JPS5811590A - Coal liquefaction - Google Patents

Coal liquefaction

Info

Publication number
JPS5811590A
JPS5811590A JP11023881A JP11023881A JPS5811590A JP S5811590 A JPS5811590 A JP S5811590A JP 11023881 A JP11023881 A JP 11023881A JP 11023881 A JP11023881 A JP 11023881A JP S5811590 A JPS5811590 A JP S5811590A
Authority
JP
Japan
Prior art keywords
coal
solvent
substance
alkali
slurry
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP11023881A
Other languages
Japanese (ja)
Inventor
Sadatoshi Obe
大部 貞利
Sadazumi Obe
大部 貞純
Toshiyuki Obe
大部 利幸
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.)
OBE SADASHI
OBE TOSHINORI
Original Assignee
OBE SADASHI
OBE TOSHINORI
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 OBE SADASHI, OBE TOSHINORI filed Critical OBE SADASHI
Priority to JP11023881A priority Critical patent/JPS5811590A/en
Publication of JPS5811590A publication Critical patent/JPS5811590A/en
Pending legal-status Critical Current

Links

Landscapes

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

Abstract

PURPOSE:To liquefy coal easily at low cost, by stirring coal with an alkali solution. CONSTITUTION:For example, 100pts.wt. coal such as bituminous coal, brown coal, etc. having a particle size of 80-100 meshes is blended with preferably 45-55pts.wt. aqueous solution of a hydroxide, carbonate, etc. of an alkali (alkaline earth) metal, stirred under heating at 40-70 deg.C, and the coal is made into a brown slurry substance. The slurry substance is extracted with a solvent such as benzene, pyridine, etc., to give a light oil, etc.

Description

【発明の詳細な説明】 本発明はアルカリ性溶液を使用した石炭の液化方法に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for liquefying coal using an alkaline solution.

従来から知られている石炭液化方法は、一般に加温・加
圧の状態で直接または間接に石炭に水素を添加して液状
化する方法である。
Conventionally known coal liquefaction methods generally involve adding hydrogen directly or indirectly to coal under heating and pressurization to liquefy it.

このよう・な石炭液化方法には主としてソルボリシス法
、溶剤抽出法、直接水添法があるが、いずれも経済的に
採算がと些ないという欠点がある。
Such coal liquefaction methods mainly include the solvolysis method, the solvent extraction method, and the direct hydrogenation method, but all of them have the disadvantage that they are not economically viable.

本発明者は思いかけずもアルカリ性溶液が石炭を溶解す
ることを見い出し本発明をなすに至った。
The present inventor unexpectedly discovered that an alkaline solution dissolves coal, and has accomplished the present invention.

すなわち、本発明は石炭とアルカリ性溶液とを攪拌して
スラリー状物質を得、このスラリー状物質を溶剤抽出す
る石炭の液化方法である。
That is, the present invention is a coal liquefaction method in which a slurry-like substance is obtained by stirring coal and an alkaline solution, and this slurry-like substance is extracted with a solvent.

本発明において使用される石炭は瀝青炭から亜炭までで
あるが、液状化しやすいのは瀝青炭および褐炭である。
Coal used in the present invention ranges from bituminous coal to lignite, but bituminous coal and lignite tend to liquefy.

石炭の粒度は100メツシユ以下、好ましくは80〜1
00メツシユである。80メツシユに満たないものは液
化に時間を要し、また100メツシユを越えるものはコ
ストが高くつく。
The particle size of the coal is 100 mesh or less, preferably 80-1
It is 00 mesh. If it is less than 80 meshes, it will take time to liquefy, and if it is more than 100 meshes, the cost will be high.

本発明において使用するアルカリ性溶液にはアルカリ金
属、13aおよびSr等の水酸化物水溶液やアルカリ金
属の炭酸塩水溶液、塩基性酸化物(アルカリ金属、アル
カリ土類金属の酸化物等)の水溶液、アルカリ金属の炭
酸塩の水溶液、アルカリ金属の炭酸水素塩の水溶液、ア
ンモニア水溶液、アルコール、アミン水溶液等があげら
れる。
The alkaline solutions used in the present invention include aqueous solutions of hydroxides of alkali metals, 13a and Sr, aqueous carbonate solutions of alkali metals, aqueous solutions of basic oxides (oxides of alkali metals, alkaline earth metals, etc.), alkali Examples include aqueous metal carbonate solutions, alkali metal hydrogen carbonate aqueous solutions, ammonia aqueous solutions, alcohols, amine aqueous solutions, and the like.

