JPS6366292A - Production of multipurpose coal-water slurry - Google Patents

Production of multipurpose coal-water slurry

Info

Publication number
JPS6366292A
JPS6366292A JP21128086A JP21128086A JPS6366292A JP S6366292 A JPS6366292 A JP S6366292A JP 21128086 A JP21128086 A JP 21128086A JP 21128086 A JP21128086 A JP 21128086A JP S6366292 A JPS6366292 A JP S6366292A
Authority
JP
Japan
Prior art keywords
coal
ash
water slurry
water
deashed
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
JP21128086A
Other languages
Japanese (ja)
Inventor
Noboru Sato
昇 佐藤
Masabumi Yagi
八木 正文
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.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki Heavy Industries Ltd
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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP21128086A priority Critical patent/JPS6366292A/en
Publication of JPS6366292A publication Critical patent/JPS6366292A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain a multipurpose coal.water slurry, ready in handling of pumping, shipping, storage, etc., by subjecting a raw material coal to gravity concentration and wet-grinding coarse grains having low ash content and on the other hand, by wet-grinding an adjusted coal containing fine grains having low ash content to provide slurry. CONSTITUTION:A raw material coal is subjected to gravity concentration to give a low ash coal, medium ash coal and high ash coal and said low ash coal is separated into coarse grains and fine grains. then, deashed coarse grains are subjected to wet grinding with water and a dispersing agent to afford a deashed coal.water slurry. On the other hand, fine-grained low ash coal, medium ash coal and high ash coal are blended to give an adjusted coal which is then subjected to wet grinding with water and a dispersing agent to provide an adjusted coal.water slurry.

Description

【発明の詳細な説明】 [産業上の利用分野コ 本発明は多目的石炭・水スラリーの製造方法に関する。[Detailed description of the invention] [Industrial application fields] The present invention relates to a method for producing a multi-purpose coal-water slurry.

[従来の技術] 石炭・水スラリーは、固体燃料である石炭を流体化する
ことにより、ポンプ輸送、積出、貯蔵などの取扱いが簡
便で、かつ発電用および産業用ボイラ、流動床ボイラ、
ガス化装置、内燃機関などにおける燃料もしくは炭素源
などとして利用することができる。
[Conventional technology] Coal/water slurry is made by converting coal, which is a solid fuel, into a fluid, making it easy to handle such as pumping, shipping, and storing, and it can be used in power generation and industrial boilers, fluidized bed boilers,
It can be used as a fuel or carbon source in gasifiers, internal combustion engines, etc.

石炭・水スラリーの石炭中灰分は無機鉱物などよりなり
、例えば、発電用ボイラにおいて燃焼させる場合、高温
度のもとて灰が部分的溶融などによりボイラ伝熱面に付
着して汚れを伴い、また、伝熱面を摩耗させたり、伝熱
効果を低下させてしまう。
The ash content in the coal of the coal/water slurry consists of inorganic minerals, etc., and when it is burned in a power generation boiler, for example, the ash will partially melt under high temperatures and adhere to the boiler heat transfer surface, causing dirt. Moreover, the heat transfer surface may be worn out, and the heat transfer effect may be reduced.

また、流動床ボイラなどにおいて燃焼させる場合には、
若干の灰分が含有されていても、反応温度が比較的低い
こともあり、かつ、大部分の灰が流動床から排出される
ので、残余の灰がボイラ伝熱面に付着して汚れを伴うこ
とか減少される。
In addition, when burning in a fluidized bed boiler etc.
Even if some ash is contained, the reaction temperature is relatively low, and most of the ash is discharged from the fluidized bed, so the remaining ash may adhere to the boiler heat transfer surface and cause fouling. It will be reduced.

この様に、石炭・水スラリーの利用形態によって石炭中
灰分による影響が相異している。
In this way, the influence of the ash content in coal differs depending on the usage form of the coal/water slurry.

