JP3992879B2 - Carbonized gas and carbide mixed treatment burner - Google Patents

Carbonized gas and carbide mixed treatment burner Download PDF

Info

Publication number
JP3992879B2
JP3992879B2 JP14195499A JP14195499A JP3992879B2 JP 3992879 B2 JP3992879 B2 JP 3992879B2 JP 14195499 A JP14195499 A JP 14195499A JP 14195499 A JP14195499 A JP 14195499A JP 3992879 B2 JP3992879 B2 JP 3992879B2
Authority
JP
Japan
Prior art keywords
carbide
dry distillation
distillation gas
gas
combustion 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.)
Expired - Fee Related
Application number
JP14195499A
Other languages
Japanese (ja)
Other versions
JP2000329318A (en
Inventor
龍己 名塚
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.)
Furukawa Co Ltd
Original Assignee
Furukawa 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 Furukawa Co Ltd filed Critical Furukawa Co Ltd
Priority to JP14195499A priority Critical patent/JP3992879B2/en
Publication of JP2000329318A publication Critical patent/JP2000329318A/en
Application granted granted Critical
Publication of JP3992879B2 publication Critical patent/JP3992879B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Incineration Of Waste (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、特別管理を含む一般廃棄物や産業廃棄物をガス化溶融処理する廃棄物処理設備で用いられる、乾留ガスと炭化物の混合処理バーナーに関する。
【0002】
【従来の技術】
従来、一般廃棄物や産業廃棄物等は、焼却、埋め立てによる処理が行われてきたが、ダイオキシン等の有害物の発生や埋め立て用の適地が得られなくなっていることから、近年、廃棄物のガス化溶融処理が注目されている。ガス化溶融処理では、廃棄物を熱分解して乾留ガスと炭化物に変えて高温で燃焼させ、焼却灰は溶融してスラグとして回収する。
【0003】
廃棄物をガス化溶融処理する廃棄物処理設備によれば、ダイオキシン等の有害物の排出抑制や焼却灰の減容・再利用、さらに鉄やアルミ等の資源物の回収、エネルギーの有効利用などが可能となる。
廃棄物をガス化溶融処理する廃棄物処理設備には、廃棄物を分解ガス化炉で熱分解して乾留ガスと炭化物を発生させ、炭化物は溶融炉で燃焼させ、乾留ガスはガス燃焼炉で燃焼させるもの、廃棄物を分解溶融炉で熱分解して乾留ガスと炭化物を発生させ、炭化物は分解溶融炉で燃焼させ乾留ガスはガス燃焼炉で燃焼させるもの、廃棄物を分解ガス化炉で熱分解して乾留ガスと炭化物を発生させ、乾留ガスと炭化物を溶融炉で燃焼させるもの等、種々の型式があるが、いずれの場合も乾留ガス、炭化物、及び燃焼空気は、それぞれ個別に炉内に供給して燃焼させている。
【0004】
乾留ガスと炭化物とを別個の炉で燃焼させて処理する廃棄物処理設備は、設備費が高価となり、各々の炉に補助燃料が必要になるので、ランニングコストも増加する。
これに対し、乾留ガスと炭化物とを一つの炉で燃焼させて処理する廃棄物処理設備は、設備費、ランニングコストを低減できる。
【0005】
【発明が解決しようとする課題】
しかし、乾留ガスと炭化物とを一つの炉で燃焼させて処理する廃棄物処理設備でも、乾留ガスと炭化物と燃焼空気とは個別に炉内へ供給されるので、乾留ガスと燃焼空気、炭化物と燃焼空気の混合が不十分で不完全燃焼を生じたり、炉内温度分布の不均一を生じることがある。
【0006】
本発明は、廃棄物をガス化溶融処理する廃棄物処理設備における上記問題を解決するものであって、乾留ガスと炭化物と燃焼空気とを一つのバーナーで効率よく混合して燃焼させ、安定した燃焼と均一な炉内温度分布を得ることのできる乾留ガスと炭化物の混合処理バーナーを提供することを目的とする。
【0007】
【課題を解決するための手段】
本発明の乾留ガスと炭化物の混合処理バーナーは、廃棄物をガス化溶融処理する廃棄物処理設備において、発生した乾留ガスと炭化物とを加熱燃焼空気と共に供給して燃焼させるものであって、炭化物供給シュートから供給される炭化物と加熱燃焼空気ノズルから供給される加熱燃焼空気とを混合して先端から噴出させる混合ノズルの周囲に、乾留ガスを流入旋回させ混合ノズルの先端周囲から噴出させる乾留ガス旋回コーンを設けることにより上記の課題を解決している。
【0008】
廃棄物をガス化溶融処理する廃棄物処理設備において、発生した炭化物は混合処理バーナーの炭化物供給シュートから混合ノズルに供給される。同時に混合ノズルには加熱燃焼空気ノズルから加熱燃焼空気が供給され、ベンチュリ効果によって炭化物と加熱燃焼空気とが混合されて混合ノズルの先端から噴出する。
一方、乾留ガスは、乾留ガス旋回コーンに供給される。乾留ガス旋回コーンに流入した乾留ガスは、旋回流となって混合ノズルの先端周囲から噴出するので、混合処理バーナーの出口において炭化物と加熱燃焼空気との混合物と衝突混合される。
【0009】
このように、混合燃焼効果の悪い炭化物を加熱燃焼空気と混合ノズルで予備混合し、この混合物を混合処理バーナーの出口で着火性のよい乾留ガスと混合して燃焼させることにより、安定した燃焼を行うことができ、均一な炉内温度分布が得られる。
【0010】
【発明の実施の形態】
図1は、本発明の実施の一形態である乾留ガスと炭化物の混合処理バーナーの縦断面図、図2は乾留ガスと炭化物の混合処理バーナーの平面図、図3は乾留ガスと炭化物の混合処理バーナーの底面図、図4は乾留ガスと炭化物の混合処理バーナーの混合作用の説明図である。
【0011】
この混合処理バーナー1は、混合ノズル2と、混合ノズル2を中心としてその周囲に設けられた乾留ガス旋回コーン3とを備えており、廃棄物をガス化溶融処理する廃棄物処理設備において、乾留ガスと炭化物とを燃焼させる炉に設けて使用される。
混合ノズル2は円筒状で先端部に円錐形の分散板4、後端部に加熱燃焼空気ノズル5が設けられており、加熱燃焼空気ノズル5の先端位置付近の混合ノズル2の側面には炭化物供給シュート6の先端が開口している。
【0012】
乾留ガス旋回コーン3は、上部が円筒状、下部が漏斗状で、上部外周面には接線方向に乾留ガスGを流入させるガス供給管7が設けられている。
廃棄物をガス化溶融処理する廃棄物処理設備において、発生した炭化物Cは、混合処理バーナー1の炭化物供給シュート6から混合ノズル2に供給される。同時に混合ノズル2には加熱燃焼空気ノズル5から加熱燃焼空気Aが供給され、加熱燃焼空気ノズル5の先端部のベンチュリ効果によって炭化物Cと加熱燃焼空気Aが混合され、混合ノズル2の先端部の分散板4に衝突してその周囲から炭化物Cと加熱燃焼空気Aの混合物が噴出する。
【0013】
一方、乾留ガスGは、ガス供給管7から乾留ガス旋回コーン3の上部に供給される。乾留ガスGは、乾留ガス旋回コーン3に対して接線方向に流入し、乾留ガス旋回コーン3内で混合ノズル2を中心とする旋回流となって混合ノズル2の先端周囲から噴出するので、混合処理バーナーの出口8において炭化物Cと加熱燃焼空気Aとの混合物と衝突混合される。
【0014】
このように、混合燃焼効果の悪い炭化物Cを加熱燃焼空気Aと混合ノズル2で予備混合し、この混合物を混合処理バーナー1の出口8で着火性のよい乾留ガスGと混合して燃焼させることにより、安定した燃焼を行うことができ、均一な炉内温度分布が得られる。
【0015】
【発明の効果】
以上説明したように、本発明の乾留ガスと炭化物の混合処理バーナーは、廃棄物をガス化溶融処理する廃棄物処理設備において、乾留ガスと炭化物と燃焼空気とを一つのバーナーで効率よく混合して燃焼させ、安定した燃焼と均一な炉内温度分布を得ることができる。
【図面の簡単な説明】
【図1】本発明の実施の一形態である乾留ガスと炭化物の混合処理バーナーの縦断面図である。
【図2】乾留ガスと炭化物の混合処理バーナーの平面図である。
【図3】乾留ガスと炭化物の混合処理バーナーの底面図である。
【図4】乾留ガスと炭化物の混合処理バーナーの混合作用の説明図である。
【符号の説明】
1 混合処理バーナー
2 混合ノズル
3 乾留ガス旋回コーン
4 分散板
5 加熱燃焼空気ノズル
6 炭化物供給シュート
7 ガス供給管
A 加熱燃焼空気
C 炭化物
G 乾留ガス
