JPH09328686A - Carbonizing furnace for waste plastics and shredder dust - Google Patents
Carbonizing furnace for waste plastics and shredder dustInfo
- Publication number
- JPH09328686A JPH09328686A JP9041308A JP4130897A JPH09328686A JP H09328686 A JPH09328686 A JP H09328686A JP 9041308 A JP9041308 A JP 9041308A JP 4130897 A JP4130897 A JP 4130897A JP H09328686 A JPH09328686 A JP H09328686A
- Authority
- JP
- Japan
- Prior art keywords
- combustible gas
- inner pot
- vessel
- waste plastics
- shredder dust
- 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.)
- Pending
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
Landscapes
- Processing Of Solid Wastes (AREA)
- Carbon And Carbon Compounds (AREA)
- Coke Industry (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、産業廃棄物の焼却
部門において、廃プラスチック類及びシュレッダーダス
トの乾留熱分解をするためにバッチ式の二重釜乾留炉の
装置で、産業廃棄物からのエネルギーの確保と、活性炭
の製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a batch type double kettle carbonization furnace device for performing carbonization pyrolysis of waste plastics and shredder dust in an industrial waste incineration department. Ensuring energy and manufacturing method of activated carbon.
【0002】[0002]
【従来の技術】廃プラスチック類は焼却や乾留ガス化焼
却装置で焼却する炉が一般的に知られている。又シュレ
ッダーダストは未だ焼却処理に成功していない。2. Description of the Related Art A furnace in which waste plastics are incinerated or incinerated by a dry distillation gasification incinerator is generally known. Also, shredder dust has not been successfully incinerated.
【0003】[0003]
【発明が解決しようとする課題】従来の乾留炉はチャー
(炭化物)が不完全な炭化物でしたが、本発明は、より
純度の高い活性炭と高温の可燃性ガスが取り出せるよう
にし、ダイオキシンを熱分解し除去するようにしたもの
です。In the conventional carbonization furnace, char (carbide) is incomplete char. However, the present invention makes it possible to take out higher purity activated carbon and combustible gas at high temperature, and to heat dioxin. It is designed to be disassembled and removed.
【0004】[0004]
【課題を解決するための手段】従来の乾留炉は一重釜で
したが、本発明では、二重釜方式にし、内釜を完全に密
封し酸素を遮断し蒸し焼きにし熱分解するものです。[Means for Solving the Problems] The conventional dry distillation furnace was a single kettle, but in the present invention, a double kettle system is used, in which the inner kettle is completely sealed, oxygen is shut off, and it is steamed and pyrolyzed.
【0005】[0005]
【発明の実施の形態】発明の実施の形態を実施例にもと
づき図面を参照して説明する。図1において、乾留炉内
釜14に廃プラスチック類やシュレッダーダストを入
れ、廃油バーナー17で、乾留炉外釜15を加熱し、軸
受け11で乾留炉内釜14を回転させながら蒸し焼き状
態で生成ガスを発生させる。BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described based on examples with reference to the drawings. In FIG. 1, waste plastics and shredder dust are put in the dry distillation furnace inner pot 14, the dry distillation furnace outer pot 15 is heated by the waste oil burner 17, and the produced gas is steamed while rotating the dry distillation furnace inner pot 14 by the bearing 11. Generate.
【0006】発生した生成ガスを可燃性ガス通路3で外
部のタンク16に取り出し、その可燃ガスを減圧調整期
7で一定圧にし、可燃ガス供給管4にエアーブロアー9
で空気と混合し混合バーナー8と廃油バーナー17によ
り外釜(15)の温度を高温で保ち乾留を速める。The generated gas generated is taken out to the external tank 16 through the combustible gas passage 3, the combustible gas is kept at a constant pressure in the decompression adjusting period 7, and the combustible gas supply pipe 4 is provided with an air blower 9
Then, the temperature of the outer pot (15) is kept high by the mixing burner 8 and the waste oil burner 17 to accelerate the dry distillation.
【0007】乾留炉内釜14内の廃プラスチック類やシ
ュレッダーダストは、酸欠の状態で熱せられるため熱分
解をおこし、最後に水蒸気賦活で純度の高い活性炭に変
化させる。この活性炭を可燃物投入口12からかくはん
板13で反転して活性炭を取り出す。[0007] Waste plastics and shredder dust in the dry distillation furnace inner kettle 14 are heated in the oxygen-deficient state so that they are thermally decomposed, and finally activated by steam to be changed to high-purity activated carbon. This activated carbon is inverted by the stirring plate 13 from the combustibles input port 12 to take out the activated carbon.
