JP2853916B2 - Apparatus and method for rapid pyrolysis of coal - Google Patents

Apparatus and method for rapid pyrolysis of coal

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Publication number
JP2853916B2
JP2853916B2 JP13503791A JP13503791A JP2853916B2 JP 2853916 B2 JP2853916 B2 JP 2853916B2 JP 13503791 A JP13503791 A JP 13503791A JP 13503791 A JP13503791 A JP 13503791A JP 2853916 B2 JP2853916 B2 JP 2853916B2
Authority
JP
Japan
Prior art keywords
coal
gas
reactor
reaction vessel
temperature gas
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 - Lifetime
Application number
JP13503791A
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Japanese (ja)
Other versions
JPH04359991A (en
Inventor
小林勝明
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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Filing date
Publication date
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Priority to JP13503791A priority Critical patent/JP2853916B2/en
Publication of JPH04359991A publication Critical patent/JPH04359991A/en
Application granted granted Critical
Publication of JP2853916B2 publication Critical patent/JP2853916B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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、石炭から化学原料、燃
料ガスおよび炭素質原料を製造する方法において、石炭
と高温ガスとを混合して石炭の熱分解反応を行わせる石
炭の熱分解装置および方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a chemical raw material, a fuel gas and a carbonaceous raw material from coal, in which a coal and a high-temperature gas are mixed to perform a thermal decomposition reaction of the coal. And methods.

【0002】[0002]

【従来の技術】石炭の加工プロセスの一つとして、石炭
の熱分解プロセスがある。石炭を熱分解(乾留)すると
高発熱量ガス、タール、およびコークスが得られる。こ
れらは燃料、化学原料、金属精錬用還元材として使用さ
れている。石炭の急速熱分解反応を起こさせると従来の
コークス炉における熱分解反応に比べてガス、タール等
の気液成分の収率が高くなることはよく知られている。
そのために石炭から気液成分を多く回収したい場合は石
炭の急速熱分解法が好ましい。
2. Description of the Related Art One of coal processing processes is a coal pyrolysis process. Pyrolysis (dry distillation) of coal produces high calorific value gas, tar and coke. These are used as fuels, chemical raw materials, and reducing materials for metal refining. It is well known that the rapid pyrolysis reaction of coal increases the yield of gas-liquid components such as gas and tar as compared with the pyrolysis reaction in a conventional coke oven.
Therefore, when it is desired to recover a large amount of gas-liquid components from coal, a rapid pyrolysis method of coal is preferable.

【0003】石炭の急速熱分解プロセスとしてよく用い
られる方法として気流層反応器を用いる方法がある。こ
れは石炭と高温ガスを反応器内部に吹き込み、そこで混
合、熱分解を行わせるものである。この構造により石炭
の熱分解を効率よく行わせるためには、石炭粒子を気相
中に広く分散させ、石炭粒子と高温ガスの混合を均一に
かつ、反応器内壁における石炭の付着・成長がないこと
が必要である。
[0003] As a method frequently used as a rapid pyrolysis process of coal, there is a method using a gas-bed reactor. In this method, coal and high-temperature gas are blown into the reactor, where they are mixed and thermally decomposed. In order to efficiently perform pyrolysis of coal by this structure, coal particles are widely dispersed in the gas phase, the mixture of coal particles and high-temperature gas is uniform, and there is no adhesion or growth of coal on the inner wall of the reactor It is necessary.

