CN101870900A - Desulphurizing powder produced by using alkaline residue and production process thereof - Google Patents
Desulphurizing powder produced by using alkaline residue and production process thereof Download PDFInfo
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- CN101870900A CN101870900A CN201010211392A CN201010211392A CN101870900A CN 101870900 A CN101870900 A CN 101870900A CN 201010211392 A CN201010211392 A CN 201010211392A CN 201010211392 A CN201010211392 A CN 201010211392A CN 101870900 A CN101870900 A CN 101870900A
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Abstract
The invention relates to desulphurizing powder produced by using alkaline residue and a production process thereof. The desulphurizing powder is prepared by mixing the following components in part by weight: 30 to 85 parts of alkaline residue, 5 to 45 parts of light burned dolomite powder, 1 to 25 parts of fine mullite powder, 1 to 30 parts of aid A, 0.2 to 15 parts of aid B, 0.3 to 20 parts of aid C and 0.1 to 10 parts of aid D. The production process comprises the following steps of: drying the alkaline residue, mixing the alkaline residue, the light burned dolomite powder, the fine mullite powder, the aid A, the aid B, the aid C and the aid D in a high-speed mixer for 10 to 30 minutes, uniformly mixing and packaging. The production process has the advantages that: the industrial waste alkaline residue is taken as a main raw material, so the waste is changed into a new resource, the production cost of the desulphurizing powder is reduced, and the problem that the stacked alkaline residue occupies land is solved; and the aids improve the effect of removing SO2, and the desulphurizing effect is obvious.
Description
Technical field
The present invention relates to a kind of sweetening agent, particularly the desulfurization powder and the production technique thereof of producing with the industrial waste waste soda residue.
Background technology
New energy revolution will take place in 21 century in the world, the total trend of this revolution is with more flexible, more convenient, cleaner novel energy replaces the backward use-pattern of traditional energy and the general layout of the unordered discharging of obnoxious flavour, making the energy give modern today provides necessary power to go to realize outside production and the life requirement, can make requirement discharging up to specification of various obnoxious flavoures or zero release again, also clean more blue sky, the white clouds in the world.
Make a general survey of the present world, because the irresponsibility of some advanced developed country, developing country's science and technology does not pass a test, and has more aggravated Greenhouse effect, acid rain wildness, ozonosphere are destroyed relevant with unordered discharge of noxious gases invariably, are the SO in the example obnoxious flavour with China
290%, N
2, CO 70%, CO
280% all because form in the primary energy source working process, therefore improve the thermo-efficiency of primary energy source, reduce environmental pollution and become the task of top priority; China is energy expenditure big country, SO in the time of 2000
2Quantity discharged is 2,460 ten thousand tons, as benchmark, and Eleventh-Five Year Plan SO
2Reduce discharging 20%, realize this goal, shoulder heavy responsibilities.
Developing the cleanburning technology is that China solves the strategical decision that the primary energy source combustion product gases pollutes the atmosphere polluting problem that is the master, is the important technology direction that realizes economy, social sustainable development and economy, energy environment coordinated development; The core of cleanburning technology is the burning of primary energy source high cleaning, and wherein the solid sulphur of primary energy source desulfurization is the reduction of discharging SO of a suitable China's national situation
2One of technical measures.
Under such prerequisite, study novel desulfurization powder, extremely strong vitality will be arranged, can use in fields such as metallurgy, generating, cement, Industrial Boilers, have popularity, advance and ubiquity, can be implemented in primary energy source and add the solid sulphur of certain proportion in being mixed, can in combustion processes, spray into again and fully absorb SO in burner hearth or the flue gas
2, and make SO in the atmosphere
2Concentration is reduced in the environmental permission scope or zero release.
Existing desulfurization technology uses basic oxide such as CaO in a large number, causes a large amount of mining Wingdales, CO
2Discharging and the waste that produces the energy because of calcining, not only contaminate environment has also increased desulphurization cost, makes sweetening agent if adopt waste soda residue to do main raw material, can reduce desulphurization cost, and its application prospect will be very good.
