CN105080330A - White mud-gypsum method wet flue gas desulfurization method - Google Patents
White mud-gypsum method wet flue gas desulfurization method Download PDFInfo
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- CN105080330A CN105080330A CN201510600089.XA CN201510600089A CN105080330A CN 105080330 A CN105080330 A CN 105080330A CN 201510600089 A CN201510600089 A CN 201510600089A CN 105080330 A CN105080330 A CN 105080330A
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Abstract
The invention provides a white mud-gypsum method wet flue gas desulfurization method. The method comprises the steps that 1, white mud is taken, water is added for stirring, and white mud slurry is obtained; 2 the white mud slurry obtained in the first step is sent to absorption towers, flue gas to be treated is sent to the absorption tower, wet desulphurization is conducted, and treated flue gas and gypsum slurry are obtained. According to the white mud-gypsum method wet flue gas desulfurization method, the technology is simple, the white mud is adopted as desulfurizer, the desulphurization cost can be reduced, good desulphurization effect can be achieved, and meanwhile the effect of two-way control over the white mud and sulfur dioxide is achieved.
Description
Technical field
The present invention relates to chemical industry wet desulphurization field, in particular to a kind of white clay-gypsum smoke-gas wet desulfurization method.
Background technology
White clay is the secondary pollution solid waste that paper mill produces in process of production, often produces 1 ton of paper or 1 ton of slurry, on average can produce about 0.8 ton of paper white sludge.For the process of white clay, some external and domestic large-scale paper mills are all adopt limekiln calcination method to the recycling of white clay, make white clay pass through regeneration, produce quick lime again, recycle in causticization, thus reduce operating cost.And domestic some middle-size and small-size enterprises in pulp and paper industry in addition, for various reasons, or white clay reclaimer is not supporting, or dialogue sludge-polluted understanding is not enough, white clay can not get dealing carefully with all the time, or draws and fill out hole and pave the way, or directly enters rivers, both caused environmental pollution, huge charges for disposing pollutants must be paid simultaneously.In recent years along with efforts at environmental protection are strengthened day by day, white clay is administered just becomes many papermaking enterprises a great problem in the urgent need to address.
At present, most of thermal power plant of China still generates electricity using coal as main fuel, strengthens thermal power plant SO
2control dynamics particularly urgent and necessary.Flue gas desulfurization is current control SO
2one of the most effective approach.According to statistics, have more than the ten kind of flue gas desulfurization technique technology such as Wet Limestone-desulfurization of gypsum method, ciculation fluidized bed process, Sea water respiratory distress syndrome, desulphurizing and dust-removing integral method, semidry method, rotary spraying and drying method, in-furnace calcium spraying tail flue gas humidification activation method, active coke absorption method, electronic beam method to be applied.Wherein, Wet Limestone-desulfurization of gypsum method because of advantages such as its desulfuration efficiency are high, operational reliability is good, become be most widely used in the world at present, flue gas desulfurization technique that technology is the most ripe, but shortcoming to be cost higher, accessory substance easily produces secondary pollution.
In view of this, special proposition the present invention.
Summary of the invention
The object of the present invention is to provide a kind of white clay-gypsum smoke-gas wet desulfurization method, described white clay-gypsum smoke-gas wet desulfurization method has that technique is simple, cost is low, desulfurized effect is good, can carry out advantages such as white clay and sulfur dioxide two-way treatments simultaneously.
In order to realize above-mentioned purpose of the present invention, spy by the following technical solutions:
A kind of white clay-gypsum smoke-gas wet desulfurization method, comprises the steps:
(1) get white clay, add water stirring, obtains white clay slurries;
(2) step (1) gained white clay slurries are delivered to absorption tower, pending flue gas is sent into absorption tower and carries out wet desulphurization, obtain the flue gas after processing and gypsum slurries.
