CN1053083A - A kind of additive for fire coal and using method thereof - Google Patents
A kind of additive for fire coal and using method thereof Download PDFInfo
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- CN1053083A CN1053083A CN 89105828 CN89105828A CN1053083A CN 1053083 A CN1053083 A CN 1053083A CN 89105828 CN89105828 CN 89105828 CN 89105828 A CN89105828 A CN 89105828A CN 1053083 A CN1053083 A CN 1053083A
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- additive
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Abstract
A kind of additive for fire coal and using method thereof, described additive for fire coal contain solid sulphur composition, oxidation catalysis composition and filler.Described solid sulphur composition is to contain calcium oxide, magnesian mineral or slag, the oxidation catalysis composition is the mineral (slag) that contain ferric oxide, Manganse Dioxide, filler is the mineral (slag) of silicon-dioxide, aluminium sesquioxide, and described oxide content sum accounts for more than 69% of gross weight.Above-mentioned additive for fire coal in use should be followed the ash content total amount must not be higher than 40% specified requirement.When using this additive for fire coal, can obtain good social benefit and economic benefit by the method for the present invention's regulation.
Description
The present invention relates to a kind of additive for fire coal, it belongs to for improving burns with additive to solid-fuelled processing class.
Except country few in number, exploitation, the utilization to carbonic solid fuels all shows more and more higher interest mostly in the world.In coal exploitation, utilizing, at first to solve and improve burning (comprise and improve actual thermal value and reduce exhaust emission) problem, secondly be adopt, waste effectively utilizes problem in the coal separation operation.In being seen all patents and non-Patent data so far, be solution basically for first problem.Special public clear 62-2139 has just announced a kind of low temperature (referring to be lower than 800 ℃) sweetening component that both contained as Japanese Patent, contains the compositions of additives of high-temperature desulfurization agent again.It is said and in the temperature range of broadness, to play excellent desulfurizing effect; The technical scheme that the special public clear 62-21400 of Japanese Patent then recommends to reduce with the byproduct manganese mud of making potassium permanganate CO content in the coal-fired flue-gas.And so on.
The objective of the invention is to properly settle and promote the incendiary problem, solve preferably again simultaneously mine, waste effectively utilizes problem in the coal separation.Because the contriver is having carried out successful trial (referring to Chinese patent 87102028.9) aspect the industrial furnace cinder introducing additive that fixed carbon content is reached more than 15%, so done certain basis like this.
The present invention relates to a kind of additive for fire coal of being made up of solid sulphur composition, oxidized form catalyst component and filler, described solid sulphur composition is to contain calcium oxide, magnesian mineral (slag).Described oxidized form catalyst component is the mineral (slag) that contain ferric oxide, Manganse Dioxide.Described filler is the mineral (slag) that contain silicon-dioxide, aluminium sesquioxide.These mineral (slag) have following characteristics when being combined into the present invention's additive for fire coal: the content sum of all metal oxides should account for more than 69% of additive gross weight; Wherein the amount of contained silicon-dioxide is the twice of calcium oxide content, also is the twice of aluminium sesquioxide amount; Magnesium oxide, ferric oxide, Manganse Dioxide content sum are 0,6~1,0 with the ratio of calcium oxide content; Manganse Dioxide content is the twice of ferric oxide amount at least, and iron oxide content is close with content of magnesia.Particularly, the proportioning of recommendation is as follows:
Calcium oxide 15~20(weight percent, down together)
Magnesium oxide 2~5
Aluminium sesquioxide 15~20
Ferric oxide 2~4
Manganse Dioxide 5~10
Silicon-dioxide 30~40
In order to reach purpose of the present invention, recommend with the waste of boiler cinder or coal stone or coal separation or be rich in Al
2O
3, SiO
2Other material as filler component; Recommendation with rhombspar, Wingdale, marble, chalk, magnesite, magnesia, talcum, monticellite etc. as solid sulphur composition; And the oxidized form catalyst component of recommending can comprise: the slag of refining ferromanganese blast furnace, bixbyite, garnet, fayalite, ferrodolomite, spathic iron ore etc.Wherein preferable combination has: boiler cinder or coal stone add rhombspar and add iron oxide red and add rich manganese slag or manganese mud; Boiler cinder or coal stone add calcination pyrite and add magnesite and add wilkinite and add calcium mineral (slag).For those volatile matters coal on the low side, the used preferably potassium permanganate of Manganse Dioxide composition that contains sometimes even will add and account for additive total amount 1~2,0% oxymuriate or nitrate, preferably adds oxymuriate.
