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JPS6241555B2 - - Google Patents
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JPS6241555B2 - - Google Patents

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Publication number
JPS6241555B2
JPS6241555B2 JP56148718A JP14871881A JPS6241555B2 JP S6241555 B2 JPS6241555 B2 JP S6241555B2 JP 56148718 A JP56148718 A JP 56148718A JP 14871881 A JP14871881 A JP 14871881A JP S6241555 B2 JPS6241555 B2 JP S6241555B2
Authority
JP
Japan
Prior art keywords
carbonization
zone
gas
residual carbon
carbon treatment
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
Application number
JP56148718A
Other languages
Japanese (ja)
Other versions
JPS5852385A (en
Inventor
Kengo Yoshioka
Shozo Minami
Akira Sato
Michiaki Haraoka
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
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP14871881A priority Critical patent/JPS5852385A/en
Publication of JPS5852385A publication Critical patent/JPS5852385A/en
Publication of JPS6241555B2 publication Critical patent/JPS6241555B2/ja
Granted legal-status Critical Current

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  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Processing Of Solid Wastes (AREA)

Description

【発明の詳細な説明】 本発明は油母頁岩の乾留方法及びその設備に係
り、特に一つの炉で原料の予熱乾留、残カーボン
処理、冷却を行なう矩型堅型乾留炉に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for carbonizing oil base shale and its equipment, and more particularly to a rectangular vertical carbonization furnace that performs preheating carbonization, residual carbon treatment, and cooling of a raw material in one furnace.

油母頁岩からいわゆるシエールオイルを回収す
る方法は、大別すると堅型炉、火格子炉、キルン
炉の各種があるが、このうち堅型炉型式は密に充
填した油母頁岩微粒子と加熱媒体としてのガスと
の接触効率が良好なためガス量を少量に止めるこ
とが可能で、このための設備費や運転費の節減を
図ることが可能であり、既に数種のプロセスが開
発されている。
Methods for recovering so-called shale oil from oil matrix shale can be broadly classified into vertical furnaces, grate furnaces, and kiln furnaces. Among these, the vertical furnace type uses densely packed oil matrix shale particles and gas as a heating medium. Since the contact efficiency is good, it is possible to keep the amount of gas to a small amount, thereby reducing equipment costs and operating costs, and several types of processes have already been developed.

これらの従来システムとしては、予熱乾留工程
と残カーボン処理工程を別炉で行なうか又は残カ
ーボン処理を全く行なわないかの2つの方法が知
られている。これらの方法で問題となることは別
炉処理する場合においては設置スペースが必要
である。乾留炉から残カーボン処理炉への原料
運搬工程が必要である。原料運搬のために原料
を一旦冷却する必要が生じ、熱ロスが大きい。
Two methods are known as these conventional systems: either the preheating carbonization step and the residual carbon treatment step are performed in separate furnaces, or the residual carbon treatment is not performed at all. The problem with these methods is that they require installation space when processing in a separate furnace. A process of transporting raw materials from the carbonization furnace to the residual carbon processing furnace is required. In order to transport the raw materials, it is necessary to cool them once, resulting in large heat loss.

又残カーボン処理を全く行なわない場合におい
ては、草木、地下水への影響等公害上の問題があ
る。
Furthermore, if no residual carbon treatment is performed at all, there are pollution problems such as effects on plants and groundwater.

又従来の予熱、乾留、残カーボン処理冷却より
なる乾留炉は、乾留により得られた乾留ガスの一
部を用いて熱源としていた。又残カーボン処理帯
で生成した低カロリーガスが上部の乾留域に流入
することによつて、乾留域内で生成した高カロリ
ーガス(石油相当成分)と混合し、結果として得
られる乾留ガスのカロリーを低減するという欠点
があつた。
In addition, conventional carbonization furnaces consisting of preheating, carbonization, residual carbon treatment and cooling use a portion of the carbonization gas obtained by carbonization as a heat source. In addition, the low-calorie gas generated in the residual carbon treatment zone flows into the upper carbonization zone and mixes with the high-calorie gas (component equivalent to petroleum) generated in the carbonization zone, reducing the calorie content of the resulting carbonization gas. It had the disadvantage of being reduced.