そこで、発電用ボイラなどに利用する石炭・水スラリー
の製造において灰分含有量の多い原炭を使用する場合、
製造工程において脱灰処理を行い、脱灰率50%程度の
もとて、灰分含有量の少い石炭・水スラリーが製造され
る。
Therefore, when raw coal with a high ash content is used in the production of coal/water slurry for use in power generation boilers, etc.
Deashing treatment is performed during the manufacturing process, and a coal/water slurry with a low ash content is produced with a deashing rate of about 50%.

石炭の脱灰処理として、比較的粗い粒度で選炭し、低灰
分炭のみを石炭・水スラリー川原料として微粉砕し、石
炭・水スラリーを製造する方法も行われている。しかし
ながら、か\る方法によれば低灰分炭以外の石炭は石炭
・水スラリー用原料として使用しないため、石炭利用に
おける歩留りを著しく低下させてしまう。
As a deashing treatment for coal, a method is also used in which coal is washed to a relatively coarse particle size and only low ash coal is pulverized as raw material for coal/water slurry to produce coal/water slurry. However, according to this method, coal other than low ash coal is not used as a raw material for the coal-water slurry, so the yield in coal utilization is significantly reduced.

さらに、石炭の脱灰処理として、石炭を微粉砕して全量
を浮選法などにより浮遊物を低灰分炭として、沈下物を
硬(高灰分炭)とする方法もあるが、脱灰処理設備は単
位処理能力が低いこともあって設備が大型化し、処理費
が増大するのみならず、新たに多量の硬の処理を必要と
するなどの問題があった。
Furthermore, as a deashing treatment for coal, there is a method of finely pulverizing the coal and flotating the entire amount to convert the suspended matter into low ash coal and the settled material into hard (high ash coal), but deashing treatment equipment Because the unit processing capacity is low, the equipment becomes larger, which not only increases processing costs but also requires a large amount of hard material to be processed.

このような問題を解決するため、単一の製造方法をもち
いて最終製品である石炭・水スラリーの利用形態、選別
工程ならびに選別された各品位炭の利用のいずれも配慮
した多目的石炭・水スラリーの製造方法が提供されてい
る。(特願昭61−172421号参照) [発明が解決しようとする問題点コ しかしながら、上記従来の多目的石炭・水スラリーの製
造方法では、原料石炭の機械的分離による粗粒炭と細粒
炭とに分離するための工程ならびに分離装置を必要とす
るため、前記製造方法ならびに該製造方法を実施するた
めの装置が複雑となってしまうという問題があった。
In order to solve these problems, we have created a multi-purpose coal/water slurry using a single manufacturing method that takes into consideration the utilization form of the final product, the sorting process, and the use of each grade of coal. A manufacturing method is provided. (Refer to Japanese Patent Application No. 61-172421.) [Problems to be Solved by the Invention]However, in the above-mentioned conventional method for producing multi-purpose coal/water slurry, coarse coal and fine coal are separated by mechanical separation of raw coal. Since a step and a separation device are required to separate the two, there is a problem in that the manufacturing method and the device for carrying out the manufacturing method become complicated.

本発明はこのような従来の問題を解決するものであり、
原料石炭の粘土分などの遊離灰分を分離するための機械
的分離工程を省略した簡易な工程のもとで、最終製品で
ある石炭・水スラリーの多目的利用形態に応じることが
でき、選別工程のもとで選別された各品位炭を総合的に
利用することができる優れた多目的石炭・水スラリーの
製造方法を提供することを目的とするものである。
The present invention solves these conventional problems,
The simple process eliminates the mechanical separation process for separating free ash content such as clay from raw coal, and the final product, the coal/water slurry, can be used for multiple purposes, making it easy to use in the sorting process. The purpose of this invention is to provide an excellent method for producing a multipurpose coal/water slurry that can comprehensively utilize each grade of coal that has been sorted under the same conditions.