【0004】石炭の急速熱分解のための反応器の従来技
術として、例えば特開平2−265995号の装置があ
る。図2に同装置による反応器の一例を示す。石炭は反
応器上部の石炭導入管1より反応器内に吹き込まれ、高
温ガスは石炭導入管の吹き出し口周辺のノズル5より吹
き込まれ、ここで石炭とガスが混合し、熱分解反応が起
こるようになっている。
[0004] As a prior art of a reactor for rapid pyrolysis of coal, there is, for example, an apparatus disclosed in Japanese Patent Application Laid-Open No. Hei 2-265959. FIG. 2 shows an example of a reactor using the same apparatus. Coal is blown into the reactor from a coal inlet pipe 1 in the upper part of the reactor, and high-temperature gas is blown from a nozzle 5 around an outlet of the coal inlet pipe, where the coal and gas are mixed and a thermal decomposition reaction occurs. It has become.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、上記の
装置の反応器においては、熱可塑性のある石炭を用いた
場合、反応器内壁に石炭が付着・成長し石炭の熱分解反
応が阻害される。石炭の急速熱分解により良質のガス、
タール等の気液成分を多く取るためには熱可塑性を有す
る石炭が好ましいことはよく知られている。
However, when thermoplastic coal is used in the reactor of the above-described apparatus, the coal adheres to and grows on the inner wall of the reactor, and the thermal decomposition reaction of the coal is inhibited. Good quality gas by rapid pyrolysis of coal,
It is well known that coal having thermoplasticity is preferable in order to obtain a large amount of gas-liquid components such as tar.

【0006】本発明の目的は、反応器内壁における石炭
の付着・成長を防止することにより、熱可塑性を示す石
炭を含む広範囲の石炭を使用し、良質のガス、タール等
の気液成分を効率良く製造し、また原料石炭の制約の少
ない石炭の急速熱分解装置および方法を提供するもので
ある。
An object of the present invention is to prevent the adhesion and growth of coal on the inner wall of a reactor, thereby making it possible to use a wide range of coal including thermoplastic coal and efficiently remove gas and liquid components such as high-quality gas and tar. It is an object of the present invention to provide an apparatus and a method for rapid pyrolysis of coal which are well produced and have less restrictions on raw coal.

【0007】[0007]

【課題を解決するための手段および作用】本発明は、そ
の目的を達成するために、石炭導入管、ガス導入部、ガ
ス噴射用ノズルおよび反応器よりなる石炭熱分解装置に
おいて、ガス導入部およびガス噴射用ノズルを2系統も
うけ、第1の系統は石炭の熱分解用の高温ガス吹き込み
を、第2の系統は反応器内壁での石炭付着防止用ガス吹
き込みを配置することを特徴とする石炭熱分解装置であ
る。また、本発明において第2系統より吹き込むガスに
石炭チャーとの反応性が高いガスを含有させることを特
徴とする石炭熱分解方法である。
SUMMARY OF THE INVENTION In order to achieve the object, the present invention provides a coal pyrolysis apparatus comprising a coal inlet pipe, a gas inlet, a gas injection nozzle and a reactor. Coal characterized in that two gas injection nozzles are provided, a first system is provided with a high-temperature gas injection for thermal decomposition of coal, and a second system is provided with a gas injection for preventing coal adhesion on the inner wall of the reactor. It is a pyrolysis device. Further, in the present invention, there is provided a coal pyrolysis method characterized in that the gas blown from the second system contains a gas having high reactivity with coal char.

【0008】以下、本発明を詳細に説明する。図1に本
発明における石炭熱分解装置の概念図を示す。この装置
では管1を通って気流搬送されてきた石炭と、第1系統
のガス吹き込み装置ではガスを管3より装置上部4に送
りノズル5から反応器2に吹き込み、その高温ガスと反
応器2内で混合し、石炭を加熱・分解する構造を、また
第2系統のガス吹き込み装置ではガスを管6より反応器
周辺部7に送りノズル8から反応器内壁部分に吹き込
み、反応器内壁での石炭の付着・成長を防止する構造を
有する。第2系統のガス吹き込み装置の作用は反応器内
に噴射される石炭粒子が反応器壁方向に向かうのと逆方
向にガスを噴射し、石炭粒子が反応器内壁に近寄り難く
する機能を持っている。
Hereinafter, the present invention will be described in detail. FIG. 1 shows a conceptual diagram of a coal pyrolysis apparatus according to the present invention. In this apparatus, coal fed by airflow through a pipe 1 and, in a first gas blowing apparatus, gas is sent from a pipe 3 to an upper part 4 of the apparatus, and is blown into a reactor 2 from a nozzle 5, and the high-temperature gas and the reactor 2 In the second gas blowing device, gas is sent from a pipe 6 to a peripheral portion 7 of the reactor, and is blown from a nozzle 8 into the inner wall portion of the reactor. Has a structure to prevent coal adhesion and growth. The function of the gas injection device of the second system is to inject the gas in the opposite direction to the direction in which the coal particles injected into the reactor are directed toward the reactor wall, and to prevent the coal particles from approaching the reactor inner wall. I have.

