CN101967415B - Method for preparing coal-based fuel carbon - Google Patents

Method for preparing coal-based fuel carbon Download PDF

Info

Publication number
CN101967415B
CN101967415B CN 201010542089 CN201010542089A CN101967415B CN 101967415 B CN101967415 B CN 101967415B CN 201010542089 CN201010542089 CN 201010542089 CN 201010542089 A CN201010542089 A CN 201010542089A CN 101967415 B CN101967415 B CN 101967415B
Authority
CN
China
Prior art keywords
coal
percent
based fuel
fuel carbon
carbon
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 - Fee Related
Application number
CN 201010542089
Other languages
Chinese (zh)
Other versions
CN101967415A (en
Inventor
黄光许
刘全润
马名杰
张传祥
邢宝林
秦欣欣
黄山秀
夏浩
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.)
Henan University of Technology
Original Assignee
Henan University of Technology
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 Henan University of Technology filed Critical Henan University of Technology
Priority to CN 201010542089 priority Critical patent/CN101967415B/en
Publication of CN101967415A publication Critical patent/CN101967415A/en
Application granted granted Critical
Publication of CN101967415B publication Critical patent/CN101967415B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

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

Landscapes

  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

The invention discloses a method for preparing coal-based fuel carbon, which comprises the following steps of: a, taking the following components in percentage by mass: 80 to 95 percent of bituminous coal, 0 to 10 percent of crop straw and 4 to 10 percent of organic binder, uniformly mixing, and adding a proper amount of water for uniform mixing; b, pressing materials obtained in the step a into spheroids on a molding machine, and naturally airing the obtained green pellets; and c, putting the naturally aired green pellets into a carbonization furnace, carbonizing at the temperature of between 400 and 700 DEG C for 980 to 120 minutes, and cooling to prepare the coal-based fuel carbon. The coal-based fuel carbon has the advantages of cheap and readily available raw materials, low cost, effective utilization of biomass energy, the compressive strength of the prepared fuel carbon product of 25kg/piece, 75 percent of fixed carbon, 10 percent of volatile matter, 10 percent of ash content, 6,500 kilocalorie/kg of heat value, 0.4 percent of sulfur content, easy ignition, fire resistance, complete combustion, no smoke, no spark or smoke dust, high furnace surface temperature, high stability, and no collapse or break in the combustion process.