The present invention is with papermaking waste material---and white clay is desulfurizing agent, carries out desulfurization process, limestone scrubbing FGD to the waste gas of power plant emission, is be desulfurizing agent with lime stone slurry, carries out spray washing, make the SO in flue gas in absorption tower to flue gas
2reaction generates CaSO
3, the slurries simultaneously to absorption tower blast gas, make CaSO
3be converted into accessory substance---CaSO
4, i.e. gypsum.Wherein, the expense of lime stone is a capital expenditure of this technique, accounts for 17% of whole sulfur removal technology total cost.As Thermal Power Enterprises, under guaranteeing that environmental protection index is up to standard and reaching the prerequisite of effect, the desulfurizing agent that sorting charge is lower has important meaning to the operating cost reducing desulfurizer.
White clay of the present invention-gypsum smoke-gas wet desulfurization method technique is simple, and employing white clay is desulfurizing agent, can reduce desulphurization cost, and can reach good desulfurized effect, white clay and sulfur dioxide is obtained to the effect of two-way treatment simultaneously.
Preferably step (2) gained gypsum slurries is dewatered, obtain gypsum.
Gypsum is sweetening process accessory substance, can be used for industrial application or sells as product.
Use white clay as desulfurization absorbent, because white clay composition contains insoluble matter black powdered carbon, some equipment in desulfurization later stage may be affected, as dewaterer dehydrating effect etc.
Preferably step (2) gained gypsum slurries is carried out substep dehydration, ensure dehydrating effect; Described substep is preferably twice; Gained gypsum slurries carries out first time dehydration, obtains the gypsum slurries after dewatering and overflowing liquid.
Gained overflowing liquid is preferably recycled in step (1) white clay pulping process, step (2) absorption tower or Waste Water Treatment.
Gained overflowing liquid can be recycled as required, contributes to cost-saving further, improves desulfurized effect.
Gypsum slurries after described dehydration carries out second time dehydration and obtains finished product gypsum and filtrate.
Gained filtrate is preferably recycled in step (2) described absorption tower or Waste Water Treatment.
Gained filtrate can be recycled as required, contributes to cost-saving further, improves desulfurized effect.
In described step (1), in gained white clay slurries, the volume fraction of white clay is 10%-50%, is preferably 15%-35%, more preferably 20%-25%.
Adopt the white clay slurries containing designated volume mark white clay, contribute to improving desulfurized effect.
In described step (1), the pH value of gained white clay slurries is 4-7, is preferably 4.3-6, more preferably 4.8-5.3.
Adopt the white clay slurries of certain ph, contribute to keeping clay wash liquid system to stablize, and improve desulfurized effect.
When carrying out wet desulphurization in described step (2), the liquid-gas ratio of white clay slurries and flue gas is 1-30L/Nm
3, be preferably 10-20L/Nm
3, more preferably 14-16L/Nm
3.
Adopt specific white clay slurries and flue gas liquid-gas ratio when carrying out wet desulphurization, contribute to improving desulfurized effect, and control white clay consumption, cost-saving.
Flue gas upflow velocity when carrying out wet desulphurization in described step (2) is 1-10m/s, is preferably 2-6m/s, more preferably 3.2-4m/s.
Adopt specific flue gas upflow velocity when carrying out wet desulphurization, contribute to improving desulfurized effect and desulfuration efficiency.
The present invention can utilize white clay as raw material, reaches the effect to white clay and sulfur dioxide two-way treatment.Wherein white clay be pulp and paper making in the solid waste of carrying out producing in black liquor of pulp making alkali recovery process, sulfur dioxide be coal-fired power plant burning produce Air Pollutants.In heat-engine plant desulfurized system, by adding a certain proportion of lime stone slurry of white clay blending, remove the sulfur dioxide in flue gas, thus reach the object of white clay and sulfur dioxide two-way treatment and resource comprehensive scientific utilization, realize the doulbe-sides' victory of enterprise in environmental benefit and economic benefit.