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a dry-burning gas and carbide mixed treatment burner used in a waste treatment facility for gasifying and melting general waste and industrial waste including special management.
[0002]
[Prior art]
Conventionally, general waste and industrial waste have been treated by incineration and landfill. However, the generation of hazardous materials such as dioxins and the land for landfilling are no longer available. Gasification and melting treatment has attracted attention. In the gasification and melting treatment, the waste is pyrolyzed, converted into dry distillation gas and carbide and burned at a high temperature, and the incinerated ash is melted and recovered as slag.
[0003]
According to the waste treatment facility that gasifies and melts waste, discharge of harmful substances such as dioxins, volume reduction and reuse of incineration ash, recovery of resources such as iron and aluminum, and effective use of energy, etc. Is possible.
In a waste treatment facility that gasifies and melts waste, the waste is pyrolyzed in a cracking and gasification furnace to generate dry distillation gas and carbide. The carbide is burned in the melting furnace, and the dry distillation gas is burned in the gas combustion furnace. Combustion, waste is pyrolyzed in cracking and melting furnace to generate dry distillation gas and carbide, carbide is burned in cracking and melting furnace, dry distillation gas is burned in gas combustion furnace, waste is decomposed in gasification furnace There are various types, such as pyrolysis gas to generate dry distillation gas and carbide, and to burn dry distillation gas and carbide in a melting furnace. In each case, dry distillation gas, carbide and combustion air are individually furnaces. It is supplied and burned.
[0004]
A waste treatment facility that burns and processes carbonized gas and carbide in separate furnaces increases the cost of the equipment and requires auxiliary fuel in each furnace, thus increasing the running cost.
On the other hand, a waste treatment facility that burns and processes dry distillation gas and carbide in a single furnace can reduce facility costs and running costs.
[0005]
[Problems to be solved by the invention]
However, even in a waste treatment facility that burns and processes dry distillation gas and carbide in one furnace, dry distillation gas, carbide, and combustion air are separately supplied into the furnace, so that dry distillation gas, combustion air, and carbide Incomplete combustion may result in incomplete combustion or non-uniform temperature distribution in the furnace.
[0006]
The present invention solves the above-mentioned problem in the waste treatment facility for gasifying and melting waste, and efficiently mixing and burning dry distillation gas, carbide and combustion air with a single burner. An object of the present invention is to provide a mixed treatment burner of dry distillation gas and carbide capable of obtaining combustion and uniform furnace temperature distribution.
[0007]
[Means for Solving the Problems]
The mixed distillation burner of carbonized gas and carbide according to the present invention is a waste treatment facility that gasifies and melts waste to supply the generated dry distillation gas and carbide together with the heated combustion air to burn. Carbonized gas supplied from the supply chute and heated combustion air supplied from the heated combustion air nozzle and mixed with the heated combustion air to be ejected from the tip of the mixing nozzle. The above-described problem is solved by providing a swivel cone.
[0008]
In a waste treatment facility for gasifying and melting waste, generated carbides are supplied to a mixing nozzle from a carbide supply chute of a mixing treatment burner. At the same time, the heated combustion air is supplied to the mixing nozzle from the heated combustion air nozzle, and the carbide and the heated combustion air are mixed by the venturi effect and ejected from the tip of the mixing nozzle.
On the other hand, the dry distillation gas is supplied to the dry distillation gas swirl cone. The dry distillation gas that has flowed into the dry distillation gas swirl cone is swirled and ejected from the periphery of the tip of the mixing nozzle, so that it is collided with a mixture of carbide and heated combustion air at the outlet of the mixing treatment burner.