本発明はこれらの課題を解決するものであつ
て、その目的は大気汚染あるいは地下水汚染等の
環境破壊を防止した堅型炉による油母頁岩の乾留
方法を提供するものである。
The present invention is intended to solve these problems, and its purpose is to provide a method for carbonizing oil base shale using a vertical furnace, which prevents environmental damage such as air pollution or groundwater pollution.

本発明の他の目的は、上記乾留方法をエネルギ
ーロスなく高カロリーガスを回収する油母頁岩の
乾留設備を提供するものである。
Another object of the present invention is to provide a carbonization equipment for oil base shale that can recover high-calorie gas without energy loss using the carbonization method described above.

即ち本発明は油母頁岩を予熱、乾留、残カーボ
ン処理、冷却して処理する方法において、前記乾
留域と残カーボン処理域の間に不感帯を設けるこ
とによつて乾留域の下部に設けた残カーボン処理
域で生成した炉内ガスを残カーボン処理域の上端
部より炉外に取り出し、該炉内ガスを用いて前記
乾留域に供給する乾留用ガスを加熱することを特
徴とする油母頁岩の乾留方法を第1発明とする。
That is, the present invention provides a method for treating oil base shale by preheating, carbonization, residual carbon treatment, and cooling, in which a dead zone is provided between the carbonization zone and the residual carbon treatment zone, so that the residual carbon treatment is performed at the lower part of the carbonization zone. A method for carbonizing oil base shale, characterized in that the in-furnace gas generated in the carbon removal zone is taken out of the furnace from the upper end of the residual carbon treatment zone, and the in-furnace gas is used to heat the carbonization gas supplied to the carbonization zone. This is the first invention.

又本発明は予熱帯、乾留帯、残カーボン処理
帯、冷却帯を備えた堅型炉の上部に装入装置を設
け、下部に排出装置を設けて、前記残カーボン処
理帯の下端部に蒸気、空気の吹込口を配設し、残
カーボン処理帯の上端部に炉内ガス取出口を設
け、乾留帯の下端部と予熱帯の上端部とに循環路
を形成し、該循環路に油回収装置、乾留用ガス加
熱器を設け、該加熱器と残カーボン処理帯に設け
たガス取出口とを連通し、更に乾留帯と残カーボ
ン処理帯との間にガス混合防止手段を構成したこ
とを特徴とする油母頁岩の乾留設備を第2発明と
する。
Further, the present invention provides a charging device in the upper part of a vertical furnace equipped with a pre-heating zone, a carbonization zone, a residual carbon treatment zone, and a cooling zone, and a discharge device in the lower part, so that steam is provided at the lower end of the residual carbon treatment zone. , an air inlet is provided, an in-furnace gas outlet is provided at the upper end of the residual carbon treatment zone, a circulation path is formed between the lower end of the carbonization zone and the upper end of the preheating zone, and an oil inlet is provided in the circulation path. A recovery device and a gas heater for carbonization are provided, the heater is communicated with a gas outlet provided in the residual carbon treatment zone, and a gas mixing prevention means is configured between the carbonization zone and the residual carbon treatment zone. A second invention is a carbonization equipment for oil base shale characterized by the following.

以下本発明を図面によつて詳述する。 The present invention will be explained in detail below with reference to the drawings.

本発明の乾留設備は堅型炉10とガス循環系2
0と炉内ガス取出系30とからなる。堅型炉型式
として油母頁岩乾留炉は、予熱、乾留、残カーボ
ン処理、冷却の各域から構成されることが知られ
ているが、装入された原料の流れは概ね次の説明
により理解される。
The carbonization equipment of the present invention includes a vertical furnace 10 and a gas circulation system 2.
0 and a furnace gas extraction system 30. It is known that the oil shale carbonization furnace, which is a hard furnace type, is composed of preheating, carbonization, residual carbon treatment, and cooling sections, but the flow of the charged raw materials can be generally understood from the following explanation. .

1は装入装置の1タイプでありシール構造を用
いるが、図では整流板を設けた例を示している。
装入された原料は、予熱2―1、乾留ゾーン2―
2を経て、残カーボン処理ゾーン3を通つて切出
装置4にて切出され、ホツパー5に貯留冷却さ
れ、シール弁6が開きホツパー7に貯められ、シ
ール弁8が開き、排出される。
1 is one type of charging device that uses a seal structure, but the figure shows an example in which a rectifying plate is provided.
The charged raw materials are preheated 2-1 and carbonized in the carbonization zone 2-1.
2, residual carbon processing zone 3, cut out by cutting device 4, stored in hopper 5 and cooled, seal valve 6 opened and stored in hopper 7, seal valve 8 opened and discharged.

