JPS6032894A - Manufacture of modified coal - Google Patents
Manufacture of modified coalInfo
- Publication number
- JPS6032894A JPS6032894A JP13944283A JP13944283A JPS6032894A JP S6032894 A JPS6032894 A JP S6032894A JP 13944283 A JP13944283 A JP 13944283A JP 13944283 A JP13944283 A JP 13944283A JP S6032894 A JPS6032894 A JP S6032894A
- Authority
- JP
- Japan
- Prior art keywords
- coal
- low
- temperature
- tar
- mixed 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.)
- Pending
Links
Landscapes
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の利用分野〕
本発明は、改質炭の製造方法に係り、特に低品位炭を防
湿性の優れた石炭に改質するのに好適な改質炭の製造方
法に関するものである。[Detailed Description of the Invention] [Field of Application of the Invention] The present invention relates to a method for producing modified coal, and particularly to a method for producing modified coal suitable for reforming low-rank coal into coal with excellent moisture resistance. It is about the method.
亜瀝青炭や褐炭等の低品位炭を防湿性の優れた石炭に改
質する技術としては、例えば、特公昭57−11596
5公報記載のものがある。As a technique for reforming low-grade coal such as sub-bituminous coal and lignite into coal with excellent moisture resistance, for example,
There is one described in 5 publications.
二の技術では、加熱昇温速度100℃/亀以上で、最終
加熱温度300℃〜500℃まで急速加熱し、次いで冷
却降温速度50℃/電以上で、250℃以下まで急速冷
却して、石炭の熱分解の際に石炭の表面ににじみ出て(
る液状タール物質を揮発させることなしに固化させて石
炭中の細孔を塞ぎ、石炭中の比表面積を低下させて石炭
の吸湿量を低下させるものである。In the second technology, the coal is rapidly heated to a final heating temperature of 300 to 500 degrees Celsius at a heating temperature increase rate of 100 degrees Celsius or more, and then rapidly cooled to 250 degrees Celsius or less at a cooling temperature decrease rate of 50 degrees Celsius or more. oozes out onto the surface of the coal during thermal decomposition (
This method solidifies the liquid tar substance without volatilizing it, plugs the pores in the coal, lowers the specific surface area of the coal, and reduces the amount of moisture absorbed by the coal.
しかしながら、石炭のこのような加熱処理により得られ
たタールは、沸点が200℃以下の低沸点物質が90%
と多い。このため、タールのガス化速度が速く石炭の表
面ににじみ出たタールをガス化しないで石炭表面に固化
させることは非常に困難であり、したがって、石炭の吸
湿量を低下、すなわち、防湿性の優れた石炭に改質する
のには問題がある。However, the tar obtained by such heat treatment of coal contains 90% of low-boiling substances with a boiling point of 200°C or less.
There are many. For this reason, the gasification rate of tar is fast, and it is very difficult to solidify the tar on the surface of the coal without gasifying it. There are problems with reforming coal into solid coal.
本発明の目的は、石炭の低温乾留処理により留出したタ
ールを低温乾留処理された石炭(以下、乾留炭と略)の
表面に確実にコーティングさせるニとで低品位炭を防湿
性の優れた石炭に改質できる改質炭の製造方法を提供す
ることにある。The purpose of the present invention is to reliably coat the surface of low-temperature carbonized coal (hereinafter abbreviated as carbonized coal) with tar distilled by low-temperature carbonization treatment of coal, and to convert low-grade coal into a material with excellent moisture resistance. The object of the present invention is to provide a method for producing reformed coal that can be reformed into coal.
本発明は、石炭を低温乾留処理した後、該処理により石
炭から留出したタール蒸気と水蒸気とでなる混合ガスを
乾留炭)ユ直接接触させることを特徴とするもので、タ
ール蒸気の選4R(1着性を利用して留出したタールを
乾留炭表面(二確実にコーティングさせようとするもの
である。The present invention is characterized in that after coal is subjected to low-temperature carbonization treatment, a mixed gas consisting of tar vapor and water vapor distilled from the coal by the treatment is brought into direct contact with the carbonization coal. (It is intended to ensure that distilled tar is coated on the surface of carbonized coal by utilizing its one-stick property.
本発明の一実施例を図面により説明する0図面で、石炭
、例えば、低品位炭1は粉砕i!L2で粉砕後、乾留装
置3に供給され、ここで、例えば、不活性ガス界囲気状
態、常圧下、温度250℃〜500℃の条件で低温乾留
処理される、この処理により低品位炭からは温度が乾留
温度であるタール蒸気と水蒸気とでなる混合ガス4が留
出する。一方、乾留炭5は、乾留装置3から冷却装置6
に供給され、ここで乾留温度から所定温度まで冷却され
る。乾留炭5の冷却処理が完了した時点で、冷却装置6
には、温度が乾留温度である混合ガス4が供給され、こ
の混合ガス4は乾留炭5に直接接触させられる。これに
より、乾留炭5には、混合ガス4の内のタール蒸気の選
択付着性を利用してその表面にタールが確実にコーティ
ングされコーティング炭7が得られる。その後、このコ
ーティング炭7は、自然発火等を考慮して冷却装置8で
常温付近まで冷却される。このようにして防湿性が優れ
た改質炭9が製造される。An embodiment of the present invention is explained using drawings. In drawing 0, coal, for example, low-grade coal 1 is crushed i! After pulverization in L2, it is supplied to the carbonization device 3, where it is subjected to low-temperature carbonization treatment under conditions of an inert gas atmosphere, normal pressure, and a temperature of 250°C to 500°C. Through this treatment, low-rank coal is A mixed gas 4 consisting of tar vapor and water vapor whose temperature is the carbonization temperature is distilled out. On the other hand, the carbonized coal 5 is transferred from the carbonized distillation device 3 to the cooling device 6.
