JPS6044432A - Transporting method of molded coal - Google Patents

Transporting method of molded coal

Info

Publication number
JPS6044432A
JPS6044432A JP15066683A JP15066683A JPS6044432A JP S6044432 A JPS6044432 A JP S6044432A JP 15066683 A JP15066683 A JP 15066683A JP 15066683 A JP15066683 A JP 15066683A JP S6044432 A JPS6044432 A JP S6044432A
Authority
JP
Japan
Prior art keywords
coal
molded
mixture
briquette
molded coal
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
JP15066683A
Other languages
Japanese (ja)
Inventor
Kazuhide Ishida
一秀 石田
Mitsuki Hamamoto
浜本 光祈
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.)
Kansai Coke and Chemicals Co Ltd
Original Assignee
Kansai Coke and Chemicals Co 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 Kansai Coke and Chemicals Co Ltd filed Critical Kansai Coke and Chemicals Co Ltd
Priority to JP15066683A priority Critical patent/JPS6044432A/en
Publication of JPS6044432A publication Critical patent/JPS6044432A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00Solid fuels

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Auxiliary Methods And Devices For Loading And Unloading (AREA)
  • Coke Industry (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

PURPOSE:To transport molded coal without breaking it by mixing the molded coal in pulverized coal so that the mixing ratio of the molded coal becomes a specific ratio and transporting the molded coal under this mixture condition when the molded coal is to be transported using a transporting means such as a ship. CONSTITUTION:Molded coal (a) produced at a molded-coal production facility 2 in a main plant 1 is merged with pelverized coal (b) fed on a conveyor belt from a pelverized-coal storage tank 3 and is temporarily stored in a mixture storage tank 4 as a molded coal-pelverized coal mixture c1. In this case, the mixing ratio of the molded coal (a) is set to 60wt% or less, where the total sum of the molded coal (a) and the pelverized coal (b) is 100wt%. Next, after the said mixture is heaped c3 at a loading yard 5, it is loaded on a ship 6 and is transported to a plant of destination. Thereby, the molded coal (a) can be prevented from being broken due to shocks during loading and vibrations during transportation, and the function of the molded coal (a) as a coke production material with excellent quality can be properly kept.

Description

【発明の詳細な説明】 この発明は、近年冶金用の原料として注目されている成
型炭を、遠隔地間であってもこわれることなく、船、ト
ラック、貨車等の移送手段を用いて移送する方法に係る
ものである。
[Detailed Description of the Invention] The present invention is capable of transporting briquette coal, which has been attracting attention as a raw material for metallurgy in recent years, without breaking even between remote locations using transportation means such as ships, trucks, and freight cars. It is related to the method.

近年、原料事情の悪化に伴ない、従来冶金用のコークス
を製造するための原料としては適さないとされる非粘結
炭や微粘結炭等の劣質炭を使用して、良質のコークスを
得る方策が種々検討されており、その中の一つに、すで
に実用段階に入って久しい成型炭一部配合法がある。こ
の成型炭一部配合法は、粉炭に源青物からなる結合剤を
混入して混練捏和後加圧成型して得られる豆炭状の成型
炭を、通常の配合粉炭内に混入し、得られた混合物を通
常の水平式コークス炉に装入して乾留する方法であり、
原料粉炭中にすでに加圧された成型炭が混っていること
、及び成型炭中の結合剤に粘結性を補填する効果がある
ことから、従来よりもより多く安価な劣質炭を使用する
ことができるばかりか、石炭乾留に対して新たな設備投
資を行なうことなく、従来からある通常のコークス炉を
用いることができるという利点もあり、現在では最も効
果的な方法の一つであると目され、各所で実施されてい
る。
In recent years, with the deterioration of the raw material situation, it has become increasingly difficult to produce high-quality coke using inferior quality coals such as non-caking coal and slightly caking coal, which are conventionally considered unsuitable as raw materials for producing metallurgical coke. Various methods have been studied to obtain this, and one of them is a method of partially blending briquette charcoal, which has already been put into practical use for some time. This method of partially blending pulverized charcoal involves mixing powdered coal with a binder made from raw materials, kneading, kneading, and then pressurizing the charcoal. This is a method in which the mixture is charged into a normal horizontal coke oven and carbonized.
Because the pulverized raw coal already contains pressurized briquette coal, and the binder in the briquette has the effect of compensating for caking, more cheap inferior quality coal is used than in the past. Not only can it be used for coal carbonization, but it also has the advantage of being able to use conventional coke ovens without investing in new equipment, and is currently considered to be one of the most effective methods. It is being implemented in various places.