[問題点を解決するための手段] 本発明は上記目的を達成するために、石炭・水スラリー
を製造するにさいし、原料石炭を低灰分炭、中灰分炭、
高灰分炭とに比重選別し、該低灰分炭を粗粒と細粒とに
分離したのち、実質上脱灰炭である前記粗粒を水、分散
剤とともに微粉砕機へ供給し、湿式粉砕により脱灰石炭
・水スラリーを製造し、前記細粒低灰分炭と中灰分炭と
高灰分炭とを配合して調整炭となし、該調整炭を水、分
散剤とともに別の微粉砕機へ供給し、湿式粉砕により調
整石炭・水スラリーを製造するようにしたものである。
[Means for Solving the Problems] In order to achieve the above-mentioned object, the present invention provides a method for producing coal/water slurry by converting the raw material coal into low ash coal, medium ash coal,
After separating the low ash coal into coarse particles and fine particles, the coarse particles, which are essentially deashed coal, are fed to a pulverizer together with water and a dispersant, and wet-pulverized. A deashed coal/water slurry is produced, the fine low ash coal, medium ash coal, and high ash coal are blended to form adjusted coal, and the adjusted coal is sent to another pulverizer together with water and a dispersant. The system is designed to produce a prepared coal/water slurry through wet pulverization.

[作 用コ 本発明は上記のような構成により次のような作用を有す
る。すなわち、原料石炭は予め選炭工場で粘土分などの
遊離灰分が実質上除去されており、直接に選別機へ供給
して比重選別を行い、石炭の沈降速度などの物理的性状
などの差異を利用して比重、灰分ならびに発熱量などの
品位の異なる低灰分炭、中灰分炭、高灰分炭とに選別す
る。
[Function] The present invention has the following effects due to the above configuration. In other words, the raw material coal has been virtually removed from clay and other free ash in a coal preparation factory, and is then directly fed to a sorter for specific gravity sorting, taking advantage of the differences in physical properties such as the sedimentation rate of the coal. The coal is then sorted into low ash coal, medium ash coal, and high ash coal, which have different grades such as specific gravity, ash content, and calorific value.

低灰分炭は原料石炭と比較して灰分が少く脱灰せられて
いるため、そのまま湿式篩分は処理を行って粗粒と細粒
とに分離したのち、実質上脱灰炭である粗粒は脱灰石炭
・水スラリ一工程へ導かれ、水、分散剤とともに微粉砕
機へ供給し、湿式粉砕により低灰分の脱灰石炭・水スラ
リーを製造することができる。
Low ash coal has a lower ash content than coking coal and has been deashed, so the wet sieve is treated to separate coarse particles and fine particles, which are essentially deashed coal. is led to a deashed coal/water slurry step, which is then fed to a pulverizer together with water and a dispersant, and wet pulverization can produce a deashed coal/water slurry with a low ash content.

細粒は水を伴っているために濃縮および脱水処理を行っ
て細粒の水分を分離したのち、選別された中灰分炭、高
灰分炭とともに所要の発熱量が得られるように配合調整
を行って調整炭となし、調整炭を水、分散剤とともに前
記と別の微粉砕機へ供給し湿式粉砕により調整石炭・水
スラリーを製造することができる。
Since the fine particles are accompanied by water, the moisture in the fine particles is separated by concentration and dehydration treatment, and then the blend is adjusted to obtain the required calorific value with the selected medium-ash and high-ash coals. It is possible to produce a prepared coal/water slurry by wet pulverization by supplying the prepared coal together with water and a dispersant to a separate pulverizer.

したがって、本発明によれば簡単な工程よりなる単一の
製造方法をもちいて原料石炭の利用歩留りが高く、硬の
発生を実質上抑制させて、脱灰石炭・水スラリーと調整
石炭・水スラリーからなる多目的石炭・水スラリーを製
造することができ、多目的の石炭・水スラリーの利用形
態に対応することができる。
Therefore, according to the present invention, by using a single production method consisting of simple steps, the utilization yield of raw coal is high, the generation of hardness is substantially suppressed, and deashed coal/water slurry and adjusted coal/water slurry are produced. It is possible to produce a multi-purpose coal/water slurry consisting of the following, and it is possible to correspond to the usage form of multi-purpose coal/water slurry.