The main process that white clay produces is: produce in paper-making process inside black liquor and be rich in fiber and alkali compounds, black liquor becomes fused mass after atomization in special alkali recovery furnace, burning after evaporation and concentration, through said process, initial NaOH is converted into sodium carbonate substantially; Utilize Na
2cO
3solution and lime (CaO) react, and generate CaCO
3precipitation and NaOH solution, wherein NaOH solution returns pulping system and recycles after clarification; CaCO
3slurries transport outward landfill or stacking after vacuum filtration.The chemical equation producing white clay is as follows:
Na
2CO
3+CaO+H
2O→2NaOH+CaCO
3↓
White clay is containing CaCO
3be about 85%, wherein, particle diameter accounts for more than 90% below 45 μm, better desulphurizing activated, the promotion composition Na simultaneously containing desulfurization
2the compositions such as O, MgO, can effectively desulfurization.
The present invention by Automobile Transportation to the white clay of factory after the stirring that adds water, being diluted to slurries, as required slurries are transported to absorption tower respectively again and carry out sulfur dioxide absorption reaction, generate stable chemical nature, environment is not easily polluted, and can be for sale as building material, continue byproduct---the gypsum of the creation of value, thus realize the innoxious comprehensive utilization of white clay.
Compared with prior art, beneficial effect of the present invention is:
White clay of the present invention-gypsum smoke-gas wet desulfurization method technique is simple, and employing white clay is desulfurizing agent, can reduce desulphurization cost, and can reach good desulfurized effect, white clay and sulfur dioxide is obtained to the effect of two-way treatment simultaneously.
Accompanying drawing explanation
In order to be illustrated more clearly in the specific embodiment of the invention or technical scheme of the prior art, be briefly described to the accompanying drawing used required in detailed description of the invention or description of the prior art below, apparently, accompanying drawing in the following describes is some embodiments of the present invention, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
The white clay that Fig. 1 uses for the embodiment of the present invention 1 method-gypsum Wet FGD structural representation;
Reference numeral:
1-serum pot; 2-serum pot discharge nozzle 3-white clay slurrying pond;
Road;
4-feeding warehouse; 5-discharging bin; 6-white clay slurries excavationg pump;
7-slurrying district blowoff basin; 8-agitating device; 9-controlled valve;
10-pressure valve; 11-absorption tower; 12-sample tap;
13-densitometer; 14-filter screen; 15-slush pump;
16-white clay slurrying pond goes out
Material pipeline.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, technical scheme of the present invention is clearly and completely described, but it will be understood to those of skill in the art that, following described embodiment is the present invention's part embodiment, instead of whole embodiments, only for illustration of the present invention, and should not be considered as limiting the scope of the invention.Based on the embodiment in the present invention, those of ordinary skill in the art, not making the every other embodiment obtained under creative work prerequisite, belong to the scope of protection of the invention.Unreceipted actual conditions person in embodiment, the condition of conveniently conditioned disjunction manufacturer suggestion is carried out.Agents useful for same or the unreceipted production firm person of instrument, be and can buy by commercially available the conventional products obtained.
In describing the invention, it should be noted that, orientation or the position relationship of the instruction such as term " " center ", " on ", D score, "left", "right", " vertically ", " level ", " interior ", " outward " they be based on orientation shown in the drawings or position relationship; be only the present invention for convenience of description and simplified characterization; instead of instruction or imply the device of indication or element must have specific orientation, with specific azimuth configuration and operation, therefore can not be interpreted as limitation of the present invention.In addition, term " first ", " second ", " the 3rd " only for describing object, and can not be interpreted as instruction or hint relative importance.
In describing the invention, it should be noted that, unless otherwise clearly defined and limited, term " installation ", " being connected ", " connection " should be interpreted broadly, and such as, can be fixedly connected with, also can be removably connect, or connect integratedly; Can be mechanical connection, also can be electrical connection; Can be directly be connected, also indirectly can be connected by intermediary, can be the connection of two element internals.For the ordinary skill in the art, concrete condition above-mentioned term concrete meaning in the present invention can be understood.
