JPS58127792A - Controlling spontaneous ignition of low-grade coal - Google Patents
Controlling spontaneous ignition of low-grade coalInfo
- Publication number
- JPS58127792A JPS58127792A JP1054082A JP1054082A JPS58127792A JP S58127792 A JPS58127792 A JP S58127792A JP 1054082 A JP1054082 A JP 1054082A JP 1054082 A JP1054082 A JP 1054082A JP S58127792 A JPS58127792 A JP S58127792A
- Authority
- JP
- Japan
- Prior art keywords
- coal
- water
- kerosene
- low
- oil
- 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、褐炭等の低品位炭を産炭地よシ消費地まで輸
送して使用する際の低品位炭の自然発火抑制法に関する
。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for suppressing spontaneous combustion of low-grade coal such as lignite when it is transported from a coal-producing area to a consuming area for use.
褐炭は、世界各国に莫大な埋蔵量を有し、大規模な露天
掘炭田が多いことから、今後その活用が期待されている
。しかし褐炭は水分含有量が極めて多く、また、非常に
反応性に冨むため、自然発火を起し易い性質を有する。There are huge reserves of lignite in various countries around the world, and there are many large-scale open-pit coal fields, so it is expected that it will be used in the future. However, lignite has an extremely high water content and is highly reactive, making it prone to spontaneous combustion.
したがって、褐炭を(1)
大量に輸入しその利用拡大をはかるためには脱水処理技
術および自然発火防止技術の開発が重要である0
従来、褐炭の自然発火抑制法として、石炭表面を界面活
性剤や油などで被覆する方法や貯炭表面を粘土などで被
覆する方法がよく知られている。Therefore, in order to import lignite in large quantities and expand its use, it is important to develop dehydration treatment technology and technology to prevent spontaneous ignition.0 Conventionally, as a method of suppressing spontaneous ignition of lignite, the surface of the coal was coated with surfactant. Well-known methods include coating the surface of stored coal with clay or the like.
また産炭地から消費地まで輸送する方法として、トラッ
ク輸送、鉄道輸送およびパイプライン輸送等がよく知ら
れている。しかし、従来の石炭の自然発火抑制法は、油
や界面活性剤等の高価なものを使用しているので高くつ
き、また粘土等を使用するので、石炭に粘土が混じり、
灰分が増加して褐炭の脱水を行いにくい等の欠点があっ
た。また輸送する方法についても、産炭地の立地条件や
輸送対象物のハンドリング等を考慮すると、輸送量が少
なく、また環境破壊の問題があった。しかも輸送前後の
処理にも問題があった。Also, truck transportation, rail transportation, pipeline transportation, etc. are well known as methods for transporting coal from coal producing areas to consumption areas. However, conventional methods for suppressing spontaneous combustion of coal are expensive because they use expensive materials such as oil and surfactants, and they also use clay, which causes clay to mix with the coal.
There were disadvantages such as increased ash content making it difficult to dehydrate lignite. Regarding the transportation method, considering the location conditions of the coal producing area and the handling of the objects to be transported, there was a problem that the amount of transportation was small and that it was environmentally destructive. Moreover, there were also problems with processing before and after transportation.
本発明は、この様な問題を解決して、強固で自然発火を
押えた無水の低品位炭を得ることを目的とし、低品位炭
を微粉砕した後、目的地捷で水・(2)
スラリー輸送し、次に該低品位炭の水・スラIJ−に灯
油とピッチの混合油を添加して湿式造粒で含油造粒炭全
造粒し、次に該含油造粒炭を水から分離した後、圧縮成
型し、次に該圧縮成型されだ含油造粒炭を乾燥すること
によってその目的を達成するものであシ、これにより、
褐炭等の低品位炭を水・スラリー輸送することで、輸送
量の増大が図れ、灯油とピッチの混合油を結合剤として
用いたことで、低品位炭の親油化処理なしで湿式造粒と
ともに脱灰でき、llf縮成型成型後燥することで、灯
油(低沸点油)の回収ができる強固でかつ自然発火を抑
制した無水の低品位炭を得ることができるものである。The purpose of the present invention is to solve such problems and obtain anhydrous low-grade coal that is strong and suppresses spontaneous combustion.After pulverizing the low-grade coal, water and (2) The slurry is transported, and then a mixed oil of kerosene and pitch is added to the water/slurry IJ- of the low-rank coal to completely granulate the oil-impregnated granulated coal by wet granulation, and then the oil-impregnated granulated coal is separated from water. After separation, the purpose is achieved by compression molding and then drying the compression molded oil-impregnated granulated coal.
