JPS5940184B2 - Combustible waste processing furnace - Google Patents
Combustible waste processing furnaceInfo
- Publication number
- JPS5940184B2 JPS5940184B2 JP11272678A JP11272678A JPS5940184B2 JP S5940184 B2 JPS5940184 B2 JP S5940184B2 JP 11272678 A JP11272678 A JP 11272678A JP 11272678 A JP11272678 A JP 11272678A JP S5940184 B2 JPS5940184 B2 JP S5940184B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- zone
- combustible waste
- processing furnace
- combustion
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B1/00—Retorts
- C10B1/02—Stationary retorts
- C10B1/04—Vertical retorts
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/02—Fixed-bed gasification of lump fuel
- C10J3/20—Apparatus; Plants
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/02—Fixed-bed gasification of lump fuel
- C10J3/20—Apparatus; Plants
- C10J3/22—Arrangements or dispositions of valves or flues
- C10J3/24—Arrangements or dispositions of valves or flues to permit flow of gases or vapours other than upwardly through the fuel bed
- C10J3/26—Arrangements or dispositions of valves or flues to permit flow of gases or vapours other than upwardly through the fuel bed downwardly
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/74—Construction of shells or jackets
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0913—Carbonaceous raw material
- C10J2300/0946—Waste, e.g. MSW, tires, glass, tar sand, peat, paper, lignite, oil shale
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0953—Gasifying agents
- C10J2300/0956—Air or oxygen enriched air
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0953—Gasifying agents
- C10J2300/0959—Oxygen
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0953—Gasifying agents
- C10J2300/0973—Water
- C10J2300/0976—Water as steam
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
- Coke Industry (AREA)
- Incineration Of Waste (AREA)
Description
【発明の詳細な説明】
本発明は可燃性廃棄物などの有機物を熱分解し、ガスや
油などを回収するための可燃性廃棄物の処理炉に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a combustible waste processing furnace for thermally decomposing organic matter such as combustible waste and recovering gas, oil, and the like.
従来可燃性廃棄物などを処理する場合、固定床(移動層
)成熱分解炉を用いて有機物を熱分解することが国内外
で多く行なわれている。Conventionally, when treating combustible wastes, fixed bed (moving bed) thermal decomposition furnaces are often used to thermally decompose organic matter.
かかる熱分解炉を用いて有機物の熱分解を行なわせる場
合に重大な問題点は、炉内廃棄物のチャンネリングやブ
リッジ現象の生起を何如に防止し得るかにあり、その程
度が熱分解効率の良否、持続性及び安定性に大きな影響
を及ぼす。A serious problem when using such a pyrolysis furnace to pyrolyze organic matter is how to prevent the channeling of waste in the furnace and the occurrence of bridging phenomena, and the extent to which this occurs depends on the pyrolysis efficiency. It has a great influence on the quality, sustainability and stability of the product.
特にチャンネリングの問題は都市ごみなどのように組成
が大幅に変動するものを竪形炉で熱分解させる場合に重
要である。The problem of channeling is particularly important when a vertical furnace is used to thermally decompose materials whose composition varies significantly, such as municipal waste.
本発明は以上の点に鑑みてなされたものであり、以下そ
の実施例を図面に基づき説明する。The present invention has been made in view of the above points, and embodiments thereof will be described below based on the drawings.
第1図において、1aは炉頂部に形成された可燃性廃棄
物の投入口である。In FIG. 1, 1a is a combustible waste inlet formed at the top of the furnace.
炉内に投入された可燃性廃棄物は炉下部で適宜燃焼せし
められる。The combustible waste thrown into the furnace is appropriately burned in the lower part of the furnace.
可燃性廃棄物の燃焼で生成した燃焼ガスは炉内を上昇し
、炉頂部の排ガス通孔1bから外部へ放出される。Combustion gas generated by combustion of combustible waste rises in the furnace and is discharged to the outside from the exhaust gas vent 1b at the top of the furnace.
このような炉において、有機物の熱分解は燃焼ガスの顕
熱により生起せしめられる。In such a furnace, thermal decomposition of organic matter is caused by the sensible heat of the combustion gas.
したがって炉内には燃焼域Aの上層部に熱分解域Bが形
成され、さらに熱分解域Bの上層部に乾燥域Cが形成さ
れる。Therefore, a pyrolysis zone B is formed in the upper layer of the combustion zone A in the furnace, and a drying zone C is further formed in the upper layer of the pyrolysis zone B.
