019178844A (en) Waste moisture percentage measuring apparatus, stoker-type waste incinerator, waste moisture percentage measuring method, and waste incineration method
JP2019178845A (en) Waste moisture percentage measuring apparatus, stoker-type waste incinerator, waste moisture percentage measuring method, and waste incineration method
JPS57132211A (en) Temperature control method for heater
SU1093951A1 (en) Device for adjusting feed of gaseous suspensions
SU1510925A1 (en) Method of controlling the process of producing water-coal suspension
US3324715A (en) Apparatus for measuring the thermal power input of a combustion chamber
SU1702110A1 (en) Method of automatic control of air supply to boiler unit burners
JPS57122221A (en) Combustion controlling device for air heating equipment of combustion type
JPS6450080A (en) Toner density controller
SU656981A1 (en) Device for regulating glass melt temperature
KR20010057399A (en) The coal flow control for circulati on fluidized bed combustion boiler

Legal Events

Date Code Title Description
N231 Notification of change of applicant
A201 Request for examination
N231 Notification of change of applicant
E902 Notification of reason for refusal
N231 Notification of change of applicant
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20130110

Year of fee payment: 10

FPAY Annual fee payment

Payment date: 20140103

Year of fee payment: 11

FPAY Annual fee payment

Payment date: 20150105

Year of fee payment: 12