JPH06184571A - Production of composite solid fuel of coal with vegetable matter, and composite solid fuel - Google Patents

Production of composite solid fuel of coal with vegetable matter, and composite solid fuel

Info

Publication number
JPH06184571A
JPH06184571A JP9654092A JP9654092A JPH06184571A JP H06184571 A JPH06184571 A JP H06184571A JP 9654092 A JP9654092 A JP 9654092A JP 9654092 A JP9654092 A JP 9654092A JP H06184571 A JPH06184571 A JP H06184571A
Authority
JP
Japan
Prior art keywords
solid fuel
coal
composite solid
powder
sulfur
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.)
Withdrawn
Application number
JP9654092A
Other languages
Japanese (ja)
Inventor
Chuichi Mizoguchi
忠一 溝口
Yutaka Yamamoto
裕 山本
Takafumi Hagino
孝文 萩野
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.)
Taiyo Steel Co Ltd
Taiyo Ltd
Original Assignee
Taiyo Steel Co Ltd
Taiyo 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 Taiyo Steel Co Ltd, Taiyo Ltd filed Critical Taiyo Steel Co Ltd
Priority to JP9654092A priority Critical patent/JPH06184571A/en
Priority to CN 93102572 priority patent/CN1042041C/en
Publication of JPH06184571A publication Critical patent/JPH06184571A/en
Withdrawn legal-status Critical Current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
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/02Use of additives to fuels or fires for particular purposes for reducing smoke development
    • 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
    • Y02E50/10Biofuels, e.g. bio-diesel
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

PURPOSE:To provide a process for producing a composite solid fuel which comprises coal and vegetable matter and is decreased in the amt. of sulfur oxides in the flue gas. CONSTITUTION:In a process for producing a composite solid fuel through compression molding of a starting material mixture of a coal powder with 20-25wt.% vegetable matter powder, slaked lime as a desulfurizing agent is added in such an amt. that the molar ratio of calcium in slaked lime to sulfur contained in the coal powder in the starting material mixture is in the range of 1.0 to 1.8. When the fuel is combusted, sulfur is fixed in ash by added slaked lime to greatly decrease the amt. of sulfur oxides contained in the flue gas.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、石炭粉末に植物質の粉
末を混合した原料をロールプレスによって圧縮成形して
複合固形燃料を得る、石炭と植物質との複合固形燃料の
製法及び複合固形燃料に関する。
FIELD OF THE INVENTION The present invention relates to a method for producing a composite solid fuel of coal and plant matter and a composite solid fuel, in which a raw material prepared by mixing coal powder with vegetable powder is compression molded by a roll press to obtain a composite solid fuel. Regarding fuel.

【0002】[0002]

【従来の技術】従来から石炭は、家庭用暖房ストーブ、
あるいはボイラー等の燃料として広く使用され、その石
炭は通気性を良好にするため50〜100mmの程度の
塊状のものが一般に使われている。また採掘、搬送、選
炭過程で生じる数mm以下の微粉石炭はバインダーを添
加してロールプレスによって圧縮成形した石炭ブリケッ
トとして使われている。
2. Description of the Related Art Conventionally, coal has been used for household heating stoves,
Alternatively, it is widely used as a fuel for boilers and the like, and the coal is generally in the form of lumps of about 50 to 100 mm in order to improve the air permeability. Further, pulverized coal having a diameter of several mm or less generated during mining, transportation and coal preparation processes is used as a coal briquette which is added with a binder and compression-molded by a roll press.

【0003】しかし、世界的に多く埋蔵され、広く使用
されている低品位石炭は灰分が15〜30重量%も含
み、発熱量が低く、着火性、持続性が悪く、ばい煙量も
多く、更に燃焼の際灰分が溶融して大きな塊状のクリン
カーとなって、通気を悪化して燃焼効率を低くする等の
不具合を有する。
However, low-grade coal, which is widely stored and widely used all over the world, contains 15 to 30% by weight of ash, has a low calorific value, is poor in ignitability and sustainability, and has a large amount of soot and smoke. At the time of combustion, the ash is melted to form a large lump clinker, which deteriorates ventilation and reduces combustion efficiency.