Embodiment 1
White clay-gypsum Wet FGD structure that the present embodiment adopts as shown in Figure 1, comprises serum pot 1, absorption tower 11 and white clay slurrying pond 3; Described serum pot 1 is connected with absorption tower 11 by serum pot discharging pipeline 2; Described white clay slurrying pond 3 is connected with serum pot 1 with absorption tower 11 respectively by white clay slurrying pond discharging pipeline 16;
In described white clay slurrying pond 3, middle part arranges filter screen 14, and white clay slurrying pond 3 is divided into feeding warehouse 4 and discharging bin 5 by described filter screen 14; Described feeding warehouse 4 is connected with agitating device 8 respectively with discharging bin 5; Described discharging bin 5 is connected with white clay slurrying pond discharging pipeline 16, and described white clay slurrying pond discharging pipeline 16 arranges white clay slurries excavationg pump 6.
White clay slurrying pond 3 is divided into feeding warehouse 4 and discharging bin 5 by filter screen 14 by the present invention, and filter screen 14 can effectively stop the white clay block that in feeding warehouse 4, volume is larger to enter discharging bin 5, thus is discharged by discharging bin 5, enters follow-up system, affects wet desulphurization effect; At feeding warehouse 4 and discharging bin 5 place, agitating device 8 is set respectively, stirred respectively by the white clay in agitating device 8 pairs of feeding warehouses 4 and discharging bin 5, enable the white clay in feeding warehouse 4 fully broken, slurry is made into water, the middle white clay slurry of discharging bin 5 can not harden into block, ensures subsequent wet desulfurized effect.
Described serum pot 1 is connected with slurrying district blowoff basin 7 by pipeline, is preferably formed closed-loop path.
Described closed pipeline preferably arranges controlled valve 9.
Described slurrying district blowoff basin 7 is preferably connected with agitating device 8.
Described circulation closes on pipeline and preferably arranges slush pump 15.
When slurries are too much in serum pot 1, unnecessary slurries can be discharged by circulation line in slurrying district blowoff basin 7, store for future use; When slurries in slurry pipe are not enough, slurrying district blowoff basin 7 can pump into slurries by circulation line in serum pot 1.Stirred by the slurries in agitating device 8 pairs of slurrying district blowoff basins 7, make the mobility that slurries keep good.
Described serum pot discharging pipeline 2 arranges controlled valve 9 and pressure valve 10 respectively.
Described serum pot discharging pipeline 2 is 1 or many, is preferably 4, preferably every bar serum pot discharging pipeline 2 arranges controlled valve 9 and pressure valve 10 respectively.
The present invention adds slurry by 1 or many serum pot discharging pipelines 2 in absorption tower 11, ensures reinforced efficiency; By being arranged on controlled valve 9 on serum pot discharging pipeline 2 and pressure valve 10, controlling adding and adding speed of slurry, making it meet wet desulfurizing process needs.
Described absorption tower 11 is one or more, and be preferably 2, each absorption tower 11 is connected with serum pot discharging pipeline 2 respectively, disposablely can carry out large-scale wet desulfurizing process.
White clay slurrying pond discharging pipeline 16 arranges controlled valve 9 and pressure valve 10 respectively.
Described white clay slurrying pond discharging pipeline 16 is 1 or many, is preferably 4, preferably every bar white clay slurrying pond discharging pipeline 16 arranges slurries excavationg pump, controlled valve 9 and pressure valve 10 respectively.
The present invention adds white clay by 1 or many white clay slurrying pond discharging pipelines 16 in absorption tower 11, ensures reinforced efficiency; By being arranged on controlled valve 9 on white clay slurrying pond discharging pipeline 16 and pressure valve 10, control adding and adding speed of white clay, it is made to meet wet desulfurizing process needs, and by mobility that slurries excavationg pump makes white clay slurries keep good, can add in time in absorption tower 11, carry out subsequent wet sulfur removal technology.
Described white clay slurrying pond 3 is connected with sampling line.
Described sampling line is arranged respectively controlled valve 9, sample tap 12 and densitometer 13.
Carry out real time on-line monitoring by the white clay slurries in the clay stock tank 3 of the controlled valve 9 on sampling line, sample tap 12 and densitometer 13 dialogue, after the white clay slurries in white clay slurrying pond 3 reach requirement, can discharge, carry out subsequent technique.
