JPH0315677B2 - - Google Patents
Info
- Publication number
- JPH0315677B2 JPH0315677B2 JP11524683A JP11524683A JPH0315677B2 JP H0315677 B2 JPH0315677 B2 JP H0315677B2 JP 11524683 A JP11524683 A JP 11524683A JP 11524683 A JP11524683 A JP 11524683A JP H0315677 B2 JPH0315677 B2 JP H0315677B2
- Authority
- JP
- Japan
- Prior art keywords
- coal
- slurry
- concentration
- water
- viscosity
- 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.)
- Expired
Links
- 239000003245 coal Substances 0.000 claims description 47
- 239000002002 slurry Substances 0.000 claims description 43
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 37
- 238000004519 manufacturing process Methods 0.000 claims description 10
- 238000010298 pulverizing process Methods 0.000 claims description 6
- 239000002245 particle Substances 0.000 description 14
- 238000009826 distribution Methods 0.000 description 10
- 239000000843 powder Substances 0.000 description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 239000003250 coal slurry Substances 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 6
- 238000000227 grinding Methods 0.000 description 5
- 238000003860 storage Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000000295 fuel oil Substances 0.000 description 3
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000001186 cumulative effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
Landscapes
- Liquid Carbonaceous Fuels (AREA)
Description
本発明は低粘度化石炭−水スラリの製造方法に
係り、特に石炭濃度の低下を要することなく低粘
度の石炭−水スラリを製造する方法に関するもの
である。
固体燃料である石炭は、石油等の液体燃料に比
べ安価で、埋蔵量も多くかつ出炭地も世界各国に
もわたつていることから、その供給は安定してい
るが、反面、輸送や貯蔵が煩雑になるという欠点
を有している。そこで、重油−石炭スラリ
(COM)、メタノール−石炭スラリ(CMM)お
よび高濃度の石炭−水スラリ(CWM)等に見ら
れるように、石炭を液状媒体でスラリ化すること
により流体化させるための技術開発が積極的に進
められている。上記のスラリのうち、COMは重
油を流動化媒体として用いた石炭のスラリである
が、輸送抵抗の面から重油の割合を50%(重量、
以下同じ)以下に低下させることは困難であり、
そのため多量の重油が必要になるという欠点を有
している。また、CMMはメタノールを流動化媒
体として用いた石炭スラリであるが、メタノール
自体が現状の製造技術の下では高価になるという
欠点があり、実用化に到つていない。一方、
CWMは水を流動化媒体とする石炭スラリである
ため、水の供給にともなう熱的な損失がボイラ等
において、問題とされるが、65%以上の石炭を含
む高濃度の水スラリとすればこれらの問題も低減
するとされている。すなわち、従来、石炭を燃料
として使用するボイラの場合には、該使用原炭中
に水が予め10〜30%程度含まれていることおよび
排ガス中の亜硫酸ガスを除去する脱硫塔では湿式
法が一般的であり、ここでも多量の水が蒸発し熱
損失を生じていること等を考慮すると、石炭−水
スラリ中の水分を35%程度以下に抑えることがで
きれば、水の添加による熱的な損失はそれほど問
題にならないといえる。そして、CWMとするこ
とにより、従来貯炭時等に問題であつた微粉炭の
自然発火や火災等の危険がなくなる上、タンク貯
蔵やパイプ輸送が可能となるため貯蔵面積を小さ
くでき、かつ開放部がなくなるので安全で無公害
なシステムを組むことができる。CWMはこのよ
うな種々の利点を有するが、反面、石炭の濃度が
増加するに従がつてスラリの粘度が増加し、パイ
プ輸送等では圧損が増加するという大きな問題が
ある。従つてこのような粘度上昇の問題がなく、
かつ熱的損失の影響がない石炭濃度65%以上、好
ましくは70%以上の高濃度CWMを作るために
は、石炭の粒子と粒子の間にさらに小さな石炭粒
子が入り、これにより石炭濃度を上げるような粒
径分布、すなわちフラーの粒径分布で示されるよ
うな幅の広い粒径分布を持ち、しかも微粉を多量
に含むスラリとすることが望まれていた。このよ
うなスラリを得るためには、現状では数種の粉砕
機を組み合せる等の複雑なシステムを組む必要が
あるが、この場合においても、幅の広い粒径分布
を連続した分布で得るためにはさらに複雑な制御
を必要とする。
本発明の目的は、上記した従来技術の欠点をな
くし、簡単な操作で石炭濃度を高く維持しながら
スラリの粘度を低下させることができる低粘度化
石炭−水スラリの製造法を提供することにある。
本発明者らは、石炭を湿式粉砕するに当り、高
濃度の石炭含有下でこれを行う際には摩砕作用の
割合が増大し、これにともない微粉生成率の向上
と粒径分布幅の拡大が達成されることを実験によ
り見出した。
本発明は上記知見に基づきなされたもので、石
炭を湿式粉砕することにより石炭−水スラリを製
造する方法において、上記石炭の粉砕を先づ高濃
度の石炭含有下で行い、次いで得られた高濃度の
石炭−水スラリに水を添加し、輸送および貯蔵等
の取扱に適した低粘度の製品石炭−水スラリを得
るものである。
本発明において、石炭の粉砕を高濃度の石炭含
有下で行う理由は以下の通りである。すなわち、
高濃度かつ低粘度の石炭−水スラリを得るために
は、粉砕した石炭の粒径分布の幅を広くするとと
もに微粉の割合を多くすることが有効であるとさ
れている。ところで、常法に従いミル内で石炭を
粉砕する場合、その破砕の機構は衝撃破砕と摩砕
とに大別されるが、その際、広い粒径分布幅でし
かも微粉の割合を増すためには摩砕の割合を増加
させることが望ましい。そして、この摩砕割合を
増加させるためには、第1図に示す実験結果から
も明らかなように、石炭を75〜80%程度の高濃度
に保つて粉砕することが最も効果的である。この
理由として以下が考えられる。すなわち、湿式ボ
ールミルでは、ケーシングを回転するに従がいミ
ル内のボールは持ち上げられたのち落下するとい
う運動をくり返すこととなる。その際、第1図に
示す衝撃破砕の領域では、水分が非常に多いか、
あるいは少ない状態にあるためミル内におけるス
ラリの粘度は低く、そのため第2図Aに示すよう
にミル(ケーシング)1の回転につれて持ち上げ
られたボール2は勢いよく落下し、この時の衝撃
で石炭が粉砕されるので、衝撃を中心とした破砕
が行われることとなる。そのため、スラリ中の石
炭の粒径分布幅は狭い上、微粉の割合も少なくな
るので、濃度の高い石炭−水スラリを製造するこ
とはできなくなる。一方、石炭の濃度を75〜80%
程度に高濃度化して粉砕するとミル内の粘度は高
くなるので、第2図Bに示すように、持ち上げら
れたボール2がミル1の内壁を滑り落ちるような
運動を起して摩砕を中心とした粉砕が行われるこ
ととなり、これにより微粉の割合が多くかつ粒径
分布幅の広い微粉炭が得られることとなる。
さらに、上記により得られた高濃度の石炭−水
スラリに水を添加することにより、水添加後に湿
式粉砕して同一濃度にしたものよりも大幅な低粘
度化が達成されることがわかつた。この水添加は