[0009]
Thus, stable combustion is achieved by pre-mixing the carbide with poor mixed combustion effect with the heated combustion air with the mixing nozzle, and mixing this mixture with the ignitable dry distillation gas at the outlet of the mixing treatment burner and burning it. And a uniform furnace temperature distribution can be obtained.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
FIG. 1 is a longitudinal sectional view of a dry distillation gas and carbide mixing treatment burner according to an embodiment of the present invention, FIG. 2 is a plan view of a dry distillation gas and carbide mixing treatment burner, and FIG. 3 is a dry distillation gas and carbide mixing. FIG. 4 is an explanatory view of the mixing action of the mixed processing burner of dry distillation gas and carbide.
[0011]
This mixing treatment burner 1 is provided with a mixing nozzle 2 and a dry distillation gas swivel cone 3 provided around the mixing nozzle 2, and in a waste treatment facility for gasifying and melting waste, Used in a furnace for burning gas and carbide.
The mixing nozzle 2 is cylindrical and is provided with a conical dispersion plate 4 at the front end and a heated combustion air nozzle 5 at the rear end. A carbide is provided on the side surface of the mixing nozzle 2 near the front end position of the heated combustion air nozzle 5. The tip of the supply chute 6 is open.
[0012]
The dry distillation gas swirl cone 3 has a cylindrical shape at the top and a funnel shape at the bottom, and a gas supply pipe 7 through which dry distillation gas G flows in a tangential direction is provided on the upper outer peripheral surface.
In the waste treatment facility for gasifying and melting waste, the generated carbide C is supplied from the carbide supply chute 6 of the mixing treatment burner 1 to the mixing nozzle 2. At the same time, the heating combustion air A is supplied to the mixing nozzle 2 from the heating combustion air nozzle 5, and the carbide C and the heating combustion air A are mixed by the venturi effect at the tip of the heating combustion air nozzle 5. Colliding with the dispersion plate 4, a mixture of the carbide C and the heated combustion air A is ejected from the periphery.
[0013]
On the other hand, the dry distillation gas G is supplied from the gas supply pipe 7 to the upper part of the dry distillation gas swivel cone 3. The dry distillation gas G flows in a tangential direction with respect to the dry distillation gas swirl cone 3, and is swirled around the mixing nozzle 2 in the dry distillation gas swirl cone 3 and ejected from the periphery of the mixing nozzle 2. At the outlet 8 of the treatment burner, it is impinged with a mixture of carbide C and heated combustion air A.
[0014]
In this way, the carbide C having a poor mixed combustion effect is premixed with the heated combustion air A by the mixing nozzle 2, and this mixture is mixed with the dry distillation gas G having good ignitability at the outlet 8 of the mixing treatment burner 1 and burned. Thus, stable combustion can be performed and a uniform furnace temperature distribution can be obtained.
[0015]
【The invention's effect】
As described above, the dry distillation gas and carbide mixing treatment burner of the present invention efficiently mixes dry distillation gas, carbide and combustion air with a single burner in a waste treatment facility for gasifying and melting waste. And stable combustion and uniform temperature distribution in the furnace can be obtained.
[Brief description of the drawings]
FIG. 1 is a longitudinal sectional view of a dry distillation gas and carbide mixed treatment burner according to an embodiment of the present invention.
FIG. 2 is a plan view of a mixed distillation burner of carbonized gas and carbide.
FIG. 3 is a bottom view of a mixed distillation burner of carbonized gas and carbide.
FIG. 4 is an explanatory view of a mixing action of a mixed distillation burner of carbonized gas and carbide.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Mixing process burner 2 Mixing nozzle 3 Dry distillation gas swirl cone 4 Dispersion plate 5 Heating combustion air nozzle 6 Carbide supply chute 7 Gas supply pipe A Heating combustion air C Carbide G Dry distillation gas

