US20110290162A1 - Carbon treatment system for supplying decomposition heat to waste tires - Google Patents

Carbon treatment system for supplying decomposition heat to waste tires Download PDF

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Publication number
US20110290162A1
US20110290162A1 US13/145,985 US200913145985A US2011290162A1 US 20110290162 A1 US20110290162 A1 US 20110290162A1 US 200913145985 A US200913145985 A US 200913145985A US 2011290162 A1 US2011290162 A1 US 2011290162A1
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United States
Prior art keywords
carbon
waste tires
combustion
storage tank
supplying
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.)
Abandoned
Application number
US13/145,985
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English (en)
Inventor
Yeong Min Jeon
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Individual
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Individual
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Filing date
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Publication of US20110290162A1 publication Critical patent/US20110290162A1/en
Abandoned 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
    • F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/12—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of plastics, e.g. rubber
    • 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
    • F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
    • F23G5/0276—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage using direct heating
    • 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
    • F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
    • F23G5/14—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
    • F23G5/16—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber
    • F23G5/165—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber arranged at a different level
    • 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
    • F23G5/44—Details; Accessories
    • F23G5/46—Recuperation of heat
    • 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
    • F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2204/00—Supplementary heating arrangements
    • F23G2204/10—Supplementary heating arrangements using auxiliary fuel
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2206/00—Waste heat recuperation
    • F23G2206/10—Waste heat recuperation reintroducing the heat in the same process, e.g. for predrying
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2207/00—Control
    • F23G2207/60—Additives supply
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2209/00—Specific waste
    • F23G2209/28—Plastics or rubber like materials
    • F23G2209/281—Tyres
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2209/00—Specific waste
    • F23G2209/30—Solid combustion residues, e.g. bottom or flyash