しかしながら、このような成型炭一部配合法であっても
、成型炭分製造するための設備は必須であって、これの
ための設備投資は避けられない。ところで、成型炭製造
設備dコークス炉の前方に建設されるのであるが、すべ
てのコークス製造工場内にこの成型炭製造設備を建設す
るのは、スペース的にも建設コストの上からもFiなは
だ不利であることから、主カニ場内にのみ成型炭製造設
備を建設し、遠隔地にある他工場には、主カニ場で製造
した成型炭を船、トラックあるいは貨車等の移送手段に
よって転送して用いることが好ましい。しかし、成型炭
を上述のような移送手段で転送するに際しての過酷なハ
ンドリング(取扱い)によって、せっが〈豆炭状に加圧
成型しである成型炭が割れて粉化し、結果として被転送
先の工場では、成型炭としての効果が半減するという不
都合があった。
However, even with such a method of partially blending briquette coal, equipment for producing briquette coal is essential, and investment in equipment for this is unavoidable. By the way, the briquette manufacturing equipment is constructed in front of the coke oven, but it would be unreasonable in terms of space and construction costs to construct this briquette manufacturing equipment in every coke manufacturing plant. Therefore, briquette production facilities are constructed only within the main crab farm, and the briquettes produced at the main crab farm are transported to other factories in remote areas by means of transport such as ships, trucks, or freight cars. It is preferable to use it. However, due to the harsh handling when transferring the briquettes using the above-mentioned transfer means, the briquettes (which have been pressure-molded into small charcoal shapes) crack and become powder, resulting in damage to the destination. At the factory, the inconvenience was that its effectiveness as briquette charcoal was halved.

本発明は、従来のこのような欠点を解消せんがためにな
されたものであって、例え過酷なハンドリングがあって
も、成型炭を製造している工場から遠隔地の工場に成型
炭をこわさずに移送せしめる方法を提供することを目的
とし、その要旨は、成型炭を船、トラック、貨車等の移
送手段を用いて移送するに当り、予め成型炭の混合率が
60重景%以下となるように該成型炭を粉炭内に混合し
て成型炭と粉炭の混合物を調製し、該混合物の状態で成
型炭を移送すること全特徴とする成型炭の移送方法に存
する。
The present invention was made in order to eliminate these drawbacks of the conventional methods, and even if the briquettes are handled in a harsh manner, they can be transported from a factory that manufactures briquettes to a factory in a remote location without damaging the briquettes. The purpose of this is to provide a method for transporting briquette coal by means of transportation such as ships, trucks, and freight cars, and the gist of this is that when briquette coal is transported by means of transportation such as ships, trucks, and freight cars, the mixing ratio of briquette coal must be 60% or less. The method of transferring briquette coal is characterized in that the briquette coal is mixed in powdered coal to prepare a mixture of briquette coal and pulverized coal, and the briquette coal is transferred in the state of the mixture.

以下本発明を図面を基に詳細に酸1明する。The present invention will be explained in detail below with reference to the drawings.

第1図は、本発明方法を説明するための流れ図である。FIG. 1 is a flow chart for explaining the method of the present invention.

