JPH05264021A - Continuous generating device using carbonized gas from industrial waste - Google Patents

Continuous generating device using carbonized gas from industrial waste

Info

Publication number
JPH05264021A
JPH05264021A JP11512992A JP11512992A JPH05264021A JP H05264021 A JPH05264021 A JP H05264021A JP 11512992 A JP11512992 A JP 11512992A JP 11512992 A JP11512992 A JP 11512992A JP H05264021 A JPH05264021 A JP H05264021A
Authority
JP
Japan
Prior art keywords
gas
industrial waste
dry distillation
furnace
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.)
Granted
Application number
JP11512992A
Other languages
Japanese (ja)
Other versions
JP3125195B2 (en
Inventor
Nobuaki Debari
宣明 出張
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.)
Individual
Original Assignee
Individual
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Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP11512992A priority Critical patent/JP3125195B2/en
Publication of JPH05264021A publication Critical patent/JPH05264021A/en
Application granted granted Critical
Publication of JP3125195B2 publication Critical patent/JP3125195B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/12Heat utilisation in combustion or incineration of waste

Landscapes

  • Gasification And Melting Of Waste (AREA)

Abstract

PURPOSE:To prevent the leakage of foul odor or smoke even from the industrial waste high in water content by a method wherein the industrial waste high in water content is dried by hot air from a hot air heat exchanger and the exhaust gases containing foul odor are introduced into a gas carbonizing furnace to undergo thermal decomposition. CONSTITUTION:The industrial waste high in water content in a drying hopper 3 is dried by sending the hot water obtained from a gas cleaning cooler 23 and by heating with the exhaust heat from a gas engine to a hot air heat exchanger 7 by a circulating pump 8 and by driving the fan to send air through the sloping holes of an air screen 5. Dry and malodorous exhaust gases are sucked by a dry air blower 20 separated from dusts by an exhaust gas cyclone separator 4 provided at the upper part of the chamber of the drying hopper and then sent to a combustion layer D inside a gas carbonizing furnace 15 to undergo thermal decomposition. In this way the leakage of foul odor and smoke from the device can be prevented.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は産業廃棄物乾留ガス連続
発電装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an industrial waste dry distillation gas continuous power generator.

【0002】[0002]

【従来の技術】この種類の産業廃棄物乾留ガス連続発電
装置として産業廃棄物乾燥部と連動し悪臭対策を施した
装置としては特公昭62−169919号公報によって
提案されているがこの発明は密閉構造の焼却炉と空気分
解装置を用いて、発生した酸素で燃焼させ熱交換器でタ
ービンを回して発電する無公害な装置で有るが、構造が
複雑で低コストの処理が要求される廃棄物処理が不可能
であった。また産業廃棄物発電としては特公昭63−1
86920号公報によって知られているが廃棄物を汚水
処理槽を用いて大量のガスを発生させガスタービン発電
機を用いて800℃以上の燃焼温度で無臭に処理するた
め,ガスタービンを回転させるに必要なガスを発生させ
るためには大容量の分解処理槽が必要であり実現は困難
である。さらに産業廃棄物の乾燥に関しては特公平2−
50012号公報によって提案がなされているが、この
発明は通常の焼却炉の内部に熱交換器を設けて温水をつ
くり廃棄物搬送コンベア部で温風乾燥させるもので搬送
距離と停留時間の関係で多湿な廃棄物の完全乾燥は不可
能で悪臭漏出など問題点を有しており産業廃棄物乾留ガ
ス化炉の応用は不可能である。さらにまた乾留ガス化炉
の気密保持と分離した液体の炉内注入処理に関連しては
特公昭58−2382号公報によって提案がされている
が、この発明は排煙処理と外気の流入により熱分解が阻
害される点に問題がありそのために高性能な乾留ガスを
得る事が困難でタールだけで無く多くの水分と粉塵や塩
基性物質を含み処理に問題がある。また乾留ガス化炉内
での産業廃棄物の堆積高さに関しては特公昭64−46
575公報があるが、産業廃棄物の焼却で炉内で発生す
る高温悪性ガスに曝され熱電対の耐久性に問題があっ
た。
2. Description of the Related Art Japanese Patent Publication No. Sho 62-169919 proposes a device for continuous distillation of gas for industrial waste dry distillation gas, which is linked to an industrial waste drying unit and has a countermeasure against bad odor. It is a pollution-free device that uses an incinerator and an air decomposition device with a structure to burn with generated oxygen and rotate a turbine with a heat exchanger to generate electricity, but the structure is complicated and waste that requires low-cost treatment. It was impossible to process. In addition, as a power generation system for industrial waste
As is known from Japanese Patent Publication No. 86920, in order to rotate waste gas turbines, a waste gas treatment tank is used to generate a large amount of gas and a gas turbine generator is used to odorlessly treat the gas at a combustion temperature of 800 ° C. or higher. A large-capacity decomposition treatment tank is required to generate the required gas, which is difficult to achieve. Furthermore, regarding the drying of industrial waste
Although proposed by Japanese Patent Publication No. 50012, the present invention is to provide a heat exchanger inside a normal incinerator to generate hot water and dry it with warm air in a waste transport conveyor section. It is impossible to completely dry high-humidity waste, and there are problems such as foul odor leakage, and it is impossible to apply an industrial waste dry distillation gasifier. Further, Japanese Patent Publication No. 58-2382 proposes a method for maintaining the airtightness of a dry distillation gasification furnace and a process for injecting a separated liquid into the furnace. There is a problem in that decomposition is impeded, and therefore it is difficult to obtain a high-performance dry distillation gas, and not only tar but also a large amount of water, dust and basic substances are involved in the treatment. Regarding the deposition height of industrial waste in the carbonization gasification furnace, Japanese Examined Patent Publication No. 64-46
Although there is 575 publication, there is a problem in the durability of the thermocouple because it is exposed to the high temperature malignant gas generated in the furnace when the industrial waste is incinerated.