In white clay slurrying pond 3, inlet side arranges filter screen 14, tentatively filters the raw material after the fragmentation added in white clay slurrying pond 3, makes the white clay raw material entered in feeding warehouse 4 be easier to be mixed into the slurry with good fluidity with water.
A kind of white clay-gypsum smoke-gas wet desulfurization method, comprises the steps:
(1) get white clay, add water stirring, obtains white clay slurries; CaCO in described white clay
3mass fraction be 85.7%, in gained white clay slurries, the volume fraction of white clay is 10%, and pH value is 4;
(2) step (1) gained white clay slurries are delivered to absorption tower, pending flue gas is sent into absorption tower and carries out wet desulphurization, obtain the flue gas after processing and gypsum slurries; The liquid-gas ratio of white clay slurries and flue gas is 30L/Nm
3, flue gas upflow velocity is 1m/s.
(3) gained gypsum slurries carries out first time dehydration, obtains the gypsum slurries after dewatering and overflowing liquid; Gained overflowing liquid is recycled in step (1) white clay pulping process, step (2) absorption tower or Waste Water Treatment;
(4) gypsum slurries after described dehydration carries out second time dehydration and obtains finished product gypsum and filtrate; Gained filtrate is recycled in step (2) described absorption tower or Waste Water Treatment.
Embodiment 2
Adopt the device identical with embodiment 1, carry out white clay-gypsum smoke-gas wet desulfurization, comprise the steps:
(1) get white clay, add water stirring, obtains white clay slurries; CaCO in described white clay
3mass fraction be 85.2%, in gained white clay slurries, the volume fraction of white clay is 50%, and pH value is 7;
(2) step (1) gained white clay slurries are delivered to absorption tower, pending flue gas is sent into absorption tower and carries out wet desulphurization, obtain the flue gas after processing and gypsum slurries; The liquid-gas ratio of white clay slurries and flue gas is 1L/Nm
3, flue gas upflow velocity is 10m/s.
(3) gained gypsum slurries carries out first time dehydration, obtains the gypsum slurries after dewatering and overflowing liquid; Gained overflowing liquid is recycled in step (1) white clay pulping process, step (2) absorption tower or Waste Water Treatment;
(4) gypsum slurries after described dehydration carries out second time dehydration and obtains finished product gypsum and filtrate; Gained filtrate is recycled in step (2) described absorption tower or Waste Water Treatment.
Embodiment 3
Adopt the device identical with embodiment 1, carry out white clay-gypsum smoke-gas wet desulfurization, comprise the steps:
(1) get white clay, add water stirring, obtains white clay slurries; CaCO in described white clay
3mass fraction be 84.3%, in gained white clay slurries, the volume fraction of white clay is 15%, and pH value is 4.3;
(2) step (1) gained white clay slurries are delivered to absorption tower, pending flue gas is sent into absorption tower and carries out wet desulphurization, obtain the flue gas after processing and gypsum slurries; The liquid-gas ratio of white clay slurries and flue gas is 20L/Nm
3, flue gas upflow velocity is 2m/s.
(3) gained gypsum slurries carries out first time dehydration, obtains the gypsum slurries after dewatering and overflowing liquid; Gained overflowing liquid is recycled in step (1) white clay pulping process, step (2) absorption tower or Waste Water Treatment;
(4) gypsum slurries after described dehydration carries out second time dehydration and obtains finished product gypsum and filtrate; Gained filtrate is recycled in step (2) described absorption tower or Waste Water Treatment.
Embodiment 4
Adopt the device identical with embodiment 1, carry out white clay-gypsum smoke-gas wet desulfurization, comprise the steps:
(1) get white clay, add water stirring, obtains white clay slurries; CaCO in described white clay
3mass fraction be 85.1%, in gained white clay slurries, the volume fraction of white clay is 35%, and pH value is 6;
(2) step (1) gained white clay slurries are delivered to absorption tower, pending flue gas is sent into absorption tower and carries out wet desulphurization, obtain the flue gas after processing and gypsum slurries; The liquid-gas ratio of white clay slurries and flue gas is 10L/Nm
3, flue gas upflow velocity is 6m/s.
