CN106701022A - Raise dust inhibitor with function of catalyzing coal combustion and preparation method thereof - Google Patents
Raise dust inhibitor with function of catalyzing coal combustion and preparation method thereof Download PDFInfo
- Publication number
- CN106701022A CN106701022A CN201611024071.0A CN201611024071A CN106701022A CN 106701022 A CN106701022 A CN 106701022A CN 201611024071 A CN201611024071 A CN 201611024071A CN 106701022 A CN106701022 A CN 106701022A
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- China
- Prior art keywords
- components
- coal
- inhibiting agent
- fugitive dust
- water vapor
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- Pending
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- 239000000428 dust Substances 0.000 title claims abstract description 34
- 239000003245 coal Substances 0.000 title claims abstract description 31
- 238000002360 preparation method Methods 0.000 title claims abstract description 7
- 239000003112 inhibitor Substances 0.000 title abstract 5
- 238000009841 combustion method Methods 0.000 title description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 238000010521 absorption reaction Methods 0.000 claims abstract description 11
- 238000002485 combustion reaction Methods 0.000 claims abstract description 10
- 230000000694 effects Effects 0.000 claims abstract description 10
- 239000003795 chemical substances by application Substances 0.000 claims description 20
- 230000002401 inhibitory effect Effects 0.000 claims description 19
- 238000003756 stirring Methods 0.000 claims description 15
- 238000006555 catalytic reaction Methods 0.000 claims description 12
- 210000003298 dental enamel Anatomy 0.000 claims description 5
- JLRJWBUSTKIQQH-UHFFFAOYSA-K lanthanum(3+);triacetate Chemical compound [La+3].CC([O-])=O.CC([O-])=O.CC([O-])=O JLRJWBUSTKIQQH-UHFFFAOYSA-K 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- VHSHLMUCYSAUQU-UHFFFAOYSA-N 2-hydroxypropyl methacrylate Chemical class CC(O)COC(=O)C(C)=C VHSHLMUCYSAUQU-UHFFFAOYSA-N 0.000 claims description 4
- 229920000858 Cyclodextrin Polymers 0.000 claims description 4
- 239000001116 FEMA 4028 Substances 0.000 claims description 4
- WHGYBXFWUBPSRW-FOUAGVGXSA-N beta-cyclodextrin Chemical compound OC[C@H]([C@H]([C@@H]([C@H]1O)O)O[C@H]2O[C@@H]([C@@H](O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O3)[C@H](O)[C@H]2O)CO)O[C@@H]1O[C@H]1[C@H](O)[C@@H](O)[C@@H]3O[C@@H]1CO WHGYBXFWUBPSRW-FOUAGVGXSA-N 0.000 claims description 4
- 235000011175 beta-cyclodextrine Nutrition 0.000 claims description 4
- 229960004853 betadex Drugs 0.000 claims description 4
- VGBWDOLBWVJTRZ-UHFFFAOYSA-K cerium(3+);triacetate Chemical compound [Ce+3].CC([O-])=O.CC([O-])=O.CC([O-])=O VGBWDOLBWVJTRZ-UHFFFAOYSA-K 0.000 claims description 4
- 229920000642 polymer Polymers 0.000 claims description 4
- 238000013019 agitation Methods 0.000 claims description 2
- 239000004094 surface-active agent Substances 0.000 claims description 2
- 238000010792 warming Methods 0.000 claims description 2
- 238000007084 catalytic combustion reaction Methods 0.000 abstract 2
- 238000005507 spraying Methods 0.000 abstract 2
- 230000005764 inhibitory process Effects 0.000 abstract 1
- 238000002791 soaking Methods 0.000 abstract 1
- 238000009736 wetting Methods 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 3
- 239000000843 powder Substances 0.000 description 2
- 229920000881 Modified starch Polymers 0.000 description 1
- 239000004368 Modified starch Substances 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- HRXZUGNDGULQSA-UHFFFAOYSA-N acetic acid;cerium Chemical compound [Ce].CC(O)=O.CC(O)=O.CC(O)=O HRXZUGNDGULQSA-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000002817 coal dust Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000006253 efflorescence Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 230000010534 mechanism of action Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 235000019426 modified starch Nutrition 0.000 description 1
- 206010037844 rash Diseases 0.000 description 1
- 231100000241 scar Toxicity 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000001629 suppression Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K3/00—Materials not provided for elsewhere
- C09K3/22—Materials not provided for elsewhere for dust-laying or dust-absorbing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/04—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing carboxylic acids or their salts