【0003】[0003]

【発明が解決しようとする問題点】産業廃棄物はその性
質状、屋外での貯蔵又は保管が主で風雨を受けて常に多
湿な状態であり、一般には含水率25〜50%wdであ
る、乾燥するには粉塵と悪臭が発生するため通常は処理
前に乾燥し焼却炉で処理する事は不可能であった。この
ような多湿の産業廃棄物を従来は未乾燥のまま乾留ガス
化炉内に直接投入して炉内の乾燥層で乾燥し熱分解させ
ているが、熱分解され排出される乾留ガス中に多量の水
分を含みまた、排出される乾留ガスの温度を低下させて
高カロリーの乾留ガスを得ることは困難であった、そし
て乾留ガス化炉の内部では水分が凝縮して蓄積され水棚
を形成し架橋現象を起こして乾留ガス化炉内部で産業廃
棄物の自然落下を妨げたり、空洞部を形成し火道を形成
し部分燃焼を起こして乾留ガスの発生を著しく阻害して
いたが、多湿な産業廃棄物でも悪臭や煙の漏出する事が
無い、安全でクリーンな処理が可能で、有害な2次環境
汚染物質を発生させず、取扱い操作が簡単な産業廃棄物
乾留ガス連続発電装置が要求されていた。
[Problems to be Solved by the Invention] The nature of industrial waste is that it is mainly stored or stored outdoors and is constantly in a humid state due to wind and rain, and generally has a water content of 25 to 50% wd. Dust and offensive odor are generated when dried, so it was usually impossible to dry before treatment and treat in an incinerator. Conventionally, such high-humidity industrial waste, which is still undried, is directly put into the dry distillation gasification furnace and dried and pyrolyzed in the dry layer in the furnace. It was difficult to obtain a high-calorie dry distillation gas by containing a large amount of water and reducing the temperature of the dry distillation gas to be discharged. Although it formed and caused a cross-linking phenomenon to prevent the natural fall of industrial waste inside the carbonization gasification furnace, or formed a cavity to form a conduit and caused partial combustion to significantly inhibit the generation of carbonization gas. Continuous and dry distillation gas continuous power generation system for industrial waste that does not leak off foul odors and smoke even if it is humid and can be processed safely and cleanly, does not generate harmful secondary environmental pollutants, and is easy to handle. Was required.

