JPH0125360B2 - - Google Patents
Info
- Publication number
- JPH0125360B2 JPH0125360B2 JP13180381A JP13180381A JPH0125360B2 JP H0125360 B2 JPH0125360 B2 JP H0125360B2 JP 13180381 A JP13180381 A JP 13180381A JP 13180381 A JP13180381 A JP 13180381A JP H0125360 B2 JPH0125360 B2 JP H0125360B2
- Authority
- JP
- Japan
- Prior art keywords
- carbonization
- gas
- furnace
- air supply
- cylinder
- 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
-
- 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
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or 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
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Coke Industry (AREA)
- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Description
【発明の詳細な説明】
産業上の利用分野
この発明は、乾留ガスの簡易発生装置に関し、
殊に使用済み廃タイヤを乾留して簡便に乾留ガス
を発生させ、省資源・省エネルギーに寄与するこ
とを企図した乾留ガス発生装置に関するものであ
る。[Detailed Description of the Invention] Industrial Application Field This invention relates to a simple generation device for carbonized gas,
In particular, the present invention relates to a carbonization gas generation device designed to easily generate carbonization gas by carbonization of used waste tires, thereby contributing to resource and energy conservation.
従来技術
自動車の普及が今日の如く飛躍的に増大するに
つれて、使用済みのタイヤが大量に廃棄されるよ
うになり、これら廃タイヤの処理が廃棄物行政の
大きな課題となるに至つている。一般にこの種廃
タイヤは、船舶等の緩衝用防舷材としての用途
や、風水害対策として河川岸や崖に敷設される土
塁代りの用途程度しか再利用されておらず、その
大部分は焼却したり、破砕した細片を埋立てに供
したりしているのが実情である。この場合に、廃
タイヤを焼却処理するに際しては、焼却炉中にタ
イヤを直接投入して着火し、炉床底部から空気を
強制供給する所謂「直燃法」が採用されている。BACKGROUND OF THE INVENTION As the popularity of automobiles increases dramatically today, used tires are being disposed of in large quantities, and the treatment of these discarded tires has become a major issue for waste management. In general, this kind of waste tires are only reused as buffer fenders for ships, etc., or as earthworks laid on riverbanks and cliffs to prevent wind and flood damage, and the majority of them are incinerated. The reality is that the crushed pieces are sent to landfill. In this case, when incinerating waste tires, the so-called "direct combustion method" is adopted, in which the tires are directly placed in an incinerator, ignited, and air is forcibly supplied from the bottom of the hearth.
発明が解決しようとする課題
ところで、タイヤは石油系炭化水素化合物の重
合体で構成されており、主成分は典型的にはゴム
53%、カーボンブラツク25%、コード類9%、化
学薬品6%、オイル5%等であるので可燃性に富
み、その燃焼時には亜硫酸ガスや悪臭等を発生す
る。そこで、これら公害要因の発生を抑えるため
完全燃焼させると、1500℃以上の高温となり、通
常の焼却炉では炉体が損傷する欠点がある。これ
に対照するため、炉体外装を二重壁構造の水套
(ウオータージヤケツト)として構成し、水を循
環させて炉体の強制水冷を行なう特殊な炉構造が
提案されているが、これは炉の構築コストが大き
く嵩む難点がある。Problems to be Solved by the Invention Incidentally, tires are composed of polymers of petroleum-based hydrocarbon compounds, and the main component is typically rubber.
It is highly flammable as it is made up of 53% carbon black, 25% carbon black, 9% cords, 6% chemicals, and 5% oil, and when burned, it releases sulfur dioxide gas and bad odors. Therefore, if complete combustion is performed to suppress the occurrence of these pollution factors, the temperature reaches a high temperature of over 1,500°C, which has the drawback of damaging the furnace body in a normal incinerator. In order to contrast this, a special furnace structure has been proposed in which the furnace body exterior is configured as a double-walled water jacket and water is circulated to perform forced water cooling of the furnace body. However, the disadvantage is that the construction cost of the furnace increases significantly.
また、この種の廃タイヤ専焼炉は、タイヤの完
全燃焼による焼却処理を指向しているので、燃焼
時の発生熱量の有効利用は殆ど考慮されておら
ず、最近に至つて温水・温風機としての活用が僅
かに実現されている程度に過ぎない。 In addition, this type of waste tire incineration furnace is aimed at incineration by complete combustion of the tire, so there is little consideration given to the effective use of the heat generated during combustion, and until recently it has been used as a hot water/hot air generator. However, the utilization of this technology has only been realized to a limited extent.
