JPS5930895A - Modification of coal - Google Patents
Modification of coalInfo
- Publication number
- JPS5930895A JPS5930895A JP13992382A JP13992382A JPS5930895A JP S5930895 A JPS5930895 A JP S5930895A JP 13992382 A JP13992382 A JP 13992382A JP 13992382 A JP13992382 A JP 13992382A JP S5930895 A JPS5930895 A JP S5930895A
- Authority
- JP
- Japan
- Prior art keywords
- coal
- oil
- binder
- granulated
- aqueous 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
Links
Landscapes
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、石炭の改質方法に係り、特に乾留せずに脱灰
造粒が可能な低品位炭をカロリ・アップした石炭に改質
するのに好適な石炭の改質方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a coal reforming method, and in particular to a coal reforming method suitable for reforming low-grade coal that can be deashed and granulated without carbonization into coal with increased calories. This relates to a modification method.
褐炭、亜瀝宵炭に代表される低品位炭は、高品位炭であ
る瀝青炭に比べ含有灰分並びに水分が多いため、低カロ
リであるとともにハンドリング性。Low-grade coal, such as lignite and sub-bituminous coal, contains more ash and water than bituminous coal, which is high-grade coal, so it is low in calories and easy to handle.
燃焼効率が劣るという欠点がある。したがって、このよ
うな低品位炭を有効利用するためには、低品位炭に脱灰
並びに脱水操作を施こし含有灰分並びに水分を減少させ
てカロリ・アップした石炭に改質することが重要である
。The disadvantage is that combustion efficiency is poor. Therefore, in order to effectively utilize such low-rank coal, it is important to perform deashing and dewatering operations on the low-rank coal to reduce its ash and water content and reform it into coal with increased calories. .
しかし、現在は、高品位炭の利用が先行しており、可能
脱炭1.が豊富であるにもかかわらず低品位炭の改質技
術の開発については、はとんど手がつけられていない。However, currently, the use of high-grade coal is leading, and decarbonization is possible. Despite the abundance of low-rank coal, the development of reforming technology for low-rank coal has remained largely untouched.
本発明の目的は、含有灰分並びに水分を減少させて低品
位炭なカロリ・アップした石炭に改質できる石炭の改質
方法を提供することにある。An object of the present invention is to provide a method for reforming coal that can be reformed into low-rank coal with increased calories by reducing the ash content and water content.
本発明の特徴は、石炭を微粉砕する工程と、この微粉砕
された石炭に水を混合して水性スラリにする工程と、こ
の水性スラリに結合剤として油分を添加し脱灰造粒して
造粒炭を形成する工程と、二〇造粒炭を乾留して油分並
びに水分を抽出する工程と、この抽出された油分を結合
剤として回収する工程とよりなり、低品位炭の含有灰分
並びに水分を減少させてカロリ・アップした石炭に改質
することにある。The features of the present invention include the steps of pulverizing coal, mixing water with the pulverized coal to form an aqueous slurry, and adding oil as a binder to this aqueous slurry to decalcify and granulate it. It consists of a step of forming granulated coal, a step of dry distilling the granulated coal to extract oil and moisture, and a step of recovering the extracted oil as a binder. The purpose is to reduce the water content and reform the coal into a coal with increased calories.
本発明の一実施例を図面により説明する。An embodiment of the present invention will be described with reference to the drawings.
図面で、石炭、°例えば、低品位炭lは、微粉砕fi2
で微粉砕された後に、水が混合されて水性スラリとなり
水中造粒装置3に供給される。水中造粒装置3に供給さ
れた水性スラリには、結合剤として油分4が添加され脱
灰造粒される。これにより、灰分5が除去されると共に
造粒炭6が形成される。この造粒炭6は、乾留装置U7
で常圧下で、かつ、−OH,−COOH基等の含酸素結
合基が分解する200℃〜500℃の温度範囲で乾留さ
れる。これにより、水分8が抽出されて除去されると共
に、抽出された油分4が結合剤として回収される。この
結果、含有灰分並び憂こ水分が減少し、カロリ・アップ
した改質炭9が得られる、本実施例に従い含有灰分並び
に水分が19%。In the drawing, coal, for example low rank coal, is pulverized fi2
After being pulverized, water is mixed to form an aqueous slurry, which is supplied to the underwater granulation device 3. Oil 4 is added as a binder to the aqueous slurry supplied to the underwater granulator 3, and the slurry is deashed and granulated. As a result, ash 5 is removed and granulated coal 6 is formed. This granulated coal 6 is produced by carbonization device U7.