Definitions

  • the present invention relates to a system for treating carbon generated during the decomposition process in a system for recycling waste tires comprising thermally decomposing waste tires that are industrial waste by direct heating, and separating and extracting various energy sources to be recycled. More particularly, the present invention relates to a carbon treatment system for supplying decomposition heat to waste tires that secures economic feasibility so that the heat generated during combustion can be recycled while increasing convenience in maintenance by simplifying the structure.
  • waste tires are mainly made of synthetic polymer compounds, having about 34 MJ/kg of heating value, which is higher than the reference heating value of coal, 29MJ/kg.
  • the average composition of a piece of tire is composed of 43.5 wt % of styrene-butadiene copolymer (SBR polymer), 32.6 wt % of carbon black, 21.7 wt % of oil, and 2.2 wt % of additives such as sulfur, zinc oxide, etc.
  • SBR polymer styrene-butadiene copolymer
  • additives such as sulfur, zinc oxide, etc.
  • waste tires other than by combustion have been studied, and recycled products such as sidewalk blocks, reproduced tires, reproduced rubbers, artificial reefs, buffers of various structures, etc. are being produced, but to a limited scope.
  • recycled products such as sidewalk blocks, reproduced tires, reproduced rubbers, artificial reefs, buffers of various structures, etc.
  • wastes and air pollution are another concern.
  • thermal decomposition furnaces for thermally decomposing waste tires are employed. According to heating methods, thermal decomposition furnaces are divided into direct heating type thermal decomposition furnaces and indirect heating type thermal decomposition furnaces.
  • direct heating type thermal decomposition furnaces could face explosion caused by chemical reaction of spark produced when heating waste tires with oxygen within the thermal decomposition furnaces.
  • the oil produced from direct heating type thermal decomposition furnaces contains moisture and free carbon, which deteriorate the quality of the extracted oil.
  • indirect heating type thermal decomposition furnaces do not have danger of explosion of direct heating type thermal decomposition furnaces as explained above.
  • most of the oil obtained as a by-product has to be used as fuel.
  • waste tires recycling systems wherein indirect heating type thermal decomposition furnaces are employed are economically infeasible and it is difficult to deal with carbon obtained as a by-product.
  • the system is designed to put waste tires into a thermal decomposition furnace, float a carrier gas to extract and purify oil generated from the tires, and recycle gas as energy sources of the system.
  • the system is designed to incinerate waste carbon separated during a process of thermally decomposing waste tires, and resupply the heat generated therefrom to the thermal decomposition furnace.
  • the present invention has been created in order to solve the above problems that existing techniques have.
  • the present invention is to provide a carbon treatment system for supplying decomposition heat to waste tires, capable of preventing the generation of contaminants by increasing incineration efficiency of waste carbon contained in waste tires, and supplying heat source generated in combustion of carbon to a thermal decomposition furnace for thermally decomposing waste tires to maximize the economical operation thereof.
  • a carbon treatment system for supplying decomposition heat to waste tires is characterized by comprising a carbon storage tank which receives carbon separated from a thermal decomposition furnace for thermally decomposing waste tires; a burner which receives oil or gas contained in the steam generated during a process of thermally decomposing waste tires and burns the received oil or gas; and a combustion furnace arranged at one side of the burner to burn the carbon supplied by the carbon storage tank using the burner as an ignition source and connected to the thermal decomposition furnace ( 3 ) by pipe to supply heat generated during the combustion to the thermal decomposition furnace.
  • a desirable characteristic according to the present invention lies in that the combustion furnace is connected to the carbon storage tank by a carbon supplying pipe to receive carbon from the carbon storage tank, and is connected to the thermal decomposition furnace by a heat source suuplying pipe and to supply heat generated to the thermal decomposition furnace when burning carbon.
  • Another desirable characteristic according to the present invention lies in that the burner is configured to discharge flame at the bottom of inside the combustion furnace, and the combustion furnace is connected by pipe to inlet carbon to the upper side of the flame.
  • combustion furnace is configured to comprise a blowing element at one side so that the carbon supplied can be scattered.
  • combustion furnace is arranged with a plate-type combustion plate punched with holes in same intervals at one part of inside the plate, and that a pipe to inlet carbon is located above the combustion plate and a burner discharging flame is located below the combustion plate.
  • the upper part of the combustion plate comprises a plurality of heat congestion plates placed to intercross each other at intervals in a direction horizontal to each other, so that the heat generated during the combustion process is congested.
  • Another desirable characteristic according to the present invention lies in that a transfer screw rotating in one direction by driving force of driving source is installed in the carbon supplying pipe connecting the combustion furnace and the carbon storage tank.
  • blowing element is a blow fan that operates the fan which receives power supply from outside.
  • combustion furnace is connected to a cleaning distillation tower by piping to remove contaminants generated while burning carbon.
