JPH0352994A - Production of molded fuel - Google Patents

Production of molded fuel

Info

Publication number
JPH0352994A
JPH0352994A JP18829689A JP18829689A JPH0352994A JP H0352994 A JPH0352994 A JP H0352994A JP 18829689 A JP18829689 A JP 18829689A JP 18829689 A JP18829689 A JP 18829689A JP H0352994 A JPH0352994 A JP H0352994A
Authority
JP
Japan
Prior art keywords
molded
coal
paraffin
mixture
slaked lime
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.)
Granted
Application number
JP18829689A
Other languages
Japanese (ja)
Other versions
JPH0768530B2 (en
Inventor
Toshihiko Maruyama
敏彦 丸山
Katsumi Fujishima
藤島 勝美
Satoru Takemichi
竹道 覚
Mitsushi Kamiide
上出 光志
Eizo Ishiyama
石山 栄三
Tatsuro Fujiwara
達郎 藤原
Hideo Murakami
英穂 村上
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.)
Sanei Kogyo KK
Original Assignee
Sanei Kogyo KK
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 Sanei Kogyo KK filed Critical Sanei Kogyo KK
Priority to JP1188296A priority Critical patent/JPH0768530B2/en
Publication of JPH0352994A publication Critical patent/JPH0352994A/en
Publication of JPH0768530B2 publication Critical patent/JPH0768530B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

PURPOSE:To improve water resistance of molded fuel without requiring heating by blending sulfur containing coal powder with fibrous biomass powder and slaked lime to give a mixture, molding the mixture under high pressure and treating the surface. CONSTITUTION:(A) 100 pts.wt. coal powder containing >=1.0wt.% combustible sulfur (anhydrous base) is blended with (B) 15-45 pts.wt. fibrous biomass powder such as woody waste, bagasse or strained lees of cotton seed oil having 2-3mm particle diameter and (C) slaked lime. The mixture is molded under 2,000-5,000 kgf/cm<2> high pressure into a briquette state and the prepared granulated material is subjected to surface treatment with a solution of paraffin and heavy oil A having weight ratio of paraffin and heavy oil A=(1:9)-(5:5) to give the objective molded material.

Description

【発明の詳細な説明】[Detailed description of the invention]

[産業上の利用分野J 本発明は、高疏黄分を含有する石炭粉を主原料として、
これに!+1原料である織維質バイオマス粉、及び脱硫
剤として消石灰を配合した高圧造粒物を表面処理により
耐水性を付与することを特徴とする成型燃料の製造法に
関するものである.
[Industrial Field of Application J The present invention uses coal powder containing high chlorous content as the main raw material,
to this! This invention relates to a method for producing molded fuel, which is characterized by imparting water resistance through surface treatment to high-pressure granules containing woven fibrous biomass powder as +1 raw material and slaked lime as a desulfurizing agent.

【従来の技術】[Conventional technology]