【0008】図2において、乾留炉内釜14内に廃プラ
スチック類及びシュレッダーダストを投入し、始めは廃
油バーナー17で内釜14を加熱し、可燃ガスを発生さ
せそのガスを可燃ガスバーナー8で内釜14を更に加熱
し乾留を速める。In FIG. 2, waste plastics and shredder dust are put into the dry distillation furnace inner kettle 14, and the waste oil burner 17 heats the inner kettle 14 at first to generate combustible gas and the combustible gas burner 8 generates the combustible gas. The inner kettle 14 is further heated to accelerate dry distillation.
【0009】図2の外釜ずれ止め19は、修理及び掃除
の時に留炉内釜14と外釜に分離した後結合する時の外
釜15と内釜14の結合部がずれないようにする金具で
す。The outer hook stopper 19 shown in FIG. 2 prevents the connecting portion between the outer hook 15 and the inner hook 14 from being displaced when the inner furnace hook 14 and the outer hook are separated from each other and then connected during repair and cleaning. It is a metal fitting.
【0010】図3は内釜14と軸受け11が外釜15と
分離した内釜14部です。1は外釜キャスタブルで、2
は内釜14の耐熱鋼鈑です。FIG. 3 shows the inner pot 14 part in which the inner pot 14 and the bearing 11 are separated from the outer pot 15. 1 is the outer pot castable and 2
Is a heat-resistant steel plate for the inner pot 14.
【0011】図4は図3で分離した外釜15部です。FIG. 4 shows the 15 parts of the outer pot separated in FIG.
【0012】図5は図3の側面の断面図で撹拌板13で
す。FIG. 5 is a side sectional view of FIG. 3 showing the stirring plate 13.
【0013】図6は可燃ガス貯蔵タンク16と可燃ガス
充填ポンプ18、可燃ガス逆流防止弁6及び可燃ガス調
整弁4です。FIG. 6 shows a combustible gas storage tank 16, a combustible gas filling pump 18, a combustible gas backflow prevention valve 6 and a combustible gas adjusting valve 4.
【0014】[0014]
【実施例】最初は廃油補助バーナーで外釜を加熱し、内
釜から可燃性ガスが発生してきたら、可燃ガス誘導管を
へて可燃ガス充填ポンプで可燃ガス貯蔵タンク貯蔵し、
可燃ガス調整弁で一定圧でエアーブロアーで空気と混合
し可燃ガスバーナーで更に内釜を加熱乾留し内釜内は酸
欠の為活性炭ができる。可燃ガスが出終わったら、投入
口から水蒸気を注入し、賦活する。[Example] First, the outer kettle is heated by the waste oil auxiliary burner, and when flammable gas is generated from the inner kettle, the flammable gas guide pipe is fed to the flammable gas storage pump to store the flammable gas storage tank.
The combustible gas adjusting valve mixes the air with the air with an air blower at a constant pressure, and the combustible gas burner heats and dry-distills the inner pot. When the combustible gas has been discharged, steam is injected from the charging port to activate it.
【0015】[0015]
【発明の効果】本発明の可燃性ガスは焼却炉に高温の熱
エネルギーの燃料として使用できる。又残ったチャー
(活性炭)は排ガスの脱硫、脱硝などの公害対策の吸着
剤として再利用できるという効果と、外釜部と内釜部と
に分離する為に掃除や修理、補修が非常に簡易に行える
効果がある。又酸素を遮断しているのでダイオキシンが
除去される。INDUSTRIAL APPLICABILITY The combustible gas of the present invention can be used as a fuel for high temperature heat energy in an incinerator. Also, the remaining char (activated carbon) can be reused as an adsorbent for pollution control such as desulfurization and denitration of exhaust gas, and it is very easy to clean, repair and repair because it is separated into an outer pot and an inner pot. There is an effect that can be done. Since oxygen is blocked, dioxins are removed.
【図1】本発明の二重釜と加熱構造を示した正面図の断
面図FIG. 1 is a sectional view of a front view showing a double pot and a heating structure of the present invention.
【図2】図1の側面図の断面図2 is a sectional view of the side view of FIG.