Carbonization is carried out under normal pressure at a temperature range of 200°C to 500°C at which oxygen-containing bonding groups such as -OH and -COOH groups are decomposed. As a result, water 8 is extracted and removed, and the extracted oil 4 is recovered as a binder. As a result, the ash content and moisture content are reduced, and a modified coal 9 with increased calories can be obtained.According to this example, the ash content and moisture content are 19%.
21%の低品位炭の改質を行ったところ次のような結果
を得た。When 21% low rank coal was reformed, the following results were obtained.
まず、上記低品位炭を一74μm80%の大きさまで微
粉砕し、これに水を混合して水性スラリとした後に、結
合剤として油分20%を添加して脱灰造粒した。この結
果、含有灰分並びに水分が7%、21%の造粒炭を得た
。その後、二〇造粒炭を常圧下で、かつ、400℃の温
度で乾留し、この結果、含有灰分並びに水分が11%、
9%に減少し、したがって、カロリ・アップした改質炭
を得た。なお、この場合、水性スラリに結合剤として油
分20チを添加するため、造粒炭を形成する油分く結合
剤として添加された油分)と低品位炭の油分より乾留時
に20%だけ油分を抽出2回収した。First, the above-mentioned low-rank coal was pulverized to a size of -74 μm and 80%, water was mixed with this to form an aqueous slurry, and 20% of oil was added as a binder to demineralize the slurry. As a result, granulated coal containing ash and water content of 7% and 21% was obtained. Thereafter, 20 granulated coals were carbonized under normal pressure and at a temperature of 400°C, and as a result, the ash and moisture content was 11%.
9%, thus obtaining modified coal with increased calories. In this case, 20% of the oil is added as a binder to the aqueous slurry, so 20% of the oil is extracted from the oil that forms the granulated coal (the oil added as a binder) and the oil of the low-grade coal during carbonization. 2 were recovered.
本実施例のような石炭の改質方法では、次のような効果
を得ることができる。The coal reforming method as in this embodiment can provide the following effects.
(1)石炭な脱灰造粒して造粒炭を形成した後に、この
造粒炭を乾留しているので、含有灰分並びに水分が減少
し、したがって、カロリ・アップした改質炭が得られる
。(1) After coal is deashed and granulated to form granulated coal, this granulated coal is carbonized, so the ash content and moisture content are reduced, resulting in modified coal with increased calories. .
(2)結合剤として水性スラリに添加される油分を、造
粒炭の乾留により抽出1回収した油分としているので、
油質を均一化できるとともに、乾留による油分の抽出1
回収を効率的に行うことができる。(2) Since the oil added to the aqueous slurry as a binder is the oil extracted and recovered by carbonization of granulated coal,
In addition to homogenizing oil quality, oil content can be extracted by carbonization1.
Collection can be performed efficiently.
(3)造粒炭の油分を乾留により全て抽出1回収しない
ので、改質炭の防湿性を良好に維持できるとともに、微
粉化するのを防止できる。(3) Since the oil content of the granulated coal is not entirely extracted and recovered by carbonization, the moisture-proof property of the modified coal can be maintained well and it can be prevented from being pulverized.