低硫黄分石炭粉を主原料に、m it *バイオマスの
一種である木質粉を副原料とし、石炭及びバイオマス原
料の配合比が本発明の1I求範囲にある成型燃料に関し
ては、本発明者等による二件の発明+11121によっ
て公知である.その一つは、原料組成比(重量)を石炭
二 木震廃材=9:1〜5:5として、例えば温度20
0℃、圧力300kg/a1のもとで得られる成型燃料
である.また、もう一つは、上述の石炭・木質粉混合物
を80〜100゜Cの温度範囲において水蒸気共存下で
一定時間保持することによって、混合物中の木材成分に
バインダー活性を付与することを特徴とする成型燃料の
製造法である.このようにして帰られる石炭・木質成型
燃料は石炭単昧に比して、以下に述べる特徴を有する.
<L)f1m焼時にばい煙発生量がきわめて少ない.(
2)燃焼時の形状保持性がよい. (3〉灰分が少ない. (4)着火性が良い。 (5)粉状原科を用いるので、燃焼器具・燃焼機横に合
せて任意の形状・寸法に成型することが出来る. (6)バインダーを用いないので安価である.(7)木
質廃材を利用するので省資源となる.〔発明が解決しよ
うとする問題点】 従来の技術によって得られる石炭・木質成型燃料は前述
の特徴を有するが、次の点においてさらに改良されなけ
れば、現在の石油エネルギー事情から言って石炭・木質
成型燃料は石油代替エネルギーとして、経済性及び品質
の面から受1ブ入れられにくい. すなわち、■主原料である石炭において、その品質が広
く対象になり、例えば高硫黄分のものであっても使用可
能であること.■副原料である繊維責バイオマスが木質
廃材に止まらず、種々のものが使用可能なこと.■省エ
ネルギー上、加熱せずに成型可能であること.■成型燃
料に耐水性が付与されていること、などである.
Regarding the molded fuel in which low sulfur content coal powder is used as the main raw material and wood powder, which is a type of biomass, is used as an auxiliary raw material, and the blending ratio of coal and biomass raw materials is within the range required by 1I of the present invention, the present inventors et al. It is publicly known due to two inventions +11121 by. One method is to set the raw material composition ratio (weight) of coal, wood, and wood waste from 9:1 to 5:5, and for example, at a temperature of 20
This is a molded fuel obtained at 0°C and a pressure of 300 kg/a1. Another feature is to impart binder activity to the wood components in the mixture by holding the above-mentioned coal/wood powder mixture in the coexistence of water vapor at a temperature range of 80 to 100°C for a certain period of time. This is a method for producing molded fuel. The coal/wood molded fuel returned in this way has the following characteristics compared to just coal.
<L) The amount of smoke generated during f1m firing is extremely small. (
2) Good shape retention during combustion. (3) Low ash content. (4) Good ignitability. (5) Since powdered raw material is used, it can be molded into any shape and size to match the side of the combustion equipment or combustion machine. (6) It is inexpensive because it does not use a binder. (7) It saves resources because it uses wood waste. [Problems to be solved by the invention] The coal/wood molded fuel obtained by the conventional technology has the above-mentioned characteristics. However, unless further improvements are made in the following points, it is difficult to accept coal/wood molded fuel as an alternative energy to petroleum in terms of economy and quality given the current petroleum energy situation.In other words, main raw materials The quality of coal is subject to a wide range of targets, for example, it can be used even if it has a high sulfur content.■ The auxiliary raw material, fiber biomass, is not limited to wood waste, and various types can be used. ■For energy saving purposes, it can be molded without heating.■The molded fuel has water resistance, etc.