Claims (1)

廃棄物をガス化溶融処理する廃棄物処理設備において、発生した乾留ガスと炭化物とを加熱燃焼空気と共に供給して燃焼させる乾留ガスと炭化物の混合処理バーナーであって、炭化物供給シュートから供給される炭化物と加熱燃焼空気ノズルから供給される加熱燃焼空気とを混合して先端から噴出させる混合ノズルの周囲に、乾留ガスを流入旋回させ混合ノズルの先端周囲から噴出させる乾留ガス旋回コーンを設けたことを特徴とする乾留ガスと炭化物の混合処理バーナー。In a waste treatment facility for gasifying and melting waste, a dry distillation gas and carbide mixed treatment burner for supplying and burning the generated dry distillation gas and carbide together with heated combustion air, which is supplied from a carbide supply chute A dry distillation gas swirl cone was provided around the mixing nozzle that mixed carbide and heated combustion air supplied from the heated combustion air nozzle and spouted from the tip, and swirled the dry distillation gas and spouted from the periphery of the mixing nozzle. A carbonization mixed gas and carbide burner.
JP14195499A 1999-05-21 1999-05-21 Carbonized gas and carbide mixed treatment burner Expired - Fee Related JP3992879B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14195499A JP3992879B2 (en) 1999-05-21 1999-05-21 Carbonized gas and carbide mixed treatment burner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14195499A JP3992879B2 (en) 1999-05-21 1999-05-21 Carbonized gas and carbide mixed treatment burner