一般に、従来のこの種スラリの濃度水準である70
%程度まで行えば十分である。
以下、実施例により本発明をさらに詳しく説明
する。なお、各実施例中の%は、特に記載のない
限り重量%を意味する。
実施例 1
第1表に示す条件下で石炭の粉砕とと粉砕スラ
リに対する水添加を行い、ミル出口での石炭濃度
がそれぞれ70%の本発明のスラリ(実施例1)と
従来法に基づくスラリ(比較例1)を得た。得ら
れたスラリの石炭濃度はともに70%ではあるが、
実施例1のスラリ粘度は80cpであり、比較例1
の1500opに比し大幅に粘度低下することが明ら
かである。
The present invention relates to a method for producing a low-viscosity coal-water slurry, and particularly to a method for producing a low-viscosity coal-water slurry without reducing the coal concentration. Coal, which is a solid fuel, is cheaper than liquid fuels such as oil, has large reserves, and is produced in various countries around the world, so its supply is stable. It has the disadvantage that it is complicated. Therefore, as seen in heavy oil-coal slurry (COM), methanol-coal slurry (CMM), and highly concentrated coal-water slurry (CWM), it is necessary to slurry coal with a liquid medium to make it fluid. Technology development is being actively promoted. Among the above slurries, COM is a coal slurry that uses heavy oil as a fluidizing medium, but from the viewpoint of transportation resistance, the proportion of heavy oil is 50% (weight,
(the same applies below), it is difficult to reduce the
Therefore, it has the disadvantage of requiring a large amount of heavy oil. Furthermore, CMM is a coal slurry that uses methanol as a fluidizing medium, but methanol itself has the disadvantage of being expensive under current production technology, and has not been put into practical use. on the other hand,
Since CWM is a coal slurry that uses water as a fluidizing medium, thermal loss due to water supply is a problem in boilers, etc., but if it is a highly concentrated water slurry containing more than 65% coal, It is said that these problems will also be reduced. In other words, in the case of conventional boilers that use coal as fuel, the raw coal used already contains about 10 to 30% water, and the desulfurization tower that removes sulfur dioxide gas from exhaust gas requires a wet method. This is common, and considering that a large amount of water evaporates and causes heat loss, if the water content in the coal-water slurry can be suppressed to about 35% or less, the thermal It can be said that losses are not that much of an issue. By using CWM, there is no risk of spontaneous ignition of pulverized coal or fire, which was a problem during conventional coal storage, and the storage area can be reduced because it can be stored in tanks or transported through pipes. Since there is no pollution, it is possible to build a safe and non-polluting system. Although CWM has various advantages as described above, on the other hand, as the concentration of coal increases, the viscosity of the slurry increases, resulting in an increase in pressure drop during pipe transportation, which is a major problem. Therefore, there is no problem of viscosity increase,
In order to create a high-concentration CWM with a coal concentration of 65% or more, preferably 70% or more, without the influence of thermal loss, even smaller coal particles are inserted between the coal particles, thereby increasing the coal concentration. It has been desired to produce a slurry having such a wide particle size distribution as shown in Fuller's particle size distribution, and containing a large amount of fine powder. In order to obtain such a slurry, it is currently necessary to set up a complex system such as combining several types of crushers, but even in this case, it is necessary to create a continuous particle size distribution with a wide width. requires more complex control. An object of the present invention is to provide a method for producing a low-viscosity coal-water slurry, which eliminates the drawbacks of the prior art described above and can reduce the viscosity of the slurry while maintaining a high coal concentration with simple operations. be. The