In order to reach purpose of the present invention, the prescription of GPRS additive of the present invention not only, and should grasp the method for using this additive.The emphasis of this method is: this additive mixes that the ash oontent in the gained mixture should not be higher than 40% in the raw coal.The normal coal of every volatilization content, its thermal value be the above person of 5000 kilocalories/kg, sneaks into the ash oontent behind the additive, all can courageously take 40% this higher limit.It is very convenient that this " ash content total amount principle " uses, as to establish coal-fired ash content content be X
1, consumption Y
1, additive ash content content X
2, consumption is Y
2(all being weight percentage) is because Y
1+ Y
2=1, so mixture ash content total amount can be represented by the formula:
X
1Y
1+ X
2Y
2=X
1(1-Y
2)+X
2Y
2=0,4 thus formula can calculate additive amount Y
2:
Y
2=(0、4-X
1)÷(X
2-X
1)
X wherein
1Known, X
2Additive for given raw material is got on very well, and also can calculate out easily.Know X
1, X
2Just can obtain Y rapidly
2
If the ash oontent of raw coal has approached 40%, then mentioned above principle can not be used, and the adaptation of this moment is only to stay solid sulphur composition and oxidation catalysis composition in the additive, and consumption accounts for 10% of raw coal and gets final product.
Embodiment 1:
Get the boiler slag 5 minutes that contains fixed carbon 20%, 2 fens (compositions: calcium oxide 34,8%, magnesium oxide 6,34%, ferric oxide 5,78%, Manganse Dioxide 24,3%, silicon-dioxide 28% of manganese mud; 800 ℃ of following calcinations 15 minutes weightless 8,98%) rhombspar 0,88 minutes and iron oxide red 0,12 lease making fragmentations, mix after, make the additive for fire coal product, it is as follows to survey its component:
Silicon-dioxide 34,5(weight percent, down together)
Aluminium sesquioxide 18,75
Calcium oxide 16,81
Magnesium oxide 2,85
Manganse Dioxide 6,2
Ferric oxide 2,5
Carbon 12,5
Obviously, all metal oxide content sums 78,76% of this additive promptly are its ash oontent.The bituminous coal of getting ash content 25% mixes with it, by ash content total amount principle of the present invention, can determine that additive and bituminous coal should be by agent 0,27 minutes, 0,73 minutes mixed of coal.Produce 3 tons of propellant combinations.Examination was burnt 8 hours continuously on the 4 tons of shop-assembled boilers in certain chemical plant, and 2,827 tons of propellant combination consumptions steam 11,20 tons, promptly produce 1 ton of steam consumption propellant combination 252,4kg; Use the bituminous coal of thermal value 5050 kilocalories/kg under similarity condition, the consumption coal was 3,117 tons in continuous 8 hours, steamed 10,22 tons, promptly produced 1 ton of steam consumption coal 305kg.Two compare, and use additive for fire coal of the present invention, singly are one of ton steam coal conservations, just can be up to (305-252 * 73%) kg, promptly 120,75kg.From drawing two conclusions here at least: the one, additive for fire coal of the present invention can play the remarkable outstanding effect of improving combustion position when practical application, and oke exhaust blackness reduces obviously, and carbon content reduces over half in the deslagging; The 2nd, when correct use additive of the present invention, 58, the additive of 05kg can be equivalent to 110, the bituminous coal of 65kg (thermal value 5050 kilocalories/kg), and the production cost of additive of the present invention is starkly lower than the production cost of coal, and as seen how considerable its social benefit and economic benefit have.