【問題を解決するための手段] 前述の請点を改良すべく種々検討した結果、量産性が高
く、しかも高圧下で造粒できるロール式プレス法によっ
て、特許請求の範囲に記載する如くの本発明に至ったも
のである. 以下、本発明による製造法について説明する.本発明に
よる製造工程は、原料調整(1)、混合( I1 )、
成型(Ill)、成型物のパリ取り( +V )及び表
面処理(V)の各工程に大別される.原料調整工1m(
1)では、主原料である石炭については固有水分量程度
までに乾燥し、粒径2〜3膳量以下に粉砕する.又、バ
イオマスについては、オが屑、樹皮などの木質廃材の他
に、バガス(砂糖きびの絞り粕)、ビートパルプ、モミ
ガラ、麦藁等も対象になり、それらを水分10%以下に
乾燥し、粒径2〜3ms+以下に粉砕する.混合工程(
 II )では、上記の工程で粒度、水分を調整した原
料を用い、石炭粉1001m量部に対して繊維責バイオ
マス粉15〜45重量部と、さらに石炭の有する燃焼性
硫黄分の100〜150%当量に相当する重量の消石灰
を配合し、均一に撹判混合する.本発明では燃焼性硫黄
分がl.Owt%以上の石炭を対称としており、それ未
満の石炭を使用した成型燃料では硫黄分のきわめて少な
いバイオマスが配合されたため、硫黄酸化物の発生の点
で、実用上あまり問題にならない. 成型工程( Ill )では、それらの混合物はフィー
ダーを通してロール型プレスにより、加熱することなし
に、圧力2,Goo〜5,OOOkgf/ cm”の条
件下で連続的にブリケット状に造粒され、次の工程(I
V)のスクリーンを通してパリが除去された追粒物は表
面処理工$1 (V)に供給される.一方パリは再びフ
ィーダーを通してロールプレスにより成型される. 表面処理工程(V)では、得られた造粒物を重量比がパ
ラフィン =A重油=l:9〜5:5範囲の溶液に数秒
間漫潰し、造粒物の表面部に上記の溶液層を形成させる
. 以下、本発明について実施例により詳細に説明する. 【実施例】 実施例に供した燃料は、石炭として低品位のリグナイト
 またNI#I質バイオマスとして木質廃材、バガス、
麦藁、綿実油絞り粕、モミガラである.これらの原料を
それぞれ2■以下に粉砕した壕、所定の原料組成比にな
るように配合し、無加熱下で十分に撹判混合した.次に
これらの混合物15kgをスクリュー式フィーダーによ
りロールプレスに供給し、表1に示す条件下で成型を行
った.この操作を1混合試料につき5回繰り返し、合計
75kgの原料を連続的に成型し、造粒物のパリ部分は
lesmフルイを通して取り除いた.引き続き、得られ
た造粒物をパラフィンlO%とA重油90%(重量比)
から成る溶液に約3秒間漫漬徨引き上げ、室温にて放置
した.このように得られた造粒物の破壊強度を表2に示
した. この表から明らかなように、バイオマスの種類によって
、得られる成型物の強度は異なるが、いずれのバイオマ
スであっても、特別な結合剤を使用せずに、しかも無加
熱下で高圧ロールプレスにより石炭・バイオマス系成型
燃料は製造可能であった.なお表2にはバイオマス20
wt%配合の例しか示していないが造粒物の強度はバイ
オマスの配合量の増大とともに増大することは言うまで
もない.  表3は原炭及びバイオマスの例として木質
廃材、バガスを用いた遺粒物の分析値であるが、合わせ
て脱硫剤による効果比較も示した.原炭は熱分解温度の
低い黄鉄鉱のような絋物質を多く含んでおり、硫黄分の
きわめて高い低品位の石炭で、そのままでは燃料時にお
ける大量の硫黄酸化物が発生するため使用に耐えない.
  しかしバイオマスと消石灰を配合することによって
リグナイト原炭に比して硫黄酸化物の発生量を大幅に低
減され帰た.このことは実際の石炭ストーブで燃焼させ
た後の燃焼灰中に含まれる不燃焼性硫黄分の測定によっ
ても確認されている.したがって石炭中に含まる燃焼性
硫黄分は燃焼時に消石灰と反応して.8ilえば無水石
こうの形で灰中に固定されたことにほかならない. ま
た、本造粒物は前述した公知である石炭・木貢系成型燃
料と同様の燃焼特性を有していることは言うまでもない
脱硫剤による効果では、表3の造粒物I1と■の比較か
ら明らかなように消石灰は炭酸カルシウムに比較して脱
硫効果は大きい.このことは両者の熱分解温度の相違に
よるものであり、本発明によるような成型燃料の場合、
脱硫剤として消石灰の方が適している.また、カルシウ
ム化合物の脱硫剤として生石灰があるが、そのままの状
態で成型物に存在すると、その強度の低下を来たす欠点
があるため、最終的にはCa(OH)aになるように手
段を講じなければならない.したがって、本発明におい
て消石灰を使用するのは以上のような理由によるもので
ある. 造粒物の耐水性については、スプレーにより降水量50
mm/h,  120分間の条件下で試験した結果、無
処理の造粒物は直ちにll潤して崩壊するのに対して、
表面処理した造硫物は降水120分間徨においても何ら
形に変化がみ見られず、その吸水量もl.O wt%前
後と小さく、大幅な耐水性の向上がfl認された.した
がって、本発明による成型燃料は通常の野外貯蔵、輸送
中における一時的な降雨による被水には十分に耐え帰り
、しかもその際の吸水量も小さいことから、被水した場
合であっても、乾燥せずに、そのまま燃料として使用可
能である.従来からの成型燃料の耐水性を付与する表面
処理剤としてパラフィンを使用することは公知である.
しかし、パラフィンは価格の高い原料であり、その使用
量が少量に止めることが1,IIコストの面から望まし
い.本発明では高価なパラフィンを安価なものによりで
きるだけ代替し、しかもパラフィン単味と同程度の耐水
性を付与することを目的として種々検討した結果をもと
に見い出したものである.すなわち、実施例で示したご
とく、パラフィンの90%を安価なAlk油で代替した
場合でも十分な耐水性が帰られ、しかもこの混合溶液を
使用した場合、A重油成分は主として成型燃料の内部へ
と移行し、一方のパラフィン成分は表面部に止まり結果
としてパラフィン単昧を使用したときと同様の表面状態
を呈する.したがって、本発明において表面処理剤とし
てパラフィン、重油溶液を使用するのは以上の知見に基
づいている.【発明の効果J 以上、本発明について説明したように本成型燃料の製造
法は高硫黄分石炭及び種々のバイオマスを原料として、
公知の石炭・木質廃材成型燃料と同様に優れた燃焼特性
を有することに加えて、製造工程において原料の混合・
成型時に加熱を必要とせず、しかも耐水性を付与するこ
とを大きな特徴としている.従って、本発明は品質、燃
焼特性の面からも、又経清性、工場立地の多様性、製造
の容易性などの点においても優れた成型燃料を提供する
ものであり、未利用エネルギー資源の有効利用を促進す
ると共に、省資源・エネルギーの立場からも大きく寄与
するものである。 表 1 成型条件 表 2 造粒物の破壊強度 (kgf) リグナイ ト(資)、 バイオマス20、 消石灰10%配合 表  3 原炭及び造粒物の分析値 A゛ B ゜ C ゜ D゜ 水分   (X) 灰分   (χ) 揮発分  (X) 固定炭素 (z) 総発熱量(kcal八区〉 全硫黄(鴬,無水基) 不燃性硫黄(〃) 燃焼性硫黄(〃) l2.0 24.2 34.2 29.2 4,410 6.8 0.5 6.3 6.5 39.8 36.4 17.3 4,250 4.2 3.7 0.5 6.3 40,2 37.O l6.5 4 , 230 4.5 3.9 0.6 6.9 33.3 39.2 20.6 4,260 4.9 1.2 3.7 15%
[Means for solving the problem] As a result of various studies to improve the above-mentioned points, we have developed a book as described in the claims by using a roll press method that is highly mass-producible and can be granulated under high pressure. This led to the invention. The manufacturing method according to the present invention will be explained below. The manufacturing process according to the present invention includes raw material preparation (1), mixing (I1),
It is roughly divided into the following steps: molding (Ill), deburring (+V) of the molded product, and surface treatment (V). Raw material adjustment 1m (