It is then cooled from the carbonization temperature to a predetermined temperature. When the cooling process of the carbonized coal 5 is completed, the cooling device 6
A mixed gas 4 whose temperature is the carbonization temperature is supplied to the carbonization coal 5, and this mixed gas 4 is brought into direct contact with the carbonization coal 5. Thereby, tar is reliably coated on the surface of carbonized coal 5 by utilizing the selective adhesion of tar vapor in mixed gas 4, and coated coal 7 is obtained. Thereafter, this coated charcoal 7 is cooled to around room temperature in a cooling device 8 in consideration of spontaneous combustion and the like. In this way, modified charcoal 9 with excellent moisture resistance is produced.
ここで重要な因子は、乾留炭と混合ガスとを直接接触さ
せる際の乾留炭の温度である。乾留炭の温度が200℃
の場合は、タール蒸気は液化して乾留炭表面に付着し、
一方、水蒸気の乾留炭表面へのイ」着は細論のこと吸着
も生じない。乾留炭の温度が250℃以上の場合は、タ
ール蒸気は液化せず、したがって、タールが乾留炭表面
に付着することは期待できず、また、タールの組成から
吸着もほとんど生じない。乾留炭の温度が110℃の場
合は、タール蒸気は液化して乾留炭表面に更に付着する
と共に水蒸気は、その一部が乾留炭表面に吸着される。An important factor here is the temperature of the carbonized coal when the carbonized coal and the mixed gas are brought into direct contact. The temperature of carbonized coal is 200℃
In the case of , the tar vapor liquefies and adheres to the carbonized coal surface,
On the other hand, the adhesion of water vapor to the carbonized coal surface does not cause any adsorption. When the temperature of carbonized coal is 250° C. or higher, tar vapor does not liquefy, so tar cannot be expected to adhere to the carbonized coal surface, and adsorption hardly occurs due to the tar composition. When the temperature of the carbonized coal is 110° C., tar vapor is liquefied and further adheres to the surface of the carbonized coal, and a portion of water vapor is adsorbed on the surface of the carbonized coal.
しかし、この場合、吸着される水分は固有水分程度であ
り、実用上1問題とならない。乾留炭の温度が110℃
以下の場合は、タール蒸気は液化して乾留炭表面に更に
付着するが同時に吸着される水分が固有水分以上となる
ため、実用上、不都合となる。二の結果、乾留炭と混合
ガスとを直接接触させる際の乾留炭の温度を110℃〜
250℃と規定した。However, in this case, the amount of moisture adsorbed is about the same as the inherent moisture, and does not pose any practical problem. The temperature of carbonized coal is 110℃
In the following cases, the tar vapor is liquefied and further adheres to the carbonized coal surface, but at the same time the adsorbed moisture exceeds the inherent moisture, which is practically inconvenient. As a result of (2), the temperature of the carbonized coal when directly contacting the carbonized coal with the mixed gas is 110℃~
The temperature was defined as 250°C.
本発明は、以上説明したように石炭を低温乾留処理した
後、該処理1こより石炭から留出したタール蒸気と水蒸
気とでなる混合ガスを乾留炭に直接接触させることで、
石炭の低温乾留処理により留出したタールを乾留炭の表
面に確実にコーチイブできるので低品位炭を防湿性の優
れた石炭に改質できる効果がある。In the present invention, after the coal is subjected to low-temperature carbonization treatment as explained above, a mixed gas consisting of tar vapor and water vapor distilled from the coal from the treatment 1 is brought into direct contact with the carbonization coal.
Since the tar distilled by low-temperature carbonization treatment of coal can be reliably coached onto the surface of carbonized coal, it has the effect of reforming low-grade coal into coal with excellent moisture resistance.
図面は、本発明を実施した改質炭製造プロセスの一例を
示すプロセス・フロー図である。
l・・・・・低品位炭、3・・・・・・乾留装置、4・
・・・・・混合ガス、5・・・・・・乾留炭、6・・・
・・冷却装置代理人 弁理士 高 橋 明 夫The drawing is a process flow diagram showing an example of a modified coal production process in which the present invention is implemented. l...Low rank coal, 3...Carry distillation equipment, 4.
...mixed gas, 5...carbonized coal, 6...
...Representative of cooling system Patent attorney Akio Takahashi
Claims (1)
留出したタール蒸気と水蒸気とでなる混合ガスを低温乾
留処理された石炭に直接接触させることを特徴とする改
質炭の製造方法。 2、前記低温乾留処理された石炭の温度を110℃ない
し250℃とし前記混合ガスを直接接触させる特許請求
の範囲第1項記載の改質炭の製造方法。[Claims] 1. A modification characterized in that after coal is subjected to a low-temperature carbonization treatment, a mixed gas consisting of tar vapor and water vapor distilled from the coal by the treatment is brought into direct contact with the low-temperature carbonization-treated coal. How to make quality charcoal. 2. The method for producing reformed coal according to claim 1, wherein the temperature of the low-temperature carbonized coal is set at 110° C. to 250° C. and the mixed gas is brought into direct contact with the coal.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13944283A JPS6032894A (en) | 1983-08-01 | 1983-08-01 | Manufacture of modified coal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13944283A JPS6032894A (en) | 1983-08-01 | 1983-08-01 | Manufacture of modified coal |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6032894A true JPS6032894A (en) | 1985-02-20 |
Family
ID=15245291
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13944283A Pending JPS6032894A (en) | 1983-08-01 | 1983-08-01 | Manufacture of modified coal |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6032894A (en) |
-
1983
- 1983-08-01 JP JP13944283A patent/JPS6032894A/en active Pending
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