【0004】この対策として煙量の発生が少なく、着火
性、持続性が良好であることから石炭に木材、バガス等
の植物質を20〜25重量%混合して高圧縮力で成形し
た、石炭と植物質との複合固形燃料(以下複合固形燃料
と称す)が用いられている。
As a measure against this, since the amount of smoke is small, and the ignitability and sustainability are good, 20 to 25% by weight of plant materials such as wood and bagasse are mixed with coal, and the mixture is molded with a high compression force. A mixed solid fuel of plant and plant matter (hereinafter referred to as a mixed solid fuel) is used.

【0005】複合固形燃料の製法は、石炭及び木材、バ
ガス等から成る植物質を乾燥、粉砕して数mm以下に調
整した原料に、炭種に応じて更にパインダーを添加混合
し、ロール外周面にブリケットの母形となるポケットが
形成された互いに対向する一対のロールからなるブリケ
ットマシーンと称するロールプレスで圧縮成形すること
によってなされる。
The method for producing a composite solid fuel is as follows. A raw material prepared by drying and crushing plant matter such as coal, wood, bagasse, etc. to a size of several mm or less is further mixed with a pinder depending on the type of coal, and the outer peripheral surface of the roll is then mixed. Is formed by compression molding with a roll press called a briquette machine consisting of a pair of rolls facing each other in which pockets forming the briquette mother form are formed.

【0006】この複合固形燃料は、褐炭、亜瀝青炭、瀝
青炭等の炭種にかかわらず広範囲の石炭を原料とするこ
とができ、特に低品位炭を利用した場合クリーン化の効
率が大であり、植物質原料には廃木材、バガスなどの有
効利用が可能であることから利用が期待されている。
This composite solid fuel can use a wide range of coal as a raw material regardless of the type of coal such as brown coal, sub-bituminous coal, and bituminous coal, and especially when low-grade coal is used, the efficiency of cleaning is high, Since it is possible to effectively use waste wood, bagasse, etc. for plant raw materials, it is expected to be used.

【0007】[0007]

【発明が解決しようとする課題】しかし、上記複合固形
燃料の原料、特に低品位炭では灰分が15〜30重量
%、硫黄が5〜8重量%と多く含むことから燃焼排ガス
中に硫黄酸化物が含まれ、大気中に放出されることから
環境汚染の原因となる等の不具合がある。
However, since the raw materials of the above-mentioned composite solid fuel, especially low-grade coal, contain a large amount of ash content of 15 to 30% by weight and sulfur content of 5 to 8% by weight, sulfur oxides are contained in the combustion exhaust gas. Since it is included in the air and is released into the atmosphere, there are problems such as causing environmental pollution.

【0008】従って本発明の目的は燃焼排ガス中の硫黄
酸化物の減少が得られる複合固形燃料の製法及び複合固
形燃料を提供することにある。
Accordingly, it is an object of the present invention to provide a method for producing a composite solid fuel and a composite solid fuel which can reduce sulfur oxides in flue gas.

【0009】[0009]

【課題を解決するための手段】上記目的を達成する本発
明の複合固形燃料の製法は、石炭粉末に植物質粉末を2
0〜25重量%混合した原料をロールプレスで圧縮成形
する複合固形燃料の製法において、上記原料中に石炭粉
末中に含有される硫黄に対するカルシウムのモル比が
1.0〜1.8の範囲になる量の消石灰を脱硫剤として
添加するものであり、複合固形燃料は、石炭粉末に植物
質粉末を20〜30重量%及び上記石炭粉末中に含有さ
れる硫黄に対するカルシウムのモル比が1.0〜1.8
の範囲の量の消石灰を混合した原料をロールプレスで圧
縮成形したものである。
A method for producing a composite solid fuel according to the present invention, which achieves the above-mentioned object, is a method in which coal powder is mixed with vegetable powder.
In a method for producing a composite solid fuel in which a raw material mixed with 0 to 25% by weight is compression molded by a roll press, the molar ratio of calcium to sulfur contained in the coal powder in the raw material is in the range of 1.0 to 1.8. The amount of slaked lime is added as a desulfurizing agent, and the composite solid fuel has a plant powder of 20 to 30% by weight in the coal powder and a molar ratio of calcium to sulfur contained in the coal powder of 1.0. ~ 1.8
The raw material mixed with slaked lime in the range of is compressed and molded by a roll press.