Description

A kind of making method of coal-based fuel carbon
Technical field
The present invention relates to a kind of fuel, relate to specifically a kind of making method of coal-based fuel carbon.
Background technology
In recent years, increasing to the demand as the various fuel carbons of heating and food and drink fuel both at home and abroad, along with the protection increasing of country to the forest reserves, the former char yield take natural forest as raw material constantly descends.Machine-made charcoal is the substitute products of charcoal, has density large, and calorific value is high, smokeless, tasteless, pollution-free, do not explode, the advantage such as inflammable, be the Green Product of generally acknowledging in the world, current throughput even can not meet the market requirement.Machine-made carbon is take forest and agricultural biomass such as sawdust, stalks as raw material, processes through operations such as super-dry, plasticizing forming, charing, cooling, packings.Plasticizing forming is to utilize the contained xylogen of biomass self cohesiveness that (140-280 ℃) produces when being heated, and adopts the screw extruding forming technique, makes the grain formings such as wood chip under certain pressure; Charing is the pyrolytic process of wood chip rod in kiln of moulding, finally obtains machine-made carbon, simultaneously recyclable inflammable gas and wood vinegar.
The problem of machine-made carbon industry existence at present is that the screw extruding forming technique yields poorly, energy consumption is high, the consumable accessory life-span is short, ingredient requirement is harsh; In addition, the production of machine-made carbon is difficult to obtain continuous and sufficient raw material supply.
Summary of the invention
Purpose of the present invention provides a kind of making method of coal-based fuel carbon just for existing weak point in above-mentioned prior art.
Purpose of the present invention can realize by following technique measures:
The making method of coal-based fuel carbon of the present invention comprises the steps:
A, get bituminous coal 80 ~ 95, agricultural crop straw 0 ~ 10 and organic binder bond 4 ~ 10 in mass ratio, after puddling evenly, add appropriate moisture again to mix thoroughly;
B, the resulting material of step a is pressed into spheroplast on forming machine, afterwards the gained green-ball is dried in air naturally;
C, will put into charring furnace through the green-ball that naturally dries, be 400~700 ℃ in temperature, and carbonization time is to carry out charing under the condition of 90min~120min, then through cooling coal-based fuel carbon.
The granularity of bituminous coal described in the present invention is less than 3mm; Described agricultural crop straw is to be crushed to particle diameter less than 3mm with pulverizer after natural air drying; Described organic binder bond is Sodium salts humic acids; The moisture 14-16% of material before moulding.
Forming machine described in the present invention is roller briquetting machine commonly used in moulded coal industry.
Carbonization time described in the present invention contains the heating-up time.
Beneficial effect of the present invention is as follows:
Coal-based fuel carbon of the present invention is take bituminous coal and agricultural crop straw as main raw material, and is cheap and easy to get, adds the combustioncharacteristics that agricultural crop straw can effectively utilize biomass energy, improve the fuel carbon product.Material forming is selected roller briquetting machine, and output is high, energy consumption is low, equipment attrition is little.Carbonization temperature is low, the time is short, energy consumption is little.Gained coal-based fuel carbon product physical strength is high, ultimate compression strength〉25kg/; Fixed carbon〉75%; Fugitive constituent〉10%; Ash<10%; Calorific value〉7000 kilocalories/Kg; Easily igniting, anti-burning, burning are complete, smoke smell free, high without Mars flue dust, stove table temperature.
Embodiment
The present invention is further described below with reference to embodiment:
Embodiment 1
Get granularity less than 3mm bituminous coal, granularity is mixed according to the mass ratio of 85:10:5 less than 3mm agricultural crop straw and Sodium salts humic acids and mixed thoroughly after the natural wind dry doubling is pulverized, total mass is 5kg, adds water and again mixes thoroughly, and the material total moisture is controlled at 14-16%; With the moulding on roller briquetting machine of above-mentioned material, the gained green-ball dries in air naturally; The charing in charring furnace of green-ball through drying, carbonization temperature are 600 ℃, and carbonization time is that 100min(contains the heating-up time), then through the cooling coal-based fuel carbon that gets.Gained coal-based fuel carbon product physical strength is high, ultimate compression strength 35kg/; Moisture 1.8%; Fixed carbon 83.5%; Fugitive constituent 7%; Ash 7.7 %; 7180 kilocalories/Kg of calorific value; Sulphur content 0.31%.
Embodiment 2
Get granularity less than 3mm bituminous coal, granularity is mixed according to the mass ratio of 82:10:8 less than 3mm and Sodium salts humic acids and mixed thoroughly after the natural wind dry doubling is pulverized, total mass is 5kg, adds water and again mixes thoroughly, and the material total moisture is controlled at 14-16%; With the moulding on roller briquetting machine of above-mentioned material, the gained green-ball dries in air naturally.The charing in charring furnace of green-ball through drying, carbonization temperature are 700 ℃, and carbonization time is that 120min(contains the heating-up time), then through the cooling coal-based fuel carbon that gets.Gained coal-based fuel carbon product physical strength is high, ultimate compression strength 30kg/; Moisture 2.0%; Fixed carbon 82.1%; Fugitive constituent 8.3%; Ash 6.8%; 7088 kilocalories/Kg of calorific value; Sulphur content 0.35%.
Embodiment 3
Get granularity and mix thoroughly according to the mass ratio mixing of 94:6 less than 3mm bituminous coal and Sodium salts humic acids, total mass is 5kg, adds water and again mixes thoroughly, and the material total moisture is controlled at 14-16%; With the moulding on roller briquetting machine of above-mentioned material, the gained green-ball dries in air naturally; The charing in charring furnace of green-ball through drying, carbonization temperature are 500 ℃, and carbonization time is that 90min(contains the heating-up time), then through the cooling coal-based fuel carbon that gets.Gained coal-based fuel carbon product physical strength is high, ultimate compression strength 28kg/; Moisture 1.9%; Fixed carbon 84%; Fugitive constituent 6.5%; Ash 7.6%; 7178 kilocalories/Kg of calorific value; Sulphur content 0.33%.

Claims (2)

1. the making method of a coal-based fuel carbon, it is characterized in that: described method comprises the steps:
A, get 4 ~ 10 parts of 0 ~ 10 part, 80 ~ 95 parts, bituminous coal, agricultural crop straw and organic binder bonds in mass ratio, after puddling evenly, add appropriate moisture again to mix thoroughly; Wherein: described bituminous coal granularity is less than 3mm; Described agricultural crop straw is to be crushed to particle diameter less than 3mm with pulverizer after natural air drying; Described organic binder bond is Sodium salts humic acids; Before moulding, the moisture of material is 14-16%;
B, the resulting material of step a is pressed into spheroplast on forming machine, afterwards the gained green-ball is dried in air naturally;
C, will put into charring furnace through the green-ball that naturally dries, be 400~700 ℃ in temperature, and carbonization time is to carry out charing under the condition of 90min~120min, then through cooling coal-based fuel carbon; And described carbonization time contains the heating-up time.
2. making method according to claim 1 is characterized in that: described forming machine is roller briquetting machine commonly used in moulded coal industry.
CN 201010542089 2010-11-13 2010-11-13 Method for preparing coal-based fuel carbon Expired - Fee Related CN101967415B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201010542089 CN101967415B (en) 2010-11-13 2010-11-13 Method for preparing coal-based fuel carbon