【0004】[0004]

【問題点を解決するための手段】乾留ガス化炉で生成し
た熱分解ガスの不純物を凝縮除去するために設けた、熱
交換器やガスエンジンで熱吸収をした高温水を循環し、
多湿な産業廃棄物を温風熱交換器によって乾燥し悪臭を
含んだ排気を乾留ガス化炉に導入して熱分解による処理
と廃棄物投入口より流入する外気を防止するために設け
た、吸引ブロワーの排気を利用して焼却残渣を搬送しサ
イクロンで分離し煙と悪臭を含んだ排気を産業廃棄物乾
留ガス連続発電装置外への漏出を防止し、乾留ガスの改
質ため凝縮分離させたタールと冷却洗浄した粉塵と塩基
性汚水やサイクロンで捕捉した分離水を薬液注入で中和
処理した水と混合し乾留ガス化炉壁部のコイル管で加熱
して炉内の冷却層に注入し水蒸気反応により発熱量の大
幅な向上を図り、炉の過熱防止と熱損失を防いで、汚染
水の処理をする、産業廃棄物乾留ガス連続発電装置。
[Means for Solving Problems] Circulating high-temperature water that has been heat-absorbed by a heat exchanger or a gas engine, which is provided to condense and remove impurities of pyrolysis gas generated in a dry distillation gasification furnace,
Suction that is provided to prevent humidification of industrial waste by drying with a hot air heat exchanger and introducing an exhaust containing odor into a carbonization gasification furnace to prevent thermal decomposition and external air flowing from the waste input port. The incineration residue was transported using a blower exhaust and separated by a cyclone, and the exhaust containing smoke and odor was prevented from leaking out of the industrial waste carbonization gas continuous power generation equipment and condensed to reform the carbonization gas. Tar and cooling Dust washed and mixed with basic sewage and separated water captured by a cyclone are mixed with water neutralized by chemical injection, heated in a coil tube in the dry distillation gasification furnace wall and injected into the cooling layer in the furnace. Industrial waste dry distillation gas continuous power generator that treats contaminated water by significantly increasing the amount of heat generated by steam reaction, preventing overheating and heat loss in the furnace.

【0005】[0005]

【作用】産業廃棄物を乾留ガス化炉で熱分解して生成し
た乾留ガス中のタール及び水分を凝縮除去するために設
けた、水冷サイクロンとガス冷却器やガスエンジンの熱
交換器で冷却水が吸熱した温水を廃棄物乾燥ホッパーの
下部に設けた温風熱交換器によって温風に換え、多湿な
産業廃棄物を乾燥した空気と、乾留ガス炉への外気流入
防止のため設けた吸引ブロワーの排気を利用して焼却残
渣を搬送し煙と悪臭を含んだ排気をサイクロンで分離
し、乾留空気ブロワーによって乾留ガス化炉内の燃焼層
に圧送し、熱分解で煙と悪臭を処理して乾留ガス化を促
進させて連続的に熱分解して、生成した乾留ガスの凝縮
除去と洗浄により捕捉したタールと汚染水を乾留ガス炉
内で水性ガス反応によって発熱量を大幅に増強した、高
性能でクリーンな乾留ガスによってガスエンジンを運転
し発電機で連続的に発電する。
[Operation] A water-cooled cyclone provided for condensing and removing tar and water in the dry-distilled gas produced by thermally decomposing industrial waste in the dry-distillation gasifier, and cooling water with a heat exchanger of a gas cooler or a gas engine. The hot water that has absorbed heat is changed to warm air by the hot air heat exchanger provided at the bottom of the waste drying hopper, and the humid air is used to prevent the inflow of outside air into the dry distillation gas furnace. The incineration residue is transported by using the exhaust of the air, and the exhaust containing smoke and malodor is separated by a cyclone, and is sent to the combustion layer in the carbonization gasification furnace by a carbonization air blower to treat the smoke and malodor by thermal decomposition. It promotes dry distillation gasification and continuously pyrolyzes, and the tar and contaminated water captured by the condensation removal and washing of the produced dry distillation gas and the calorific value are greatly enhanced by the water gas reaction in the dry distillation gas furnace. Performance and clean dry Continuously generated by the generator to operate the gas engine by the gas.