In 1), the main raw material, coal, is dried to its own moisture content and crushed to a particle size of 2 to 3 grains or less. Regarding biomass, in addition to wood waste materials such as sawdust and bark, we also target bagasse (sugar cane lees), beet pulp, rice hulls, and wheat straw, which are dried to a moisture content of 10% or less and made into grains. Grind to a diameter of 2 to 3 ms+ or less. Mixing process (
In II), using raw materials whose particle size and moisture content have been adjusted in the above steps, 15 to 45 parts by weight of fiber-containing biomass powder is added to 1001 m parts of coal powder, and 100 to 150% of the combustible sulfur content of the coal is added. Add an equivalent weight of slaked lime and stir to mix uniformly. In the present invention, the combustible sulfur content is l. Owt% or more coal is the target, and molded fuel using less than that amount of coal contains biomass with an extremely low sulfur content, so there is no practical problem in terms of the generation of sulfur oxides. In the forming process (Ill), the mixture is continuously granulated into briquettes through a feeder by a roll press under a pressure of 2,000 to 5,000 kgf/cm'' without heating, and then granulated into briquettes. The process (I
The additional grains from which pari has been removed through the screen of V) are supplied to the surface treatment process $1 (V). Meanwhile, the paris are passed through the feeder again and formed by a roll press. In the surface treatment step (V), the obtained granules are crushed for several seconds in a solution having a weight ratio of paraffin = heavy oil A = l:9 to 5:5, and the above solution layer is formed on the surface of the granules. Form. Hereinafter, the present invention will be explained in detail with reference to Examples. [Example] The fuel used in the example was low-grade lignite as coal, wood waste wood, bagasse as NI#I biomass,
They are wheat straw, cottonseed oil press lees, and rice hulls. These raw materials were pulverized to 2 μm or less each, mixed to a predetermined raw material composition ratio, and mixed thoroughly with stirring without heating. Next, 15 kg of these mixtures were fed to a roll press using a screw feeder and molded under the conditions shown in Table 1. This operation was repeated five times for each mixed sample to continuously mold a total of 75 kg of raw material, and the pars of the granules were removed through a LESM sieve. Subsequently, the obtained granules were mixed with 10% paraffin and 90% heavy oil A (weight ratio).
The sample was soaked in a solution consisting of for about 3 seconds and then left at room temperature. Table 2 shows the fracture strength of the granules thus obtained. As is clear from this table, the strength of the molded product differs depending on the type of biomass, but any biomass can be made by high-pressure roll press without using any special binder and without heating. It was possible to produce coal/biomass-based molded fuel. Table 2 shows biomass 20
Although only an example of wt% blending is shown, it goes without saying that the strength of the granules increases as the amount of biomass blended increases. Table 3 shows the analysis values of grains using wood waste and bagasse as examples of raw coal and biomass, and also shows a comparison of the effects of desulfurization agents. Raw coal is a low-grade coal with an extremely high sulfur content, containing a large amount of pyrite-like substances that have a low thermal decomposition temperature, and cannot be used as is because it generates large amounts of sulfur oxides when used as fuel.
However, by blending biomass and slaked lime, the amount of sulfur oxides generated was significantly reduced compared to raw lignite coal. This has also been confirmed by measuring the amount of non-combustible sulfur contained in combustion ash after combustion in an actual coal stove. Therefore, the combustible sulfur contained in coal reacts with slaked lime during combustion. 8il, it is nothing but fixed in the ash in the form of anhydrite. In addition, it goes without saying that this granule has the same combustion characteristics as the well-known coal-wood molded fuel mentioned above, and in terms of the effect of the desulfurization agent, the comparison between granules I1 and ① in Table 3. As is clear from the above, slaked lime has a greater desulfurization effect than calcium carbonate. This is due to the difference in thermal decomposition temperature between the two, and in the case of the shaped fuel according to the present invention,