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/07—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases in which combustion takes place in the presence of catalytic material
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
The present invention discloses a raise dust inhibitor with a function of catalyzing coal combustion and a preparation method thereof, and is dedicated to water vapor absorption components for coal storage sites of thermoelectric enterprises. The raise dust inhibitor consists of the following components in percentages by weight: 20-30% of catalytic combustion components, 20-30% of water vapor absorption components, 1-2% of soaking and wetting components, and the balanced being water. By spraying the products on coal yards, the raise dust inhibitor can maintain significant dust inhibition effects within 30 days. After spraying the products, during the combustion of the coal and under the effects of the catalytic combustion components, the raise dust inhibitor can at the same time realize the effect of reducing the coal consumption.
Description
Technical field
The invention belongs to energy-conserving and environment-protective technical fiel, more particularly to a kind of airborne dust to coal with catalysis combustion function presses down
Preparation.
Background technology
China is the energy resource structure based on coal electricity, and domestic each place all has substantial amounts of Thermal Power Enterprises, single fire at present
Electric enterprise is owned by the large-scale indoor coal storage yard or coal open storage ground of oneself.With the passage of coal storage time, coal progressively wind
Change, efflorescence, ultimately cause dust pollution.
Fugitive dust inhibiting agent primarily occur ins the countries such as English, U.S., and with progressively tightening up for Environmental Protection in China requirement, the country was in recent years
Start such product occur.Domestic existing Fugitive dust inhibiting agent technology, is film forming Fugitive dust inhibiting agent, i.e., by modified starch
Deng material, one layer of solid film is formed to reach the purpose for suppressing to form by being covered in dust surface.Such as Chinese patent
CN201410257710.2, is sprayed on product coal, Hui Chang surfaces can be made to form one layer of cured film at miberal powder accumulation, to reduce
The pollution and airborne dust loss in storage, transportation to surrounding enviroment such as coal, miberal powder.
As Chinese society develops, environment protection requirement is necessarily improved year by year.In view of China's fire coal contact scar weather is tight
High property, cleaning for coal is further urgent using requiring.
The content of the invention
In order to overcome the shortcomings of the presence of prior art, primary and foremost purpose of the invention is to provide a kind of with catalysis coal
Fugitive dust inhibiting agent of combustion and preparation method thereof.
The purpose of the present invention is achieved through the following technical solutions:A kind of airborne dust with catalysis coal burning effect suppresses
Agent.The Fugitive dust inhibiting agent is made up of the component of following part by weight:Catalysis combustion components 20~30%, water vapor absorption group
Divide 20~30%, be impregnated with moistening components 1~2%, water for surplus.Wherein, above-mentioned catalysis combustion components are lanthanum acetate and acetic acid
Cerium, weight ratio is 1:1;The water vapor absorption component is MW=800~1000 modified HPMA and MW=1000~
One kind of 2000 beta cyclo dextrin polymers or its mixture;The moistening components that are impregnated with are for the fast T in commercial surfactant.
Present invention also offers the preparation method of above-mentioned Fugitive dust inhibiting agent, comprise the following steps:(1) add in enamel still
Enter the water of surplus, be warming up to 70 DEG C;(2) then under agitation, it is slowly added to be catalyzed combustion components, stirring is to complete molten;(3) stir
Lower addition water vapor absorption component, keeps being stirred 20-40 minutes at a temperature of 70 DEG C of system;(4) it is eventually adding and is impregnated with moistening components
Afterwards, stir 0.5-1 minutes and stop.