そこで発明者は、廃タイヤが前記の如く石油系
炭化水素合物の重合体であつて、燃焼条件をコン
トロールすることによつて良好な可燃物となる事
実に着眼し、従来技術のように充分な酸素供給の
下に燃焼させることに代えて乾留を行ない、燃焼
成分を揮発させて乾留ガスを発生させ、得られた
ガスをバーナーによる熱源として利用すれば、廃
タイヤの処理と有効な熱利用とが一挙に達成され
ることを突き止めた。この場合、一般に木材や石
炭等の乾留ガス化法は公知となつているが、燃
料中にガス化促進剤である空気や水蒸気をむらな
く均一に供給するこ、炉内を乾留ガス化に最適
な温度に保持すること、および防爆対策に万全
を期することが、技術上の難点として指摘されて
おり、これは廃タイヤの乾留ガス化に際しても解
決すべき重要な共通課題となつている。 Therefore, the inventor focused on the fact that waste tires are polymers of petroleum-based hydrocarbon compounds as described above, and can be made into a good combustible material by controlling combustion conditions. If carbonization is performed instead of combustion under a sufficient oxygen supply, the combustion components are volatilized to generate carbonization gas, and the resulting gas is used as a heat source by a burner, it is possible to process waste tires and use heat effectively. It was discovered that these can be achieved all at once. In this case, the carbonization gasification method for wood, coal, etc. is generally known, but the inside of the furnace is ideal for carbonization gasification by evenly and uniformly supplying air and water vapor, which are gasification promoters, into the fuel. It has been pointed out that maintaining the temperature at a certain temperature and taking all possible explosion-proof measures are technical difficulties, and these are important common issues that need to be solved when converting waste tires to carbonized gas.
発明の目的
本発明は、このように一般に乾留ガス化が困難
とされていた、例えば廃タイヤによる乾留ガス化
を手軽に実現化し、しかもそのガス化操業を特殊
な専門技能者を要することなく行ない得るように
した乾留ガス簡易発生装置を提供することを目的
とする。Purpose of the Invention In this way, the present invention easily realizes the carbonization gasification of waste tires, which is generally considered to be difficult, and also allows the gasification operation to be carried out without requiring special technicians. The object of the present invention is to provide a simple carbonization gas generation device that can obtain the following effects.
課題を解決するための手段
前記の課題を克服し、所期の目的を好適に達成
するために、本発明に係る乾留ガス簡易発生装置
は、外周に通気孔を穿設した外筒と、この外筒に
同心的に挿通され、上方開口部が拡開して外筒の
上部を閉塞する内筒とから二重管体を構成し、
耐火内張を施した乾留炉の内部に、被乾留物を
収納可能な所要空間を介して前記二重管体を直立
配置し、
外部送風源に連通する第1空気供給管を前記外
筒の下部に接続すると共に、先端にガスバーナー
チツプを有し前記乾留炉の外方に導出した乾留ガ
ス送給管を前記内筒の下部に接続し、
前記第1空気供給管から分岐導出した第2空気
供給管を、前記乾留ガス送給管に同心的に内挿し
て、その管体開口部を前記ガスバーナーチツプ近
傍に臨ませ、
更に乾留炉の炉室に、熱風供給機の吹出し口を
連通接続するように構成したことを特徴とする。Means for Solving the Problems In order to overcome the above-mentioned problems and suitably achieve the intended purpose, a simple carbonization gas generator according to the present invention includes an outer cylinder having ventilation holes in its outer periphery, and The inner cylinder is inserted concentrically into the outer cylinder, and the upper opening expands to close the upper part of the outer cylinder, forming a double pipe body. The double pipe body is arranged upright through a required space capable of storing objects, a first air supply pipe communicating with an external air blowing source is connected to the lower part of the outer pipe, and a gas burner tip is provided at the tip. A carbonization gas feed pipe led out to the outside of the carbonization furnace is connected to the lower part of the inner cylinder, and a second air supply pipe branched out from the first air supply pipe is connected concentrically to the carbonization gas feed pipe. It is characterized by being inserted into the tube so that the opening of the tube faces the vicinity of the gas burner chip, and further connecting the outlet of the hot air supply device to the furnace chamber of the carbonization furnace.