【図3】図1の解放時の内釜部及び軸受け部の断面図FIG. 3 is a sectional view of the inner hook portion and the bearing portion at the time of release in FIG.
【図4】図1の解放時の外釜部の断面図FIG. 4 is a cross-sectional view of the outer hook portion when released in FIG.
【図5】図3の側面図の断面図5 is a sectional view of the side view of FIG.
【図6】可燃ガスの充填ポンプ及び可燃ガス貯蔵タンク
の断面図FIG. 6 is a sectional view of a combustible gas filling pump and a combustible gas storage tank.
1 外釜キャスタブル 2 内釜耐熱鋼鈑 3 可燃ガス誘導管 4 可燃性ガス供給管 5 排ガス排出管 6 可燃ガス逆流防止弁 7 可燃ガス調整器 8 可燃ガスバーナー 9 可燃ガス供給エアーブロア 10 投入口密閉ふた 11 回転軸受け 12 廃プラスチック類及びシュレッダーダスト投入
口兼活性炭 13 撹拌板 14 乾留炉内釜 15 乾留炉外釜 16 可燃ガス貯蔵タンク 17 廃油バーナー 18 可燃ガス充填ポンプ 19 外釜ずれ止め1 Outer pot castable 2 Inner pot heat-resistant steel plate 3 Combustible gas induction pipe 4 Combustible gas supply pipe 5 Exhaust gas discharge pipe 6 Combustible gas backflow prevention valve 7 Combustible gas regulator 8 Combustible gas supply air blower 10 Inlet cap 11 rotating bearing 12 waste plastics and shredder dust input port and activated carbon 13 stirring plate 14 dry distillation furnace inner kettle 15 dry distillation furnace outer kettle 16 combustible gas storage tank 17 waste oil burner 18 combustible gas filling pump 19 outer kettle misalignment
Claims (5)
め内釜の外部にキャスタブル(2)(耐火セメント)を
張り、内釜の下方部に乾留焼却穴(3)(空気を遮断し
て燃焼させる穴)を開け、内釜が熱分解し易くより多く
の可燃性ガスを取り出せるようにしました。従来の乾留
炉との違いは、二重釜にした点と、外釜(15)に送風
機(9)より流動層空気1kg当たり原料処理料2とし
て1分間2.51Nm3の空気を送り、二次乾留を行い
二次可燃ガス(5)となって、焼却炉に高温の可燃性ガ
スと成り、炎燃焼がより完全な状態になる装置。1. A castable (2) (refractory cement) is attached to the outside of the inner pot to keep the temperature inside the inner pot (14) constant, and a dry distillation incinerator hole (3) (air is shut off in the lower part of the inner pot). A hole for combustion is opened so that the inner pot is easily decomposed by heat and more combustible gas can be taken out. The difference from the conventional dry distillation furnace is that it has a double kettle, and that 2.51 Nm 3 of air is sent to the outer kettle (15) from the blower (9) as a raw material treatment charge 2 per kg of fluidized bed air for 1 minute. A device that performs secondary carbonization to form a secondary combustible gas (5), which becomes a high-temperature combustible gas in the incinerator, so that flame combustion becomes more complete.
(15)を分離解放部(11)で分離できるようにした
装置。2. An apparatus in which an inner pot (14) and an outer pot (15) can be separated by a separating and releasing section (11) for repair and cleaning.
一定に保ち内部の可燃物熱分解を速める為に円筒形の回
転式に変更した。3. The inner pot (14) of claim 1 is changed to a cylindrical rotary type in order to keep the temperature of heat constant and accelerate thermal decomposition of combustible substances inside.
(3)を除去し、空気を完全に遮断するように改造し
た。4. The dry distillation incinerator hole (3) is removed to remove dioxin, and the dioxin is modified so as to completely block air.
(活性炭)に分解、内釜(14)内のチャー(活性炭)
に水蒸気を注入し賦活する事により表面積の広い活性炭
が得られる。5. The char (activated carbon) in the inner pot (14) is pyrolyzed into combustible gas, produced oil and char (activated carbon).