2は主カニ賽1″内に設けられた成型炭製造設備であシ
、該製造設備2で製造された成型炭aは、配合槽などの
粉度貯槽3からコンベヤベルト上に切シ出される粉戻す
上に合流し、成型炭粉炭混合物C1となって混合物貯槽
4内に一時貯蔵される。しかしてこの場合の粉炭すは、
特定銘柄のみの単味炭であっても、ある程黒配合された
中間配合炭であってもよいが、被移送先でさらに配合操
作を行なわずそのまま後述するコークス炉10に装入す
るためには、すでに完全に配合操作の完了した1合粉炭
であることが好ましい。又、成型炭aの混合率は、粉炭
と成型炭の合計量’57100重脩%とした場合、60
重量%以下となるように設定すべきであり、それよりも
多くなると成型炭に対する粉炭のU衝効果が急激に低下
して、各所で行なわれるハンドリング時に成型炭はその
成型効果が失なわれる程度にまで破壊する。なお、ここ
でいう成型炭混合率は粉炭と混合される時点での混合率
であって、この混合までのハンドリングで成型炭が粉化
するのであれば、その粉化量は粉炭とみなして混合する
必要がある。下限については特には限定はないが、成型
炭の混合率が余りに小さくては成型炭移送の趣旨に沿わ
なくなるので、少なくとも10%、通常は20%以上と
することが好ましい。混合物貯槽4に一旦貯蔵された成
型炭粉炭混合物C1は適宜抜き出され(・C2)、図示
せざるトラック、貨′車、コンベヤベルトなどの移送手
段を用いて、荷役のための精通ヤード5Vc山積みされ
(・C3)、適宜荷役設備によって船6に積み込まれて
遠隔地にある被移送工場7に送られる。
2 is a molded coal production equipment installed in the main crab die 1'', and the molded coal a produced in the production equipment 2 is cut onto a conveyor belt from a powder storage tank 3 such as a blending tank. The pulverized coal is combined with the pulverized coal mixture C1 and temporarily stored in the mixture storage tank 4.The pulverized coal in this case is
It may be a single coal of a specific brand or an intermediate blend coal with a certain amount of black blend, but in order to charge it into the coke oven 10 described later without further blending operation at the destination. It is preferable that pulverized coal is one that has already been completely blended. In addition, the mixing ratio of briquette coal a is 60% when the total amount of pulverized coal and briquette coal is 57,100% by weight.
It should be set so that it is less than % by weight; if it exceeds this value, the U-impingement effect of powdered coal on briquette coal will decrease rapidly, and the briquette will lose its shaping effect during handling at various locations. destroy it to the extent of The briquette coal mixing ratio here is the mixing ratio at the time it is mixed with powdered coal, and if the briquette coal is pulverized during handling up to this point, the amount of powdered coal is considered to be pulverized coal and mixed. There is a need to. There is no particular limit on the lower limit, but if the mixing ratio of briquette coal is too small, the purpose of transferring briquette coal will not be met, so it is preferably at least 10%, usually 20% or more. The pulverized coal mixture C1 once stored in the mixture storage tank 4 is extracted as appropriate (・C2), and is piled up at the familiar yard 5Vc for cargo handling using transport means such as trucks, wagons, and conveyor belts (not shown). (・C3), and is loaded onto a ship 6 by appropriate cargo handling equipment and sent to a factory 7 located in a remote location.

被移送工場7′に船6によって転送された成型炭粉炭混
合物C4は図示せざるアンローダ−等の荷役設備によっ
て陸揚け(・C5)され、一旦原料ヤード8に野積みさ
れてのち、適宜ガントリークレーン、コンベヤベルト等
の移送手段により配合槽9に送られる(C6)。
The pulverized coal mixture C4 transferred to the transferred factory 7' by the ship 6 is unloaded (C5) by cargo handling equipment such as an unloader (not shown), and once loaded in the open at the raw material yard 8, it is transferred to the gantry as appropriate. It is sent to the blending tank 9 by a transport means such as a crane or a conveyor belt (C6).

配合槽9に貯蔵された成型炭粉炭混合物C6は、それが
すでに所定のコークス強度が得られるように配合済であ
る場合はそのまま、そうでない場合は予め決められた配
合割合に基づき、新たに他の銘柄の石炭と同時に切り出
して配合を完成させ、装Δ炭dとなってコークス炉10
に装入され、乾留されてコークスとなる。
If the pulverized coal mixture C6 stored in the blending tank 9 has already been blended to obtain a predetermined coke strength, it is left as it is; if not, it is newly blended with other materials based on a predetermined blending ratio. The brand of coal was cut out at the same time to complete the blend, and the coal d was produced in the coke oven 10.
The coke is then carbonized into coke.