  • a system for supplying decomposition heat to waste tires is characterized by comprising a carbon storage tank which receives carbon in powder state; a burner which receives oil or gas from outside and burns the received oil or gas; a combustion furnace to which an exhaust pipe is connected to discharge heat generated and is connected to the carbon storage tank arranged at one side where carbon is supplied therefrom using the burner as ignition source; a transfer element comprising a driving motor installed at the pipe connecting the carbon storage tank and the combustion furnace to supply power to the element transferring carbon and generate driving force, and a transfer screw connected to the driving motor to rotate in one direction inside the pipe; a carbon detector detecting the amount of carbon stored in the carbon storage tank; a temperature detector detecting the temperature of the burner; and a controller electronically connected to the carbon detector and temperature detector to receive detection information, so as to selectively control operation of the driving motor.
  • the thus-configured carbon treatment system for supplying decomposition heat to waste tires of the present invention completely burns the carbon separated from waste tires to prevent contamination and reutilizes the heat generated during combustion to maximize the economical operation thereof, and therefore is of great industrial usefulness.
  • FIG. 1 is a schematic drawing for explaining a carbon treatment system for supplying decomposition heat to waste tires according to the present invention.
  • FIG. 2 is a drawing briefly showing a control circuit of a controller according to the present invention.
  • FIG. 1 is a schematic drawing for explaining a carbon treatment system for supplying decomposition heat to waste tires according to the present invention
  • FIG. 2 is a drawing briefly showing a control circuit of a controller (c) according to the present invention.
  • a known thermal decomposition furnace ( 3 ) for thermally decomposing waste tires extracts oil and incondensible gas during a process of thermally decomposing inputted waste tires, and separates carbon and iron core, which are residues.
  • the present invention relates to a system for incinerating and treating carbon among residues which are separated during a process for thermally decomposing waste tires.
  • the present invention is configured to comprise a carbon storage tank ( 10 ) which receives carbon separated from a thermal decomposition furnace ( 3 ), a combustion furnace ( 30 ) that is connected by a pipe to the carbon storage tank ( 10 ) to selectively receive carbon and burn the carbon, and a burner ( 20 ) arranged at one side of the combustion furnace ( 30 ) to discharge flame inside the combustion furnace ( 30 ) to burn the carbon.
  • a carbon storage tank ( 10 ) which receives carbon separated from a thermal decomposition furnace ( 3 )
  • a combustion furnace ( 30 ) that is connected by a pipe to the carbon storage tank ( 10 ) to selectively receive carbon and burn the carbon
  • a burner ( 20 ) arranged at one side of the combustion furnace ( 30 ) to discharge flame inside the combustion furnace ( 30 ) to burn the carbon.
  • the carbon storage tank ( 10 ) is connected to the thermal decomposition furnace ( 3 ) by a carbon supplying pipe ( 15 a ) to supply carbon, and is connected to the thermal decomposition furnace ( 3 ) by a heat source supplying pipe ( 15 b ) to supply heat generated during the combustion of carbon to the thermal decomposition furnace ( 3 ).
  • the carbon storage tank ( 10 ) is desirable to be connected to a cleaning distillation tower ( 40 ) to remove residual contaminants generated while burning carbon.
  • the cleaning distillation tower ( 40 ) may be performed by various known techniques, and thus the detailed explanation thereon is omitted.
  • the drawings of the present invention exemplify a case where the carbon storage tank ( 10 ) is connected by piping to the thermal decomposition furnace ( 3 ).
  • the carbon storage tank ( 10 ) may be modified to the form of inputting collected carbon.
  • the carbon supplying pipe ( 15 a ) is an element for inserting and moving the carbon into the carbon storage tank ( 10 ), and a driving motor ( 16 ) that is the driving source receiving power from outside to generate driving force and a transfer screw ( 17 ) connected to the driving motor ( 16 ) and receiving the driving force to rotate in one direction, the transfer screw arranged inside the carbon supplying pipe ( 15 a ), are additionally installed.
  • a burner ( 20 ) is a device for receiving gas or oil from outside to burn using the received gas or oil as fuel.
  • it may be configured to supply the fuel from outside, or configured to receive oil or gas included in vapor generated in the thermal decomposition process of the thermal decomposition furnace ( 3 ) to burn using the received oil or gas as fuel.
  • the burner ( 20 ) could be carried out by known technologies, so its detailed description will be omitted.
  • the burner ( 20 ) of the present invention is configured to be arranged at the bottom of inside the combustion furnace ( 30 ) and discharge flame to the upper side of the combustion furnace ( 30 ) to burn the inlet carbon to the upper side of the flame.
  • the burner ( 20 ) having such configuration is integrally comprised with the combustion furnace ( 30 ) to be described below.
  • the combustion furnace ( 30 ) is one type of incinerator, which is arranged at one side of the burner ( 20 ) and burns carbon supplied from the carbon storage tank ( 10 ) using the burner as an ignition source. Such combustion furnace ( 30 ) is piped to supply heat generated in the combustion process of carbon to the thermal decomposition furnace ( 3 ).