実施例
次に、本発明に係る乾留ガス簡易発生装置につ
き、好適な実施例を挙げて、添付図面を参照しな
がら以下説明する。なお図示の実施例は、好適例
としての一実施態様を示すものであつて、本発明
が図示の構造に限定されるものでないことは勿論
である。Embodiments Next, preferred embodiments of the carbonized gas simple generator according to the present invention will be described below with reference to the accompanying drawings. Note that the illustrated embodiment shows one embodiment as a preferred example, and it goes without saying that the present invention is not limited to the illustrated structure.
第1図は本発明に係る乾留ガス簡易発生装置の
一実施例の縦断面を概略図示したものであつて、
参照符号10は乾留ガス発生装置の本体をなす乾
留炉を示す。この乾留炉10は、内壁に耐火セメ
ントの如き内張を施して、耐火性と保温性とを付
与した好ましくは円筒状の炉体として構成され、
この円筒状炉体の内部に、被乾留物としての廃タ
イヤ12が重畳的に多数収納されるようになつて
いる。前記炉体10の底部近傍には適宜のロスト
ル(火格子)14を張架して、このロストル14
により炉体内を炉室16と燃焼残渣回収室18と
に画成する。 FIG. 1 is a schematic longitudinal cross-sectional view of an embodiment of a simple carbonized gas generator according to the present invention.
Reference numeral 10 indicates a carbonization furnace that forms the main body of the carbonization gas generator. This carbonization furnace 10 is preferably configured as a cylindrical furnace body whose inner wall is lined with a refractory cement to provide fire resistance and heat retention.
Inside this cylindrical furnace body, a large number of waste tires 12 as materials to be carbonized are stored in an overlapping manner. A suitable rostle (grate) 14 is stretched near the bottom of the furnace body 10, and this rostle 14
The inside of the furnace body is defined into a furnace chamber 16 and a combustion residue recovery chamber 18.
次いで、図示のように耐火性に優れた金属を材
質とする空気供給筒20を炉室16に中心に垂直
に立設する。この空気供給筒20は、廃タイヤ1
2をタイヤ中心孔を介して挿通し得る程度の直径
を有する外部円筒22と、その外部円筒22の内
部に同心的に内挿した内部円筒24とからなる中
空二重構造となつている。そして、外部円筒22
は、その上部を前記内部円筒24のラツパ状に拡
開する上部開口により閉塞されると共に、下部に
おいて空気供給管26を介して送風機28に接続
されている。また外部円筒22には空気孔30が
適宜数穿設されて、廃タイヤ12の周辺に空気を
供給するようになつているが、この空気孔30の
穿孔数は、筒体上部が比較的疎で、下方に行くに
従つて密となるように穿設するのが好ましい。 Next, as shown in the figure, an air supply cylinder 20 made of a metal with excellent fire resistance is vertically installed in the center of the furnace chamber 16. This air supply tube 20 is a waste tire 1.
The tire has a double hollow structure consisting of an outer cylinder 22 having a diameter large enough to allow a tire to be inserted through the center hole of the tire, and an inner cylinder 24 concentrically inserted into the outer cylinder 22. And the outer cylinder 22
is closed at its upper part by the upper opening of the inner cylinder 24 which expands in a flared shape, and is connected to a blower 28 via an air supply pipe 26 at its lower part. Further, an appropriate number of air holes 30 are bored in the outer cylinder 22 to supply air around the waste tire 12, but the number of air holes 30 is relatively small in the upper part of the cylinder. It is preferable to drill the holes so that they become denser toward the bottom.