(3) gained gypsum slurries carries out first time dehydration, obtains the gypsum slurries after dewatering and overflowing liquid; Gained overflowing liquid is recycled in step (1) white clay pulping process, step (2) absorption tower or Waste Water Treatment;
(4) gypsum slurries after described dehydration carries out second time dehydration and obtains finished product gypsum and filtrate; Gained filtrate is recycled in step (2) described absorption tower or Waste Water Treatment.
Embodiment 5
Adopt the device identical with embodiment 1, carry out white clay-gypsum smoke-gas wet desulfurization, comprise the steps:
(1) get white clay, add water stirring, obtains white clay slurries; CaCO in described white clay
3mass fraction be 84.5%, in gained white clay slurries, the volume fraction of white clay is 20%, and pH value is 4.8;
(2) step (1) gained white clay slurries are delivered to absorption tower, pending flue gas is sent into absorption tower and carries out wet desulphurization, obtain the flue gas after processing and gypsum slurries; The liquid-gas ratio of white clay slurries and flue gas is 16L/Nm
3, flue gas upflow velocity is 3.2m/s.
(3) gained gypsum slurries carries out first time dehydration, obtains the gypsum slurries after dewatering and overflowing liquid; Gained overflowing liquid is recycled in step (1) white clay pulping process, step (2) absorption tower or Waste Water Treatment;
(4) gypsum slurries after described dehydration carries out second time dehydration and obtains finished product gypsum and filtrate; Gained filtrate is recycled in step (2) described absorption tower or Waste Water Treatment.
Embodiment 6
Adopt the device identical with embodiment 1, carry out white clay-gypsum smoke-gas wet desulfurization, comprise the steps:
(1) get white clay, add water stirring, obtains white clay slurries; CaCO in described white clay
3mass fraction be 85.3%, in gained white clay slurries, the volume fraction of white clay is 25%, and pH value is 5.3;
(2) step (1) gained white clay slurries are delivered to absorption tower, pending flue gas is sent into absorption tower and carries out wet desulphurization, obtain the flue gas after processing and gypsum slurries; The liquid-gas ratio of white clay slurries and flue gas is 14L/Nm
3, flue gas upflow velocity is 4m/s.
(3) gained gypsum slurries carries out first time dehydration, obtains the gypsum slurries after dewatering and overflowing liquid; Gained overflowing liquid is recycled in step (1) white clay pulping process, step (2) absorption tower or Waste Water Treatment;
(4) gypsum slurries after described dehydration carries out second time dehydration and obtains finished product gypsum and filtrate; Gained filtrate is recycled in step (2) described absorption tower or Waste Water Treatment.
Adopt various embodiments of the present invention scheme to carry out wet desulphurization to certain thermal power plant flue gas, result is as follows:
Table 1 various embodiments of the present invention desulfurized effect
Can be found out by table 1, white clay of the present invention-gypsum smoke-gas wet desulfurization method can carry out desulfurization process to the flue gas that thermal power plant produces, and obtains good desulfurized effect; In addition, utilize white clay as desulfurization absorbent, realize the treatment of wastes with processes of wastes against one another, target to white clay and sulfur dioxide two-way treatment, and obtain finished product gypsum, can be used as raw materials for production or sell with commercial form.
Although illustrate and describe the present invention with specific embodiment, however it will be appreciated that can to make when not deviating from the spirit and scope of the present invention many other change and amendment.Therefore, this means to comprise all such changes and modifications belonged in the scope of the invention in the following claims.
Claims (10)
1. white clay-gypsum smoke-gas wet desulfurization method, is characterized in that, comprise the steps:
(1) get white clay, add water stirring, obtains white clay slurries;
(2) step (1) gained white clay slurries are delivered to absorption tower, pending flue gas is sent into absorption tower and carries out wet desulphurization, obtain the flue gas after processing and gypsum slurries.