Publications (2)

Publication Number Publication Date
JP2000329318A JP2000329318A (en) 2000-11-30
JP3992879B2 true JP3992879B2 (en) 2007-10-17

Family

ID=15304003

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14195499A Expired - Fee Related JP3992879B2 (en) 1999-05-21 1999-05-21 Carbonized gas and carbide mixed treatment burner

Country Status (1)

Country Link
JP (1) JP3992879B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2430957B1 (en) * 2009-05-15 2015-11-04 Pellytech Co., Ltd Cooking pan provided with exhaust device
KR101298717B1 (en) * 2011-05-09 2013-08-21 주식회사 케이와이지엔텍 cyclone burner for fuelgas obtained from high carbonaceous waste
CN103836631A (en) * 2014-03-07 2014-06-04 湖州市千金宝云机械铸件有限公司 Environment-friendly combustion furnace
CN110530137B (en) * 2019-09-05 2021-07-02 广东非凡实业有限公司 High-density high-efficiency mud blank drying room

Also Published As

Publication number Publication date
JP2000329318A (en) 2000-11-30

Similar Documents

Publication Publication Date Title
JP4548785B2 (en) Waste gasification melting apparatus melting furnace, and control method and apparatus in the melting furnace
EP0952393A1 (en) Method and apparatus for operating melting furnace in waste treatment facilities
CN104998888A (en) Medical waste plasma processing apparatus
JP3992879B2 (en) Carbonized gas and carbide mixed treatment burner
RU2198349C2 (en) Method of burning combustible materials and reactor for method embodiment
JP3850088B2 (en) Burner for powder combustion of industrial waste incinerator
JPS6235004B2 (en)
JPH08245966A (en) Treatment of waste by carbonization
JP2945311B2 (en) Waste incineration method
HUT72158A (en) Method and apparatus for the yield of heat energy from waste materials, mainly from refuse
JP2005180881A (en) Waste treatment device
JPH09243027A (en) Combustion burner and combustion method
JP3779095B2 (en) Glass fiber waste material recycling equipment
KR100529700B1 (en) A burner used the waste oil
KR20020019359A (en) Combustible waste equipment thereof
JP5974950B2 (en) Mixed gas blowing device, waste gasification and melting furnace having the same, mixed gas blowing method, and waste gasification and melting method using the same
JP2001027410A (en) Separate type incineration ash melting facility, and its operation controlling method
JP2002195519A (en) Method and system for gasifying/melting refuse
JPH09329309A (en) Combustion melting furnace and its combustion method
JP3861397B2 (en) Internal melting furnace
JP3549044B2 (en) Rotary kiln using powder burner fueled with coated nugget debris and method of operating the kiln
JPH06307614A (en) Wasted matter incinerating method
JP2004169931A (en) Waste treatment apparatus
KR20050083488A (en) Brown gas ash melting furnace
JP2014190597A (en) Mixture gas blowing device, waste gasification melting furnace with the same, mixture gas blowing method, and waste gasification melting method using the same

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20060306

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20070613

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20070703

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20070725

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100803

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100803

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110803

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120803

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130803

Year of fee payment: 6

LAPS Cancellation because of no payment of annual fees