Embodiment 2
With the coal separation waste residue in somewhere, Heilongjiang Province, rich manganese slag, peridotites and lime is raw material, and each expects that proportioning is that the powder additive that coal separation waste residue 80 minutes, manganese slag 10 minutes, peridotites 7.7 minutes, lime made in 2.3 minutes has following composition after tested:
Silicon-dioxide 30.00(weight percent, down together)
Aluminium sesquioxide 15.15
Calcium oxide 15.03
Magnesium oxide 2.17
Ferric oxide 2.38
Manganse Dioxide 5.02
It is about 25% to wait to mix the local coal ash content of this additive, and volatile content is approximately 20%, thermal value 5527 kilocalories/kg.According to ash content total amount principle of the present invention, as can be known should be by agent: coal=1: 2(be that additive accounts for 33,3%, and raw coal accounts for 66,7%) regulation preparation propellant combination.This propellant combination is burnt and burns and done contrast (operating time is continuous 16 hours) with the situation of raw coal in 6 tons of horizontal package boiler pilot scales in local paper mill, and the result is as follows:
Use propellant combination and use raw coal
Consume fuel 16490kg 17136kg
Tear open and close raw coal 10999kg 17136kg
Steam production 99,0T 99,45T
Coal vapour than 111,1kg/T vapour 172,31kg/T vapour
Coal saving rate 35,5%
Claims (3)
1, a kind of additive for fire coal of forming by solid sulphur composition, oxidized form catalyst component and filler, described solid sulphur composition is to contain calcium oxide, magnesian mineral (slag), described oxidized form catalyst component is the mineral (slag) that contain ferric oxide, Manganse Dioxide, described filler is the mineral (slag) that contain silicon-dioxide, aluminium sesquioxide, it is characterized in that:
The content sum of calcium oxide, magnesium oxide, ferric oxide, aluminium sesquioxide Manganse Dioxide and silicon-dioxide should account for more than 69% of additive total amount in a, the described additive;
The amount of contained silicon-dioxide is the twice of calcium oxide content in b, the additive, also is the twice of aluminium sesquioxide amount;
Magnesium oxide, ferric oxide, Manganse Dioxide content sum are 0,6~1,0 with the ratio of calcium oxide content in c, the described additive;
The content of Manganse Dioxide is the twice of iron oxide content at least in d, the additive, and iron oxide content is close with magnesian content.
2, additive for fire coal according to claim 1 is characterized in that, each oxide components has following proportioning:
Calcium oxide 15~20(weight percent, down together)
Magnesium oxide 2~5
Aluminium sesquioxide 15~20
Ferric oxide 2~4
Manganse Dioxide 5~10
Silicon-dioxide 30~40
3, the using method of a kind of additive for fire coal according to claim 1 is characterized in that the ash amount of controlling mixture makes it to be equal to or less than 40%.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 89105828 CN1053083A (en) | 1989-12-25 | 1989-12-25 | A kind of additive for fire coal and using method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 89105828 CN1053083A (en) | 1989-12-25 | 1989-12-25 | A kind of additive for fire coal and using method thereof |
Publications (1)
Publication Number | Publication Date |
---|---|
CN1053083A true CN1053083A (en) | 1991-07-17 |
Family
ID=4856476
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CN 89105828 Pending CN1053083A (en) | 1989-12-25 | 1989-12-25 | A kind of additive for fire coal and using method thereof |
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Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1056172C (en) * | 1994-01-14 | 2000-09-06 | 药朝辉 | Energy-saving desulfurizing decontaminating agent for coal |
CN1064994C (en) * | 1995-01-28 | 2001-04-25 | 西安正阳环保能源有限公司 | Sulfur-immobilizing coal-saving additive |
CN1099453C (en) * | 1998-12-30 | 2003-01-22 | 宝山钢铁股份有限公司 | Method of producing sulfur fixing agent for briquette |