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201010542089 CN101967415B (en) 2010-11-13 2010-11-13 Method for preparing coal-based fuel carbon

Publications (2)

Publication Number Publication Date
CN101967415A CN101967415A (en) 2011-02-09
CN101967415B true CN101967415B (en) 2013-06-26

Family

ID=43546641

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201010542089 Expired - Fee Related CN101967415B (en) 2010-11-13 2010-11-13 Method for preparing coal-based fuel carbon

Country Status (1)

Country Link
CN (1) CN101967415B (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102925178B (en) * 2012-10-19 2013-12-18 西安建筑科技大学 Method for preparing iron alloy, calcium carbide and formed coke for gasification industry from low-metamorphic powdered coal
CN103466616B (en) * 2013-08-23 2015-11-04 宁夏宝塔石化科技实业发展有限公司 The preparation method of coal mass active carbon is reclaimed for organic solvent
CN105316013B (en) * 2014-07-31 2018-03-09 宝山钢铁股份有限公司 A kind of method that coal production coke in part is substituted using wood chip
CN104694191B (en) * 2014-12-09 2017-04-19 山东大学 Gas-containing coal similar material and preparation method thereof
CN104962334B (en) * 2015-06-16 2017-11-10 中南大学 A kind of agglomeration for iron mine biomass char hybrid fuel
CN106190410A (en) * 2016-08-24 2016-12-07 太湖县享有新能源有限责任公司 A kind of straw biomass rod of combustion-supporting type desulfurization and preparation method thereof

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1337441A (en) * 2001-09-03 2002-02-27 李志远 Metallurgical coke briquette
CN1560195A (en) * 2004-03-12 2005-01-05 李玉林 Production method of formed coke using coking powder as row-material and special formed coke furnace
CN101139537A (en) * 2007-10-09 2008-03-12 赵宜文 High-temperature casting molded coal and method for producing the same
CN101550372A (en) * 2009-05-16 2009-10-07 山西中元煤洁净技术有限公司 Method for producing carbonized coal with coal material

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54146803A (en) * 1978-05-10 1979-11-16 Nippon Kokan Kk <Nkk> Production of metallurgical briquette coke

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1337441A (en) * 2001-09-03 2002-02-27 李志远 Metallurgical coke briquette
CN1560195A (en) * 2004-03-12 2005-01-05 李玉林 Production method of formed coke using coking powder as row-material and special formed coke furnace
CN101139537A (en) * 2007-10-09 2008-03-12 赵宜文 High-temperature casting molded coal and method for producing the same
CN101550372A (en) * 2009-05-16 2009-10-07 山西中元煤洁净技术有限公司 Method for producing carbonized coal with coal material

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
JP昭54-146803A 1979.11.16

Also Published As

Publication number Publication date
CN101967415A (en) 2011-02-09

Similar Documents

Publication Publication Date Title
CN101967415B (en) Method for preparing coal-based fuel carbon
JP4130826B2 (en) Method for producing molded charcoal for fuel
CN103937574B (en) A kind of biomass granule fuel
CN102020274A (en) New process for producing straw active carbon once by utilizing physical activation method
CN104528717B (en) Preparation method of briquetted active carbon
Zhang et al. Torrefaction of cultivation residue of Auricularia auricula-judae to obtain biochar with enhanced fuel properties
CN103275783B (en) Pure biomass barbecue charcoal and manufacturing method thereof
CN101629083A (en) Treatment method of wood processing residues and charcoal prepared thereby
CN104629782A (en) Production process of machine-made charcoal
CN105062601A (en) Preparation method and system for green carbon containing biomass
CN103131442B (en) Preparing method for high-calorific-value charcoal
KR101308397B1 (en) Preparation method of wood solid-fuel having high heating value by semi-carbonization at low temperature
KR100365069B1 (en) The method of making charcoal using calm charcoal powder
CN101824348B (en) Method for preparing biomass compact fuel with rubber seed hull
CN103525497A (en) Environment-friendly novel process for recycling and comprehensively utilizing machine-made wood charcoal and waste heat
CN104946337A (en) Method for producing biomass forming carbon
CN101899344A (en) Biomass compound coal for tobacco flue-curing and preparation method thereof
CN101440294A (en) Coke production process
CN106085544A (en) A kind of composite biomass fuel and processing technique thereof
KR101069112B1 (en) Solid biomass fuel manufacturing method
KR102180572B1 (en) Method for manufacturing formed charcoal using semi-carbonized wood powder and formed charcoal manufactured thereby
CN102206525A (en) Method for preparing biomass fuels by domestic fungus residue
CN112938972A (en) Production method of coal-based molded activated carbon integrated with carbon activation
CN105670662A (en) Environment-friendly charcoal and preparing method thereof
Murni et al. The effect of pyrolysis temperature on charcoal briquettes from biomass waste

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130626

Termination date: 20161113