【0006】[0006]

【実施例】以下本発明の産業廃棄物乾留ガス連続発電装
置を図面に基づいて詳述する。図1は産業廃棄物乾留ガ
ス連続発電装置の全体構成図で、廃プラスチック類、紙
木屑、ゴム屑などの多湿な有機性産業廃棄物は投入口1
より床と一体となって斜面に設けたエアスクリーン5に
よって構成された乾燥ホッパー3内に投入される、床下
の温風室6の側面に固定された温風熱交換器7のモータ
ーでファンが駆動され外気を温風に換えエアスクリーン
5の斜孔部より通風して乾燥ホッパー3内の停留廃棄物
を乾燥する、乾燥して悪臭を含んだ排気は乾燥ホッパー
3室上部に設けた排気分離サイクロン4によってダスト
と分離され乾留空気ブロワー20によって吸引され乾留
ガス化炉15炉内部のD燃焼層に送られ熱分解処理され
る、産業廃棄物の投入時は投入口開閉スイッチ2に連動
して温風熱交換器7のファンは停止し、同時に排気分離
サイクロン4の下部が開放されて捕捉されたダストが乾
燥ホッパー3内に排出される機構で悪臭と煙が装置外部
への漏出が生じない構造である。乾燥ホッパー3内で乾
燥された停留廃棄物はスクリュー駆動モーター11によ
って斜行回転する竪搬送スクリュー9によってホッパー
室10まで上昇搬送され斜落し、同時に竪搬送スクリュ
ー9と連動駆動している投入スクリュー12によって乾
留ガス化炉15内に投入される、必要投入量は乾留ガス
化炉15の上部に設けたレベルスイッチ14によって乾
留ガス化炉15の内部で産業廃棄物は常に一定基準面を
維持する事が可能なシステムである。乾留ガス化炉15
内部の圧力は常に負圧であるため竪搬送スクリュー9や
スクリュー駆動モーター11などの隙間から外気が流入
して投入スクリュー12部より炉内部に流入し熱分解を
著しく阻害するため、ホッパー室10の気圧を乾留ガス
化炉15内部と同等な圧力かまたは負圧にする必要があ
り、ホッパー室10の上部に設けた圧力保持ブロワー1
3によってホッパー室10内の空気が排出され乾留ガス
化炉15内部と同等な圧力または負圧とする事で外気の
進入は防止される、臭気と煙を含んだ排出空気は残渣排
出スクリュー19の先端部に接続して設けられた残渣搬
送エジェクター37によって焼却残渣を残渣サイクロン
38に気送搬送させ焼却残渣と分離された排気は温風室
6内に排出して循環されるため装置より外部への煙と悪
臭の漏出を防止する。乾留ガス化炉15内に投入された
産業廃棄物は乾燥ホッパー3より煙と悪臭を含んだ空気
が乾留空気ブロワー20によって炉内の周壁部の複数の
通気孔と一体の中央部通気孔16からD燃焼層へ給気さ
れ産業廃棄物を熱分解し生成した乾留ガスは、炉上部よ
り吸引ブロワー22によって排出され水冷サイクロン2
1の通過時に水冷熱交換コイルによってタールが凝縮除
去されて更にガス洗浄冷却器23で乾留ガス密度を下げ
同時に散水装置により洗浄され粉塵や塩基性物質が除去
されて排気ブロワー25の吸引によって加速された乾留
ガスは除湿サイクロン24によって気水分離がなされ、
クリーンな乾留ガスが連続的に発生してガスエンジン2
9に供給されガスエンジンを回転させて発電機28を駆
動し電気を発生する、燃焼したガスは消音器30を通過
し大気中に放出される。図2は乾燥装置、焼却残渣処理
装置、乾留ガス炉及びガス浄化冷却装置の詳細図で、乾
留ガス化炉15の内部で産業廃棄物は熱分解処理により
上部よりA乾燥層、B熱分解層、C還元層、D燃焼層、
E冷却層によって構成され、炉最下部に残渣排出口18
が設けられ乾留ガス化反応を終了した焼却残渣は残渣排
出スクリュー19によって炉外に排出される。産業廃棄
物乾燥の熱源は水冷サイクロン21の冷却コイルやガス
洗浄冷却器23とガスエンジン排熱で加熱された温水を
循環ポンプ8によって温風熱交換器7に送られファンが
駆動され外気で冷却する密閉式循環システムで内部の循
環水の圧力が規定以上の圧力になった場合はガス洗浄冷
却器23の上部に設置した減圧弁33が開放され大気中
に放出し減圧し装置の破損を防ぐ構造である。乾留ガス
改質のために設けられた水冷サイクロン21で捕捉分離
されたタールは下部の排出パイプによってタール水タン
ク26のタール部35に排出される、ガス洗浄冷却器2
3で洗浄されて粉塵や塩基性物質を除去された乾留ガス
は除湿サイクロン24で気水分離され、洗浄した粉塵や
塩基性物質と分離捕捉した水は下部の排出パイプによっ
てタール水タンク26の洗浄水部36に排出され中和材
注入ポンプ34で薬液によってpH調整され洗浄水循環
ポンプ32によってガス洗浄冷却器23で再度散水され
る、洗浄水部36よりの中和水が補給されて混合され
た、タール含中和水は定量ポンプ27によって乾留ガス
化炉15の周壁内のコイル管で加熱され水蒸気となり水
タール給水孔17より乾留ガス炉15内下部のE冷却層
に給水されて、燃焼後に焼却残渣が保持する熱量で水性
ガス反応し乾留ガスの発生量の増加とガス発熱量の大幅
な強化をはかり併せて残渣排出装置の過熱と熱損失を防
止し、蒸発や給水で不足した水はフロートバルブ31に
よって外部より補給し常に一定の水面を保持する構成で
ある。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The industrial waste dry distillation gas continuous power generation apparatus of the present invention will be described in detail below with reference to the drawings. Fig. 1 is an overall configuration diagram of a continuous distillation gas continuous power generation system for industrial waste. It is an input port for humid organic waste such as waste plastics, paper chips, and rubber chips.
The fan is driven by the motor of the warm air heat exchanger 7 fixed to the side surface of the warm air chamber 6 under the floor, which is thrown into the drying hopper 3 constituted by the air screen 5 provided on the slope more integrally with the floor. The outside air is driven to change to warm air and is ventilated through the oblique holes of the air screen 5 to dry the retained waste in the drying hopper 3, and the dry exhaust gas containing a foul odor is separated from the exhaust gas provided in the upper part of the drying hopper 3 chamber. It is separated from