熱分解域Bではガス状又は油状物質が生成する一方、燃
焼域Aでは一部炭素物質を含む残留物質が生成する。In the pyrolysis zone B, gaseous or oily substances are produced, while in the combustion zone A, residual substances containing some carbon substances are produced.
残留物質は燃焼域Aの下部層りを通して外部へ排出され
る。The residual material is discharged to the outside through the lower layer of combustion zone A.
乾燥域Cと熱分解域B、熱分解域Bと燃焼域Aなどの境
界は明確に現れるものではないが、その概略位置は定ま
っている。Although the boundaries between the drying zone C and the pyrolysis zone B, the pyrolysis zone B and the combustion zone A, etc. do not appear clearly, their approximate positions are fixed.
そこでこの実施例では、燃焼域A及び熱分解域Bの炉壁
面2A、2Bにテーパを有せしめることにより、両者の
境界部3につづく燃焼域Aの一部を下部がり状、熱分解
域Bを上部がり状としている。Therefore, in this embodiment, by tapering the furnace wall surfaces 2A and 2B of the combustion zone A and the pyrolysis zone B, the part of the combustion zone A that continues to the boundary 3 between the two is shaped like a lower part, and the pyrolysis zone B The upper part is tapered.
このようにすると、熱分解域Bにおいては被処理物と炉
壁との面圧を一定以上に保持することができるのでチャ
ンネリングの生起が防止され、また燃焼域Aで燃焼空間
が確保されるため効果的な燃焼を行なわしめることがで
きる。In this way, the surface pressure between the material to be treated and the furnace wall can be maintained above a certain level in the pyrolysis zone B, thereby preventing the occurrence of channeling, and ensuring a combustion space in the combustion zone A. Therefore, effective combustion can be carried out.
なお乾燥域C及びその上部の壁面2Cは垂直となってい
る。Note that the drying area C and the wall surface 2C above it are vertical.
第2図は変形例を示している。FIG. 2 shows a modification.
この実施例では乾燥域Cの壁面2Cと熱分解域Bの壁面
2B及び燃焼域Aの壁面2Aと下層部りの壁面2Dとを
それぞれ同一テーパとすることにより、燃焼域Aと熱分
解域Bとの境界部3の上部を上部がり状、下部を下部が
り状としている。In this embodiment, the wall surface 2C of the drying zone C, the wall surface 2B of the pyrolysis zone B, the wall surface 2A of the combustion zone A, and the wall surface 2D of the lower layer are each made to have the same taper. The upper part of the boundary part 3 with the upper part is in the form of an upper bulge, and the lower part is in the form of a lower part.
このようにしても前記効果が得られる。The above effect can also be obtained in this manner.
第3図、第4図は本発明の効果を確認するための実験結
果を表わしたものである。FIGS. 3 and 4 show experimental results for confirming the effects of the present invention.
この実験は乾燥域入口部相当部分の周方向壁面に等角度
おきに四個の温度計T1〜T4を設置して行なったもの
で、これら相互間の検出温度差からチャンネリングの有
無及び程度を確認できる。This experiment was conducted by installing four thermometers T1 to T4 at equal angles on the circumferential wall of the portion corresponding to the entrance of the drying area, and the existence and degree of channeling was determined from the detected temperature difference between them. Can be confirmed.
すなわち第3図は燃焼域及び熱分解域の各壁面に何らテ
ーパを有せしめてない炉におけるものである。That is, FIG. 3 shows a furnace in which the walls of the combustion zone and the pyrolysis zone do not have any taper.
この炉においては温度計T4の設置箇所でチャンネリン
グが生起されたことが判明する。In this furnace, it was found that channeling occurred at the location where the thermometer T4 was installed.
これに対し第4図は本発明に係る炉におけるもので、こ
の図から温度計T1〜T4のどの設置箇所においてもチ
ャンネリングの生起が防止されているのが判る。On the other hand, FIG. 4 shows the furnace according to the present invention, and from this figure it can be seen that channeling is prevented from occurring at any location where the thermometers T1 to T4 are installed.
以上の説明から明らかなように本発明は非常に簡単な構
成でありながらチャンネリングの生起を有効に防止する
ことができる。As is clear from the above description, although the present invention has a very simple configuration, it is possible to effectively prevent channeling from occurring.
この結果廃棄物の処理量が増加し、加えて熱分解によっ
て生成する可燃性ガス量が増加し、生成ガス組成が改善
される。As a result, the amount of waste to be treated increases, and in addition, the amount of combustible gas produced by thermal decomposition increases, and the composition of the produced gas is improved.