また、前記二重筒体20の内部円筒24は、上
部を開放して後述する乾留ガスの流路として使用
される。そして内筒24の下部は、先端にガスバ
ーナーチツプ34を備え乾留炉外方へ導出した乾
留ガス送給管32に接続されている。この場合、
前記送風機28に接続する空気供給管26は、こ
れを中途で分岐して第2空気供給管36を導出
し、これを図示のように乾留ガス送給管32中に
同心的に挿通して、その開口先端部を前記ガスバ
ーナーチツプ34近傍に臨ませるようにしておく
のが好ましい。なお、第1空気供給管26および
第2空気供給管36には、夫々ダンパ38,40
を設けて空気供給量を調節し得るようにしてお
く。更に、前記内部円筒24の上部は全開放状態
のままとしておいてもよいが、図示のように適宜
数の通孔42を穿設した笠44を被せて、この内
部円筒24中に吸引される乾留ガスのガス濃度を
均一に拡散させるようにしておくのが好ましい。 Further, the inner cylinder 24 of the double cylinder body 20 has an open upper part and is used as a flow path for carbonization gas, which will be described later. The lower part of the inner cylinder 24 is connected to a carbonization gas feed pipe 32 having a gas burner chip 34 at its tip and led out to the outside of the carbonization furnace. in this case,
The air supply pipe 26 connected to the blower 28 is branched in the middle to lead out a second air supply pipe 36, which is concentrically inserted into the carbonized gas supply pipe 32 as shown in the figure. It is preferable that the opening end face the vicinity of the gas burner chip 34. Note that the first air supply pipe 26 and the second air supply pipe 36 are provided with dampers 38 and 40, respectively.
be installed so that the air supply amount can be adjusted. Furthermore, although the upper part of the inner cylinder 24 may be left completely open, it is covered with a cap 44 having an appropriate number of through holes 42 as shown in the figure, so that the inner cylinder 24 is sucked into the inner cylinder 24. It is preferable to uniformly diffuse the gas concentration of the carbonized gas.
次に、炉室16の下方に開口部46が穿設さ
れ、この開口部46は管体48を介して熱風供給
機50に接続されている。この熱風供給機50
は、電気容量の大きい電熱ヒーターを内蔵し、極
めて高温の熱風を発生して、短時間で炉内温度を
任意の高温度に調節し得るようになつている。な
お、この熱風供給機50および先に述べた送風機
28は、何れも送気を目的とするものであるか
ら、送風能力の全開状態で送風を行なうと、乾留
炉10の炉室16内に充分の酸素供給を行なつて
しまうことになり、乾留(すなわち蒸し焼き状
態)条件を満たさないことになつてしまう。従つ
て、熱風供給機50および送風機28により炉室
16に供給される空気量は、炉室16の内容積並
びに乾留される廃タイヤの量に応じて調節し、良
好な乾留状態を維持するに足るだけの酸素が全体
として送られるようにする必要がある。この場
合、熱風供給機50は適切な機種選定を行なうこ
とによつて、風景が少くてしかも高静圧が得られ
るものを使用することができ、これによつて乾留
状態を保ちながら炉内を高温に制御可能である。 Next, an opening 46 is bored below the furnace chamber 16, and this opening 46 is connected to a hot air supply device 50 via a pipe 48. This hot air supply machine 50
The furnace has a built-in electric heater with a large electric capacity and generates extremely high-temperature hot air, allowing the temperature inside the furnace to be adjusted to a desired high temperature in a short period of time. Note that this hot air supply device 50 and the above-mentioned blower 28 are both used for the purpose of blowing air, so if air is blown with the blowing capacity fully open, there will be enough air in the furnace chamber 16 of the carbonization furnace 10. Therefore, the carbonization (that is, steaming state) conditions would not be satisfied. Therefore, the amount of air supplied to the furnace chamber 16 by the hot air supply device 50 and the blower 28 is adjusted according to the internal volume of the furnace chamber 16 and the amount of waste tires to be carbonized to maintain a good carbonization condition. It is necessary to ensure that enough oxygen is delivered throughout the body. In this case, by selecting an appropriate model for the hot air supply device 50, it is possible to use one that provides a small amount of scenery and high static pressure. Can be controlled at high temperatures.
なお、第1図において参照符号52は廃タイヤ
投入口を示し、参照符号54および56は、夫々
炉内覗窓および燃焼残渣(一般には灰)回収口を
示す。 In FIG. 1, reference numeral 52 indicates a waste tire input port, and reference numerals 54 and 56 indicate an in-furnace viewing window and a combustion residue (generally ash) collection port, respectively.