Slaked lime is more suitable as a desulfurizing agent. In addition, quicklime is used as a desulfurizing agent for calcium compounds, but if it is present in molded products as it is, it has the disadvantage of reducing its strength, so measures are taken to ensure that the final product is Ca(OH)a. There must be. Therefore, the reason why slaked lime is used in the present invention is as mentioned above. Regarding the water resistance of the granules, the amount of precipitation 50% was determined by spraying.
mm/h for 120 minutes, the results showed that untreated granules immediately became wet and disintegrated;
The surface-treated sulfur-forming product showed no change in shape even after 120 minutes of precipitation, and its water absorption amount was 1. Although it was small at around 0 wt%, a significant improvement in water resistance was observed. Therefore, the molded fuel according to the present invention can sufficiently withstand exposure to water due to temporary rain during normal outdoor storage and transportation, and also has a small amount of water absorption at that time, so even if it is exposed to water, It can be used as fuel without drying. The use of paraffin as a surface treatment agent to impart water resistance to conventional molded fuels is well known.
However, paraffin is an expensive raw material, and it is desirable to keep its usage to a small amount from the viewpoint of cost. The present invention was made based on the results of various studies aimed at replacing expensive paraffin with inexpensive paraffin as much as possible, and at the same time imparting the same level of water resistance as paraffin alone. In other words, as shown in the example, sufficient water resistance can be achieved even when 90% of paraffin is replaced with inexpensive Alk oil, and when this mixed solution is used, the A heavy oil component mainly flows into the inside of the molded fuel. One paraffin component remains on the surface, resulting in a surface condition similar to when paraffin alone is used. Therefore, the use of paraffin and heavy oil solutions as surface treatment agents in the present invention is based on the above findings. [Effects of the Invention J] As explained above about the present invention, the present method for producing shaped fuel uses high sulfur content coal and various biomass as raw materials.
In addition to having excellent combustion characteristics similar to well-known coal and wood waste molded fuels, it is possible to mix and process raw materials during the manufacturing process.
Its main feature is that it does not require heating during molding and is water resistant. Therefore, the present invention provides a molded fuel that is excellent not only in terms of quality and combustion characteristics, but also in terms of economical cleanliness, diversity of factory locations, and ease of production, and it is possible to utilize unused energy resources. It not only promotes effective utilization but also makes a major contribution from the standpoint of resource conservation and energy conservation. Table 1 Molding conditions Table 2 Breaking strength of granules (kgf) Lignite (material), biomass 20, slaked lime 10% composition table 3 Analysis values of raw coal and granules A゛B ゜C ゜D゜Moisture (X) Ash content (χ) Volatile content (X) Fixed carbon (z) Total calorific value (kcal 8 wards) Total sulfur (sulfur, anhydride) Nonflammable sulfur (〃) Combustible sulfur (〃) l2.0 24.2 34. 2 29.2 4,410 6.8 0.5 6.3 6.5 39.8 36.4 17.3 4,250 4.2 3.7 0.5 6.3 40.2 37.O l6 .5 4 , 230 4.5 3.9 0.6 6.9 33.3 39.2 20.6 4,260 4.9 1.2 3.7 15%