次にガスの流れを説明する。 Next, the flow of gas will be explained.

9は乾留用熱ガス吹込み装置であり、予熱、乾
留ゾーン2で、原料を約500℃に加熱し乾留する
もので、炉頂ガス抜出し管23を通つて炉外に取
り出される。残カーボン処理ゾーン3では、切出
装置4の上部から約800〜1000℃の加熱空気11
とスチーム14を吹込み、乾留後油母頁岩に残つ
ているカーボンと水性ガス化反応を行わせ、ガス
捕集管13より炉外15へ回収される。
Reference numeral 9 denotes a hot gas blowing device for carbonization, which heats the raw material to about 500° C. and carbonizes it in the preheating and carbonization zone 2, and takes it out of the furnace through the furnace top gas extraction pipe 23. In the residual carbon processing zone 3, heated air 11 at about 800 to 1000°C is supplied from the top of the cutting device 4.
and steam 14 are blown in to cause a water gasification reaction with the carbon remaining in the oil base shale after carbonization, and the gas is recovered to the outside of the furnace 15 through the gas collection pipe 13.

12は、ガスパージ管で、上記水性ガス化終了
後のガスが、乾留ゾーン2に入り込まないように
炉下に向けて吹きパージするもので、熱ガス管部
9下部とガス捕集管13上部との間の原料による
ガスシールを捕強している。
Reference numeral 12 designates a gas purge pipe that blows and purges the gas after the completion of the water gasification toward the bottom of the furnace so that it does not enter the carbonization zone 2. A gas seal is created by the raw material between the two.

15は廃原料を冷却する為の冷却ガス吹込み装
置であり、ホツパー5下部より冷却ガスを入れて
いる。残カーボン処理ゾーン3での燃焼生成ガス
が、上部の乾留ゾーン2に流入しないように遮断
する方法として、ガス捕集管13を設けてカーボ
ンとの水性ガス化反応による低カロリーの炉内ガ
スを系外に回収し、必要によりN2等の不活性ガ
スを用いて、管12からパージガスを圧入噴出す
るとよい。本明細書においては以下かゝる技術構
成を乾留帯と残カーボン処理帯との間のガス混合
防止手段という。
15 is a cooling gas blowing device for cooling the waste raw material, and cooling gas is introduced from the lower part of the hopper 5. As a method of blocking the combustion generated gas in the residual carbon processing zone 3 from flowing into the upper carbonization zone 2, a gas collection pipe 13 is installed to collect low-calorie in-furnace gas from the water gasification reaction with carbon. It is preferable to collect the purge gas outside the system and, if necessary, use an inert gas such as N 2 to inject and blow out the purge gas from the pipe 12. In this specification, such a technical configuration will be referred to as means for preventing gas mixture between the carbonization zone and the residual carbon treatment zone.

即ち上述のガス混合防止手段は前記の乾留帯と
残カーボン処理帯との間に設けられるが、その態
様は後述するように、粉体、気体、固体によるシ
ールでその目的が達成され、いわゆるガスの不感
帯と指称しうるものを得て、乾留操作上極めて実
技に適している。
That is, the above-mentioned gas mixing prevention means is provided between the carbonization zone and the residual carbon treatment zone, but as described later, its purpose is achieved by sealing with powder, gas, or solid, and the so-called gas This method provides what can be called a dead zone, making it extremely suitable for practical use in carbonization operations.

第3図は前記ガス混合防止手段の他の例を示し
ているが、乾留ゾーンの下に冷却ガス16で冷却
して、切出し装置17を追加設置して固体シール
とし、N2による気体シールと股状ホツパー32
内の原料の粉体シールの3シールを得ている。
FIG. 3 shows another example of the above-mentioned gas mixing prevention means, in which a cooling gas 16 is used to cool the area under the carbonization zone, a cut-out device 17 is additionally installed to form a solid seal, and a gas seal by N2 is used. Crotch-shaped hopper 32
We have obtained 3 seals for the powder seals for the raw materials.