実施例の作用
次に、前述した構成を有する本実施例に係る乾
留ガス簡易発生装置の使用の実際につき説明す
る。使用に際しては、廃タイヤ投入口52より使
用済みの廃タイヤ12を、そのタイヤ中心孔を空
気供給筒20に挿通するようにして適宜数積み重
ね、一番上層にある廃タイヤ新聞紙等を種火とし
て上付け着火を行なう。併せて、空気供給管26
のダンパ38を全開し、送風機28より多量の空
気を供給して廃タイヤの燃焼を促進させ、炉内温
度が充分高まつたところで前記ダンパ38の開放
を絞り、乾留に必要な程度の酸素を供給する。こ
のように炉内温度が乾留に必要な程度にまで高ま
ると、廃タイヤ12はその表面から溶融し、可燃
性のガスが揮発し始め、炉室16内に滞留する。
これが乾留ガスである。Effects of the Embodiment Next, the actual use of the carbonization gas simple generator according to the present embodiment having the above-described configuration will be explained. When in use, an appropriate number of used waste tires 12 are stacked from the waste tire inlet 52 with the tire center hole inserted into the air supply cylinder 20, and the top layer of waste tire newspaper or the like is used as a pilot light. Perform top ignition. In addition, the air supply pipe 26
The damper 38 is fully opened and a large amount of air is supplied from the blower 28 to promote the combustion of the waste tires. When the temperature inside the furnace has risen sufficiently, the damper 38 is closed to release the amount of oxygen necessary for carbonization. supply When the temperature inside the furnace rises to a level necessary for carbonization, the waste tire 12 melts from its surface, and flammable gas begins to volatilize and stays in the furnace chamber 16.
This is carbonized gas.
次いで、前記熱風供給機50の運転を開始し
て、高温の熱風を開口部46より炉室16に送り
込み、炉内温度を乾留条件に応じて適宜コントロ
ールすることにより、安定した乾留操業を行なう
ことができる。炉室16内に充満した乾留ガス
は、空気供給筒20に穿設した空気孔30からの
噴気により炉室内が正圧に保持されているため、
図示のように内部円筒24中へ強制的に送り出さ
れ、乾留ガス送給管32を介してガスバーナーチ
ツプ34に向かう。このとき、先に述べたように
ガスバーナーチツプ34の近傍に第2空気供給管
36の開口部が臨んでいるので、この第2空気供
給管36からの憤出空気によつて乾留ガスは伴流
現像を生じ、急速にガスバーナーチツプ34に供
給されると共に、適切な空気混合が行われる。す
なわちバーナーチツプは、空気加圧で乾留ガスの
供給を行なうエジエクターとして作用する。この
状態でガスバーナーチツプ34に点火すれば、乾
留ガスは良好に燃焼するから、この燃焼エネルギ
ーをボイラーその他の熱源として有効に利用すれ
ばよい。 Next, the operation of the hot air supply device 50 is started, high temperature hot air is sent into the furnace chamber 16 from the opening 46, and the temperature inside the furnace is appropriately controlled according to the carbonization conditions to perform stable carbonization operation. Can be done. The carbonized gas filling the furnace chamber 16 is maintained at a positive pressure inside the furnace chamber by the fumes from the air holes 30 formed in the air supply tube 20.
As shown, the gas is forced into the inner cylinder 24 and directed to the gas burner chip 34 via the carbonization gas feed pipe 32. At this time, as mentioned above, since the opening of the second air supply pipe 36 faces the vicinity of the gas burner chip 34, the carbonized gas is entrained by the air discharged from the second air supply pipe 36. Flow development occurs and is rapidly fed to the gas burner chip 34 with proper air mixing. In other words, the burner chip acts as an ejector that supplies carbonization gas by pressurizing air. If the gas burner chip 34 is ignited in this state, the carbonized gas will burn well, so this combustion energy can be effectively used as a heat source for boilers and other devices.
なお、乾留を開始した当初は、可燃性が充分で
ない稀薄ガスが発生するが、これは一般に臭気を
伴うものである。そこで、乾留ガス送給管32の
ガスバーナーチツプ34接続部近傍に電熱コイル
からなるバンドヒーター58を巻付けて、最初に
到来する稀薄ガスを充分に加熱し、脱臭およびガ
ス燃焼の促進を図るのが望ましい。また、バンド
ヒーターに代えて、前記熱風供給機50からの高
温熱風を分岐導出して稀薄ガスに混入し、脱臭を
図るようにしてもよい。 In addition, at the beginning of carbonization, dilute gas with insufficient flammability is generated, which is generally accompanied by an odor. Therefore, a band heater 58 made of an electric heating coil is wound around the connection part of the gas burner chip 34 of the carbonization gas feed pipe 32 to sufficiently heat the diluted gas that arrives first to promote deodorization and gas combustion. is desirable. Furthermore, in place of the band heater, high-temperature hot air from the hot air supply device 50 may be branched out and mixed into the diluted gas for deodorization.