【0009】第2系統のガス吹き込み装置において、ガ
ス噴射ノズル8の反応器における配置は必ずしも全反応
器壁に配置する必要はない。石炭の反応器内壁への付着
は石炭が熱可塑性を示す温度で反応器内壁に接触する場
合におこる。一般に石炭が熱可塑性を示す温度は200
〜600℃の範囲である。従って、反応器内壁へのガス
噴射ノズル8の配置は最小限反応器内壁部近辺の石炭粒
子が熱可塑性を示す温度になる領域に配置することが必
要である。
In the gas injection device of the second system, the arrangement of the gas injection nozzles 8 in the reactor need not necessarily be arranged on all the reactor walls. Coal deposition on the reactor inner wall occurs when the coal contacts the reactor inner wall at a temperature at which the coal is thermoplastic. Generally, the temperature at which coal exhibits thermoplasticity is 200
~ 600 ° C. Therefore, it is necessary to arrange the gas injection nozzle 8 on the inner wall of the reactor at least in a region near the inner wall of the reactor where the temperature of the coal particles becomes thermoplastic.

【0010】また、第2系統のガス吹き込み装置から吹
き込むガス中に石炭チャーと反応性の高い成分、例えば
水蒸気、炭酸ガスおよび酸素ガス等の酸化性ガスの一種
または数種を含ませることは、反応器内壁に付着した石
炭チャーを早期に酸化させて反応器内壁での石炭チャー
の成長を防止する作用を持たせるものである。なお、吹
き込みガス中の酸化成分は反応器内壁部分で石炭チャー
と反応してH2,COガスに変化するために製品ガスの
品質を落とすことはない。
[0010] Further, it is preferable that the gas blown from the gas blowing device of the second system contains a component highly reactive with coal char, for example, one or several oxidizing gases such as steam, carbon dioxide and oxygen gas. The function is to oxidize the coal char adhered to the inner wall of the reactor at an early stage to prevent the growth of the coal char on the inner wall of the reactor. The oxidizing component in the blown gas reacts with the coal char at the inner wall of the reactor and changes into H 2 and CO gas, so that the quality of the product gas does not deteriorate.

【0011】以上述べてきたように、石炭熱分解装置に
おいて反応器内壁周辺部からガスを噴出する装置をもう
け、またそこから吹き込むガスに石炭チャーと反応しや
すい酸化性ガスを含有させることは反応器内壁での石炭
チャーの付着・成長を防止し、安定した石炭の熱分解操
業、良質な製品の確保および広範囲な原料石炭の使用に
多大の貢献を果たすものである。
As described above, in the coal pyrolysis apparatus, a device for ejecting gas from the peripheral portion of the inner wall of the reactor is provided, and the gas blown from the device contains an oxidizing gas which easily reacts with coal char. It prevents coal char from adhering and growing on the inner wall of the vessel and plays a major role in stable coal pyrolysis operation, securing high-quality products, and using a wide range of raw coal.

【0012】[0012]

【実施例】以下に本発明装置および方法を利用した場合
の実施例について述べる。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment using the apparatus and method of the present invention will be described below.