斜上の実施例ではいずれも熱分解域の壁面全高に亘って
テーパを形成したものを示しているが、本発明の効果は
その一部にテーパを有せしめること、つまり少なくとも
燃焼域と熱分解域の境界上部を上部がり状、該境界下部
を下部がり状とすることによって奏し得る。In all of the embodiments above, a taper is formed over the entire height of the wall surface of the pyrolysis zone, but the effect of the present invention is to have a taper in a part of the wall surface, that is, at least the combustion zone and the pyrolysis zone. This can be achieved by making the upper part of the boundary of the area into an upper ridge shape and the lower part of the boundary into a lower ridge shape.
なお本発明において炉内壁面の上部がり状部分のテーパ
度は被処理物がブリッジ現象を生起し得ない範囲内で定
めることが望ましい。In the present invention, it is desirable that the degree of taper of the upper curved portion of the inner wall surface of the furnace is determined within a range in which the object to be treated does not cause a bridging phenomenon.
第1図、第2図は本発明の実施例を示しており、第1図
は縦断側面図、第2図は変形例の縦断側面図、第3図、
第4図は実験結果のグラフ図である。
A・・・・・・燃焼域、B・・・・・・熱分解域。1 and 2 show an embodiment of the present invention, with FIG. 1 being a longitudinal side view, FIG. 2 being a longitudinal side view of a modified example, and FIG.
FIG. 4 is a graph of the experimental results. A: combustion zone, B: thermal decomposition zone.
Claims (1)
廃棄物の処理炉において、少なくとも燃焼域と熱分解域
との境界上部を上部がり状、該境界下部を下部がり状バ
したことを特徴とする可燃性廃棄物の処理炉。1. A combustible waste processing furnace in which thermal decomposition is carried out in the upper part of the combustion zone, characterized in that at least the upper boundary between the combustion zone and the thermal decomposition zone is shaped like an upper bevel, and the lower part of the boundary is shaped like a lower bevel. A processing furnace for combustible waste.
Priority Applications (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11272678A JPS5940184B2 (en) | 1978-09-12 | 1978-09-12 | Combustible waste processing furnace |
GB7928246A GB2030273B (en) | 1978-09-12 | 1979-08-14 | Apparatus for treating combustible wastes |
DE19792934831 DE2934831C2 (en) | 1978-09-12 | 1979-08-29 | Device for the pyrolysis treatment of combustible waste materials |
FR7922104A FR2436175A1 (en) | 1978-09-12 | 1979-09-04 | APPARATUS FOR THE TREATMENT OF COMBUSTIBLE WASTE |
CH807379A CH641830A5 (en) | 1978-09-12 | 1979-09-07 | PLANT FOR TREATING COMBUSTIBLE WASTE BY PYROLYSIS. |
SE7907530A SE434273B (en) | 1978-09-12 | 1979-09-11 | APPARATUS FOR TREATMENT OF FLAMMABLE WASTE MATERIAL |
DK379079A DK160365C (en) | 1978-09-12 | 1979-09-11 | PYROLYSE TREATMENT OF FLAMMABLE WASTE PRODUCTS |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11272678A JPS5940184B2 (en) | 1978-09-12 | 1978-09-12 | Combustible waste processing furnace |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5538859A JPS5538859A (en) | 1980-03-18 |
JPS5940184B2 true JPS5940184B2 (en) | 1984-09-28 |
Family
ID=14593990
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11272678A Expired JPS5940184B2 (en) | 1978-09-12 | 1978-09-12 | Combustible waste processing furnace |
Country Status (7)
Country | Link |
---|---|
JP (1) | JPS5940184B2 (en) |
CH (1) | CH641830A5 (en) |
DE (1) | DE2934831C2 (en) |
DK (1) | DK160365C (en) |
FR (1) | FR2436175A1 (en) |
GB (1) | GB2030273B (en) |
SE (1) | SE434273B (en) |
Families Citing this family (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4291634A (en) * | 1980-05-29 | 1981-09-29 | Union Carbide Corporation | Solid refuse disposal apparatus |
GB2087054B (en) * | 1980-09-19 | 1984-03-21 | Shinryo Air Cond | Method and apparatus for incinerating sewage sludge |
US5157176A (en) * | 1990-07-26 | 1992-10-20 | Munger Joseph H | Recycling process, apparatus and product produced by such process for producing a rubber extender/plasticizing agent from used automobile rubber tires |