Activated carbon with a large surface area can be obtained by injecting water vapor into and activating it.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9041308A JPH09328686A (en) | 1996-01-19 | 1997-01-20 | Carbonizing furnace for waste plastics and shredder dust |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3863096 | 1996-01-19 | ||
JP8-38630 | 1996-01-19 | ||
JP9041308A JPH09328686A (en) | 1996-01-19 | 1997-01-20 | Carbonizing furnace for waste plastics and shredder dust |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH09328686A true JPH09328686A (en) | 1997-12-22 |
Family
ID=26377903
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9041308A Pending JPH09328686A (en) | 1996-01-19 | 1997-01-20 | Carbonizing furnace for waste plastics and shredder dust |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH09328686A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001131556A (en) * | 1999-11-02 | 2001-05-15 | Osaka Gas Engineering Co Ltd | Carbonizing furnace |
CN103215054A (en) * | 2013-03-15 | 2013-07-24 | 上海交通大学 | Batch type nitrogen gas filling single-phase pressure release low cost biological charcoal preparation apparatus and method thereof |
CN103420368A (en) * | 2013-07-20 | 2013-12-04 | 大连理工大学 | Integrated device and method for continuous preparation of activated carbon |
CN113862009A (en) * | 2021-10-28 | 2021-12-31 | 烟台市红森林节能环保科技有限公司 | Method for preparing green hydrogen energy and co-producing biochar by pyrolysis and gasification of organic waste III |
-
1997
- 1997-01-20 JP JP9041308A patent/JPH09328686A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001131556A (en) * | 1999-11-02 | 2001-05-15 | Osaka Gas Engineering Co Ltd | Carbonizing furnace |
CN103215054A (en) * | 2013-03-15 | 2013-07-24 | 上海交通大学 | Batch type nitrogen gas filling single-phase pressure release low cost biological charcoal preparation apparatus and method thereof |
CN103215054B (en) * | 2013-03-15 | 2014-10-15 | 上海交通大学 | Batch type nitrogen gas filling single-phase pressure release low cost biological charcoal preparation apparatus and method thereof |
CN103420368A (en) * | 2013-07-20 | 2013-12-04 | 大连理工大学 | Integrated device and method for continuous preparation of activated carbon |
CN113862009A (en) * | 2021-10-28 | 2021-12-31 | 烟台市红森林节能环保科技有限公司 | Method for preparing green hydrogen energy and co-producing biochar by pyrolysis and gasification of organic waste III |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR101162733B1 (en) | Waste pyrolysis system for combustible waste in vacuum without oxygen | |
KR101421478B1 (en) | Waste pyrolysis apparatus for combustible waste in vacuum without oxygen | |
CN207877656U (en) | A kind of novel household garbage pyrolysis gasification furnace | |
JP4593688B1 (en) | Method of supplying combustion air in vertical waste incinerator and vertical waste incinerator | |
CN108194926A (en) | A kind of dangerous waste incineration processing method and its system | |
JP4378360B2 (en) | Power generation method and apparatus using waste | |
NO780047L (en) | WASTE TREATMENT PROCEDURE AND DEVICE | |
JPH09328686A (en) | Carbonizing furnace for waste plastics and shredder dust | |
KR100873924B1 (en) | Carbonizing disposal equipment of waste | |
US5449439A (en) | Superheated low-pollution combustion of the gaseous products of pyrolysis, particularly in multiple small bulbous burner cups | |
KR100757781B1 (en) | Carbonization apparatus for organic waste | |
HUT72158A (en) | Method and apparatus for the yield of heat energy from waste materials, mainly from refuse | |
JP2000283427A (en) | Reaction type refuse incinerating furnace and method for incinerating refuse using the same | |
KR102046329B1 (en) | Incineration apparatus for hot water/wind | |
US6849160B2 (en) | Method and device for heat treatment of waste products | |
JPH102519A (en) | Waste pyrolysis drum and method of pyrolysis | |
JPH10332125A (en) | Wastes treatment equipment | |
JP2000234716A (en) | Incinerator | |
JPH0712321A (en) | Combustion discharged gas toxic substance thermal decomposition furnace | |
JP3015266B2 (en) | Waste melting equipment | |
JP2004161844A (en) | Recycling apparatus | |
JPH09196337A (en) | Waste pylorysis drum and pyrocysis method | |
JPH09196333A (en) | Waste pyrolysis drum | |
JPH11211033A (en) | Waste disposal plant and combustion method thereof | |
JP3069972U (en) | Incinerator equipment |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20040309 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20040318 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20040517 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20050825 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20051024 |
|
A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 20060501 |