dust by the cyclone 4 and sucked by the dry distillation air blower 20 and sent to the D combustion layer inside the dry distillation gasification furnace 15 for thermal decomposition treatment. When industrial waste is input, it interlocks with the inlet opening / closing switch 2. The fan of the hot air heat exchanger 7 is stopped, and at the same time, the lower part of the exhaust separation cyclone 4 is opened and the trapped dust is discharged into the drying hopper 3, so that no foul odor and smoke leak to the outside of the device. It is a structure. The staying waste dried in the drying hopper 3 is lifted and conveyed to the hopper chamber 10 by the vertical conveying screw 9 which is obliquely rotated by the screw drive motor 11 and is inclined, and at the same time, the feeding screw 12 which is driven in conjunction with the vertical conveying screw 9 is driven. The required amount of the industrial waste is put into the dry distillation gasification furnace 15 by the level switch 14 provided at the upper part of the dry distillation gasification furnace 15 so that the industrial waste is always maintained at a constant reference surface inside the dry distillation gasification furnace 15. It is a system that can Dry distillation gasification furnace 15
Since the internal pressure is always a negative pressure, the outside air flows into the furnace from the gaps such as the vertical conveying screw 9 and the screw drive motor 11 and flows into the furnace from the input screw 12 part, which significantly inhibits thermal decomposition. It is necessary to make the atmospheric pressure equal to or negative pressure inside the dry distillation gasification furnace 15, and the pressure holding blower 1 provided in the upper part of the hopper chamber 10.
The air in the hopper chamber 10 is discharged by 3 and the outside air is prevented from entering by making the pressure or negative pressure equivalent to the inside of the dry distillation gasification furnace 15. The discharge air containing odor and smoke is stored in the residue discharge screw 19. The incineration residue is pneumatically conveyed to the residue cyclone 38 by the residue conveyance ejector 37 connected to the tip portion, and the exhaust gas separated from the incineration residue is discharged into the warm air chamber 6 and circulated, so that it is discharged from the device to the outside. Prevent the leakage of smoke and odors. The industrial waste that has been put into the carbonization gasification furnace 15 is air from the drying hopper 3 that contains smoke and a bad odor from the central ventilation hole 16 which is integrated with a plurality of ventilation holes in the peripheral wall of the furnace by the carbonization air blower 20. The dry distillation gas, which was supplied to the D combustion layer and thermally decomposed the industrial waste, was discharged from the upper part of the furnace by the suction blower 22 and the water-cooled cyclone 2
When passing 1, the tar is condensed and removed by the water-cooled heat exchange coil, and the density of dry distillation gas is further reduced by the gas cleaning cooler 23, and at the same time, it is cleaned by the sprinkler to remove dust and basic substances and accelerated by the suction of the exhaust blower 25. The dry distillation gas is separated into water and water by the dehumidifying cyclone 24,