【0013】表1に使用した石炭の性状を示す。ここ
で、A石炭は熱可塑性の小さい石炭である。一方、B石
炭は熱可塑性の高い石炭である。
Table 1 shows the properties of the coal used. Here, the A coal is a small thermoplastic coal. On the other hand, B coal is a highly thermoplastic coal.

【0014】表1の石炭を<200meshに粉砕し、
供給量240g/hr、反応温度900℃の条件で熱分
解を行った。本実施例に用いたガスは石炭加熱用のガス
(第1系統)は加熱したN2ガスを用いた。また反応器
内壁より噴出させるガス(第2系統)はN2ガスに空気
を20%混合したガスを使用した。反応器の寸法は内径
55mm、長さ600mmで、反応器内壁周辺に配置し
たガス吹き出しノズルは反応器内壁の上半分にもうけ
た。また、同ノズル径は0.5mm
Crush the coal of Table 1 to <200 mesh
Thermal decomposition was performed under the conditions of a supply amount of 240 g / hr and a reaction temperature of 900 ° C. As a gas used in this example, a heated N 2 gas was used as a coal heating gas (first system). Further, as a gas (second system) ejected from the inner wall of the reactor, a gas obtained by mixing 20% of air with N 2 gas was used. The reactor had an inner diameter of 55 mm and a length of 600 mm, and a gas blowing nozzle arranged around the inner wall of the reactor was provided in the upper half of the inner wall of the reactor. The nozzle diameter is 0.5mm

【0015】[0015]

【表1】 [Table 1]

【0016】ノズル密度は1個/cm2とした。石炭加
熱用の第1系統からのガス流量は15Nl/min、ま
た反応器内壁面での石炭付着防止用の第2系統からのガ
ス流量は2Nl/minとした。表2に結果を示す。
The nozzle density was 1 nozzle / cm 2 . The gas flow rate from the first system for heating coal was 15 Nl / min, and the gas flow rate from the second system for preventing coal adhesion on the inner wall surface of the reactor was 2 Nl / min. Table 2 shows the results.

【0017】[0017]

【表2】 [Table 2]

【0018】また、比較例の場合は実施例において第2
系統のガス吹き込み装置を除いたもので、その他の試験
条件は実施例の場合に同じである。表3に比較例の結果
を示す。
In the case of the comparative example, the second
Except for the gas blowing device of the system, other test conditions are the same as those of the embodiment. Table 3 shows the results of the comparative example.

【0019】[0019]

【表3】 [Table 3]

【0020】[0020]

【発明の効果】以上のように本発明は熱可塑性を有する
石炭を使用しても、安定した熱分解操業ができ、また良
好な品質の製品を得ることができた。すなわち、本発明
により石炭熱分解時に反応器内壁での石炭付着・防止を
はかることにより石炭熱分解操業の安定化をはかり、良
質な製品の確保および原料石炭の制約が少なく広範囲の
石炭の使用を可能にしたもので工業的、経済的効果が大
きい。
As described above, according to the present invention, even when coal having thermoplasticity is used, a stable pyrolysis operation can be performed and a product of good quality can be obtained. In other words, the present invention stabilizes the coal pyrolysis operation by preventing coal adhesion and prevention on the inner wall of the reactor during the pyrolysis of the coal, securing high-quality products and restricting the use of raw coal. It is made possible and has great industrial and economic effects.

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

【図1】本発明の装置の例を示す概念図FIG. 1 is a conceptual diagram showing an example of an apparatus of the present invention.

【図2】従来装置の例を示す概念図FIG. 2 is a conceptual diagram showing an example of a conventional device.