  • the combustion furnace ( 30 ) is connected to the carbon storage tank ( 10 ) by the carbon supplying pipe ( 15 a ) to receive carbon from the carbon storage tank ( 10 ), and is connected to the thermal decomposition furnace ( 3 ) by the heat source supplying pipe ( 15 b ) to supply heat generated when carbon is burned to the thermal decomposition furnace ( 3 ).
  • the carbon supplying pipe ( 15 a ) and the heat source supplying pipe ( 15 b ) may be configured to be selectively regulated by a valve.
  • the combustion furnace ( 30 ) is configured to receive blow through a blowing element ( 40 ) at an inner side so that the carbon supplied through the carbon supplying pipe ( 15 a ) can be smoothly burned inside.
  • the blowing element ( 40 ) it is suggested to use the known blow fan receiving power from outside and rotating a fan to make breeze.
  • the combustion furnace ( 30 ) of the present invention is arranged with a plate-type combustion plate ( 33 ) punched with holes in same intervals at one part inside the plate, and that the carbon supplying pipe ( 15 a ) inletting carbon is located above the combustion plate ( 33 ) and a burner ( 20 ) discharging flame is located below the combustion plate ( 33 ).
  • the carbon inserted into the upper side of the combustion furnace ( 30 ) by such configuration is scattered by the blowing element ( 40 ) to be burned, and non-burned carbon is dropped at the upper surface of the punched combustion plate ( 33 ) to be burned.
  • the present invention suggests the configuration wherein in the combustion furnace ( 30 ), at the upper part of the combustion plate ( 33 ), a plurality of heat congestion plates ( 25 ) is placed to intercross each other at intervals in a direction perpendicular to each other, so that the heat generated during the combustion process is not to discharge to the heat source supplying pipe ( 15 b ) with fast speed.
  • the heat generated in the combustion furnace ( 30 ) may congest the flow discharged to the heat source supplying pipe ( 15 b ) by the plurality of heat congestion plates ( 25 ).
  • the carbon treatment system for supplying decomposition heat to decompose waste tires according to the present invention with the above configuration is preferably suggested to be connected to the thermal decomposition furnace ( 3 ), directly receive carbon to burn the carbon, and supply heat generated in the combustion process to the thermal decomposition furnace ( 3 ).
  • it is structurally difficult piping to the thermal decomposition furnace ( 3 ) they could be operated independently.
  • the system may be configured to comprise a carbon storage tank ( 10 ) comprising a hopper to receive carbon collected from outside and use heat generated in the combustion process of the combustion furnace ( 30 ) receiving the carbon from the carbon storage tank ( 10 ) as industrial or home heat source.
  • a carbon storage tank ( 10 ) comprising a hopper to receive carbon collected from outside and use heat generated in the combustion process of the combustion furnace ( 30 ) receiving the carbon from the carbon storage tank ( 10 ) as industrial or home heat source.
  • FIG. 2 is a schematic diagram briefly showing a control circuit of a controller according to the present invention.
  • the carbon treatment system ( 1 ) for supplying decomposition heat to decompose waste tires in the present embodiment comprises a carbon storage tank ( 10 ) which receives carbon powder with the particle size of 10 ⁇ m ⁇ 5 mm and stores the carbon; a burner ( 20 ) arranged at one side of the carbon storage tank ( 10 ), which receives oil or gas from outside to generate flame; a combustion furnace ( 30 ) that is one type of incinerator, using the burner ( 20 ) as an ignition source and connected to the carbon storage tank ( 10 ) arranged at one side to selectively receive carbon to burn the carbon; a transfer element supplying the carbon stored in the carbon storage tank ( 10 ) into the combustion furnace ( 30 ); respective detectors (s 1 , s 2 ) detecting the amount of carbon and the temperature of the burner ( 20 ); and a controller (c) receiving detecting signals from these detectors (s 1 , s 2 ) to control the transfer element.
  • a carbon storage tank ( 10 ) which receives carbon powder with the particle size
  • the carbon storage tank ( 10 ) is substantially the same as the configuration of one embodiment mentioned above. However, this may be independently operated without directly piping to the thermal decomposition furnace ( 3 ), and may collect waste carbon generated in the industrial sites or a waste tires recycling system and insert it. Further, the burner ( 20 ), the combustion furnace ( 30 ) and the transfer element are substantially the same as the configurations of the embodiment mentioned above, and thus their detailed descriptions will be omitted.
  • the carbon detector (s 1 ) detecting the amount of carbon stored in the carbon storage tank ( 10 ), and a temeperature detector (s 2 ) detecting the temperature of the burner ( 20 ) are additionally installed, and a controller (c) electrically connected to these detectors (s 1 , s 2 ) to receive detection information, so as to selectively control operation of the driving motor ( 16 ) configuring the transfer element.
  • the carbon detector (s 1 ) sends the detection signal to the controller (c) to stop the operation of the system.
  • the temperature detector (s 2 ) sends the detection signal to the driving motor ( 16 ) so as not to inlet the carbon into the combustion furnace ( 30 ) to prevent the incomplete combustion.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Processing Of Solid Wastes (AREA)
US13/145,985 2009-01-22 2009-11-23 Carbon treatment system for supplying decomposition heat to waste tires Abandoned US20110290162A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
KR1020090005703A KR100896789B1 (ko) 2009-01-22 2009-01-22 폐타이어 분해열원 공급용 카본처리 시스템
KR10-2009-0005703 2009-01-22
PCT/KR2009/006887 WO2010085038A2 (fr) 2009-01-22 2009-11-23 Système de traitement de carbone permettant de fournir une chaleur de décomposition à des pneumatiques usés