Claims (1)

【特許請求の範囲】[Claims] 燃焼性硫黄分を1.0wt%(無水基)以上を含有する
石炭粉100重量部に対して、繊維質バイオマス粉15
〜45重量部と適当量の消石灰を配合した混合物をブリ
ケット状に高圧成型した後、得られる造粒物について重
量比がパラフィン:A重油:1:9〜5:5範囲の溶液
により表面処理することを特徴とする成型燃料の製造法
15 parts by weight of fibrous biomass powder per 100 parts by weight of coal powder containing combustible sulfur content of 1.0 wt% or more (anhydride group)
After high-pressure molding a mixture of ~45 parts by weight and an appropriate amount of slaked lime into a briquette shape, the resulting granules are surface-treated with a solution with a weight ratio of paraffin: heavy oil A: 1:9 to 5:5. A method for producing shaped fuel characterized by
JP1188296A 1989-07-19 1989-07-19 Molded fuel manufacturing method Expired - Fee Related JPH0768530B2 (en)

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Application Number Priority Date Filing Date Title
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JPH0352994A true JPH0352994A (en) 1991-03-07
JPH0768530B2 JPH0768530B2 (en) 1995-07-26

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002050220A1 (en) * 2000-12-21 2002-06-27 Ve Gruppen A/S Method and system for production of fuel pellets and fuel pellet
WO2004063315A1 (en) * 2003-01-09 2004-07-29 Brickett Technologies Limited Handling of coal fines
JP2015078347A (en) * 2013-09-14 2015-04-23 綜研テクニックス株式会社 Briquette and briquette combustion method
WO2017138422A1 (en) * 2016-02-09 2017-08-17 宇部興産株式会社 Method for manufacturing coal molded fuel

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS476448U (en) * 1971-02-13 1972-09-21
JPS5844718A (en) * 1981-09-11 1983-03-15 Nippon Telegr & Teleph Corp <Ntt> Exposure system by charged beam
JPS62135594A (en) * 1985-12-07 1987-06-18 Norio Ohashi Molded coal
JPS6415560A (en) * 1987-07-09 1989-01-19 Toyota Motor Corp Control device for speed change of automatic transmission

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS476448U (en) * 1971-02-13 1972-09-21
JPS5844718A (en) * 1981-09-11 1983-03-15 Nippon Telegr & Teleph Corp <Ntt> Exposure system by charged beam
JPS62135594A (en) * 1985-12-07 1987-06-18 Norio Ohashi Molded coal
JPS6415560A (en) * 1987-07-09 1989-01-19 Toyota Motor Corp Control device for speed change of automatic transmission

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002050220A1 (en) * 2000-12-21 2002-06-27 Ve Gruppen A/S Method and system for production of fuel pellets and fuel pellet
WO2004063315A1 (en) * 2003-01-09 2004-07-29 Brickett Technologies Limited Handling of coal fines
JP2015078347A (en) * 2013-09-14 2015-04-23 綜研テクニックス株式会社 Briquette and briquette combustion method
WO2017138422A1 (en) * 2016-02-09 2017-08-17 宇部興産株式会社 Method for manufacturing coal molded fuel
JPWO2017138422A1 (en) * 2016-02-09 2018-11-29 宇部興産株式会社 Coal molding fuel manufacturing method

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