発明の効果
以上に説明した如く、本発明に係る乾留ガス簡
易発生装置によれば、乾留炉中に投入した廃タイ
ヤに上付け着火して、充分な空気供給のもとに廃
タイヤの燃焼を開始し、炉内温度を充分上昇させ
た後空気供給量を絞つて乾留ガス化反応をし易い
状態とし、次いで熱風供給機により高温の熱風を
炉中に供給して炉中温度を上昇させて乾留を促進
し、手軽に乾留ガスを得ることができる。すなわ
ち、炉内が乾留温度に到達した後は、熱風供給機
により高温熱風を炉内に吹込み、被乾留物の種
類、性状に応じて乾留ガス化温度を自由に設定し
得るので、実施例に示した廃タイヤに限らず、布
切れ、紙屑、プラスチツク廃棄物、木材片等多種
のものを乾留して可燃性ガスを大量に得ことがで
き、省資源、省エネルギーに寄与するところがめ
て大きいものである。Effects of the Invention As explained above, according to the simple carbonization gas generator of the present invention, a waste tire placed in a carbonization furnace is top ignited, and the waste tire is combusted with sufficient air supply. After starting the process and raising the temperature inside the furnace sufficiently, the air supply amount is reduced to facilitate the carbonization gasification reaction, and then high-temperature hot air is supplied into the furnace using a hot air supply machine to raise the temperature inside the furnace. It promotes carbonization and allows you to easily obtain carbonized gas. That is, after the inside of the furnace reaches the carbonization temperature, high-temperature hot air is blown into the furnace by the hot air supply device, and the carbonization gasification temperature can be freely set according to the type and property of the material to be carbonized. It is possible to obtain a large amount of flammable gas by carbonizing not only the waste tires shown in the figure, but also various other materials such as cloth, paper waste, plastic waste, wood chips, etc., which greatly contributes to resource and energy conservation. It is something.
なお、炉中には熱電対、サーミスタ等の温度検
手段を挿入して炉内温度を監視し、適切な乾留を
行なうに必要な最高・最低温度の範囲内で熱風供
給機を稼動させるようにしておく。 In addition, temperature detection means such as thermocouples and thermistors are inserted into the furnace to monitor the temperature inside the furnace, and the hot air supply machine is operated within the range of maximum and minimum temperatures necessary for proper carbonization. I'll keep it.
第1図は、本発明に係る乾留ガスの簡易発生装
置の概略を示す縦断面図である。
10……乾留炉、12……廃タイヤ、16……
炉室、20……二重筒体、22……外部円筒、2
4……内部円筒、26……(第1)空気供給管、
28……送風機、30……空気孔、32……乾留
ガス送給管、34……ガスバーナーチツプ、36
……第2空気供給管、42……通孔、44……
笠、46……開口部、48……管体、50……熱
風供給機、52……廃タイヤ投入口、58……バ
ンドヒーター。
FIG. 1 is a longitudinal sectional view schematically showing a simple carbonization gas generation device according to the present invention. 10... Carbonization furnace, 12... Waste tires, 16...
Furnace chamber, 20...Double cylinder, 22...External cylinder, 2
4...inner cylinder, 26... (first) air supply pipe,
28... Blower, 30... Air hole, 32... Carbonized gas feed pipe, 34... Gas burner chip, 36
...Second air supply pipe, 42...Through hole, 44...
Shade, 46...opening, 48...pipe body, 50...hot air supply machine, 52...waste tire inlet, 58...band heater.
