CN1273876A - Process for dusting and dsulfurizing fume - Google Patents

Process for dusting and dsulfurizing fume Download PDF

Info

Publication number
CN1273876A
CN1273876A CN 00103498 CN00103498A CN1273876A CN 1273876 A CN1273876 A CN 1273876A CN 00103498 CN00103498 CN 00103498 CN 00103498 A CN00103498 A CN 00103498A CN 1273876 A CN1273876 A CN 1273876A
Authority
CN
China
Prior art keywords
agent
surfactant
dusting
fume
collecting agent
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN 00103498
Other languages
Chinese (zh)
Other versions
CN1166439C (en
Inventor
宋存义
孙体昌
金龙哲
蒋仲安
段小丽
谢振华
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
University of Science and Technology Beijing USTB
Original Assignee
University of Science and Technology Beijing USTB
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by University of Science and Technology Beijing USTB filed Critical University of Science and Technology Beijing USTB
Priority to CNB001034987A priority Critical patent/CN1166439C/en
Publication of CN1273876A publication Critical patent/CN1273876A/en
Application granted granted Critical
Publication of CN1166439C publication Critical patent/CN1166439C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

A process for dusting and desulfurizing fume includes passing the fume into absorption tower, where it reacts on the sprayed out removing agent containing sodium hydroxide solution, catcher and surfactant, adding lime milk to the mixed liquid after reaction, deposition and filter. Its advantages include cyclic use of sodium hydroxide solution, high dusting effect, less possessed ground area and no secondary pollution.

Description

A kind of process for dusting and dsulfurizing fume
The present invention relates to a kind of process for dusting and dsulfurizing fume, belong to field of environment protection.
SO 2Be main atmosphere pollution, once caused a lot of serious air pollution episodes in some countries.Be control SO 2Atmosphere pollution, people have carried out many research work aspect heavy oil desulfurization, and have obtained progress, but these technology do not cost dearly, and are exactly technical also full maturity not, large-scale application to also have many difficulties; Compare, flue gas desulfurization makes fast progress.What use morely at present is the alkali metal method, it is that flue gas and lime liquor are reacted with desulfurization, but it is because of using a large amount of fat limes, so the fixation means investment is big, floor space is big, the lime handling capacity is big, and is on-the-spot messy, easily causes secondary pollutions such as lime dust, in addition, often to the efficiency of dust collection reduction of dust in the flue gas, also caused pollution control not up to standard after the desulfurization, not thorough.
The object of the present invention is to provide that a kind of floor space is little, dust removal efficiency is high, the process for dusting and dsulfurizing fume of non-secondary pollution.
The object of the present invention is achieved like this:
A kind of process for dusting and dsulfurizing fume, this method is
(1) flue gas being entered the absorption tower has an effect with the agent spraying that removes that contains caustic lye of soda;
(2) in (1) reacted mixed liquor, add an amount of lime slurry;
(3) precipitation, filtration;
(4) the NaOH clear liquid is recycled.
Described removing also contained collecting agent, surfactant in the agent.
Described collecting agent is one or more any mixing in waterglass, potassium silicate, the polyphosphate sodium.Described surfactant is one or more any mixing in sodium alkyl benzene sulfonate, Nekal BX, paregal O-20, the bleeding agent.
Described collecting agent, surfactant and the weight ratio that removes water in the agent are 1: 1-2: 10000~1: 1-3: 1000.
Below the present invention is described in detail: (1) remove NaOH in the agent content and add lime slurry amount all with flue gas in SO 2Concentration is relevant, can decide according to the measurement result to flue gas when specifically using.(2) use NaOH as desulfurizing agent, its handling capacity is little, makes that factory's fixation means investment is little, and floor space is few, and non-secondary pollution.(3) this method generates NaOH clear liquid and calcium sulfate precipitation at last, and the NaOH clear liquid can be recycled, and has reduced cost and workload, and calcium sulfate can be made gypsum and use.(4) adopting collecting agent, surfactant dedusting, is to utilize increases such as waterglass, bleeding agent to remove the viscosity and the activity of agent solution, and ion surface has static, thereby dust in flue gas is adsorbed to fall, and has reduced secondary pollution.
The present invention has following advantage than prior art: (1) is because the NaOH that uses is Powdered, and reproducible utilization, thus to fixation means require low, floor space is little; (2) the collecting agent dust removal efficiency height of choosing can reach more than 95%, almost non-secondary pollution.
Introduce two embodiment of the present invention below:
Embodiment one:
With NaOH 27%, water 69.5%, sodium metasilicate 2%, Nekal BX 1.5% composition mixture; Again above solution being joined to make in 90% the water and remove agent, regenerates with milk of lime in PH after the desulfurization>8.Desulfurization degree almost reaches 100%, and dust removal efficiency reaches 97%.
Embodiment two:
With NaOH 26%, water 70%, potassium silicate 2%, sodium alkyl benzene sulfonate 1%, bleeding agent 1% composition mixture; Above solution being joined in 90% the water, regenerates with milk of lime in PH after the desulfurization>8 again.Desulfurization degree almost reaches 100%, and dust removal efficiency reaches 97.5%.