【0010】具体的には石炭を乾燥、粉砕して得た数m
m以下の石炭粉末に20〜25重量%の木材及びバガス
等を乾燥、粉砕して得た数mm以下の植物質粉末を混合
した原料に、石炭粉末中に含まれる硫黄に対するカルシ
ウムのモル比が1.0〜1.8の範囲になる量の消石灰
を脱硫剤として添加する。次にこの混合物を、外周面に
ブリケットの母形となるポケットを有する一対の対向す
るロールからなるブリケットマシーンと称するロールプ
レスで圧縮成形することで、例えばアーモンド形で容積
約4cm3 の複合固形燃料のブリケットを製造する。
Concretely, several meters obtained by drying and crushing coal
A raw material obtained by mixing 20 to 25% by weight of wood, bagasse, and the like with coal powder of m or less and plant powder of several mm or less obtained by pulverizing the powder has a molar ratio of calcium to sulfur contained in the coal powder. Slaked lime is added as a desulfurizing agent in an amount in the range of 1.0 to 1.8. Next, this mixture is compression-molded by a roll press called a briquette machine consisting of a pair of opposed rolls having pockets that form a briquette matrix on the outer peripheral surface, and is, for example, an almond-shaped composite solid fuel having a volume of about 4 cm 3. Manufacture briquette of.

【0011】本発明によるこのような製法によって得ら
れた複合固形燃料にあっては、燃焼過程でカルシウムと
硫黄とが反応して燃焼灰中に原料中の硫黄の約80重量
%が固定化され、燃焼排ガス中に放出される硫黄酸化物
の大幅な低減が得られ、かつクリンカーの発生もない。
In the composite solid fuel obtained by such a production method according to the present invention, calcium and sulfur react in the combustion process and about 80% by weight of sulfur in the raw material is fixed in the combustion ash. A large reduction of sulfur oxides released in the combustion exhaust gas is obtained, and no clinker is generated.

【0012】次に試験例を示して本発明を詳述する。Next, the present invention will be described in detail by showing test examples.

【0013】この試験は、複合固形燃料の石炭中に含有
される硫黄量に応じた最適な消石灰の添加量を決定する
ために行われた。
This test was conducted in order to determine the optimum addition amount of slaked lime depending on the amount of sulfur contained in the coal of the composite solid fuel.

【0014】(1)複合固形燃料の製法 原料としての石炭および木材(桧、杉の混合品)を使用
し、その各元素分析値を表1に示す。石炭粉末(約3m
m以下)に木材粉末(約2mm以下)を20重量%混合
し、更に脱硫剤として消石灰を所定量添加したものをロ
ール径250mmのブリケットマシーンにより約300
HPa相当圧力で圧縮成形した。
(1) Method for producing composite solid fuel Coal and wood (mixture of cypress and cedar) are used as raw materials, and respective elemental analysis values are shown in Table 1. Coal powder (about 3m
m) and 20% by weight of wood powder (about 2 mm or less), and a predetermined amount of slaked lime added as a desulfurizing agent.
Compression molding was performed at a pressure equivalent to HPa.

【0015】 表1 灰分 炭素 水素 窒素 酸素 全硫黄 石炭粉末 11.36 72.99 4.82 1.05 7.88 2.15 木材粉末 0.81 52.10 6.14 0.10 40.82 0.04 全硫黄の値は灰分中の硫黄分を含むTable 1 Ash content Carbon Hydrogen Nitrogen Oxygen Total sulfur Coal powder 11.36 72.99 4.82 1.05 7.88 2.15 Wood powder 0.81 52.10 6.14 0.10 40.82 0.04 Total sulfur value includes sulfur content in ash

【0016】(2)燃焼排ガスの分析 300℃に加熱した電気炉(加熱部の長さ300mm)
に試料を封入した石英ガラス製の燃焼管(内径28m
m)をセットし、毎分約1.6リットルの空気を流しな
がら20分間加熱した後徐々に700℃まで昇温し、4
0分間燃焼させ燃焼生成したガスおよび余剰空気を全量
ガスバツクで補集し、ガス分析装置で二酸化硫黄を測定
した。
(2) Analysis of combustion exhaust gas Electric furnace heated to 300 ° C. (heating section length 300 mm)
Quartz glass combustion tube (inside diameter 28 m
m) is set, and while heating about 1.6 liters of air per minute for 20 minutes, the temperature is gradually raised to 700 ° C.
The gas produced by combustion by burning for 0 minutes and the surplus air were collected with a gas back, and sulfur dioxide was measured by a gas analyzer.