以上のように、特定の一工場で生産された成型炭を遠隔
地にある他の工場に移送するときには、成型炭は過酷な
荷役時の衝撃や移送時の振動を受け、通常ならばそれら
が原因となって#1とんど破壊、粉砕してしまい、長細
のコークス製造原料としての機能を喪失してし寸うので
あるが、本発明においては、上記衝撃や振動を緩衝せし
めるべく粉炭中に成型炭が埋するように成型炭と粉炭の
混合物が調製され、その混合物が移送されるので、効果
的にこの粉炭が衝撃、振動を吸収し、成型炭をはとんと
破壊することなく移送することができることから、すべ
てのコークス製造工場に成型炭製造設備を建設しなくて
も、成型炭製造設備を有する工場からの転送で対処する
ことができるなど、最小の設備投資でコークス生産活動
の自由度を向上せしめることができる。さらに、この場
合に用いられる緩衝拐としての粉炭は、成型炭共々成型
炭一部配合法の原料であることから、被移送先で一旦混
合された混合物を元の状態に分離することなく、そのま
まコークス炉への装入原料として用いることができ、極
めて都合がよい。
As mentioned above, when briquettes produced at one particular factory are transferred to another factory in a remote location, the briquettes are subjected to harsh impacts during loading and unloading and vibrations during transport, which would normally be As a result, most of the coal is destroyed and crushed, and the function as a long and thin coke production raw material is almost lost.However, in the present invention, powdered coal is used to buffer the impact and vibrations mentioned above. A mixture of briquette coal and pulverized coal is prepared so that the briquette charcoal is buried inside, and this mixture is transferred, so this pulverized coal effectively absorbs shocks and vibrations, allowing the briquettes to be transferred without being completely destroyed. Therefore, coke production activities can be started with minimal capital investment, without having to build briquette production equipment at every coke production plant, and can be handled by transferring briquette production equipment from factories that have briquette production equipment. The degree of freedom can be improved. Furthermore, since the powdered coal used as the buffer used in this case is a raw material for the briquette coal partial blending method, the mixture once mixed at the destination is not separated into its original state. It can be used as a charging material to a coke oven, which is extremely convenient.

次に実施例fあげて本発明の方法をさらに説U!J1す
る。以下1%」とあるのは重量%である。
Next, Example F is given to further explain the method of the present invention! Play J1. "Not more than 1%" indicates weight %.

実施例 粉炭と成型炭の混合割合をどのように設定すれは、成型
炭の破壊を効果的に防止しながら遠距離間の移送を行な
いうるかを知るために、所定の混合率で調製された成型
炭粉炭混合物の試料s kgを土嚢に袋詰めし、高所よ
シ複数回落下せしめてのち、成型炭未粉化率(当初使用
した成型炭中、落下試験後も粉化しなかったものの割合
)を測定した。
Example: In order to find out how to set the mixing ratio of powdered coal and molded coal, it is possible to transport the molded coal over long distances while effectively preventing the destruction of the molded coal. After packing s kg of a sample of the pulverized coal mixture into sandbags and dropping it from a high place several times, the unpulverized rate of molten coal (percentage of the molten coal initially used that did not become pulverized even after the drop test) was determined. was measured.

試験条件は以下のとおシでを)る。The test conditions are as follows.

・供試成型炭の大きさと形状 33 cc7獅、豆炭状 ・供試粉炭 通常の装入炭(amp)82%) ・成型炭粉炭混合物供試量  kg ・成型炭混合率 40.60.80.100半希%の4 ケース ・上記4ケース各々の繰り返し点数 3点 ・試料落下高さ 3、5 m (床はコンクリート) ・一点当シの落下回数 25回 ・試験実施後の未粉化成型炭の割合 15ff網目以上の篩上%で表示 なお、試料落下高さを3、sm、一点当りの落下回数を
25回としたのけ、船で成型炭を移送する場合、#1は
上記高さを上記回数落下するようなハンドリングが行な
われることをシミュレート(模擬的に実現)したからで
ある。
・Size and shape of sample briquette charcoal: 33cc7 lion, pea charcoal ・Test pulverized coal: normal charging coal (amp) 82%) ・Test amount of pulverized charcoal mixture: kg ・Multiple charcoal mixture ratio: 40.60.80. 4 cases of 100 semi-dilute % - 3 repeated points for each of the above 4 cases - Sample falling height 3.5 m (floor is concrete) - Number of drops per point 25 times - Unpulverized briquette charcoal after testing The ratio of 15ff is expressed as the percentage above the sieve with a mesh size of 15ff or higher.If the sample is dropped at a height of 3 sm and the number of drops per point is set at 25 times, and the briquette is transported by ship, #1 is the height above. This is because it was simulated (realized in a simulated manner) to be handled in such a way as to fall the number of times mentioned above.