2. a kind of white clay according to claim 1-gypsum smoke-gas wet desulfurization method, is characterized in that, is dewatered by step (2) gained gypsum slurries, obtains gypsum.
3. a kind of white clay according to claim 2-gypsum smoke-gas wet desulfurization method, is characterized in that, step (2) gained gypsum slurries is carried out first time dehydration, obtains the gypsum slurries after dewatering and overflowing liquid.
4. a kind of white clay according to claim 3-gypsum smoke-gas wet desulfurization method, is characterized in that, is recycled to by gained overflowing liquid in step (1) white clay pulping process, step (2) absorption tower or Waste Water Treatment.
5. a kind of white clay according to claim 2-gypsum smoke-gas wet desulfurization method, is characterized in that, the gypsum slurries after described dehydration carries out second time dehydration and obtains finished product gypsum and filtrate.
6. a kind of white clay according to claim 5-gypsum smoke-gas wet desulfurization method, is characterized in that, gained filtrate is recycled in step (2) described absorption tower or Waste Water Treatment.
7. a kind of white clay according to claim 1-gypsum smoke-gas wet desulfurization method, it is characterized in that, in described step (1), in gained white clay slurries, the volume fraction of white clay is 10%-50%, is preferably 15%-35%, more preferably 20%-25%.
8. a kind of white clay according to claim 1-gypsum smoke-gas wet desulfurization method, is characterized in that, in described step (1), the pH value of gained white clay slurries is 4-7, is preferably 4.3-6, more preferably 4.8-5.3.
9. a kind of white clay according to claim 1-gypsum smoke-gas wet desulfurization method, is characterized in that, when carrying out wet desulphurization in described step (2), the liquid-gas ratio of white clay slurries and flue gas is 1-30L/Nm
3, be preferably 10-20L/Nm
3, more preferably 14-16L/Nm
3.
10. a kind of white clay according to claim 1-gypsum smoke-gas wet desulfurization method, it is characterized in that, flue gas upflow velocity when carrying out wet desulphurization in described step (2) is 1-10m/s, is preferably 2-6m/s, more preferably 3.2-4m/s.
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| CN107311478A (en) * | 2017-08-16 | 2017-11-03 | 杨泽荣 | White clay reclaims the energy saving and environment friendly recovery method of comprehensive utilization |
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| CN106925088A (en) * | 2015-12-29 | 2017-07-07 | 天津市英派克石化工程有限公司 | A kind of modified technique with white clay desulfurizing agent |
| CN109173632A (en) * | 2018-09-30 | 2019-01-11 | 四川德胜集团钒钛有限公司 | A kind of method of vanadic-titanomagnetite sintering flue gas desulfurization |
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| CN201840984U (en) * | 2010-11-12 | 2011-05-25 | 武汉龙净环保工程有限公司 | Structure of wet-method flue gas desulfurization absorbing tower inlet |
| CN102228783A (en) * | 2011-05-23 | 2011-11-02 | 潍坊恒安散热器集团有限公司 | Process for removing sulfur dioxide in smoke by using white mud and its apparatus |
-
2015
- 2015-02-15 CN CN201510081996.8A patent/CN104689706A/en active Pending
- 2015-09-16 CN CN201510600089.XA patent/CN105080330A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101343077A (en) * | 2008-07-21 | 2009-01-14 | 广东南方碱业股份有限公司 | Method for preparing gypsum by removing boiler flue gas sulphur dioxide with white slime from ammonia alkali factory |
| CN201840984U (en) * | 2010-11-12 | 2011-05-25 | 武汉龙净环保工程有限公司 | Structure of wet-method flue gas desulfurization absorbing tower inlet |
| CN102228783A (en) * | 2011-05-23 | 2011-11-02 | 潍坊恒安散热器集团有限公司 | Process for removing sulfur dioxide in smoke by using white mud and its apparatus |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107311478A (en) * | 2017-08-16 | 2017-11-03 | 杨泽荣 | White clay reclaims the energy saving and environment friendly recovery method of comprehensive utilization |
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