present inventors have discovered that when wet pulverizing coal is carried out in the presence of a high concentration of coal, the rate of attrition increases, and as a result, the rate of fine powder production increases and the width of the particle size distribution increases. It has been experimentally found that expansion can be achieved. The present invention has been made based on the above findings, and includes a method for producing a coal-water slurry by wet-pulverizing coal. Water is added to a concentrated coal-water slurry to obtain a product coal-water slurry with a low viscosity suitable for handling such as transportation and storage. In the present invention, the reason why coal is pulverized with a high concentration of coal is as follows. That is,
In order to obtain a coal-water slurry with high concentration and low viscosity, it is said to be effective to widen the particle size distribution of pulverized coal and to increase the proportion of fine powder. By the way, when coal is crushed in a mill according to the conventional method, the crushing mechanism is broadly divided into impact crushing and attrition, but in order to achieve a wide particle size distribution and increase the proportion of fine powder, It is desirable to increase the rate of attrition. In order to increase this grinding ratio, as is clear from the experimental results shown in FIG. 1, it is most effective to keep the coal at a high concentration of about 75 to 80% when grinding. Possible reasons for this are as follows. That is, in a wet ball mill, when the casing is rotated, the balls in the follower mill are lifted up and then dropped, which is repeated. At that time, in the area of impact fracture shown in Figure 1, there may be a large amount of moisture, or
Alternatively, the viscosity of the slurry in the mill is low because the slurry is in a low state, so as shown in Figure 2A, the ball 2 that was lifted up as the mill (casing) 1 rotates drops with force, and the impact at this time causes the coal to explode. Since it is crushed, the crushing is mainly caused by impact. Therefore, the particle size distribution width of the coal in the slurry is narrow and the proportion of fine powder is also reduced, making it impossible to produce a highly concentrated coal-water slurry. Meanwhile, increase the concentration of coal to 75-80%
As the viscosity inside the mill becomes high when the concentration is increased to a certain degree, the viscosity inside the mill becomes high, and as shown in Fig. 2B, the lifted ball 2 causes a movement that slides down the inner wall of the mill 1, causing the grinding to become the center of the grinding. As a result, pulverized coal with a large proportion of fine powder and a wide particle size distribution can be obtained. Furthermore, it has been found that by adding water to the highly concentrated coal-water slurry obtained above, a significantly lower viscosity can be achieved than when the slurry is wet-milled to the same concentration after adding water. This water addition is generally at a concentration level of 70
It is sufficient to do this up to about %. Hereinafter, the present invention will be explained in more detail with reference to Examples. Note that % in each example means % by weight unless otherwise specified. Example 1 Coal was crushed and water was added to the crushed slurry under the conditions shown in Table 1, and the slurry of the present invention (Example 1) and the slurry based on the conventional method, each having a coal concentration of 70% at the mill outlet, were prepared. (Comparative Example 1) was obtained. Although the coal concentration of the obtained slurry was 70% in both cases,
The slurry viscosity of Example 1 was 80 cp, and that of Comparative Example 1
It is clear that the viscosity is significantly lower than that of 1500op.