By transporting low-grade coal such as brown coal with water and slurry, the amount of transport can be increased, and by using a mixed oil of kerosene and pitch as a binder, wet granulation is possible without the need for lipophilic treatment of low-grade coal. By performing ILF shrink molding and drying, it is possible to obtain strong anhydrous low-rank coal from which kerosene (low boiling point oil) can be recovered and which suppresses spontaneous combustion.
以下本発明の方法をその一実施例を示す図面に基づいて
詳細に説明する。図は本発明方法に係る各工程を示しだ
もので、大きく粉砕、輸送、造粒、圧縮成型および乾燥
の各工程を有している。産炭地で採掘された褐炭(1)
は、水分が30〜60%で25〜4Qgx塊炭であるが
、先ずこれに少量の水を加え、湿式粉砕機を用いて微粉
砕(2)する。これにより比(3)
較的濃度の高いペースト状の水・スラリーが得られる。The method of the present invention will be explained in detail below based on the drawings showing one embodiment thereof. The figure shows each process related to the method of the present invention, which mainly includes pulverization, transportation, granulation, compression molding, and drying. Lignite mined in coal-producing areas (1)
is a 25 to 4 Qgx lump coal with a moisture content of 30 to 60%; first, a small amount of water is added to it, and it is pulverized using a wet pulverizer (2). As a result, a paste-like water/slurry with a relatively high concentration (ratio (3)) is obtained.
次にこの微粉炭の水・スラリーを輸送ポンプを介してパ
イプラインへと導き、消費地捷たは積地まで輸送(3)
する。次に輸送された微粉炭の水・スラリーに、混合油
槽(4)から灯油(5)とビッヂ(6)の混合油を微粉
炭の結合剤として約20%の割合で添加混合し、この後
、湿式造粒機を用いて微粉褐炭を造粒(7)する。褐炭
(1)の灰分はもともと少ないが、該湿式造粒(7)の
工程で脱灰もされてし捷う。Next, this pulverized coal water/slurry is guided to the pipeline via a transport pump and transported to the consumption point or loading point (3)
do. Next, a mixed oil of kerosene (5) and bitch (6) from the mixed oil tank (4) is added to the transported pulverized coal water/slurry at a ratio of about 20% as a binder for the pulverized coal, and then mixed. , pulverized lignite is granulated using a wet granulator (7). Although the ash content of lignite (1) is originally low, it is deashed and crushed during the wet granulation (7) process.
次に脱水分離(8)の工程に送り、スクリーンを用いて
含油造粒炭を水(灰スラリー)から分離した後、例えば
ブランジャークイブのフリケラト・マシンに導いて圧縮
成型(9)する。この圧縮成型(9)で、含油造粒炭は
、さらに脱水されるとともに該含油造粒炭中にあるピッ
チ(約6%)を結合剤として強固な成型物となる。次に
この圧縮成型(9)により得られた成型物の水分と灯油
は、次の乾燥(油回収)工程01で除去し、このうち灯
油は回収して前記混合油槽(4)へと導き再使用する。Next, the coal is sent to a dehydration separation step (8), and after separating the oil-impregnated granulated coal from water (ash slurry) using a screen, it is led to, for example, a Blangerquibb frikerato machine and compression molded (9). In this compression molding (9), the oil-impregnated granulated coal is further dehydrated and becomes a strong molded product using pitch (about 6%) present in the oil-impregnated granulated coal as a binder. Next, the moisture and kerosene of the molded product obtained by compression molding (9) are removed in the next drying (oil recovery) step 01, of which kerosene is recovered and guided to the mixed oil tank (4) for reuse. use.