【符号の説明】[Explanation of symbols]

1…石炭導入管 2…熱分解反応器 3…第1系統ガス導入管 4…第1系統ガス
導入部 5…第1系統ガス導入ノズル 6…第2系統ガス
導入管 7…第2系統ガス導入部 8…第2系統ガス
導入ノズル
DESCRIPTION OF SYMBOLS 1 ... Coal introduction pipe 2 ... Pyrolysis reactor 3 ... 1st system gas introduction pipe 4 ... 1st system gas introduction part 5 ... 1st system gas introduction nozzle 6 ... 2nd system gas introduction pipe 7 ... 2nd system gas introduction Part 8: second system gas introduction nozzle

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C10J 3/74 C10J 3/74 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code FI C10J 3/74 C10J 3/74

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 石炭導入管、高温ガス導入部およびガス
噴射ノズルを有する反応容器内で石炭と高温ガスを接触
させて石炭を熱分解させる装置において、高温ガス導入
部およびガス噴射ノズルを2系統設け、第1の系統を石
炭の熱分解用高温ガスの供給源として、第2の系統の噴
射ノズルを反応容器内壁面の石炭が接触する面に設け、
第2の系統を反応容器内壁面への石炭付着防止手段とし
て機能せしめるよう構成してなる石炭の急速熱分解装
置。
An apparatus for thermally decomposing coal by bringing coal into contact with a high-temperature gas in a reaction vessel having a coal introduction pipe, a high-temperature gas introduction section, and a gas injection nozzle, wherein the high-temperature gas introduction section and the gas injection nozzle have two systems. The first system is provided as a supply source of a high-temperature gas for thermal decomposition of coal, and the injection nozzle of the second system is provided on a surface of the inner wall surface of the reaction vessel where the coal contacts,
An apparatus for rapid pyrolysis of coal, wherein the second system functions as means for preventing coal adhesion to the inner wall surface of the reaction vessel.
【請求項2】 石炭導入管、高温ガス導入部およびガス
噴射ノズルを有する反応容器内で石炭と高温ガスを接触
させて石炭を熱分解させる方法において、高温ガス導入
部およびガス噴射ノズルを2系統設け、第1の系統を石
炭の熱分解用高温ガスの供給源として、第2の系統の噴
射ノズルを反応容器内壁面の石炭が接触する面に設け、
第2の系統を反応容器内壁面への石炭付着防止手段とし
て機能せしめ、前記第2の系統から反応容器内へ石炭チ
ャーとの反応性が高いガスを含有するガスを吹き込むこ
とを特徴とする石炭の急速熱分解方法。
2. A method for thermally decomposing coal by bringing coal into contact with a high-temperature gas in a reaction vessel having a coal introduction pipe, a high-temperature gas introduction section, and a gas injection nozzle. The first system is provided as a supply source of a high-temperature gas for thermal decomposition of coal, and the injection nozzle of the second system is provided on a surface of the inner wall surface of the reaction vessel where the coal contacts,
Coal characterized in that the second system functions as means for preventing coal adhesion to the inner wall surface of the reaction vessel, and a gas containing a gas having high reactivity with coal char is blown into the reaction vessel from the second system. Rapid pyrolysis method.
JP13503791A 1991-06-06 1991-06-06 Apparatus and method for rapid pyrolysis of coal Expired - Lifetime JP2853916B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13503791A JP2853916B2 (en) 1991-06-06 1991-06-06 Apparatus and method for rapid pyrolysis of coal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13503791A JP2853916B2 (en) 1991-06-06 1991-06-06 Apparatus and method for rapid pyrolysis of coal

Publications (2)

Publication Number Publication Date
JPH04359991A JPH04359991A (en) 1992-12-14
JP2853916B2 true JP2853916B2 (en) 1999-02-03

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Country Link
JP (1) JP2853916B2 (en)

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* Cited by examiner, † Cited by third party
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WO1998010225A1 (en) * 1996-09-04 1998-03-12 Ebara Corporation Rotary fusing furnace and method for gasifying wastes using the rotating fusing furnace
KR101096632B1 (en) * 2009-12-10 2011-12-21 에스케이이노베이션 주식회사 Top feeding dual swirling gasifier
CN104498075B (en) * 2014-12-19 2016-03-30 中美新能源技术研发(山西)有限公司 A kind of Fast retrieval reactor and technique thereof

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JPH04359991A (en) 1992-12-14

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