Claims (4)

1. process for dusting and dsulfurizing fume, it is characterized in that: this method is
(1) flue gas being entered the absorption tower has an effect with the agent spraying that removes that contains caustic lye of soda;
(2) in (1) reacted mixed liquor, add an amount of lime slurry;
(3) precipitation, filtration;
(4) the NaOH clear liquid is recycled.
2. method according to claim 1 is characterized in that described removing also contain collecting agent and surfactant in the agent.
3. method according to claim 2 is characterized in that described collecting agent is one or more any mixing in waterglass, potassium silicate, the polyphosphate sodium.Surfactant is one or more any mixing in sodium alkyl benzene sulfonate, Nekal BX, paregal O-20, the bleeding agent.
4. according to claim 2 or 3 described methods, the weight ratio that it is characterized in that collecting agent, surfactant and remove water in the agent is 1: 1-2: 10000~1: 1-3: 1000.
CNB001034987A 2000-03-15 2000-03-15 Process for dusting and dsulfurizing fume Expired - Fee Related CN1166439C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB001034987A CN1166439C (en) 2000-03-15 2000-03-15 Process for dusting and dsulfurizing fume

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB001034987A CN1166439C (en) 2000-03-15 2000-03-15 Process for dusting and dsulfurizing fume

Publications (2)

Publication Number Publication Date
CN1273876A true CN1273876A (en) 2000-11-22
CN1166439C CN1166439C (en) 2004-09-15

Family

ID=4577031

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB001034987A Expired - Fee Related CN1166439C (en) 2000-03-15 2000-03-15 Process for dusting and dsulfurizing fume

Country Status (1)

Country Link
CN (1) CN1166439C (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101844028A (en) * 2010-03-02 2010-09-29 江苏工业学院 Composite flue gas desulfurization agent and preparation method thereof
CN104492203A (en) * 2014-12-04 2015-04-08 常州大学 Gas-liquid-phase medium flue gas dust removal method
CN104923001A (en) * 2015-06-05 2015-09-23 北京中晶佳镁环境科技股份有限公司 Dedusting composition, desulfuration composition and usages
CN104941577A (en) * 2015-04-22 2015-09-30 芜湖市鸿坤汽车零部件有限公司 Banana peel modified active carbon kieselguhr particles for desulphurization and dust removal and preparation method for banana peel modified active carbon kieselguhr particles
EP2300168B1 (en) * 2008-07-15 2019-10-02 3 Nine AB A method and a filter for capturing airborne agents

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2300168B1 (en) * 2008-07-15 2019-10-02 3 Nine AB A method and a filter for capturing airborne agents
CN101844028A (en) * 2010-03-02 2010-09-29 江苏工业学院 Composite flue gas desulfurization agent and preparation method thereof
CN104492203A (en) * 2014-12-04 2015-04-08 常州大学 Gas-liquid-phase medium flue gas dust removal method
CN104941577A (en) * 2015-04-22 2015-09-30 芜湖市鸿坤汽车零部件有限公司 Banana peel modified active carbon kieselguhr particles for desulphurization and dust removal and preparation method for banana peel modified active carbon kieselguhr particles
CN104923001A (en) * 2015-06-05 2015-09-23 北京中晶佳镁环境科技股份有限公司 Dedusting composition, desulfuration composition and usages

Also Published As

Publication number Publication date
CN1166439C (en) 2004-09-15

Similar Documents

Publication Publication Date Title
CN103768924B (en) A kind of method for purifying wet desulphurization neat stress further and device
CN106881019A (en) A kind of method that utilization red mud and activated carbon thermal activation prepare desulfurizing agent
CN104474830B (en) For removing chemical agglomeration promotor and the using method thereof of coal-fired fine particle
CN101347706A (en) Flue gas desulfurization technique using dual alkali method with acetylene sludge as recycling agent
CN101574615A (en) Desulfurizing method and synergistic agent thereof
CN1899670A (en) Method for treating SO2 in coal firing smoke by red mud
CN1272088C (en) Method of proceeding desulfurzation of smoke using waste alkali slag
CN101507932A (en) Preparation method of material capable of removing hydrogen sulphide and thiol
CN1166439C (en) Process for dusting and dsulfurizing fume
CN106268241B (en) Copper making ring collection fume desulphurization method and device
CN103566750B (en) A kind of fume desulphurization method
CN102228783A (en) Process for removing sulfur dioxide in smoke by using white mud and its apparatus
CN114229852A (en) Method for removing SO in flue gas by using steel slag2Method for synergistically extracting silica gel
CN107308783B (en) Wet-process simultaneous desulfurization and denitrification process for flue gas
CN1907548A (en) Exhaust gas purification liquid
CN108295585A (en) Coal-burning boiler flue dust stirs clarifier
CN100518893C (en) Method for purifying vanadium-contained stone coal sodium calcinating smoke
CN1448209A (en) Flue gas dry desulfurizing pollution-controlling technique
CN1123374C (en) Method for removing sulfur oxides from flue-gas by utilizing waste sludge of soda plant
CN1727055A (en) Method for carrying out flue gas desulfurization by using mineral powder of magnesite
CN109482048B (en) Low-concentration flue gas desulfurization method for smelting of silicon carbide by using water and electricity
KR100517175B1 (en) Method for desulfurizing fluegas
JPH0999234A (en) Treating agent for waste gas and soot and dust and its treatment
Karatepe et al. Effect of hydration conditions on the physical properties of fly ash-Ca (OH) 2 sorbents
CN104379238A (en) Absorption of toxic so2 and co2 compounds in emitted gasses in boron and calcium based process waste solutions and convertion of the same into commercial products

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20040915

Termination date: 20150315

EXPY Termination of patent right or utility model