It is of the invention compared with existing Fugitive dust inhibiting agent technology, its significant advantage is:(1) Fugitive dust inhibiting agent of the invention
Not only there is good suppression airborne dust to act on to the dump in Coal Yard, while having the effect of catalysis burning, energy to coal
Enough beginning burning-points and all burnt for substantially reducing coal.(2) the Fugitive dust inhibiting agent mechanism of action of the invention is different from existing commercially available
Fugitive dust inhibiting agent, i.e., by dust surface cure membrane formation mechanism.Water vapor absorption component of the invention can be with absorption air
Steam, and moisture is latched in intramolecule for a long time, keep the wet of dust surface in the case where moistening components synergy is impregnated with
Profit, prevents airborne dust from occurring.
Specific embodiment
With reference to specific embodiment, the present invention is further illustrated.
Embodiment 1
590 kilograms of water is added in the enamel still of 2L, 70 DEG C are steam heated to;Stirring is opened, 200 kilograms are slowly added to
Lanthanum acetate, stirring is to complete molten;It is subsequently added MW200 kilograms of=2000 modified HPMA, at a temperature of 70 DEG C of system of holding
Stirring 30 minutes;13 kilograms of fast T is eventually adding, is stirred 1 minute and is stopped.
Embodiment 2
590 kilograms of water is added in the enamel still of 2L, 70 DEG C are steam heated to;Stirring is opened, 200 kilograms are slowly added to
Cerous acetate, stirring is to complete molten;It is subsequently added MW=1,000 300 kilograms of beta cyclo dextrin polymers, stir at a temperature of 70 DEG C of holding system
Mix 30 minutes;15 kilograms of fast T is eventually adding, is stirred 1 minute and is stopped.
Embodiment 3
590 kilograms of water is added in the enamel still of 2L, 70 DEG C are steam heated to;Stirring is opened, 150 kilograms are slowly added to
Cerous acetate and 150 kilograms of lanthanum acetates, stirring is to complete molten;It is subsequently added MW=1,000 100 kilograms of modified HPMA, MW=
2000 100 kilograms of beta cyclo dextrin polymers, keep being stirred 30 minutes at a temperature of 70 DEG C of system;20 kilograms of fast T is eventually adding, is stirred
Mix stopping in 1 minute.
Embodiment 4
By weight 1 during Fugitive dust inhibiting agent of the invention and enterprise are reclaimed:300 are diluted, and are sprayed after stirring
In in power plant's indoor coal storage yard, surface is carried out to dump with 0.3MPa wind-force using air blower daily in 30 days according to enterprise requirements and is blown
Sweep, surface maintains Shu Run, kicked up without obvious coal dust.
Embodiment 5
By enterprise practical application attestation, in the case where the primary operating parameter the same terms such as boiler load are kept, this hair is sprayed
Coal after bright reduces by 2% in beginning burning-point with all decline, the coal consumption of ton steam mark is burnt.
| Beginning burning-point | Burn a little | Ton steam mark coal consumption | |
| Not plus Fugitive dust inhibiting agent of the present invention | 392℃ | 712℃ | 126.0kg |
| Addition Fugitive dust inhibiting agent of the present invention | 372℃ | 652℃ | 123.5kg |
Claims (5)
1. a kind of Fugitive dust inhibiting agent with catalysis coal burning effect, it is characterised in that by catalysis combustion components lanthanum acetate and
Cerous acetate, water vapor absorption component, be impregnated with moistening components and water composition, wherein each component is accounted for:Catalysis
Combustion components 20~30%, water vapor absorption component 20~30%, moistening components 1~2%, water are impregnated with for surplus.
2. it is according to claim 1 a kind of with the Fugitive dust inhibiting agent for being catalyzed coal burning effect, it is characterised in that described
Catalysis combustion components are lanthanum acetate and cerous acetate, and weight ratio is 1:1.
3. it is according to claim 1 a kind of with the Fugitive dust inhibiting agent for being catalyzed coal burning effect, it is characterised in that described
Water vapor absorption component is:MW=800~1000 modified HPMA and MW=1000~2000 beta cyclo dextrin polymers
A kind of or its mixture.