第4図は更に他の例を示し、残カーボン処理帯
3と乾留帯2との間に絞り部31を介設して切り
出し装置17の切り出し操作により原料の滞留層
高Hを生成し、ガス捕集管13の吸引力の制御に
よる粉体シールと切り出し装置17による固体シ
ールを併用した例を示している。
FIG. 4 shows still another example, in which a constriction part 31 is interposed between the residual carbon treatment zone 3 and the carbonization zone 2, and the raw material retention layer height H is generated by the cutting operation of the cutting device 17, and the gas An example is shown in which a powder seal by controlling the suction force of the collection tube 13 and a solid seal by the cutting device 17 are used together.

本発明のガス循環系20は、予熱帯2―1の上
部と乾留帯2―2の下端部に構成され、油回収装
置21と乾留用ガス加熱器24を設けている。乾
留用ガス加熱器24には炉内ガス取出系30から
分岐する炉内ガスの1部を導入して適温の乾留用
ガスを得ている。
The gas circulation system 20 of the present invention is constructed at the upper part of the pre-preparation zone 2-1 and the lower end of the carbonization zone 2-2, and is provided with an oil recovery device 21 and a carbonization gas heater 24. A part of the furnace gas branched from the furnace gas extraction system 30 is introduced into the carbonization gas heater 24 to obtain carbonization gas at an appropriate temperature.

本発明の堅型炉はその形状は特に限定されるも
のではなく、円筒形あるいは角形に構成される
が、長辺と短辺からなる矩形にしてもよい。矩形
乾留炉は予熱、乾留、残カーボン処理及び冷却の
各帯を共通に矩形状として、所望数の原料装入装
置及び廃原料排出装置を長辺側に沿つて設けると
大量処理に適する。
The shape of the vertical furnace of the present invention is not particularly limited, and may be cylindrical or square, but may be rectangular with long sides and short sides. A rectangular carbonization furnace is suitable for mass processing if the preheating, carbonization, residual carbon treatment, and cooling zones are all rectangular, and the desired number of raw material charging devices and waste material discharge devices are provided along the long sides.

以上本発明について詳述したが、本発明は次の
効果をうる。
The present invention has been described in detail above, and the present invention provides the following effects.

(1) 1つの炉で、乾留、残カーボン処理を行なう
ので、炉数が少なくでき、又、原料運搬工程が
省略できる。
(1) Since carbonization and residual carbon treatment are performed in one furnace, the number of furnaces can be reduced and the raw material transportation process can be omitted.

(2) 乾留炉から残カーボン処理炉への原料運搬工
程が無くなることにより、運搬工程にて生じる
原料の粉化による処理ロスが皆無となる。それ
と同時に原料を一旦冷却する必要もなく、熱ロ
スが格段に少なくなる。
(2) By eliminating the process of transporting raw materials from the carbonization furnace to the residual carbon processing furnace, there is no processing loss due to powdering of raw materials that occurs during the transport process. At the same time, there is no need to temporarily cool the raw material, which significantly reduces heat loss.

(3) 廃原料の残カーボン処理を乾留工程と連続し
て行なえることにより発塵もなく、又残カーボ
ン処理するので大気汚染、地下水汚染、環境破
壊等の問題が解消できる。
(3) Since the residual carbon treatment of waste raw materials can be performed continuously with the carbonization process, there is no dust generation, and since the residual carbon treatment is performed, problems such as air pollution, groundwater pollution, and environmental destruction can be solved.

(4) 残カーボン処理帯における炉内ガスを捕集し
て系外に回収するので低カロリーガスが乾留帯
に流入することがない。
(4) Since the furnace gas in the residual carbon treatment zone is collected and recovered outside the system, low-calorie gas does not flow into the carbonization zone.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明のフローを示す全体説明図、第
2図は本発明の堅型乾留炉の断面図、第3図は本
発明の実施例の部分断面図、第4図は更に本発明
の他の実施例の部分断面図である。 1;装入装置、2;乾留域、3;残カーボン処
理域、4;原料切り出し装置、5;ホツパー、1
0;乾留炉、13;ガス捕集管、20;ガス循環
路、21;油回収装置、24;ガス加熱器、3
0;ガス取出系。
Fig. 1 is an overall explanatory diagram showing the flow of the present invention, Fig. 2 is a cross-sectional view of a vertical carbonization furnace of the present invention, Fig. 3 is a partial cross-sectional view of an embodiment of the present invention, and Fig. 4 is a further illustration of the present invention. FIG. 3 is a partial cross-sectional view of another embodiment of the invention. 1; Charging device, 2; Carbonization area, 3; Residual carbon processing area, 4; Raw material cutting device, 5; Hopper, 1
0; Carbonization furnace, 13; Gas collection pipe, 20; Gas circulation path, 21; Oil recovery device, 24; Gas heater, 3
0; Gas extraction system.

