CN101560424A - Synthetic ammonia gas-production briquette and preparation method thereof - Google Patents

Synthetic ammonia gas-production briquette and preparation method thereof Download PDF

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Publication number
CN101560424A
CN101560424A CNA2009100744364A CN200910074436A CN101560424A CN 101560424 A CN101560424 A CN 101560424A CN A2009100744364 A CNA2009100744364 A CN A2009100744364A CN 200910074436 A CN200910074436 A CN 200910074436A CN 101560424 A CN101560424 A CN 101560424A
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CN
China
Prior art keywords
organic compound
compound binder
ammonia gas
stalk
naoh solution
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Pending
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CNA2009100744364A
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Chinese (zh)
Inventor
路广军
薛宝其
杨凤玲
李莹英
程芳琴
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Shanxi University
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Shanxi University
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Publication date
Application filed by Shanxi University filed Critical Shanxi University
Priority to CNA2009100744364A priority Critical patent/CN101560424A/en
Publication of CN101560424A publication Critical patent/CN101560424A/en
Pending legal-status Critical Current

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    • 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

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  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

The invention provides a synthetic ammonia gas-producing briquette, which is prepared from the following compositions by weight portion: 85 to 90 portions of pulverized anthracite and 10 to 15 portions of organic compound binder; and the organic compound binder is prepared from straws, humic acid and NaOH solution in a weight ratio of 2.5-5.5:6.5-15.5:82.0-88.0. The synthetic ammonia gas-producing briquette has wide raw material sources, low production cost, high activity and cold and heat intensity, reduces the burning point and smoke dust discharge amount due to addition of biomass, improves the burn-off rate and reduces the coal consumption of a ton of ammonia.

Description

A kind of synthesis ammonia gas preparation molded coal and preparation method thereof
Technical field
The present invention relates to moulded coal, specifically belong to a kind of synthesis ammonia gas preparation molded coal and preparation method thereof.
Background technology
The ammonia operation with coal based on the high-quality anthracite block coal because the anthracite block coal shortage of resources, on the high side.The at present feed coals that adopt moulded coal to do the ammonia operation of fertilizer plant more.Additive adopts sodium humate solution mostly, is pressed into coal briquette or coal rod through height again with pulverized anthracite mix, the system that stirs, macerates, and the oven dry fed to boiler uses.
The moulded coal shortcoming that above method is made is: degree of compactness height, active low, carbon residue rate height, ton ammonia coal consumption rate height.Thereby influence gas forming amount, improved production cost.
Technology contents
The object of the present invention is to provide a kind of active high, cost is low, the synthesis ammonia gas preparation molded coal of energy-conserving and environment-protective and preparation method thereof.
A kind of synthesis ammonia gas preparation molded coal provided by the invention, Ji following component is made by weight: pulverized anthracite 85-90, organic compound binder 10-15; Described organic compound binder be by stalk, humic acids and NaOH solution by weight 2.5-5.5: 6.5-15.5: 82.0-88.0 makes.
The preparation method of a kind of synthesis ammonia gas preparation molded coal provided by the invention comprises the steps:
(1) with the stalk natural air drying, cutting rolls to 2-3 centimetre, and pulverized anthracite is broken to below 3 millimeters;
(2) get the NaOH solution that stalk, humic acids and concentration are 1.5%-3.0% by weight 2.5-5.5: 6.5-15.5: 82.0-88.0, in reactor, add NaOH solution earlier, add stalk again, stir, heat up, when temperature rises to 90 ℃~95 ℃, add humic acids, react 40-60min down at 90 ℃~95 ℃ and make organic compound binder;
(3) in proportion organic compound binder is mixed with pulverized anthracite, stir, moulding, oven dry obtains highly active gas-making type coal product.
Compared with prior art, the invention has the advantages that:
The present invention makes organic compound binder through the NaOH solution modification simultaneously with biomass straw (corn or wheat stalk) and humic acids, can bring into play the advantage of biomass straw and Sodium salts humic acids simultaneously, produces highly active gas-making type coal.In the adhesive preparation process, biomass straw is processed into the strip of 2~3cm and through the NaOH solution modification, in moulded coal, can play the connection effect, improve moulded coal ultimate compression strength, the cavity that forms behind the biological matter straw burning in the moulded coal combustion processes can be beneficial to entering of oxygen, improved-type coal combustion effect promotes moulded coal perfect combustion more; Sodium salts humic acids with humic acids modification generation, it is a kind of water miscible binding agent, coal had very strong avidity, can wetting well coal grain surface, and infiltrate in the microvoid structure of coal, help to improve the moulded coal cold strength, Sodium salts humic acids also has the effect as sulphur capturing catalyst in the moulded coal combustion processes simultaneously.
In a word, the organic compound binder raw material that adopts among the present invention is cheap and easy to get, and production cost is low, not only can significantly improve the moulded coal reactive behavior, and moulded coal has hot and cold intensity height, the voidage height, and burning-point is low, gas forming amount height, characteristics such as the carbon residue rate is low.
Embodiment
Embodiment 1
Add 19.2 kilograms of concentration and be 1.8% NaOH solution in reactor as modification liquid, adds and stir behind 0.6 kilogram of stalk, when being warming up to 90 ℃, add 2.2 kilograms of humic acidss, it is standby to make organic compound binder after reacting 40min under 90 ℃ of conditions.With 8.5 kilograms of pulverized anthracites, 1.5 kilograms of aftershapings that stir of organic compound binder, 150 ℃ of oven dry down, the index of utilizing XY-01 type moulded coal pressure detecting instrument, CTM300 type intelligence electrothermal oven and PTC-2 type ash fusion point tester to detect finished product is:
Ultimate compression strength: 81kg/ ball, hot strength: 45kg/ ball, ash fusion point T 2: 1276 ℃.
Embodiment 2
In reactor, add 16.72 kilograms of concentration and be 2.5% NaOH solution as modification liquid, stir, heat up after adding 0.78 kilogram of stalk, when temperature rises to 95 ℃, add 2.5 kilograms of humic acid, it is standby to make organic compound binder behind reaction 50min under 95 ℃ of conditions.With 8.8 kilograms of pulverized anthracites, 1.2 kilograms of aftershapings that stir of organic compound binder, 150 ℃ of oven dry down, the index of utilizing XY-01 type moulded coal pressure detecting instrument, CTM300 type intelligence electrothermal oven and PTC-2 type ash fusion point tester to detect finished product is:
Ultimate compression strength: 86kg/ ball, hot strength: 42kg/ ball, ash fusion point T 2: 1305 ℃.
Embodiment 3
In reactor, add 17.6 kilograms of concentration and be 3.0% NaOH solution as modification liquid, stir, heat up after adding 1.0 kilograms of stalks, when temperature rises to 90 ℃, add 1.4 kilograms of humic acid, it is standby to make organic compound binder behind reaction 60min under 90 ℃ of conditions.With 8.6 kilograms of pulverized anthracites, 1.4 kilograms of aftershapings that stir of organic compound binder, 150 ℃ of oven dry down, the index of utilizing XY-01 type moulded coal pressure detecting instrument, CTM300 type intelligence electrothermal oven and PTC-2 type ash fusion point tester to detect finished product is:
Ultimate compression strength: 85kg/ ball, hot strength: 45kg/ ball, ash fusion point T 2: 1311 ℃.