The annual need of China is converted into about 5,000,000,000 tons in mark coal with primary energy source, coal wherein, coke etc. consume about 4,000,000,000 tons, by desulfurization powder (different add-ons being arranged) the add-on scope 4%-8% that needs per ton according to coal sulphur content difference, calculate by minimum 4%, consume 1.6 hundred million tons of desulfurization powders every year, China is calculated by existing production capacity, annual meeting produces 3,000 ten thousand tons of waste soda residues, add that the quantity of accumulation stacking is very surprising year after year, can satisfy the annual demand that needs with desulfurization powder fully, can remove from simultaneously because of producing large quantities of metallurgy limes and join number that several hundred million tons of Wingdales exploiting as desulfurization powder and burning Wingdale use up, can reduce discharging because of calcined limestone and enter atmospheric number with hundred million tons of CO with ten million ton coke
2, utilization of waste material is really accomplished by the tens billion of units of the fund that can save every year, resource recovery, energy-saving and emission-reduction, recycling economy will be brought huge social and economic benefit to the mankind.
Summary of the invention
The purpose of this invention is to provide a kind of desulfurization powder and production technique thereof of producing with waste soda residue, adopting the industrial waste waste soda residue is main raw material, makes waste become new resource, reduces the production cost of sweetening agent, and problem is taken up an area of in the stacking that has solved waste soda residue again; The interpolation of auxiliary agent has strengthened SO
2The effect that removes, sweetening effectiveness is obvious.
For achieving the above object, the present invention is achieved through the following technical solutions:
The desulfurization powder of producing with waste soda residue, by following composition by weight mixed form: 30～85 parts of waste soda residues, 5～45 parts in light dolomite powder, 1～25 part of mullite fine powder, 1～30 part of auxiliary agent A, 0.2～15 part of auxiliary agent B, 0.3～20 part of auxiliary agent C, 0.1～10 part of auxiliary agent D.
The Chemical Composition of waste soda residue is by mass percentage: SiO
24～14%, CaCO
340～70%, NaCl 3～8%, CaO6～12%, and CaCl 12～19%, and MgO 0.9～2.4%, Fe
2O
30.8～2.3%, Cl
-5～8%, acid non-soluble substance 3～5%, each component concentration sum is 100%; Waste soda residue granularity＜30 μ m, density 1.20～1.28g/cm
3
Light dolomite powder degree is 200～325 orders, and its Chemical Composition is by mass percentage: CaO 55.5～59.2%, and MgO 31.70～36.50%, Fe
2O
30.5～1.60%, SiO
21.0～2.13%, Al
2O
3O.8～1.2%, igloss 2.56～3.30% other 0.35～0.51%, each component concentration sum is 100%.
The mullite powder particle size is 200～325 orders, and its Chemical Composition is by mass percentage: Al
2O
345.6～48.7%, SiO
250.15～53.26%, Fe
2O
30.3～1.22%, CaO 0.3～0.98%, MgO 0.11～0.52%, TiO
20.1～0.5%, other 0.01～0.12%, each component concentration sum is 100%.
The auxiliary agent A granularity is 200～325 orders, and its Chemical Composition is by mass percentage: Fe
2O
366.40～70%, FeO9～15%, CaO 0.1～1%, and MgO 0.5～1.5%, SiO
210～17%, Al
2O
32～5.1%, other 0.1～0.5%, each component concentration sum is 100%.
Auxiliary agent B granularity＜3 μ m; By ZrO
2With Al
2O
3Form ZrO
2With Al
2O
3Be by mass percentage: ZrO
225～75%, Al
2O
375～25%; ZrO
2With Al
2O
3Mass content sum 〉=99%, other content≤1%.