【表】
なお、実施例1と比較例1で得られた各スラリ
に関して石炭粒径の累積率を求めたところ第3図
の結果となつた。図中、Aは実施例1、Bは比較
例の場合をそれぞれ示す。この図から実施例1で
得られたスラリ中の石炭粒子は比較例1のものよ
り幅の広い粒径分布を示すことがわかつた。この
ことは、実施例1の方がミル内での石炭濃度が高
く、より摩砕に適した条件下で粉砕されたゝめ、
と考えられる。
実施例 2
粉砕時の石炭濃度を60〜75%の範囲内で種々に
変化させながら石炭の粉砕を行うとともに、粉砕
後水を添加してスラリ濃度を変化させた際のスラ
リ粘度の変化を求めたところ、前者については第
4図に示す実線上のa1,b1,c1,d1およびe1、後
者については破線上のa1〜a5、b1〜b3およびc1〜
c3のようになつた。
第4図に示す結果から、石炭濃度70%以上、好
ましくは73%以上で粉砕したスラリに水を添加し
て70%程度の濃度にしたものが粘度が大幅に低下
し、輸送や貯蔵等の取扱に適したものとなること
がわかつた。
以上、本発明によれば、石炭の粉砕を先づ高濃
度で石炭を含有する水の存在下で行い、次いで得
られた高濃度の石炭−水スラリに水を添加するこ
とにより、微粉が多く、粒度分布幅の広い微粉炭
スラリ、すなわち輸送および貯蔵等の取扱に適し
た低粘度の石炭−水スラリを簡単な操作で得るこ
とができる。[Table] When the cumulative ratio of coal particle diameter was determined for each slurry obtained in Example 1 and Comparative Example 1, the results shown in FIG. 3 were obtained. In the figure, A indicates Example 1, and B indicates Comparative Example. From this figure, it was found that the coal particles in the slurry obtained in Example 1 had a wider particle size distribution than those in Comparative Example 1. This is because the coal concentration in the mill was higher in Example 1, and it was ground under conditions more suitable for grinding.
it is conceivable that. Example 2 Coal was pulverized while varying the coal concentration during pulverization within the range of 60 to 75%, and changes in slurry viscosity were determined when water was added after pulverization to change the slurry concentration. As for the former, a 1 , b 1 , c 1 , d 1 and e 1 on the solid line shown in FIG. 4, and for the latter on the broken line a 1 to a 5 , b 1 to b 3 and c 1 to
It became like c 3 . From the results shown in Figure 4, the viscosity of slurry pulverized with a coal concentration of 70% or higher, preferably 73% or higher, and when water is added to the slurry to a concentration of around 70%, the viscosity decreases significantly, making it difficult to transport, store, etc. It was found that it is suitable for handling. As described above, according to the present invention, coal is first pulverized in the presence of water containing coal at a high concentration, and then water is added to the obtained high concentration coal-water slurry, thereby producing a large amount of fine powder. A pulverized coal slurry with a wide particle size distribution, that is, a low viscosity coal-water slurry suitable for handling such as transportation and storage, can be obtained by a simple operation.