そしてこの乾燥工程θQにより得られた成型炭は、例え
ば家庭用燃料(4)
として用いる。The briquette obtained by this drying step θQ is used, for example, as household fuel (4).
以上本発明の方法によれば、次の様な効果がある。The method of the present invention has the following effects.
(1)低品位炭を微粉砕するので、比較的濃度の高いペ
ースト状の水・スラリーを得ることができ、これにより
褐炭の輸送量の増大を図ることができる。(1) Since low-grade coal is pulverized, a paste-like water/slurry with a relatively high concentration can be obtained, thereby increasing the amount of lignite transported.
(2)低品位炭の水・スラリーに、灯油とピッチの混合
油を添加して湿式造粒するので、低品位炭の親油化処理
なしで湿式造粒できるとともに脱灰でき、捷たこれによ
り含油造粒炭を得ることができる。(2) Wet granulation is performed by adding a mixed oil of kerosene and pitch to the water/slurry of low-rank coal, so wet granulation is possible without the need for lipophilic treatment of low-rank coal, and deashing is possible. Oil-impregnated granulated coal can be obtained.
(3)#式造粒で得られた含油造粒炭は、比較的大きい
(ls+m以上)ので、脱水分離がスクリーン等で容易
に行うことができる。(3) Since the oil-impregnated granulated coal obtained by # type granulation is relatively large (ls+m or more), it can be easily dehydrated and separated using a screen or the like.
(4)含油造粒炭を水から分離した後、圧縮成型するの
で、さらに脱水が進み、密度の高い強固な成型物を得る
ことができる。(4) Since oil-impregnated granulated coal is separated from water and then compression molded, dehydration progresses further and a strong molded product with high density can be obtained.
(5) 圧縮成型された含油造粒炭を乾燥させるので
、この乾燥工程で灯油(低沸点油)の回収(5)
が可能となシ、高価々油の消費を少なくすることができ
る。(5) Since the compression-molded oil-impregnated granulated coal is dried, kerosene (low boiling point oil) can be recovered (5) in this drying process, and the consumption of expensive oil can be reduced.
(6)乾燥して得られた成型炭は、無水であるとともに
ハンドリングが容易であり、またハンドリング時の発塵
がなくて済む。しかも自然発火を抑制した安定したもの
であるので、家庭用燃料として使用することができる。(6) Molded coal obtained by drying is anhydrous and easy to handle, and does not generate dust during handling. Moreover, it is stable and suppresses spontaneous combustion, so it can be used as a household fuel.
図面は本発明の一実施例を示し、本発明方法の各工程を
あられす工程図である。
(1)・・・褐炭、(2)・・・湿式粉砕、(3)・・
・水・スラリー輸送、(4)・・・混合油槽、(5)・
・・灯油、(6)・・・ピッチ、(7)・・・湿式造粒
、(8)・・・脱水分離、(9)・・・圧縮成型、(1
(>・・・乾燥
代理人 森 本 義 弘
(6)
手続補正書(睦)
昭和57年4 月ノ日
特許庁長官殿
2、発明の名称
低品位鹸の自然発火抑制法
3補正をする者
事件との関係 特許出願人
4称 (511)日立造船株式会社
4代 理 人
住 所 〒550大阪市西区立売堀1丁目6番174コ
アマノビル電話犬阪06 (532) 4025番(代
)氏名 (6808)弁理士森 本 義 弘5、
の日付(発送日)昭和 年 月
日
6、補正により増加する発明の数
7、補正の対象
明細書の発明の詳細な説明の梱
明細書の特許請求の範囲の欄
図面の全部
8、補正の内容 (1)
q)明#l書の発明の詳細な説明の楠
(1)第3同第3行目
「造粒し」とめるを「製造し」に訂正する。
(2)第5頁第10行目
「湿式造粒」とあるを「造粒」に訂正する。
e)明#I書の特許請求の範囲の榴
別紙の通り
(ル図面の全部
別紙の涌シ
(2)
2、特許請求の範囲
■、低品位炭を微粉砕した後、目的地まで水・ヌラリー
輸送し、次に該低品位炭の水・ヌフリーに灯油とピッチ
の混合油を添加して湿式造粒で含油造粒炭を’lit、
、次に該含油造粒炭を水から分離した後、圧縮成型し、
次に該圧縮成型された含油造粒炭を乾燥させることを特
徴とする低品位炭の自然発火抑制法。
(3)The drawings show one embodiment of the present invention and are process diagrams showing each step of the method of the present invention. (1)...Lignite, (2)...Wet grinding, (3)...