Auxiliary agent C granularity is 200～325 orders, and its Chemical Composition is by mass percentage: SiO
23～7%, FeO 15～21%, Al
2O
313～25%, Cr
2O
335～49%, CaO 1～3%, and MgO 13～21%, other 0.20～0.24%, each component concentration sum is 100%,
Auxiliary agent D mainly plays dissemination, and composition is ultra-fine SiO
2Particle, granularity＜3 μ m; SiO
2Content 〉=99.5%.
The production technique of the described desulfurization powder of producing with waste soda residue: after described waste soda residue oven dry, in high-speed mixer, mix to mix the back pack in 10～30 minutes with described light dolomite powder, mullite fine powder, auxiliary agent A, auxiliary agent B, auxiliary agent C, auxiliary agent D.
Compared with prior art, the invention has the beneficial effects as follows:
1. main raw material of the present invention adopts waste soda residue, uses waste soda residue to do desulfurization powder, makes waste become new resource, can solve the chemical enterprise environmental protection pressure, can solve the primary energy source desulphurization problem again, is the green economy of benefiting the nation and the people.
The present invention is the new desulfurization technology in a leading world, has solved the waste soda residue problem of complex utilization that does not generally have solution in the world, comes if promote, just can totally thoroughly solve the waste soda residue pollution problem, administer from the source, profitable on the result, the less investment output is many, promotes the well-being of mankind.
2. existing desulfurization technology uses basic oxide such as CaO in a large number, causes a large amount of mining Wingdales, CO
2Discharging and the waste that produces the energy because of calcining, not only contaminate environment also increased desulphurization cost, and the present invention adopts waste soda residue to do main raw material, can reduce desulphurization cost, and its application prospect will be very good.
3. some composition of patent utilization additive of the present invention adds the certain proportion desulfurization powder and can play outside the solid sulphur effect in primary energy source, can also improve coal efficiency of combustion 3-5 percentage point, be the energy-conservation advantageous conditions that provides.
4. several raw material granularities of the present invention are thinner, all below 325 orders, and without fine grinding, save energy, because of being that chemical action produces, epigranular, stable components are that the solid sulphur of desulfurization has been created favourable condition.
5. the present invention is owing to be to be purpose with the desulfurization, and the effect of additive mainly is in order to strengthen SO
2Remove and adsorption, except generating the sulfocompound that is difficult at high temperature decomposing, can also generate one deck to the high temperature easy protective membrane of decomposition sulfocompound down because of some additive component and some product, sweetening effectiveness is obviously improved.
The present invention to the past because waste soda residue in Cl
-Ionic exists etching apparatus and pipeline and the hard nut to crack that is not widely used, and the effect by some composition in the additive has obtained solution, and mechanism is that some composition in the additive is a complexing agent, has played inhibition Cl
-The effect of etching apparatus and pipeline.In the process of desulfurization these compositions can with metallic iron, Cl
-Thereby generate the complex compound do not have corrosive power and reach in the production process demand sweetening material Deng composition.This is an effective behave for evidence, and waste soda residue is widely used.
7. through overtesting, add a certain proportion of desulfurization powder sulfur-fixing rate of the present invention when primary energy source is mixed and reach 55%, effect is better than the present domestic solid sulphur product that other are developed simultaneously more than 10 percentage points; Aspect flue gas desulfurization, this desulfurization powder desulfurization degree reaches more than 95%, and sweetening effectiveness is in the leading level in the world, thereby reaches energy-saving and emission-reduction, improves Greenhouse effect, stops the beautiful homeland of harmony that acid rain produces, the Sustainable development that beautiful environment.
Embodiment
Embodiment 1
The desulfurization powder of producing with waste soda residue, by following composition by weight mixed form:
55 parts of industrial alkali waste slags
23 parts in light dolomite powder
6 parts of mullite fine powders
5 parts of auxiliary agent A
0.8 part of auxiliary agent B
9 parts of auxiliary agent C
1.2 parts of auxiliary agent D
Production technique: industrial alkali waste slag oven dry back and light dolomite powder, mullite fine powder, auxiliary agent A, auxiliary agent B, auxiliary agent C, auxiliary agent D uniform mixing in sending the stream mixing machine were at a high speed packed after 15 minutes.