第1図は、ミル内の石炭濃度が石炭の粉砕機構
に与える影響を説明する図、第2図Aは、衝撃破
砕時におけるボールの挙動を説明するミルの断面
図、同図Bは、摩砕時におけるボールの挙動を説
明するミルの断面図、第3図は、本発明の実施例
の効果を比較例とともに説明する図、第4図は、
本発明によつて得られる種々の石炭−水スラリの
濃度と粘度との関係を説明する図である。
1……ミル、2……ボール。
Figure 1 is a diagram explaining the influence of the coal concentration in the mill on the coal crushing mechanism, Figure 2A is a cross-sectional view of the mill explaining the behavior of the balls during impact crushing, and Figure B is a diagram explaining the influence of the coal concentration in the mill on the coal crushing mechanism. FIG. 3 is a cross-sectional view of the mill explaining the behavior of the balls during crushing, and FIG. 4 is a diagram explaining the effects of the embodiment of the present invention together with a comparative example.
It is a figure explaining the relationship between the density|concentration and viscosity of various coal-water slurries obtained by this invention. 1...mil, 2...ball.
Claims (1)
リを製造する方法において、上記石炭の粉砕を先
づ高濃度の石炭含有下で行い、次いで得られた高
濃度の石炭−水スラリに水を添加することを特徴
とする低粘度化石炭−水スラリの製造方法。 2 特許請求の範囲第1項において、石炭粉砕時
の石炭濃度が70〜80%(重量)であることを特徴
とする低粘度化石炭−水スラリの製造方法。 3 特許請求の範囲第1項において、水添加によ
つて石炭−水スラリの石炭濃度を65〜70%(重
量)にすることを特徴とする低粘度化石炭−水ス
ラリの製造方法。[Claims] 1. In a method for producing a coal-water slurry by wet-pulverizing coal, the above-mentioned coal is first pulverized in a high-concentration coal-containing state, and then the resulting high-concentration coal-water slurry is A method for producing a low viscosity coal-water slurry, which comprises adding water to the slurry. 2. The method for producing a low-viscosity coal-water slurry according to claim 1, characterized in that the coal concentration during coal pulverization is 70 to 80% (by weight). 3. The method for producing a low-viscosity coal-water slurry according to claim 1, characterized in that the coal concentration of the coal-water slurry is made 65 to 70% (by weight) by adding water.
Priority Applications (7)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11524683A JPS608393A (en) | 1983-06-28 | 1983-06-28 | Preparation of low-viscosity coal-water slurry |
| US06/625,245 US4613084A (en) | 1983-06-28 | 1984-06-27 | Process for producing a coal-water slurry |
| DE8484304372T DE3462268D1 (en) | 1983-06-28 | 1984-06-27 | Process for producing a coal-water slurry |
| EP84304372A EP0130788B1 (en) | 1983-06-28 | 1984-06-27 | Process for producing a coal-water slurry |
| ZA844946A ZA844946B (en) | 1983-06-28 | 1984-06-28 | Process for producing a coal-water slurry |
| AU30010/84A AU563646B2 (en) | 1983-06-28 | 1984-06-28 | Coal-water slurry |
| CA000457764A CA1257771A (en) | 1983-06-28 | 1984-06-28 | Process for producing a coal-water slurry |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11524683A JPS608393A (en) | 1983-06-28 | 1983-06-28 | Preparation of low-viscosity coal-water slurry |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS608393A JPS608393A (en) | 1985-01-17 |
| JPH0315677B2 true JPH0315677B2 (en) | 1991-03-01 |
Family
ID=14657954
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11524683A Granted JPS608393A (en) | 1983-06-28 | 1983-06-28 | Preparation of low-viscosity coal-water slurry |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JPS608393A (en) |
| ZA (1) | ZA844946B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2678726B2 (en) * | 1993-11-17 | 1997-11-17 | 川崎重工業株式会社 | Production method of high concentration coal / water slurry |
-
1983
- 1983-06-28 JP JP11524683A patent/JPS608393A/en active Granted
-
1984
- 1984-06-28 ZA ZA844946A patent/ZA844946B/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| ZA844946B (en) | 1985-02-27 |
| JPS608393A (en) | 1985-01-17 |
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