[実施例コ 以下、本発明の実施例について説明する。[Example code] Examples of the present invention will be described below.

第1図において、原料石炭バンカー10における原料石
炭12は予め選炭工場などにおいて粘土分などの遊離灰
分の適切な組成が得らねるように処理されており、原料
石炭12は選別機20に供給されて比重、灰分ならびに
発熱量が異なる低灰分炭26、中灰分炭24、高灰分炭
22とに比重選別される。選別機20としてはジグ選炭
機などがもちいられ、水の上下運動のもとて石炭粒の沈
降速度、すなわち比重の差を利用して分離される。そし
て石炭の再選曲線にてしめされるがごとき灰分と比重と
の間における浮沈特性のもとで、灰分15.2%の原料
石炭100部は灰分8.6%の低灰分率43部と、灰分
20.4%の中・高分炭57部とに分離される。
In FIG. 1, coking coal 12 in a coking coal bunker 10 has been treated in advance at a coal preparation factory or the like so as not to have an appropriate composition of free ash such as clay, and the coking coal 12 is supplied to a sorter 20. The coal is then sorted into low ash coal 26, medium ash coal 24, and high ash coal 22, which have different specific gravity, ash content, and calorific value. A jig coal separator or the like is used as the sorter 20, and the coal grains are separated by utilizing the settling speed of the coal particles, that is, the difference in specific gravity due to the vertical movement of water. And, under the flotation characteristics between ash content and specific gravity as shown in the reselection curve of coal, 100 parts of raw coal with an ash content of 15.2% has a low ash content of 43 parts with an ash content of 8.6%. It is separated into 57 parts of medium and high weight coal with an ash content of 20.4%.

ここに中・灰分炭28は前記の中灰分炭24と高灰分炭
22よりなる混合物である。
Here, the medium-ash coal 28 is a mixture of the medium-ash coal 24 and the high-ash coal 22 described above.

前記の水分15%の低灰分炭26は篩分は機30により
湿式篩分けされ、粗粒と細粒とに分離されて、灰分5,
2%の篩土産物33部は実質上、脱灰炭42となり、一
方、灰分18.2%の篩下産物10部は濃縮工程40な
らびに脱水工程45を経て水を分離したのち、細粒低灰
分炭36となる。脱灰炭42は、水、分散剤とともに微
粉砕機70へ供給し、湿式粉砕により石炭・水スラリー
となし分級機72により粗大粒子が分級されてポンプ7
4により輸送し、安定化剤を添加して混練機76にて混
合調整され灰分5.7%の粗大粒子を含まない脱灰石炭
・水スラリー78が製造され、発電用および産業用ボイ
ラなどにおける燃料として利用することができる。
The sieve content of the low ash coal 26 with a water content of 15% is wet sieved by a machine 30, separated into coarse particles and fine particles, and has an ash content of 5,
33 parts of the sieved souvenir with 2% ash content becomes deashed coal 42, while 10 parts of the sieved product with ash content of 18.2% undergoes a concentration step 40 and a dehydration step 45 to separate water, and then becomes fine grain low ash content. Charcoal becomes 36. The deashed coal 42 is supplied to a pulverizer 70 together with water and a dispersant, and is wet-pulverized into a coal/water slurry, with coarse particles being classified by a classifier 72 and sent to a pump 7.
A deashed coal/water slurry 78 containing no coarse particles with an ash content of 5.7% is produced by adding a stabilizer and mixing in a kneader 76. Can be used as fuel.

微粉砕機70としては粉砕媒体が充てんされているタン
プリングミルなどが用いられる。
As the fine grinder 70, a tampling mill or the like filled with grinding media is used.

脱灰炭42以外の細粒低灰分炭36および中・高灰分炭
28は廃棄せられることなく所要の発熱量が得られるよ
うに配合調整を行ったのち、若干の灰分な有している調
整石炭・水スラリーの製造のためにもちいられる。
Fine grain low ash coal 36 and medium/high ash coal 28 other than deashed coal 42 are mixed and adjusted to obtain the required calorific value without being discarded, and then adjusted to have a slight ash content. Used for producing coal/water slurry.