Claims (2)

1, a kind of synthesis ammonia gas preparation molded coal is characterized in that, Ji following component is made by weight: pulverized anthracite 85-90, organic compound binder 10-15; Described organic compound binder be by stalk, humic acids and NaOH solution by weight 2.5-5.5: 6.5-15.5: 82.0-88.0 makes.
2, by the preparation method of the described a kind of synthesis ammonia gas preparation molded coal of claim 1, it is characterized in that comprising the steps:
(1) with the stalk natural air drying, cutting rolls to 2-3 centimetre, and pulverized anthracite is broken to below 3 millimeters;
(2) get the NaOH solution that stalk, humic acids and concentration are 1.5%-3.0% by weight 2.5-5.5: 6.5-15.5: 82.0-88.0, in reactor, add NaOH solution earlier, add stalk again, stir, heat up, when temperature rises to 90 ℃~95 ℃, add humic acids, react 40-60min down at 90 ℃~95 ℃ and make organic compound binder;
(3) in proportion organic compound binder is mixed with pulverized anthracite, stir, moulding, oven dry obtains product.
CNA2009100744364A 2009-05-20 2009-05-20 Synthetic ammonia gas-production briquette and preparation method thereof Pending CN101560424A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNA2009100744364A CN101560424A (en) 2009-05-20 2009-05-20 Synthetic ammonia gas-production briquette and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNA2009100744364A CN101560424A (en) 2009-05-20 2009-05-20 Synthetic ammonia gas-production briquette and preparation method thereof

Publications (1)

Publication Number Publication Date
CN101560424A true CN101560424A (en) 2009-10-21

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102899117A (en) * 2012-11-01 2013-01-30 华东理工大学 Slurry containing biomass and use thereof
CN103923719A (en) * 2014-04-08 2014-07-16 洪洞县利众生物质能源有限公司 Composite solid fuel
CN104877727A (en) * 2015-05-20 2015-09-02 陕西煤业化工技术研究院有限责任公司 Composite biomass briquette adhesive, and preparation method and application thereof
CN106085535A (en) * 2016-06-07 2016-11-09 北京神雾环境能源科技集团股份有限公司 A kind of moulded coal and preparation method thereof
CN106085537A (en) * 2016-06-07 2016-11-09 北京神雾环境能源科技集团股份有限公司 A kind of preparation method of briquette binder

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102899117A (en) * 2012-11-01 2013-01-30 华东理工大学 Slurry containing biomass and use thereof
CN103923719A (en) * 2014-04-08 2014-07-16 洪洞县利众生物质能源有限公司 Composite solid fuel
CN103923719B (en) * 2014-04-08 2015-11-18 洪洞县利众生物质能源有限公司 A kind of composite solid fuel
CN104877727A (en) * 2015-05-20 2015-09-02 陕西煤业化工技术研究院有限责任公司 Composite biomass briquette adhesive, and preparation method and application thereof
CN104877727B (en) * 2015-05-20 2018-07-13 陕西煤业化工技术研究院有限责任公司 A kind of complex biological matter briquette binder and its preparation method and application
CN106085535A (en) * 2016-06-07 2016-11-09 北京神雾环境能源科技集团股份有限公司 A kind of moulded coal and preparation method thereof
CN106085537A (en) * 2016-06-07 2016-11-09 北京神雾环境能源科技集团股份有限公司 A kind of preparation method of briquette binder

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Application publication date: 20091021