Clean dry distillation gas is continuously generated and gas engine 2
The burned gas, which is supplied to the gas generator 9 to rotate the gas engine to drive the generator 28 to generate electricity, passes through the silencer 30 and is released into the atmosphere. FIG. 2 is a detailed view of a drying device, an incineration residue treatment device, a dry distillation gas furnace and a gas purification cooling device. Inside the dry distillation gasification furnace 15, industrial waste is pyrolyzed from the upper part to the A dry layer and the B pyrolyzed layer. , C reduction layer, D combustion layer,
It is composed of E cooling layer and has a residue discharge port 18 at the bottom of the furnace.
The incineration residue after completion of the dry distillation gasification reaction is discharged by the residue discharge screw 19 to the outside of the furnace. The heat source for drying the industrial waste is the cooling coil of the water-cooled cyclone 21, the gas cleaning cooler 23, and the hot water heated by the exhaust heat of the gas engine is sent to the warm air heat exchanger 7 by the circulation pump 8 and the fan is driven to cool it by the outside air. When the pressure of the circulating water in the closed circulation system exceeds the specified pressure, the pressure reducing valve 33 installed on the upper part of the gas cleaning cooler 23 is opened and released into the atmosphere to reduce the pressure to prevent the device from being damaged. It is a structure. The tar captured and separated by the water-cooled cyclone 21 provided for reforming the dry distillation gas is discharged to the tar portion 35 of the tar water tank 26 by the lower discharge pipe.
The dry-distilled gas that has been cleaned in step 3 to remove dust and basic substances is separated into water and water by the dehumidifying cyclone 24, and the washed dust and basic substances and the separated and captured water are washed in the tar water tank 26 by the discharge pipe at the bottom. The neutralized water from the cleaning water portion 36 was replenished and mixed, which was discharged to the water portion 36, pH-adjusted by the chemical solution by the neutralizing material injection pump 34, and was sprayed again by the cleaning water circulation pump 32 by the gas cleaning cooler 23. The tar-containing neutralized water is heated by the metering pump 27 in the coil tube in the peripheral wall of the dry distillation gasification furnace 15 to become steam, which is supplied from the water tar water supply hole 17 to the E cooling layer in the lower part of the dry distillation gas furnace 15, and after combustion. The amount of heat retained by the incineration residue reacts with water gas to increase the amount of dry distillation gas generated and significantly strengthen the gas calorific value, and at the same time prevent overheating and heat loss of the residue discharge device, and prevent evaporation and water supply. Added water is configured to hold always constant water supplemented from the outside by the float valve 31.