本発明では石炭とアルカリ性溶液とを攪拌するがその配
合割合は石炭100重址部に対しアルカリ性溶液を40
〜60重量部、好ましくは45〜55 重量部である。
In the present invention, coal and alkaline solution are stirred, and the mixing ratio is 40 parts of alkaline solution to 100 parts of coal.
-60 parts by weight, preferably 45-55 parts by weight.

それ以外の場合でも液化できないことはないが、収率が
おちる。
In other cases, liquefaction is not impossible, but the yield will be lower.

この粉砕した石炭とアルカリ性溶液とを適当が攪拌釜に
入れ、常圧で釜内温度約40℃〜70℃に加熱しなから
7oor、p、mで約90分から210分間攪拌を続け
ると、石炭粉末は茶褐色のスラリー状物質となる。
The pulverized coal and alkaline solution are placed in a suitable stirring pot, heated to an internal temperature of about 40°C to 70°C under normal pressure, and then stirred at 7oor, p, m for about 90 minutes to 210 minutes. The powder becomes a brown slurry.

このスラリー状物質を溶剤抽出する。使用溶剤はベンゼ
ン、トルエン、キシレン等の芳香族系溶剤またはピリジ
ノ等の極性有機溶剤を使用するがこれらに限定されず抽
出可能であれば何でもよい。
This slurry material is subjected to solvent extraction. The solvent used is aromatic solvents such as benzene, toluene, xylene, etc., or polar organic solvents such as pyridino, but is not limited to these, and any solvent may be used as long as extraction is possible.

溶剤抽出は使用溶剤が着色しなくなるまで繰返し行う。Solvent extraction is repeated until the solvent used is no longer colored.

次に抽出物と溶剤との混合物から溶剤を留去させ石炭液
状物を得た。こt物の赤外−線吸収スペクトルは三池炭
を使用した場合、従来の水素添加方法で得られt物と、
吸収スペクトルがほぼ洞じ箇所に出た。
Next, the solvent was distilled off from the mixture of the extract and the solvent to obtain a coal liquid. When using Miike charcoal, the infrared absorption spectrum of this material was obtained by the conventional hydrogenation method.
The absorption spectrum appeared almost at the cave.

なお本発明によって得られた石炭液状物は、原油と比較
した場合、分子量が小さく、軽質原油ないしは特軽質原
油に対応すると考えられる。
Note that the coal liquid obtained by the present invention has a small molecular weight when compared to crude oil, and is considered to correspond to light crude oil or extra light crude oil.

なお、溶剤抽出後の残留物から重質油を留出するためと
固形燃料をi4)るため乾留を行う。
Note that carbonization is performed to distill heavy oil and solid fuel from the residue after solvent extraction.

その際触媒としてケインウ士、酸性白土、アルミナ等の
単一または混合したものを使用し、約600℃に加熱す
ると重質油が留出し、残渣としてコークス状の固形燃料
が得られる。
At this time, a single catalyst or a mixture of carbon dioxide, acid clay, alumina, etc. is used as a catalyst, and when heated to about 600° C., heavy oil is distilled out and a coke-like solid fuel is obtained as a residue.

水素を添加して石炭液化を行った場合は残渣として残る
ものは灰秋物である。
When coal is liquefied by adding hydrogen, what remains as a residue is ash.

このように本発明によればアルカリ性溶液により容易に
石炭の液化がe=■能となり、経済的に採算がとれる石
炭・液化方法が提供できる。
As described above, according to the present invention, it is possible to easily liquefy coal using an alkaline solution so that e=■ability is achieved, and an economically profitable method for liquefying coal can be provided.

以下、実施例により本発明を更に詳細に説明する。Hereinafter, the present invention will be explained in more detail with reference to Examples.

実施例1 拌し、石炭液化を容易にする物質を得た。Example 1 Stirring resulted in a substance that facilitates coal liquefaction.