・Water/slurry transportation, (4)...Mixing oil tank, (5)・
... Kerosene, (6) ... Pitch, (7) ... Wet granulation, (8) ... Dehydration separation, (9) ... Compression molding, (1
(>...Drying Agent Yoshihiro Morimoto (6) Procedural Amendment (Mutsu) April 1981 Mr. Commissioner of the Japan Patent Office 2 Name of Invention Law for Suppressing Spontaneous Ignition of Low-grade Soap 3 Person who makes the amendment Relationship to the incident Patent applicant 4th name (511) 4th director of Hitachi Zosen Corporation Address 1-6-174 Tachiuribori Nishi-ku, Osaka 550 Koamano Building Telephone Inusaka 06 (532) 4025 (main) Name (6808) Patent attorney Yoshihiro Morimoto5,
Date (shipment date) Showa year month
Day 6, the number of inventions increased by the amendment 7, the detailed description of the invention in the specification subject to the amendment, the scope of claims in the packing specification, all 8 drawings, the content of the amendment (1) q) Clear #l In the Detailed Description of the Invention in Book Kusunoki (1), 3rd line, ``granulation'' is corrected to ``manufacturing''. (2) On page 5, line 10, "wet granulation" is corrected to "granulation." e) As per the appendix of the claims of Ming #I (all appendices to the drawings (2)) 2. Claims ■: After pulverizing low-grade coal, water and water are delivered to the destination. Next, a mixed oil of kerosene and pitch is added to the water/nufry of the low-rank coal, and oil-impregnated granulated coal is made by wet granulation.
, Next, after separating the oil-impregnated granulated coal from water, compression molding is performed,
A method for suppressing spontaneous combustion of low-rank coal, which comprises drying the compression-molded oil-impregnated granulated coal. (3)
Claims (1)
ー輸送し、次に該低品位炭の水・スラリーに灯油とピッ
チの混合油全添加して湿式造粒で含油造粒炭を造粒し、
次に該含油造粒炭を水から分離した後、圧縮成型し、次
に該圧縮成型された含油造粒炭を乾燥させることを特徴
とする低品位炭の自然発火抑制法。1. After pulverizing the low-rank coal, transport the water and slurry to the destination, then add all of the mixed oil of kerosene and pitch to the water and slurry of the low-rank coal, and wet granulate it to produce oil-impregnated granulated coal. Granulate,
A method for suppressing spontaneous ignition of low-grade coal, which is characterized in that the oil-impregnated granulated coal is then separated from water and then compression-molded, and then the compression-molded oil-impregnated granulated coal is dried.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1054082A JPS58127792A (en) | 1982-01-25 | 1982-01-25 | Controlling spontaneous ignition of low-grade coal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1054082A JPS58127792A (en) | 1982-01-25 | 1982-01-25 | Controlling spontaneous ignition of low-grade coal |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58127792A true JPS58127792A (en) | 1983-07-29 |
Family
ID=11753085
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1054082A Pending JPS58127792A (en) | 1982-01-25 | 1982-01-25 | Controlling spontaneous ignition of low-grade coal |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58127792A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61268793A (en) * | 1985-05-22 | 1986-11-28 | Electric Power Dev Co Ltd | Production of agglomerated coal |
US4726810A (en) * | 1984-05-23 | 1988-02-23 | Her Majesty The Queen In Right Of The Province Of Alberta As Represented By The Minister Of Energy And Natural Resources | Process for the selective agglomeration of sub-bituminous coal fines |
JP2013525536A (en) * | 2010-04-21 | 2013-06-20 | 韓国エネルギー技術研究院 | Method for producing solid fuel in which binder material and carbon source are mixed, and solid fuel produced by the method |