すなわち、細粒低灰分炭36および中・高灰分炭28は
それぞれ、灰分および発熱量などが相異しており、かか
る性状のもとて石炭・水スラリーを製造する場合には、
製品の品位が良好でなく燃料として利用するさいの便益
が低下してしまうため、上記の細粒低灰分炭36および
中・高灰分炭28を所要の重量比率をもって調整機50
により配合調整し、所要の水分、発熱量を有する調整炭
54を得るようにしている。
That is, the fine low ash coal 36 and the medium/high ash coal 28 have different ash content and calorific value, respectively, and when producing coal/water slurry with such properties,
Since the quality of the product is not good and the benefit of using it as fuel is reduced, the fine low ash coal 36 and the medium/high ash coal 28 are mixed into the adjusting machine 50 at the required weight ratio.
By adjusting the blending, adjusted charcoal 54 having the required moisture content and calorific value is obtained.

このさい、灰分18.2%の微粒低灰分炭10部、灰分
20.4%の中・高灰分炭57部をもって配合調整し、
灰分20.1%の調整炭67部が得られる。
At this time, the blend was adjusted using 10 parts of fine low ash coal with an ash content of 18.2% and 57 parts of medium/high ash content coal with an ash content of 20.4%.
67 parts of conditioned coal with an ash content of 20.1% are obtained.

引続き、調整炭54を水、分散剤とともに前記と別の微
粉砕機60へ供給し、湿式粉砕により石炭・水スラリー
となし、分級機62により粗大粒子が分葱されて、ポン
プ64により輸送し、安定化剤と添加して混練機66に
て混合調整され発熱量が調整された粗大粒子を含まない
調整石炭・水スラリー68が製造され、流動床ボイラな
はじめとする燃焼装置などにおける燃料として利用する
ことができる。
Subsequently, the conditioned coal 54 is supplied together with water and a dispersant to a separate pulverizer 60, wet-pulverized to form a coal/water slurry, coarse particles are separated by a classifier 62, and transported by a pump 64. A stabilizer is added and mixed in a kneader 66 to produce a coal/water slurry 68 that does not contain coarse particles and has an adjusted calorific value, and is used as a fuel in combustion devices such as fluidized bed boilers. can do.

このように、上記実施例によれば、原料石炭を簡単な工
程よりなる単一の製造方法をもちいて脱灰石炭・水スラ
リーと調整石炭・水スラリーからなる多目的石炭・水ス
ラリーを製造するようにしたものであり、多目的の石炭
・水スラリーの利用形態に対応することができるという
利点を有する。また、原料石炭を有効に利用し、その利
用歩留りが高く、廃棄すべき硬の発生が著しく減少され
るため、石炭利用における処理損失を実質上なくすこと
ができる。
As described above, according to the above embodiment, a multi-purpose coal/water slurry consisting of a deashed coal/water slurry and an adjusted coal/water slurry is produced using a single production method consisting of simple steps from raw coal. This method has the advantage of being compatible with the use of multi-purpose coal/water slurry. In addition, since the raw material coal is used effectively, its utilization yield is high, and the generation of hard material to be discarded is significantly reduced, processing losses in coal utilization can be substantially eliminated.

なお、本発明の実施態様は上記実施例に限定されるもの
ではなく、機械的分離、選別、脱水、配合調整などにつ
いては種々の態様が採用可能である。
It should be noted that the embodiments of the present invention are not limited to the above-mentioned embodiments, and various embodiments can be adopted for mechanical separation, sorting, dehydration, blending adjustment, etc.