本発明は、以上説明したように、石炭を微粉砕する工程
と、二の微粉砕された石炭に水を混合して水性スラリに
する工程と、この水性スラリに結合剤として油分を添加
し脱灰造粒して造粒炭を形成する工程と、二〇造粒炭を
乾留して油分並びに水分を抽出する工程と、この抽出さ
れた油分を結合剤として回収する工程とよりなる方法と
することで、低品位炭の含有灰分並びに水分を減少でき
るので、低品位炭なカロリ・アップした石炭に改質でき
る効果がある。As explained above, the present invention comprises a step of pulverizing coal, a second step of mixing water into the pulverized coal to form an aqueous slurry, and a step of adding oil as a binder to this aqueous slurry to remove the coal. The method consists of a step of granulating ash to form granulated coal, a step of dry distilling the granulated coal to extract oil and moisture, and a step of recovering the extracted oil as a binder. This reduces the ash content and moisture content of low-rank coal, which has the effect of reforming it into low-rank coal with increased calories.
図面は、本発明を実施した石炭の改質プロセスの一例ヲ
示すプロセス脅70−図である。The drawing is a process diagram 70 illustrating an example of a coal reforming process embodying the present invention.
Claims (1)
を混合して水性スラリにする工程と、該水性スラリに結
合剤として油分を添加し脱灰造粒して造粒液を形成する
工程と、該造粒炭を乾留して油分並びに水分を抽出する
工程と、該抽出された油分を前記結合剤として回収する
工程とよりなることを特徴とする石炭の改質方法。 2、前記乾留を、常圧下で、かつ、200℃ないし50
0℃の温度範囲で行う特許請求の範囲第1項記載の石炭
の改質方法。 3 前記造粒炭から抽出され的起結合剤として回収され
る油分の量を、少なくとも前記水性スラリに添加される
油分の量とする特許請求の範囲第1項記載の石炭の改質
方法。[Claims] 1. A step of pulverizing coal, a step of mixing water with the pulverized coal to form an aqueous slurry, and adding oil as a binder to the aqueous slurry to demineralize it. a step of carbonizing the granulated coal to extract oil and moisture; and a step of recovering the extracted oil as the binder. Modification method. 2. The carbonization is carried out under normal pressure and at 200°C to 50°C.
The method for reforming coal according to claim 1, which is carried out in a temperature range of 0°C. 3. The coal reforming method according to claim 1, wherein the amount of oil extracted from the granulated coal and recovered as a target binder is at least the amount of oil added to the aqueous slurry.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13992382A JPS5930895A (en) | 1982-08-13 | 1982-08-13 | Modification of coal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13992382A JPS5930895A (en) | 1982-08-13 | 1982-08-13 | Modification of coal |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5930895A true JPS5930895A (en) | 1984-02-18 |
Family
ID=15256802
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13992382A Pending JPS5930895A (en) | 1982-08-13 | 1982-08-13 | Modification of coal |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5930895A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0610739A (en) * | 1993-04-26 | 1994-01-18 | Hitachi Ltd | Air-fuel ratio controller of engine |
JPH0610740A (en) * | 1993-04-26 | 1994-01-18 | Hitachi Ltd | Air-fuel ratio controller of engine |
CN110056903A (en) * | 2019-04-29 | 2019-07-26 | 上海外高桥第二发电有限责任公司 | Fire coal mixes the coal method for determination of amount and system of different types of coal in the case of burning |
-
1982
- 1982-08-13 JP JP13992382A patent/JPS5930895A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0610739A (en) * | 1993-04-26 | 1994-01-18 | Hitachi Ltd | Air-fuel ratio controller of engine |
JPH0610740A (en) * | 1993-04-26 | 1994-01-18 | Hitachi Ltd | Air-fuel ratio controller of engine |
CN110056903A (en) * | 2019-04-29 | 2019-07-26 | 上海外高桥第二发电有限责任公司 | Fire coal mixes the coal method for determination of amount and system of different types of coal in the case of burning |
CN110056903B (en) * | 2019-04-29 | 2021-03-12 | 上海外高桥第二发电有限责任公司 | Method and system for determining coal amount of different coal types under condition of coal-fired co-combustion |
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