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A kind of flushing emulsion for wet electrostatic precipitator and preparation method thereof

A wet electrostatic precipitator and emulsion technology, which is applied in the field of washing emulsion, can solve the problems of single purpose and unsatisfactory effect, and achieve the effects of low production cost, excellent material selection, and improved gas-liquid mass transfer coefficient

Active Publication Date: 2018-03-23
JIANGSU CTIEC ENVIRONMENTAL PROTECTION RES INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The flushing water of the wet electrostatic precipitator is generally taken directly from the circulating industrial water of the power plant or connected through other water sources whose water quality is equal to the desulfurization process water. The flushing is mainly for dust removal or anti-corrosion. The purpose is relatively single, and the effect is not as expected.

Method used

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  • A kind of flushing emulsion for wet electrostatic precipitator and preparation method thereof
  • A kind of flushing emulsion for wet electrostatic precipitator and preparation method thereof
  • A kind of flushing emulsion for wet electrostatic precipitator and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] The flushing emulsion for a wet electric precipitator described in this embodiment includes the following components by weight percentage:

[0032] Solvent 7%

[0033] Surfactant 2%

[0034] Additive 0.6%

[0035] NaOH 2%

[0036] Deionized water balance.

[0037] The solvent is made by mixing and stirring oleic acid and acrylic acid at a temperature of 60° C. and a pressure of 0.6 MPa for 5 minutes, and the weight percentage of the oleic acid and acrylic acid is 68% and 32%.

[0038] The surfactant is composed of cetyltrimethylammonium bromide, C12 fatty alcohol polyoxyethylene (9) ether, and sodium lauryl sulfate mixed and stirred in the reactor for 7 minutes. The bottom of the kettle is filled with oxygen for 1 minute, and the oxygen filling amount is 4 liters / min. The weight percentages of the cetyltrimethylammonium bromide, C12 fatty alcohol polyoxyethylene (9) ether, and sodium lauryl sulfate are 30%:40%:30%.

[0039] The additives are made by mixing and stirring sodium benz...

Embodiment 2

[0057] The flushing emulsion for a wet electrostatic precipitator described in this embodiment includes the following components by weight percentage:

[0058] Solvent 5%

[0059] Surfactant 2%

[0060] Additive 0.5%

[0061] NaOH 3%

[0062] Deionized water balance.

[0063] The solvent is made by mixing and stirring oleic acid and acrylic acid at a temperature of 55° C. and a pressure of 0.8 MPa for 4 minutes, and the weight percentage of the oleic acid and acrylic acid is 70% and 30%.

[0064] The surfactant is made of cetyltrimethylammonium bromide, C12 fatty alcohol polyoxyethylene (9) ether, and sodium lauryl sulfate mixed and stirred in the reaction kettle for 8 minutes. The bottom of the kettle is filled with oxygen for 1 minute, and the oxygen filling amount is 4 liters / minute. The weight percentages of the cetyltrimethylammonium bromide, C12 fatty alcohol polyoxyethylene (9) ether, and sodium lauryl sulfate are 29%:44%:27%.

[0065] The additives are made by mixing and stirring...

Embodiment 3

[0083] The flushing emulsion for a wet electrostatic precipitator described in this embodiment includes the following components by weight percentage:

[0084] Solvent 10%

[0085] Surfactant 1%

[0086] Additive 0.8%

[0087] NaOH 1%

[0088] Deionized water balance.

[0089] The solvent is made by mixing and stirring oleic acid and acrylic acid at a temperature of 65° C. and a pressure of 0.5 MPa for 6 minutes, and the weight percentage of the oleic acid and acrylic acid is 70% and 30%.

[0090] The surfactant is composed of cetyltrimethylammonium bromide, C12 fatty alcohol polyoxyethylene (9) ether, and sodium lauryl sulfate mixed and stirred in the reaction kettle for 5 minutes. The bottom of the kettle is filled with oxygen for 2 minutes, and the oxygen filling amount is 3 liters / min. The weight percentages of the cetyltrimethylammonium bromide, C12 fatty alcohol polyoxyethylene (9) ether, and sodium lauryl sulfate are 32%: 37%: 31%.

[0091] The additive is made by mixing and stirr...

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Abstract

The invention discloses a flushing emulsion for a wet type electric dust collector. The flushing emulsion comprises the following components in percentage by weight: 5-10% of a solvent, 1-2% of a surfactant, 0.5-0.8% of an additive, 1-3% of NaOH, and the balance deionized water. According to the flushing emulsion disclosed by the invention, selected materials are excellent, a scientific processing method is adopted, and the processed flushing emulsion can cooperatively remove SOX, soluble salts, Hg and the like in smoke gas, so that the comprehensive purifying capacity is improved; emulsion droplets have relatively great interfacial areas, so that the inter-phase contact area is increased, and the heat exchange process is strengthened; and meanwhile, a hybrid type surfactant is added into the emulsion, and the flushing emulsion is prepared in a high-temperature high-pressure environment, so that a gas-liquid mass transfer coefficient can be increased, and the dispersity and the activity of the emulsion are strengthened; obvious effect-raising action is achieved on the wet type electric dust collector while ash is conveniently flushed in a flushing process, so that deep purification can be realized more effectively; and the flushing emulsion has remarkable environmental benefits, economic benefits and social benefits.

Description

Technical field [0001] The invention belongs to the technical field of flushing emulsions, and particularly relates to a flushing emulsion used for improving the efficiency of a wet electric precipitator. Background technique [0002] In order to achieve "ultra-low emission" of flue gas pollutants, coal-fired power plants will choose to install a wet electrostatic precipitator as the terminal purification device. However, the effect of wet electrostatic precipitator on the removal of fine particles is not stable enough, and the flue gas after desulfurization generally contains soluble salts (fluoride, chloride, etc.), SO X , NO X Strong corrosive substances such as high corrosion strength, strong permeability and difficult to prevent low-temperature and high-humidity dilute acid corrosion conditions. The flue gas environment (low temperature, high humidity, etc.) after desulfurization further aggravates the corrosion conditions. When the temperature of the liquid is 40℃-80℃, it i...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B03C3/16C11D1/86C11D3/60B01D53/00
CPCB01D53/00B01D2257/302B01D2257/602B03C3/16C11D1/14C11D1/62C11D1/72C11D1/86C11D3/044C11D3/046C11D3/2079C11D3/43
Inventor 张志刚王东歌李继田勇郑美玲
Owner JIANGSU CTIEC ENVIRONMENTAL PROTECTION RES INST
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