[発明の効果] 本発明は上記実施例より明らかなように原料石炭を簡単
な工程よりなる単一の製造方法をもちいて脱灰石炭・水
スラリーと調整石炭・水スラリーからなる多目的石炭・
水スラリーを製造するようにしたものであり、多目的の
石炭・水スラリーの利用形態に対応することができると
いう利点を有する。そして、さらに原料石炭を有効に利
用し、その利用歩留りが高く廃棄されていた硬の発生が
抑制されるため、石炭利用における処理損失が実質上な
くなるという優れた効果を奏する。
[Effects of the Invention] As is clear from the above examples, the present invention uses a single production method consisting of simple steps to produce multi-purpose coal and raw material coal, which are composed of deashed coal and water slurry and adjusted coal and water slurry.
This method is designed to produce water slurry, and has the advantage of being compatible with the use of multi-purpose coal/water slurry. Further, raw coal is used effectively, and the utilization yield is high, and the generation of discarded hard particles is suppressed, so there is an excellent effect that processing losses in coal utilization are substantially eliminated.

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

第1図は本発明の一実施例に係る多目的石炭・水スラリ
ーの製造方法のフローシートである。 12・・・原料原炭   22・・・高灰分炭24・・
・中灰分炭   26・・・低灰分炭42・・・脱灰炭
    54・・・調整炭80.70・・・微粉砕機 68・・・調整石炭・水スラリー 78・・・脱灰石炭・水スラリー 出 願人 川崎重工業株式会社
FIG. 1 is a flow sheet of a method for producing a multi-purpose coal/water slurry according to an embodiment of the present invention. 12...Raw coal 22...High ash coal 24...
・Medium ash coal 26...Low ash coal 42...Deashed coal 54...Adjusted coal 80.70...Fine crusher 68...Adjusted coal/Water slurry 78...Deashed coal/ Water slurry applicant Kawasaki Heavy Industries, Ltd.

Claims (1)

【特許請求の範囲】[Claims] 石炭・水スラリーを製造するにさいし、原料石炭を低灰
分炭、中灰分炭、高灰分炭とに比重選別し、該低灰分炭
を粗粒と細粒とに分離したのち、実質上脱灰炭である前
記粗粒を水、分散剤とともに微粉砕機へ供給し、湿式粉
砕により脱灰石炭・水スラリーを製造し、前記細粒低灰
分炭と中灰分炭と高灰分炭とを配合して調整炭となし、
該調整炭を水、分散剤とともに別の微粉砕機へ供給し、
湿式粉砕により調整石炭・水スラリーを製造することを
特徴とする多目的石炭・水スラリーの製造方法。
When producing coal/water slurry, raw coal is sorted by specific gravity into low ash coal, medium ash coal, and high ash coal, and after the low ash coal is separated into coarse particles and fine particles, it is substantially deashed. The coarse particles of charcoal are supplied to a pulverizer together with water and a dispersant, and a deashed coal/water slurry is produced by wet pulverization, and the fine low ash coal, medium ash coal, and high ash coal are blended. Adjusted charcoal and pear,
The adjusted coal is fed to another pulverizer together with water and a dispersant,
A method for producing a multipurpose coal/water slurry characterized by producing a prepared coal/water slurry by wet pulverization.
JP21128086A 1986-09-08 1986-09-08 Production of multipurpose coal-water slurry Pending JPS6366292A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21128086A JPS6366292A (en) 1986-09-08 1986-09-08 Production of multipurpose coal-water slurry

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21128086A JPS6366292A (en) 1986-09-08 1986-09-08 Production of multipurpose coal-water slurry

Publications (1)

Publication Number Publication Date
JPS6366292A true JPS6366292A (en) 1988-03-24

Family

ID=16603311

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21128086A Pending JPS6366292A (en) 1986-09-08 1986-09-08 Production of multipurpose coal-water slurry

Country Status (1)

Country Link
JP (1) JPS6366292A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106244267A (en) * 2016-09-28 2016-12-21 煤科院节能技术有限公司 A kind of clean combustion type water-coal-slurry and preparation method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106244267A (en) * 2016-09-28 2016-12-21 煤科院节能技术有限公司 A kind of clean combustion type water-coal-slurry and preparation method thereof

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