【0007】[0007]

【発明の効果】多湿な産業廃棄物でも乾留ガス化炉で生
成した乾留ガスの浄化のため設けた凝縮除去やガスエン
ジンで吸熱した高温水を循環利用し焼却炉への投入前に
廃棄物を乾燥し発生した悪臭と、炉上部の投入口からの
空気流入防止のため設けた吸引ブロワーの排気利用によ
る焼却残渣搬送により発生した煙を乾留ブロワーによっ
て乾留ガス化炉内部で熱分解により処理し悪臭と煙の装
置外への漏出を防いだ。乾燥する廃棄物を乾留ガス化炉
に投入する事で乾留ガス中の水分の減少と炉内部での凝
縮による架橋現象と部分燃焼を起こさず、乾留ガスの凝
縮分離と冷却洗浄で発生したタール含む中和水を乾留ガ
ス化炉内の冷却層に注入処理し水性ガス反応で発熱量を
大幅に増強する事が出来た、炉内堆積物自体がタールの
フイルターとなって、高カロリーでクリーンな乾留ガス
を連続的に発生しガスエンジンを回転させ発電する事が
できた、装置からはエンジン排気と焼却残渣以外の汚染
物質〔臭気、煙、酸性汚染水〕は一切排出しないため、
有害で多湿な廃棄物を燃料資源とし、電気エネルギーと
して回収出来る廃棄物乾留ガス連続発電装置である。
EFFECTS OF THE INVENTION Even in the case of humid industrial waste, the condensation removal provided for purification of the dry distillation gas produced in the dry distillation gasification furnace and the circulation of high temperature water absorbed by the gas engine are used to remove the waste before it is put into the incinerator. The odor generated by drying and the smoke generated by the transfer of the incineration residue by using the exhaust air of the suction blower to prevent the inflow of air from the charging port in the upper part of the furnace are treated by pyrolysis inside the dry distillation gasification furnace by a thermal decomposition to produce a bad odor. And the smoke was prevented from leaking out of the device. The dry waste is put into a carbonization gasification furnace to reduce the water content in the carbonization gas and to prevent cross-linking phenomenon and partial combustion due to condensation inside the furnace, and to include tar generated by condensation separation of carbonization gas and cooling and cleaning. Neutralization water was injected into the cooling layer in the dry distillation gasification furnace, and the calorific value could be greatly increased by the water gas reaction. The in-furnace deposit itself became a tar filter, which was high in calories and clean. We were able to continuously generate dry distillation gas and rotate the gas engine to generate electricity.Since the equipment does not emit any pollutants (odor, smoke, acidic polluted water) other than engine exhaust and incineration residue,
It is a continuous gas dry distillation gas power generation system that can recover harmful electric and humid waste as electric energy and as electric energy.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明に係わる廃棄物乾留ガス連続発電装置の
全体構成図である。
FIG. 1 is an overall configuration diagram of a waste dry distillation gas continuous power generation device according to the present invention.

【図2】同例に係わる 乾燥装置、残渣処理装置、乾留
ガス炉、ガス浄化装置の詳細図である。
FIG. 2 is a detailed view of a drying device, a residue treatment device, a dry distillation gas furnace, and a gas purification device according to the same example.

【符号の説明】[Explanation of symbols]

7温風熱交換器 10ホッパー室 12投入スクリュー 15乾留ガス化炉 17水タール給水孔 20乾留空気ブロワー 21水冷サイクロン 23ガス洗浄冷却器 24除湿サイクロン 29ガスエンジン 7 Warm Air Heat Exchanger 10 Hopper Chamber 12 Input Screw 15 Carbon Distillation Gasifier 17 Water Tar Water Supply Hole 20 Carbon Distillation Air Blower 21 Water Cooling Cyclone 23 Gas Wash Cooler 24 Dehumidifying Cyclone 29 Gas Engine