GB2462978A (en) * | 2008-02-07 | 2010-03-03 | Internat Innovative Technologi | Fuel enrichment process |
CN102010765A (en) * | 2010-12-08 | 2011-04-13 | 济源麒福节能环保技术有限公司 | Formulated fuel and preparation process thereof |
CN102134521A (en) * | 2010-01-21 | 2011-07-27 | 泰山学院 | Method for producing sulfur-fixing agent and sulfur-fixing briquette by using waste dry battery |
CN102181317A (en) * | 2011-03-29 | 2011-09-14 | 王成新 | Desulfurizer produced by utilizing mineral waste material and preparation method thereof |
CN102604712A (en) * | 2012-03-20 | 2012-07-25 | 武汉理工大学 | Steel slag composite desulfurizer for desulfurizing pulverized coal during combustion and desulfurization method using same |
CN102703159A (en) * | 2012-05-29 | 2012-10-03 | 广州中兰鼎辉材料科技有限公司 | Coal-economizing sulfur-solidifying and denitrification additive for coal |
CN101386785B (en) * | 2008-10-24 | 2012-11-14 | 中国科学院山西煤炭化学研究所 | Desulphurizer for high-sulphur coal coke making and preparation method and applications |
CN103160356A (en) * | 2011-12-19 | 2013-06-19 | 湖南晟通科技集团有限公司 | Integration fire coal additive of combustion supporting, sulfur fixation, denitration and decoking, preparation method thereof and application thereof |
CN103242929A (en) * | 2013-05-10 | 2013-08-14 | 叶绍朋 | Low calorific value blind coal prepared from sludge of domestic sewage treatment plant, and production technology and catalyst thereof |
-
1989
- 1989-12-25 CN CN 89105828 patent/CN1053083A/en active Pending
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1056172C (en) * | 1994-01-14 | 2000-09-06 | 药朝辉 | Energy-saving desulfurizing decontaminating agent for coal |
CN1064994C (en) * | 1995-01-28 | 2001-04-25 | 西安正阳环保能源有限公司 | Sulfur-immobilizing coal-saving additive |
CN1099453C (en) * | 1998-12-30 | 2003-01-22 | 宝山钢铁股份有限公司 | Method of producing sulfur fixing agent for briquette |
GB2462978A (en) * | 2008-02-07 | 2010-03-03 | Internat Innovative Technologi | Fuel enrichment process |
GB2462978B (en) * | 2008-02-07 | 2011-07-13 | Internat Innovative Technologies Ltd | Fuel enrichment process |
CN101386785B (en) * | 2008-10-24 | 2012-11-14 | 中国科学院山西煤炭化学研究所 | Desulphurizer for high-sulphur coal coke making and preparation method and applications |
CN102134521B (en) * | 2010-01-21 | 2013-10-16 | 泰山学院 | Method for producing sulfur-fixing agent and sulfur-fixing briquette by using waste dry battery |
CN102134521A (en) * | 2010-01-21 | 2011-07-27 | 泰山学院 | Method for producing sulfur-fixing agent and sulfur-fixing briquette by using waste dry battery |
CN102010765A (en) * | 2010-12-08 | 2011-04-13 | 济源麒福节能环保技术有限公司 | Formulated fuel and preparation process thereof |
CN102181317A (en) * | 2011-03-29 | 2011-09-14 | 王成新 | Desulfurizer produced by utilizing mineral waste material and preparation method thereof |
CN103160356B (en) * | 2011-12-19 | 2016-05-25 | 湖南晟通科技集团有限公司 | Integrated additive for fire coal of combustion-supporting solid sulfide denitration decoking and its preparation method and application |
CN103160356A (en) * | 2011-12-19 | 2013-06-19 | 湖南晟通科技集团有限公司 | Integration fire coal additive of combustion supporting, sulfur fixation, denitration and decoking, preparation method thereof and application thereof |
CN102604712A (en) * | 2012-03-20 | 2012-07-25 | 武汉理工大学 | Steel slag composite desulfurizer for desulfurizing pulverized coal during combustion and desulfurization method using same |
CN102604712B (en) * | 2012-03-20 | 2014-12-03 | 武汉理工大学 | Steel slag composite desulfurizer for desulfurizing pulverized coal during combustion and desulfurization method using same |
CN102703159A (en) * | 2012-05-29 | 2012-10-03 | 广州中兰鼎辉材料科技有限公司 | Coal-economizing sulfur-solidifying and denitrification additive for coal |
CN103242929A (en) * | 2013-05-10 | 2013-08-14 | 叶绍朋 | Low calorific value blind coal prepared from sludge of domestic sewage treatment plant, and production technology and catalyst thereof |
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