この物質の比重は1.0221、粘度は27.2mmポ
アズである。
This material has a specific gravity of 1.0221 and a viscosity of 27.2 mm poise.

この物質50重量部と、100メツシユ以下に粉砕しを
50℃に加熱しながら120分間攪拌して茶褐色のスラ
リー状物質を得た。このスラリー状物質をソックスレー
脂肪抽出器(Jts−に−0101)により溶剤抽出を
行った。
50 parts by weight of this material was ground into 100 meshes or less and stirred for 120 minutes while heating at 50°C to obtain a brown slurry material. This slurry material was subjected to solvent extraction using a Soxhlet fat extractor (Jts-ni-0101).

溶剤にはべ/ゼy1000市V部を使用し480分間抽
出を行った結果27重軟部の石炭液状物を得た。
Extraction was carried out for 480 minutes using Be/zey 1000 City V part as a solvent, and as a result, a coal liquid having a weight of 27 ml was obtained.

実施例2 拌して石炭液化を容易にする物質を得た。Example 2 A material was obtained that facilitated coal liquefaction by stirring.

この物質の性状は比重1.0151、粘度23mntポ
アズである。
The properties of this substance are a specific gravity of 1.0151 and a viscosity of 23 mnt poise.

この物質53重酸部と100メツシユ以下に粉砕した三
池炭(瀝青炭; 発熱置駒7300kCal/kgの燃
料炭で、その工業分析値は水分1.6チ、灰分8.3チ
揮発分40.09G、固定炭素50,1チ)100重量
部とを50℃に加熱しながら、150分間攪拌を行い茶
褐色のスラリー状物質を得た。
This substance is Miike charcoal (bituminous coal) that has been crushed to less than 100 mesh with 53 parts of heavy acid and a heating element of 7,300 kCal/kg, and its industrial analysis values are 1.6 g for moisture, 8.3 g for ash, and 40.09 g for volatile content. and 100 parts by weight of fixed carbon (50.1%) were heated to 50° C. and stirred for 150 minutes to obtain a brown slurry material.

このスラリー状物質を実施例1と同様な抽出装置にかけ
、溶剤としてベンゼン1000重量部を使用し280分
間抽出を行った結!21重量部の石炭液状物を得た。
This slurry material was applied to the same extraction device as in Example 1, and extracted for 280 minutes using 1000 parts by weight of benzene as a solvent. 21 parts by weight of coal liquid was obtained.

え、約!15℃に加熱しながら攪拌し石炭液化を容易に
する物質を得た。
Eh, about! A substance that facilitates coal liquefaction was obtained by stirring while heating to 15°C.

この物質53重量部と実施例1で使用したカナダ特許出
願人    大 部 貞 別 人  部  利  幸 大  部  貞  司 大  部  利  醍 大部真綿 代理人 弁理士  梶 原 克 彦
53 parts by weight of this substance and the Canadian patent applicant used in Example 1: Sadato Betsuto, Yukihiro Obe, Satoshi Obe, Masawa Daibe, agent, and Katsuhiko Kajihara, patent attorney.

Claims (1)

【特許請求の範囲】[Claims] 石炭とアルカリ性溶液とを攪拌してスラリー状物質を得
、このスラリー状物質を溶剤抽出することを特徴とする
石炭の液化方法
A coal liquefaction method characterized by stirring coal and an alkaline solution to obtain a slurry-like substance, and extracting this slurry-like substance with a solvent.
JP11023881A 1981-07-14 1981-07-14 Coal liquefaction Pending JPS5811590A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11023881A JPS5811590A (en) 1981-07-14 1981-07-14 Coal liquefaction

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11023881A JPS5811590A (en) 1981-07-14 1981-07-14 Coal liquefaction

Publications (1)

Publication Number Publication Date
JPS5811590A true JPS5811590A (en) 1983-01-22

Family

ID=14530602

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11023881A Pending JPS5811590A (en) 1981-07-14 1981-07-14 Coal liquefaction

Country Status (1)

Country Link
JP (1) JPS5811590A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03207793A (en) * 1989-09-28 1991-09-11 Natl Energ Council Method of making orgnic material in coal soluble

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03207793A (en) * 1989-09-28 1991-09-11 Natl Energ Council Method of making orgnic material in coal soluble

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