Publications (1)

Publication Number Publication Date
US20110290162A1 true US20110290162A1 (en) 2011-12-01

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US13/145,985 Abandoned US20110290162A1 (en) 2009-01-22 2009-11-23 Carbon treatment system for supplying decomposition heat to waste tires

Country Status (7)

Country Link
US (1) US20110290162A1 (fr)
EP (1) EP2381173A2 (fr)
KR (1) KR100896789B1 (fr)
CN (1) CN102292597A (fr)
BR (1) BRPI0920484A2 (fr)
CA (1) CA2750327A1 (fr)
WO (1) WO2010085038A2 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9692069B2 (en) 2013-03-15 2017-06-27 Ziet, Llc Processes and systems for storing, distributing and dispatching energy on demand using and recycling carbon

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101176874B1 (ko) 2010-05-06 2012-08-29 황보기철 석유화학 폐기물의 열분해 장치 및 방법
CN104033912A (zh) * 2014-06-18 2014-09-10 南京兰迪环保科技有限公司 用于废气处理及回收循环利用的装置

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3805713A (en) * 1973-05-22 1974-04-23 Heyl & Patterson Disposal of ash from coal preparation plant tailings
US4426937A (en) * 1980-08-08 1984-01-24 Sietmann Vernon H Heat exchanger furnace
JPH05172308A (ja) * 1991-12-20 1993-07-09 Electric Power Dev Co Ltd 流動床ボイラのｎ▲２▼ｏ削減方法
US5584255A (en) * 1995-06-07 1996-12-17 Proler Environmental Services, Inc. Method and apparatus for gasifying organic materials and vitrifying residual ash
US20090013985A1 (en) * 2007-03-12 2009-01-15 Robert A Little Closed-loop control system for heating systems

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS588907A (ja) * 1981-07-08 1983-01-19 Shinsaku Goto 風呂釜燃焼装置
AT387639B (de) * 1984-01-10 1989-02-27 Sonnek Rudolf Ing Vorofen zum betrieb von heizkesselanlagen
US5411714A (en) * 1992-04-06 1995-05-02 Wu; Arthur C. Thermal conversion pyrolysis reactor system
IL114750A0 (en) * 1994-07-28 1995-11-27 Ormat Ind Ltd Method of and apparatus for efficiently combusting low grade solid fuel
DE19930071C2 (de) * 1999-06-30 2001-09-27 Wolfgang Krumm Verfahren und Vorrichtung zur Pyrolyse und Vergasung von organischen Stoffen und Stoffgemischen
KR100388381B1 (ko) * 2001-08-08 2003-06-25 (주)이엘티 폐타이어를 이용한 피복 조성물 제조 시스템
KR100473763B1 (ko) * 2002-09-28 2005-03-10 천지득 폐타이어 자동연속식 유화,카본블랙,와이어코어 재생장치
CN100501268C (zh) * 2004-03-12 2009-06-17 张彦忠 一种燃气加热器
KR20050113335A (ko) * 2004-05-27 2005-12-02 정용재 폐타이어 저온열 연속분해 장치
KR100730760B1 (ko) 2005-12-15 2007-06-20 김헌우 폐타이어 열분해 자동화 장치
KR100628890B1 (ko) 2006-05-26 2006-09-27 주식회사 에이쓰 폐타이어의 재활용 시스템

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3805713A (en) * 1973-05-22 1974-04-23 Heyl & Patterson Disposal of ash from coal preparation plant tailings
US4426937A (en) * 1980-08-08 1984-01-24 Sietmann Vernon H Heat exchanger furnace
JPH05172308A (ja) * 1991-12-20 1993-07-09 Electric Power Dev Co Ltd 流動床ボイラのｎ▲２▼ｏ削減方法
US5584255A (en) * 1995-06-07 1996-12-17 Proler Environmental Services, Inc. Method and apparatus for gasifying organic materials and vitrifying residual ash
US20090013985A1 (en) * 2007-03-12 2009-01-15 Robert A Little Closed-loop control system for heating systems

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9692069B2 (en) 2013-03-15 2017-06-27 Ziet, Llc Processes and systems for storing, distributing and dispatching energy on demand using and recycling carbon

Also Published As

Publication number Publication date
CN102292597A (zh) 2011-12-21
CA2750327A1 (fr) 2010-07-29
WO2010085038A3 (fr) 2010-09-16
KR100896789B1 (ko) 2009-05-11
EP2381173A2 (fr) 2011-10-26
BRPI0920484A2 (pt) 2018-05-22
WO2010085038A2 (fr) 2010-07-29

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