【0017】(3)試験結果 木材粉末の混合比20重量%の複合固形燃料で消石灰の
添加量を変化させて燃焼した結果、試料中の全硫黄S分
に対する消石灰中のカルシウムCaのモル比Ca/S比
と硫黄の固定化率は図1に示す結果が得られた。図1よ
り明らかなように消石灰の添加量がCa/S比1までは
直線状に上昇し、更にCa/S比が1.2付近で最も固
定化率が大きく、約80%に達し、更にCa/S比が
1.8以上では固定化率が約78%と略一定であり、脱
硫剤としての消石灰の添加量はCa/S比で1〜1.8
の範囲が効果的である。なお消石灰を添加しない場合に
は約28%の固定化率である。
(3) Test Results As a result of burning the mixed solid fuel having a mixing ratio of wood powder of 20% by weight while changing the addition amount of slaked lime, the molar ratio Ca of calcium Ca in slaked lime to total sulfur S content in the sample Ca The results shown in FIG. 1 were obtained for the / S ratio and the immobilization rate of sulfur. As is clear from FIG. 1, the amount of slaked lime added increases linearly up to a Ca / S ratio of 1, and the immobilization rate reaches the maximum when the Ca / S ratio is around 1.2, reaching about 80%. When the Ca / S ratio is 1.8 or more, the immobilization rate is approximately constant at about 78%, and the addition amount of slaked lime as a desulfurizing agent is 1 to 1.8 in terms of the Ca / S ratio.
The range of is effective. When slaked lime is not added, the immobilization rate is about 28%.

【0018】[0018]

【発明の効果】石炭粉末に20〜25重量%の植物質粉
末を混合した原料をロールプレスによって圧縮成形する
複合固形燃料の製法において石炭粉末中に含有する硫黄
に対してカルシウムのモル比が1.0〜1.8の範囲に
なる量の消石灰を脱硫剤として添加することにより効率
的に燃焼排ガス中の硫黄酸化物が減少でき、環境汚染の
悪化を大幅に回避することが可能であり、着火性が増
し、ばい煙も少なく、更にクリンカーの発生がないこと
から通気が維持され、燃焼効率の向上が得られる。
INDUSTRIAL APPLICABILITY In a method for producing a composite solid fuel in which a raw material obtained by mixing 20 to 25% by weight of plant powder with coal powder is compression-molded by a roll press, the molar ratio of calcium to sulfur contained in the coal powder is 1. It is possible to efficiently reduce the amount of sulfur oxides in the combustion exhaust gas by adding slaked lime in an amount in the range of 0.0 to 1.8 as a desulfurizing agent, and it is possible to largely avoid deterioration of environmental pollution. The ignitability is increased, soot and smoke are reduced, and since no clinker is generated, ventilation is maintained and combustion efficiency is improved.

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

【図1】Ca/S比と硫黄の固定化率の関係を示す図で
ある。
FIG. 1 is a diagram showing a relationship between a Ca / S ratio and a sulfur immobilization rate.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 石炭粉末に植物質粉末を20〜25重量
%混合した原料をロールプレスで圧縮成形する複合固形
燃料の製法において、上記原料中に石炭粉末中に含有さ
れる硫黄に対するカルシウムのモル比が1.0〜1.8
の範囲になる量の消石灰を脱硫剤として添加することを
特徴とする、石炭と植物質との複合固形燃料の製法。
1. A method for producing a composite solid fuel comprising compression-molding a raw material, which is obtained by mixing 20 to 25% by weight of plant powder with coal powder, by a roll press, in a molar amount of calcium to sulfur contained in the coal powder in the raw material. The ratio is 1.0 to 1.8
A method for producing a composite solid fuel of coal and plant matter, characterized in that slaked lime in an amount within the range is added as a desulfurizing agent.
【請求項2】 石炭粉末に植物質粉末を20〜30重量
%及び上記石炭粉末中に含有される硫黄に対するカルシ
ウムのモル比が1.0〜1.8の範囲の量の消石灰を混
合した原料をロールプレスで圧縮成形したことを特徴と
する、複合固形燃料。
2. A raw material obtained by mixing coal powder with 20 to 30% by weight of vegetable powder and slaked lime in an amount in the molar ratio of calcium to sulfur contained in the coal powder in the range of 1.0 to 1.8. A composite solid fuel, characterized by being compression-molded by a roll press.
JP9654092A 1992-04-16 1992-04-16 Production of composite solid fuel of coal with vegetable matter, and composite solid fuel Withdrawn JPH06184571A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP9654092A JPH06184571A (en) 1992-04-16 1992-04-16 Production of composite solid fuel of coal with vegetable matter, and composite solid fuel
CN 93102572 CN1042041C (en) 1992-04-16 1993-03-15 Process for manufacturing composite solid fuel from coal and vegetable material, and composite solid fuel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9654092A JPH06184571A (en) 1992-04-16 1992-04-16 Production of composite solid fuel of coal with vegetable matter, and composite solid fuel