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】ガス浄化用熱交換器やガスエンジンで熱吸
収した高温水を循環させ、多湿な産業廃棄物を温風熱交
換器の熱風で乾燥し、悪臭を含んだ排気を乾留ガス化炉
内に導入し熱分解して処理したことを特徴とした産業廃
棄物乾留ガス連続発電装置。
1. A high-temperature water heat-absorbed by a gas purifying heat exchanger or a gas engine is circulated to dry humid industrial waste with hot air from a hot-air heat exchanger, and exhaust gas containing a foul odor is subjected to dry distillation gasification. A continuous distillation gas continuous power generation system for industrial waste characterized by being introduced into the furnace, pyrolyzed and treated.
【請求項2】廃棄物投入スクリュー部より乾留ガス化炉
の内部へ流入する空気を防止するために設けた、吸引ブ
ロワーの排気を利用して焼却残渣を搬送し、サイクロン
で分離した煙と悪臭を乾留ガス化炉内に導入して、熱分
解によって処理したことを特徴とした産業廃棄物乾留ガ
ス連続発電装置。
2. Smoke and bad odor separated by a cyclone are used to convey the incineration residue by using the exhaust air of a suction blower, which is provided to prevent the air from flowing into the dry distillation gasification furnace from the waste feeding screw section. Was introduced into a dry distillation gasification furnace and treated by thermal decomposition.
【請求項3】ガス改質ため凝縮分離したタールと、冷却
洗浄した粉塵や塩基性汚水を薬液注入により中和処理し
た水と混合し、焼却炉壁内部のコイル管で加熱して乾留
ガス化炉内の冷却層に注入し、水性ガス反応により発熱
量を大幅に向上し炉の過熱防止と汚染物質の処理をした
ことを特徴とした産業廃棄物乾留ガス連続発電装置。
3. Tar that has been condensed and separated for gas reforming is mixed with dust that has been cooled and washed and basic wastewater that has been neutralized by injecting a chemical solution, and the mixture is heated in a coil tube inside the wall of the incinerator and gasified by dry distillation. An industrial waste carbonization gas continuous power generation system characterized by being injected into the cooling layer in the furnace and significantly increasing the amount of heat generated by a water gas reaction to prevent overheating of the furnace and treat pollutants.
JP11512992A 1992-03-23 1992-03-23 Industrial waste carbonized gas continuous power generator Expired - Fee Related JP3125195B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11512992A JP3125195B2 (en) 1992-03-23 1992-03-23 Industrial waste carbonized gas continuous power generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11512992A JP3125195B2 (en) 1992-03-23 1992-03-23 Industrial waste carbonized gas continuous power generator

Publications (2)

Publication Number Publication Date
JPH05264021A true JPH05264021A (en) 1993-10-12
JP3125195B2 JP3125195B2 (en) 2001-01-15

Family

ID=14654995

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11512992A Expired - Fee Related JP3125195B2 (en) 1992-03-23 1992-03-23 Industrial waste carbonized gas continuous power generator

Country Status (1)

Country Link
JP (1) JP3125195B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08189624A (en) * 1995-01-09 1996-07-23 Buyu Sai Incineration equipment
JP2007132254A (en) * 2005-11-10 2007-05-31 Mitsubishi Materials Techno Corp Waste gasification power generation system
WO2015179881A1 (en) * 2014-05-22 2015-11-26 Gia Long Nguyen Gasification and pyrolysis optimization system for medical and toxic waste
JP2020065789A (en) * 2018-10-25 2020-04-30 株式会社トクヤマ Palm seed shell storage method
CN112239683A (en) * 2020-11-18 2021-01-19 刘峪箫 Negative pressure gasification furnace capable of pre-drying materials

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08189624A (en) * 1995-01-09 1996-07-23 Buyu Sai Incineration equipment
JP2007132254A (en) * 2005-11-10 2007-05-31 Mitsubishi Materials Techno Corp Waste gasification power generation system
WO2015179881A1 (en) * 2014-05-22 2015-11-26 Gia Long Nguyen Gasification and pyrolysis optimization system for medical and toxic waste
JP2020065789A (en) * 2018-10-25 2020-04-30 株式会社トクヤマ Palm seed shell storage method
CN112239683A (en) * 2020-11-18 2021-01-19 刘峪箫 Negative pressure gasification furnace capable of pre-drying materials

Also Published As

Publication number Publication date
JP3125195B2 (en) 2001-01-15

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