WO2024150818A1 (en) * | 2023-01-12 | 2024-07-18 | 日本製鉄株式会社 | Method for suppressing spontaneous heat generation in solid carbon resources, and solid carbon resource storing method using same |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54146801A (en) * | 1978-05-10 | 1979-11-16 | Mitsubishi Chem Ind Ltd | Removal of water from brown coal |
JPS5543199A (en) * | 1978-09-21 | 1980-03-26 | Atlantic Richfield Co | Reducing sulfur content in coal |
JPS562394A (en) * | 1979-06-21 | 1981-01-12 | Kawasaki Steel Corp | Treatment of brown coal |
-
1982
- 1982-01-25 JP JP1054082A patent/JPS58127792A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54146801A (en) * | 1978-05-10 | 1979-11-16 | Mitsubishi Chem Ind Ltd | Removal of water from brown coal |
JPS5543199A (en) * | 1978-09-21 | 1980-03-26 | Atlantic Richfield Co | Reducing sulfur content in coal |
JPS562394A (en) * | 1979-06-21 | 1981-01-12 | Kawasaki Steel Corp | Treatment of brown coal |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4726810A (en) * | 1984-05-23 | 1988-02-23 | Her Majesty The Queen In Right Of The Province Of Alberta As Represented By The Minister Of Energy And Natural Resources | Process for the selective agglomeration of sub-bituminous coal fines |
JPS61268793A (en) * | 1985-05-22 | 1986-11-28 | Electric Power Dev Co Ltd | Production of agglomerated coal |
JP2013525536A (en) * | 2010-04-21 | 2013-06-20 | 韓国エネルギー技術研究院 | Method for producing solid fuel in which binder material and carbon source are mixed, and solid fuel produced by the method |
WO2024150818A1 (en) * | 2023-01-12 | 2024-07-18 | 日本製鉄株式会社 | Method for suppressing spontaneous heat generation in solid carbon resources, and solid carbon resource storing method using same |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AU2016401396B2 (en) | Method for sorting and utilizing coal and rock for coal and rock combined mining face | |
US3168350A (en) | Transportation of coal by pipeline | |
DE2642201A1 (en) | FUEL MIXTURE AND PROCESS FOR ITS MANUFACTURING | |
JPS61103992A (en) | Deashing recovery of coal | |
JPS58127792A (en) | Controlling spontaneous ignition of low-grade coal | |
CN1034227C (en) | Production method of high-concentration coal-water slurry | |
US4254560A (en) | Method of drying brown coal | |
CN110128042A (en) | A kind of technique preparing active addition of cement, concrete admixture with Tungsten tailing | |
JPH0315957B2 (en) | ||
CN100551862C (en) | Utilize alkali works's alkaline residue, phosphorite tailings sand and HEC solidifying agent to make the method for engineering soil | |
AU2008341004B2 (en) | Method for producing a lignite product | |
JPH0633378B2 (en) | Waste slurry recycling method | |
JPS58127793A (en) | Method for coating low-grade coal | |
JPS62590A (en) | Dispersant for water slurry of high-concentration finely divided carbonaceous powder | |
US20210394195A1 (en) | Clean coal production system and method | |
JPS58145789A (en) | Preventing spontaneous ignition of low grade coal | |
JPH06504515A (en) | Method for activating garbage, settled sludge, and special garbage combustion ash | |
JPS6013890A (en) | Production of coal-water slurry having high concentration and lowered viscosity | |
JPS61271395A (en) | Composite fuel | |
SU1022917A1 (en) | Method of preparing coal slurry for transportation through pipelines | |
JPH0768529B2 (en) | Method for producing high-concentration coal / water slurry | |
JPS5980322A (en) | Granulation of coal | |
JPS5674191A (en) | Granulation of coal for coal slurry transportation | |
JPS58136697A (en) | Granulation of coal | |
JPS5740592A (en) | Utilization of coal including liquefaction process |