Publications (1)

Publication Number Publication Date
JPH06184571A true JPH06184571A (en) 1994-07-05

Family

ID=14167945

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9654092A Withdrawn JPH06184571A (en) 1992-04-16 1992-04-16 Production of composite solid fuel of coal with vegetable matter, and composite solid fuel

Country Status (2)

Country Link
JP (1) JPH06184571A (en)
CN (1) CN1042041C (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103343028A (en) * 2013-07-16 2013-10-09 无锡市金盛助剂厂 Desulfurization assistant
JP2015030739A (en) * 2013-07-31 2015-02-16 三菱重工業株式会社 Coal for boiler fuel

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101134920B (en) * 2006-08-30 2010-05-12 河南理工大学 Biomass coal adhesive and biomass coal prepared by the same
CN101148622B (en) * 2007-11-02 2010-06-09 山西大学 Sandwich biomass briquette and producing method thereof
CN101812346A (en) * 2010-02-02 2010-08-25 邢淦琛 Method for forming biomass fuel

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103343028A (en) * 2013-07-16 2013-10-09 无锡市金盛助剂厂 Desulfurization assistant
JP2015030739A (en) * 2013-07-31 2015-02-16 三菱重工業株式会社 Coal for boiler fuel

Also Published As

Publication number Publication date
CN1077735A (en) 1993-10-27
CN1042041C (en) 1999-02-10

Similar Documents

Publication Publication Date Title
CN102260567B (en) Biomass molding fuel for sintering iron ore and application
CN1236027C (en) Process for preparing composite biomass briquettes
CN108003960B (en) Biomass fuel for iron ore sintering and preparation method and application thereof
CN109384225B (en) Method for producing desulfurization and denitrification active carbon
CN100496673C (en) Composite sulfur fixing agent
JPH06184571A (en) Production of composite solid fuel of coal with vegetable matter, and composite solid fuel
CN112408388A (en) Preparation method of activated coke with high denitration performance
WO2007089046A1 (en) Coal/biomass composite fuel
CN108865316A (en) The preparation method of biomass fuel applied to agglomeration for iron mine
CN108329970A (en) A kind of environment-friendly biomass fuel and preparation method
CN112500901A (en) Preparation method of anti-slagging biomass fuel
CN1268552A (en) Formed coal (coke) fuel with inflammable, water-proof and sulfur-fixng functions
JPH0768530B2 (en) Molded fuel manufacturing method
CN114657001B (en) Method for manufacturing composite fuel for sintering
CN1355278A (en) Composite adhesive for industrial briquettes
CN109022078B (en) Blending method of steady-state combustion biomass fuel
CN1013879B (en) Shaped coal of bituminous coal for combustion in boiler
CN115368945A (en) Briquette prepared from gasified fine slag, semi-coke powder and biomass binder and preparation method thereof
WO2023129090A2 (en) Method for using biomass in coking coal blend
JPH04335092A (en) Solid fuel
TR2021021747A1 (en) METHOD FOR USE OF BIOMASS IN COKE BLEND
CN1014425B (en) Method of preparing smokeless fuel by using ash of pulverized coal
JPH0365398B2 (en)
CN116144413A (en) Preparation method of biomass fuel for sintering
CN113845955A (en) Blast furnace coal powder combustion improver and preparation method and application thereof

Legal Events

Date Code Title Description
A300 Withdrawal of application because of no request for examination

Free format text: JAPANESE INTERMEDIATE CODE: A300

Effective date: 19990706