4. it is according to claim 1 a kind of with the Fugitive dust inhibiting agent for being catalyzed coal burning effect, it is characterised in that described
Moistening components are impregnated with for the fast T in commercial surfactant.
5. a kind of with the preparation method for being catalyzed the Fugitive dust inhibiting agent that coal burning is acted on described in a kind of claim 1, it is special
Levy and be, comprise the following steps:(1) water of surplus is added in enamel still, 70 DEG C are warming up to;(2) then under agitation, slowly
Add catalysis combustion components, stirring is to complete molten;(3) lower addition water vapor absorption component is stirred, at a temperature of 60-80 DEG C of system of holding
Stirring 20-40 minutes;(4) it is eventually adding after being impregnated with moistening components, stirs 0.5-1 minutes and stop.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611024071.0A CN106701022A (en) | 2016-11-15 | 2016-11-15 | Raise dust inhibitor with function of catalyzing coal combustion and preparation method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611024071.0A CN106701022A (en) | 2016-11-15 | 2016-11-15 | Raise dust inhibitor with function of catalyzing coal combustion and preparation method thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106701022A true CN106701022A (en) | 2017-05-24 |
Family
ID=58941122
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611024071.0A Pending CN106701022A (en) | 2016-11-15 | 2016-11-15 | Raise dust inhibitor with function of catalyzing coal combustion and preparation method thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106701022A (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60110779A (en) * | 1983-11-21 | 1985-06-17 | Kuraray Co Ltd | Method for preventing scatter of powder |
| CN1597832A (en) * | 2003-08-28 | 2005-03-23 | 乙基石油添加剂有限公司 | Method and composition for suppressing coal dust |
| JP2009035647A (en) * | 2007-08-02 | 2009-02-19 | Daiso Chemical Co Ltd | Dust scattering inhibitor and dust treating method |
| CN103232834A (en) * | 2013-05-13 | 2013-08-07 | 吉林大学 | Dual-component wetting and single-component curing-type antifreezing dust suppressant for coal transportation and storage |
| CN104533507A (en) * | 2014-12-15 | 2015-04-22 | 山东科技大学 | Rock dust polymerization and moisture-preservation inhibitor for coal mines and adding device thereof |
| CN104593117A (en) * | 2015-01-27 | 2015-05-06 | 聚合绿能科技发展(北京)有限公司 | Coal polymeric additive capable of replacing partial coal as well as preparation method and application of coal polymeric additive |
| CN105255450A (en) * | 2015-10-29 | 2016-01-20 | 中国矿业大学 | Preparation method of wet-type dust removal agent for reducing coal dust |
-
2016
- 2016-11-15 CN CN201611024071.0A patent/CN106701022A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60110779A (en) * | 1983-11-21 | 1985-06-17 | Kuraray Co Ltd | Method for preventing scatter of powder |
| CN1597832A (en) * | 2003-08-28 | 2005-03-23 | 乙基石油添加剂有限公司 | Method and composition for suppressing coal dust |
| JP2009035647A (en) * | 2007-08-02 | 2009-02-19 | Daiso Chemical Co Ltd | Dust scattering inhibitor and dust treating method |
| CN103232834A (en) * | 2013-05-13 | 2013-08-07 | 吉林大学 | Dual-component wetting and single-component curing-type antifreezing dust suppressant for coal transportation and storage |
| CN104533507A (en) * | 2014-12-15 | 2015-04-22 | 山东科技大学 | Rock dust polymerization and moisture-preservation inhibitor for coal mines and adding device thereof |
| CN104593117A (en) * | 2015-01-27 | 2015-05-06 | 聚合绿能科技发展(北京)有限公司 | Coal polymeric additive capable of replacing partial coal as well as preparation method and application of coal polymeric additive |
| CN105255450A (en) * | 2015-10-29 | 2016-01-20 | 中国矿业大学 | Preparation method of wet-type dust removal agent for reducing coal dust |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170524 |