Embodiment 2
The desulfurization powder of producing with waste soda residue, by following composition by weight mixed form:
61 parts of industrial alkali waste slags
18 parts in light dolomite powder
8 parts of mullite fine powders
5 parts of auxiliary agent A
1.5 parts of auxiliary agent B
5.5 parts of auxiliary agent C
1 part of auxiliary agent D
Production technique: industrial alkali waste slag oven dry back and light dolomite powder, mullite fine powder, auxiliary agent A, auxiliary agent B, auxiliary agent C, auxiliary agent D uniform mixing in sending the stream mixing machine were at a high speed packed after 30 minutes.
Embodiment 3
The desulfurization powder of producing with waste soda residue, by following composition by weight mixed form:
73 parts of industrial alkali waste slags
10 parts in light dolomite powder
11 parts of mullite fine powders
3 parts of auxiliary agent A
0.5 part of auxiliary agent B
2 parts of auxiliary agent C
0.5 part of auxiliary agent D
Production technique is with embodiment 1.
Embodiment 4
The desulfurization powder of producing with waste soda residue, by following composition by weight mixed form:
38 parts of industrial alkali waste slags
25 parts in light dolomite powder
15 parts of mullite fine powders
13 parts of auxiliary agent A
0.8 part of auxiliary agent B
3.2 parts of auxiliary agent C
5 parts of auxiliary agent D
Production technique is with embodiment 1.
Embodiment 5
The desulfurization powder of producing with waste soda residue, by following composition by weight mixed form:
85 parts of industrial alkali waste slags
45 parts in light dolomite powder
25 parts of mullite fine powders
30 parts of auxiliary agent A
15 parts of auxiliary agent B
20 parts of auxiliary agent C
10 parts of auxiliary agent D
Production technique is with embodiment 1.
Embodiment 6
The desulfurization powder of producing with waste soda residue, by following composition by weight mixed form:
30 parts of industrial alkali waste slags
5 parts in light dolomite powder
1 part of mullite fine powder
1 part of auxiliary agent A
0.2 part of auxiliary agent B
0.3 part of auxiliary agent C
0.1 part of auxiliary agent D
Production technique is with embodiment 1.
In the foregoing description, the performance index of described raw material are as follows:
The Chemical Composition of waste soda residue is by mass percentage: SiO
24～14%, CaCO
340～70%, NaCl 3～8%, CaO6～12%, and CaCl 12～19%, and MgO 0.9～2.4%, Fe
2O
30.8～2.3%, Cl
-5～8%, acid non-soluble substance 3～5%, each component concentration sum is 100%; Waste soda residue granularity＜30 μ m, density 1.20～1.28g/cm
3
Light dolomite powder degree is 200～325 orders, and its Chemical Composition is by mass percentage: CaO 55.5～59.2%, and MgO 31.70～36.50%, Fe
2O
30.5～1.60%, SiO
21.0～2.13%, Al
2O
30.8～1.2%, igloss 2.56～3.30% other 0.35～0.51%, each component concentration sum is 100%.
The mullite powder particle size is 200～325 orders, and its Chemical Composition is by mass percentage: Al
2O
345.6～48.7%, SiO
250.15～53.26%, Fe
2O
30.3～1.22%, CaO 0.3～0.98%, MgO 0.11～0.52%, TiO
20.1～0.5%, other 0.01～0.12%, each component concentration sum is 100%.
The auxiliary agent A granularity is 200～325 orders, and its Chemical Composition is by mass percentage: Fe
2O
366.40～70%, FeO9～15%, CaO 0.1～1%, and MgO 0.5～1.5%, SiO
210～17%, Al
2O
32～5.1%, other 0.1～0.5%, each component concentration sum is 100%.