Claims (1)
の外筒22に同心的に挿通され、上方開口部が拡
開して外筒22の上部を閉塞する内筒24とから
二重管体20を構成し、 耐火内張を施した乾留炉10の内部に、被乾留
物12を収納可能な所要空間を介して前記二重管
体20を直立配置し、 外部送風源28に連通する第1空気供給管26
を前記外筒22の下部に接続すると共に、先端に
ガスバーナーチツプ34を有し前記乾留炉10の
外方に導出した乾留ガス送給管32を前記内筒2
4の下部に接続し、 前記第1空気供給管26から分岐導出した第2
空気供給管36を、前記乾留ガス送給管32に同
心的に内挿して、その管体開口部を前記ガスバー
ナーチツプ34近傍に臨ませ、 更に乾留炉10の炉室16に、熱風供給機50
の吹出し口を連通接続する よう構成したことを特徴とする乾留ガス簡易発生
装置。 2 外筒22の筒体外周における通気孔30の穿
設数は、筒体上部が比較的疎で下方になるにつれ
て密となるよう設定される特許請求の範囲第1項
記載の乾留ガス簡易発生装置。 3 内筒24の上部に通孔を多数穿設した笠体4
4が被着される特許請求の範囲第1項記載の乾留
ガス簡易発生装置。 4 乾留ガス送給管32には、ガスバーナーチツ
プ34との接続部近傍にバンドヒーター58が巻
着される特許請求の範囲第1項記載の乾留ガス簡
易発生装置。[Scope of Claims] 1. An outer cylinder 22 having a ventilation hole 30 formed on its outer periphery, and an inner cylinder that is inserted concentrically through the outer cylinder 22 and whose upper opening expands to close the upper part of the outer cylinder 22. The double pipe body 20 is constructed from the carbonization furnace 10 with a refractory lining, and the double pipe body 20 is arranged upright inside the carbonization furnace 10 with a refractory lining, with a required space in which the material to be carbonized 12 can be stored. A first air supply pipe 26 communicating with the air source 28
is connected to the lower part of the outer cylinder 22, and a carbonization gas feed pipe 32 having a gas burner chip 34 at the tip and leading out of the carbonization furnace 10 is connected to the inner cylinder 22.
4 and branched out from the first air supply pipe 26.
An air supply pipe 36 is inserted concentrically into the carbonization gas supply pipe 32 so that the opening of the pipe body faces the vicinity of the gas burner chip 34, and a hot air supply machine is further inserted into the furnace chamber 16 of the carbonization furnace 10. 50
1. A simple carbonization gas generator characterized in that the air outlet of the carbonization gas is configured to be connected in communication with each other. 2. The carbonized gas simple generation according to claim 1, wherein the number of vent holes 30 on the outer periphery of the outer cylinder 22 is set to be relatively sparse in the upper part of the cylinder and become denser as it goes downward. Device. 3 Shade body 4 with many through holes drilled in the upper part of the inner cylinder 24
4. The simple carbonization gas generator according to claim 1, wherein the carbonization gas generator is coated with a carbon dioxide gas. 4. A simple carbonization gas generator according to claim 1, wherein a band heater 58 is wound around the carbonization gas feed pipe 32 near the connection portion with the gas burner chip 34.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56131803A JPS5834888A (en) | 1981-08-22 | 1981-08-22 | Simplified dry distillation gas generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56131803A JPS5834888A (en) | 1981-08-22 | 1981-08-22 | Simplified dry distillation gas generator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5834888A JPS5834888A (en) | 1983-03-01 |
| JPH0125360B2 true JPH0125360B2 (en) | 1989-05-17 |
Family
ID=15066470
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56131803A Granted JPS5834888A (en) | 1981-08-22 | 1981-08-22 | Simplified dry distillation gas generator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5834888A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0692590B2 (en) * | 1990-11-14 | 1994-11-16 | 株式会社マルコシエンンジニアリング | Dry distillation gasification treatment method of polymer waste and dry distillation gasification treatment apparatus |
| RU2493234C2 (en) * | 2011-11-11 | 2013-09-20 | Благодаров Юрий Петрович | Plant for thermochemical processing of hydrocarbon raw material |
| WO2016171163A1 (en) * | 2015-04-21 | 2016-10-27 | 株式会社コクブン | Gas generation device |
| JP2022067822A (en) * | 2020-10-21 | 2022-05-09 | 株式会社仙翔精機 | Thermal decomposition furnace, thermal decomposition system, thermal decomposition method of materials for carbonization, and reforming technology of regenerated oil |
-
1981
- 1981-08-22 JP JP56131803A patent/JPS5834888A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5834888A (en) | 1983-03-01 |
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