Claims (1)

【特許請求の範囲】 1 油母頁岩を予熱、乾留、残カーボン処理、冷
却して処理する方法において、前記乾留域と残カ
ーボン処理域の間に、ガスシール機構として粉体
層、ガスパージ装置および切り出し装置を単独又
は組合せて構成される不感帯を設け、乾留域の下
部に設けた残カーボン処理域で生成した炉内ガス
を残カーボン処理域の上端部より炉外に取り出
し、該炉内ガスを用いて前記乾留域に供給する乾
留用ガスを加熱することを特徴とする油母頁岩の
乾留方法。 2 予熱帯、乾留帯、残カーボン処理帯、冷却帯
を備えた堅型炉の上部に装入装置を設け、下部に
排出装置を設けて、前記残カーボン処理帯の下端
部に蒸気、空気の吹込口を配設し、残カーボン処
理帯の上端部に炉内ガス収出口を設け、乾留帯の
下端部と予熱帯の上端部とに循環路を形成し、該
循環路に油回収装置、乾留用ガス加熱器を設け、
該加熱器と残カーボン処理帯に設けたガス取出口
とを連通し、更に乾留帯と残カーボン処理帯との
間に、粉体層ガスパージ装置および切り出し装置
を、単独又は組合せてガス混合防止手段を構成し
たことを特徴とする油母頁岩の乾留設備。
[Scope of Claims] 1. A method for treating oil mother shale by preheating, carbonization, residual carbon treatment, and cooling, in which a powder layer, a gas purge device, and a cutting device are provided as a gas sealing mechanism between the carbonization region and the residual carbon treatment region. A dead zone consisting of either one or a combination of A method for carbonizing oil base shale, comprising heating a gas for carbonization supplied to the carbonization region. 2. A charging device is installed in the upper part of a vertical furnace equipped with a preparatory zone, a carbonization zone, a residual carbon treatment zone, and a cooling zone, and a discharge device is installed in the lower part, so that steam and air are supplied to the lower end of the residual carbon treatment zone. An inlet is provided, an in-furnace gas outlet is provided at the upper end of the residual carbon treatment zone, a circulation path is formed between the lower end of the carbonization zone and the upper end of the preheating zone, and an oil recovery device is provided in the circulation path. A gas heater for carbonization is installed,
The heater is connected to a gas outlet provided in the residual carbon treatment zone, and a powder bed gas purge device and a cutting device are provided between the carbonization zone and the residual carbon treatment zone, either alone or in combination, to prevent gas mixing. A carbonization equipment for oil base shale characterized by comprising:
JP14871881A 1981-09-22 1981-09-22 Dry distillation of oil shale and equipment therefor Granted JPS5852385A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14871881A JPS5852385A (en) 1981-09-22 1981-09-22 Dry distillation of oil shale and equipment therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14871881A JPS5852385A (en) 1981-09-22 1981-09-22 Dry distillation of oil shale and equipment therefor

Publications (2)

Publication Number Publication Date
JPS5852385A JPS5852385A (en) 1983-03-28
JPS6241555B2 true JPS6241555B2 (en) 1987-09-03

Family

ID=15459040

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14871881A Granted JPS5852385A (en) 1981-09-22 1981-09-22 Dry distillation of oil shale and equipment therefor

Country Status (1)

Country Link
JP (1) JPS5852385A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63139977A (en) * 1986-12-02 1988-06-11 Agency Of Ind Science & Technol Dry distillation of hydrocarbon-containing solid
CN102492446B (en) * 2011-12-16 2013-12-11 沈阳海源干馏设备技术开发有限公司 Combined type gas full-cycle gas retort
CN102967667B (en) * 2012-11-19 2015-01-14 中国科学院广州地球化学研究所 Device for qualitatively and quantitatively analyzing shale gas and using method thereof
CN104192800B (en) * 2014-08-29 2016-01-20 华南理工大学 A combined power generation system and process for oil shale retort gas chemical chain hydrogen production
CN118222313B (en) * 2024-05-22 2024-08-30 河南天利热工装备股份有限公司 Oil shale granule carbonization furnace and operation method

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