試験結果を次表に示した。The test results are shown in the table below.

この表から判るとおり、成型炭混合率が60%以下の時
には、過酷な落下試験を行なったにも拘らず、成型炭未
粉化率は84%以上、即ち成型炭がくずれて15酊以下
の粉状となる粉化率は16%以下と良好であるのが判る
As can be seen from this table, when the blending ratio of briquette coal was 60% or less, the unpowdered charcoal rate was more than 84%, even though the severe drop test was conducted, that is, the briquette coal crumbled and the pulverization rate was 15% or less. It can be seen that the powdering rate is 16% or less, which is good.

なお、第2図は上表の結果をグラフに表わしたものであ
り、横軸に粉炭混合率、縦軸に成型炭未粉化率をとった
ものである。このグラフが著し、く、一方粉炭混合率が
40%以上、即ち成型炭混合率が60%以下となると成
型炭の粉化が抑制されることが判る。
Incidentally, FIG. 2 is a graph representing the results of the above table, in which the horizontal axis shows the pulverized coal mixing ratio and the vertical axis shows the unpulverized ratio of molded coal. This graph shows that the pulverization of briquette coal is significantly reduced when the pulverized coal mixture ratio is 40% or more, that is, when the briquette coal mixture ratio is 60% or less.

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

第1図は本発明方法全説明するための流れ図であり、第
2図は成型炭粉炭混合物の供試料に対する落下試験実施
後の粉炭混合率と成型炭未粉化率の関係を示すグラフで
ある。 1・・・主カニ場、2・・・成型炭製造設備、3・・・
粉炭貯槽、4・・・混合物貯槽、5・・・積込ヤード、
6・・・船、7・・・成型炭被移送工場、8・・・原料
ヤード、9・・・配合槽、1o・・・コークス炉、a・
・・成型炭、b・・・粉炭、ci〜c6・・・成型炭粉
炭混合物そのもの又はそれの移送行為、d・・・装入炭 第1図 第2図
Fig. 1 is a flowchart for explaining the entire method of the present invention, and Fig. 2 is a graph showing the relationship between the pulverized coal mixing ratio and the unpulverized ratio of molten coal after performing a drop test on a specimen of a pulverized coal mixture. . 1... Main crab farm, 2... Molded coal manufacturing equipment, 3...
Powdered coal storage tank, 4...mixture storage tank, 5...loading yard,
6... Ship, 7... Molded coal transfer factory, 8... Raw material yard, 9... Blending tank, 1o... Coke oven, a.
... Molded coal, b... Powdered coal, ci-c6... Molded coal and powdered coal mixture itself or the act of transferring it, d... Charged coal Figure 1 Figure 2

Claims (1)

【特許請求の範囲】[Claims] 1、 成型炭を船−トラック、貨車等の移送手段を用い
て移送するに当り、予め成型炭の混合率が60重景%以
下となるように該成型炭を粉炭内に混合して成型炭と粉
炭の混合物を調製し、該混合物の状態で成型炭を移送す
ることを特徴とする成型炭の移送方法。
1. When transporting briquette coal using transport means such as ships and trucks, freight cars, etc., the briquette coal is mixed with powdered coal in advance so that the blending ratio of briquette coal is 60% or less. A method for transferring briquette coal, which comprises preparing a mixture of pulverized coal and pulverized coal, and transferring the briquette coal in the state of the mixture.
JP15066683A 1983-08-17 1983-08-17 Transporting method of molded coal Pending JPS6044432A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15066683A JPS6044432A (en) 1983-08-17 1983-08-17 Transporting method of molded coal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15066683A JPS6044432A (en) 1983-08-17 1983-08-17 Transporting method of molded coal

Publications (1)

Publication Number Publication Date
JPS6044432A true JPS6044432A (en) 1985-03-09

Family

ID=15501822

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15066683A Pending JPS6044432A (en) 1983-08-17 1983-08-17 Transporting method of molded coal

Country Status (1)

Country Link
JP (1) JPS6044432A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018169199A (en) * 2017-03-29 2018-11-01 宇部興産株式会社 Evaluation method of coal degradation

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018169199A (en) * 2017-03-29 2018-11-01 宇部興産株式会社 Evaluation method of coal degradation

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