Auxiliary agent B granularity＜3 μ m; By ZrO
2With Al
2O
3Form ZrO
2With Al
2O
3Be by mass percentage: ZrO
225～75%, Al
2O
375～25%; ZrO
2With Al
2O
3Mass content sum 〉=99%, other content≤1%.
Auxiliary agent C granularity is 200～325 orders, and its Chemical Composition is by mass percentage: SiO
23～7%, FeO 15～21%, Al
2O
313～25%, Cr
2O
335～49%, CaO 1～3%, and MgO 13～21%, other 0.20～0.24%, each component concentration sum is 100%,
Auxiliary agent D mainly plays dissemination, and composition is ultra-fine SiO
2Particle, granularity＜3 μ m; SiO
2Content 〉=99.5%.
Claims (2)
1. the desulfurization powder of producing with waste soda residue, it is characterized in that, by following composition by weight mixed form: 30～85 parts of waste soda residues, 5～45 parts in light dolomite powder, 1～25 part of mullite fine powder, 1～30 part of auxiliary agent A, 0.2～15 part of auxiliary agent B, 0.3～20 part of auxiliary agent C, 0.1～10 part of auxiliary agent D;
The Chemical Composition of waste soda residue is by mass percentage: SiO
24～14%, CaCO
340～70%, NaCl 3～8%, CaO6～12%, and CaCl 12～19%, and MgO 0.9～2.4%, Fe
2O
30.8～2.3%, Cl
-5～8%, acid non-soluble substance 3～5%, each component concentration sum is 100%; Waste soda residue granularity＜30 μ m, density 1.20～1.28g/cm
3
Light dolomite powder degree is 200～325 orders, and its Chemical Composition is by mass percentage: CaO 55.5～59.2%, and MgO 31.70～36.50%, Fe
2O
30.5～1.60%, SiO
21.0～2.13%, Al
2O
30.8～1.2%, igloss 2.56～3.30% other 0.35～0.51%, each component concentration sum is 100%;
The mullite powder particle size is 200～325 orders, and its Chemical Composition is by mass percentage: Al
2O
345.6～48.7%, SiO
250.15～53.26%, Fe
2O
30.3～1.22%, CaO 0.3～0.98%, MgO 0.11～0.52%, TiO
20.1～0.5%, other 0.01～0.12%, each component concentration sum is 100%;
The auxiliary agent A granularity is 200～325 orders, and its Chemical Composition is by mass percentage: Fe
2O
366.40～70%, FeO9～15%, CaO 0.1～1%, and MgO 0.5～1.5%, SiO
210～17%, Al
2O
32～5.1%, other 0.1～0.5%, each component concentration sum is 100%;
Auxiliary agent B granularity＜3 μ m; By ZrO
2With Al
2O
3Form ZrO
2With Al
2O
3Be by mass percentage: ZrO
225～75%, Al
2O
375～25%; ZrO
2With Al
2O
3Mass content sum 〉=99%, other content≤1%;
Auxiliary agent C granularity is 200～325 orders, and its Chemical Composition is by mass percentage: SiO
23～7%, FeO 15～21%, Al
2O
313～25%, Cr
2O
335～49%, CaO 1～3%, and MgO 13～21%, other 0.20～0.24%, each component concentration sum is 100%;
Auxiliary agent D composition is ultra-fine SiO
2Particle, granularity＜3 μ m; SiO
2Content 〉=99.5%.