SE516080C2 (en) * | 1992-10-28 | 2001-11-12 | Alf Johansson | Process and apparatus for recycling such constituents as gas, oil and solids from, for example, rubber |
SE501249C2 (en) * | 1993-05-11 | 1994-12-19 | Lindstroem Ab Olle | Methods and apparatus for the thermal gasification of solid biofuels in two stages |
DE19630564A1 (en) * | 1996-07-19 | 1998-01-22 | Bos Berlin Oberspree Sondermas | Air lock arrangement feeding e.g. used car tyre shreddings for pyrolysis, or other materials for combustion |
DK200000417A (en) * | 2000-03-15 | 2001-09-16 | Cowi Radgivende Ingeniorer As | Process and plant for decomposition, gasification and / or combustion of moist fuel. |
US7841282B2 (en) * | 2006-09-21 | 2010-11-30 | John Kimberlin | Apparatus, system, and method for operating and controlling combustor for ground or particulate biomass |
ES2332624B1 (en) * | 2007-04-03 | 2011-01-26 | Fundacion Cidaut | ELECTRICAL AND THERMAL GENERATION PLANT FROM THE BIOMASS GASIFICATION. |
GB201015544D0 (en) * | 2010-09-17 | 2010-10-27 | O Gen Uk Ltd | Biomass gasifier and gasification plant |
ES2539246B1 (en) * | 2012-10-23 | 2016-05-12 | Fundacion Cidaut | SOLID FUEL VERTICAL BOILER |
CN112920816A (en) * | 2021-03-02 | 2021-06-08 | 济源润万家农业科技有限公司 | Internal heating type biomass carbonization furnace for flue gas recycling |
CN115899704B (en) * | 2022-09-22 | 2023-11-14 | 哈尔滨蔚蓝环保设备制造有限公司 | Household garbage low-temperature pyrolysis mineralization treatment device and application method thereof |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE555346A (en) * | ||||
GB853385A (en) * | 1957-07-10 | 1960-11-09 | Axel Arne Severin | Method of operating a gas generating shaft furnace as a gas generator, blast furnace or cupola, and a furnace for carrying out the method |
DK131745C (en) * | 1970-08-18 | 1976-01-26 | Ebara Infilco | PROCEDURE FOR WASTE BURNING AND APPARATUS FOR PERFORMANCE |
DE2244753B1 (en) * | 1972-09-08 | 1973-10-18 | Mannesmann Ag, 4000 Duesseldorf | Method and device for reinforcing gauze |
DK137404B (en) * | 1975-07-09 | 1978-02-27 | Pollution Control K S | Plant for pyrolytic decomposition of waste materials. |
US4019445A (en) * | 1975-10-08 | 1977-04-26 | The Carborundum Company | Studded hearth |
JPS5313560A (en) * | 1976-07-22 | 1978-02-07 | Agency Of Ind Science & Technol | Apparatus for thermal decomposion of a solid waste |
US4077338A (en) * | 1976-08-05 | 1978-03-07 | Union Carbide Corporation | Shaft furnace for pyrolysis of refuse with bed support structure |
DE2639165A1 (en) * | 1976-08-31 | 1978-03-02 | Patra Patent Treuhand | Agricultural waste converted into mechanical energy - by disintegrating and fluidising waste, gasifying and supplying gas with air admixture to IC engine |
-
1978
- 1978-09-12 JP JP11272678A patent/JPS5940184B2/en not_active Expired
-
1979
- 1979-08-14 GB GB7928246A patent/GB2030273B/en not_active Expired
- 1979-08-29 DE DE19792934831 patent/DE2934831C2/en not_active Expired
- 1979-09-04 FR FR7922104A patent/FR2436175A1/en active Granted
- 1979-09-07 CH CH807379A patent/CH641830A5/en not_active IP Right Cessation
- 1979-09-11 SE SE7907530A patent/SE434273B/en not_active IP Right Cessation
- 1979-09-11 DK DK379079A patent/DK160365C/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
DK379079A (en) | 1980-03-13 |
DE2934831A1 (en) | 1980-03-13 |
CH641830A5 (en) | 1984-03-15 |
JPS5538859A (en) | 1980-03-18 |
DK160365C (en) | 1991-08-26 |
FR2436175B1 (en) | 1984-10-19 |
FR2436175A1 (en) | 1980-04-11 |
DK160365B (en) | 1991-03-04 |
GB2030273A (en) | 1980-04-02 |
SE7907530L (en) | 1980-03-13 |
DE2934831C2 (en) | 1982-06-16 |
SE434273B (en) | 1984-07-16 |
GB2030273B (en) | 1983-03-30 |
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