2. the production technique of the described desulfurization powder of producing with waste soda residue of claim 1, it is characterized in that, after the oven dry of described waste soda residue, in high-speed mixer, mix to mix the back pack in 10～30 minutes with described light dolomite powder, mullite fine powder, auxiliary agent A, auxiliary agent B, auxiliary agent C, auxiliary agent D.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010211392 CN101870900B (en) | 2010-06-29 | 2010-06-29 | Desulphurizing powder produced by using alkaline residue and production process thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010211392 CN101870900B (en) | 2010-06-29 | 2010-06-29 | Desulphurizing powder produced by using alkaline residue and production process thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101870900A true CN101870900A (en) | 2010-10-27 |
| CN101870900B CN101870900B (en) | 2013-09-18 |
Family
ID=42995987
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201010211392 Expired - Fee Related CN101870900B (en) | 2010-06-29 | 2010-06-29 | Desulphurizing powder produced by using alkaline residue and production process thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101870900B (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102181317A (en) * | 2011-03-29 | 2011-09-14 | 王成新 | Desulfurizer produced by utilizing mineral waste material and preparation method thereof |
| CN104692514A (en) * | 2014-12-31 | 2015-06-10 | 浙江至美环境科技有限公司 | Granular mineralizer for conditioning desalted water as well as preparation method and application of granular mineralizer |
| CN106925250A (en) * | 2015-12-29 | 2017-07-07 | 天津市英派克石化工程有限公司 | A kind of method that dry type desulfurizing catalyst is prepared with white clay |
| CN108310936A (en) * | 2016-04-22 | 2018-07-24 | 吴士妹 | A kind of solid-state desulfurization powder of environmental protection |
| CN108579358A (en) * | 2016-04-22 | 2018-09-28 | 吴士妹 | A kind of preparation method of high-efficiency flue gas desulfurization pulvis |
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| CN1415765A (en) * | 2002-10-12 | 2003-05-07 | 吴光亮 | Desulfurizer and its producing technique |
| EP1839743A1 (en) * | 2004-12-24 | 2007-10-03 | Idemitsu Kosan Co., Ltd. | Desulfurizing agent for organosulfur compound-containing fuel oil, and process for producing hydrogen for fuel cell |
| CN101067160A (en) * | 2007-06-08 | 2007-11-07 | 东北大学 | MgO base desulfurizing agent and producing method thereof |
| CN101302577A (en) * | 2008-06-16 | 2008-11-12 | 东北大学 | MgO-based desulfurizer based on self-propagating and preparation thereof |
-
2010
- 2010-06-29 CN CN 201010211392 patent/CN101870900B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1415765A (en) * | 2002-10-12 | 2003-05-07 | 吴光亮 | Desulfurizer and its producing technique |
| EP1839743A1 (en) * | 2004-12-24 | 2007-10-03 | Idemitsu Kosan Co., Ltd. | Desulfurizing agent for organosulfur compound-containing fuel oil, and process for producing hydrogen for fuel cell |
| CN101067160A (en) * | 2007-06-08 | 2007-11-07 | 东北大学 | MgO base desulfurizing agent and producing method thereof |
| CN101302577A (en) * | 2008-06-16 | 2008-11-12 | 东北大学 | MgO-based desulfurizer based on self-propagating and preparation thereof |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102181317A (en) * | 2011-03-29 | 2011-09-14 | 王成新 | Desulfurizer produced by utilizing mineral waste material and preparation method thereof |
| CN104692514A (en) * | 2014-12-31 | 2015-06-10 | 浙江至美环境科技有限公司 | Granular mineralizer for conditioning desalted water as well as preparation method and application of granular mineralizer |
| CN106925250A (en) * | 2015-12-29 | 2017-07-07 | 天津市英派克石化工程有限公司 | A kind of method that dry type desulfurizing catalyst is prepared with white clay |
| CN108310936A (en) * | 2016-04-22 | 2018-07-24 | 吴士妹 | A kind of solid-state desulfurization powder of environmental protection |
| CN108579358A (en) * | 2016-04-22 | 2018-09-28 | 吴士妹 | A kind of preparation method of high-efficiency flue gas desulfurization pulvis |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101870900B (en) | 2013-09-18 |
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