Bittern bromine-blowing process

A kind of bittern and process technology, applied in the field of bromine extraction, can solve problems such as no bittern blowing bromine, bromine loss, etc., to avoid environmental pollution and improve the effect of obtaining rate

Inactive Publication Date: 2014-08-06
唐山三友盐化有限公司
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Problems solved by technology

[0008] At present, the mother liquor of sea salt production - bittern (brine) (2000ppm) is sun-dried and concentrated, and then enters the salt chemical workshop to produce potassium chloride, bromine (steam distillation method), and magnesium chloride. There is about 30%-40% penetration, and the loss of bromine is also caused in the production of potassium ch...

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Embodiment Construction

[0028] The present invention will be further described below in conjunction with the accompanying drawings.

[0029] The invention discloses a high-concentration bittern bromine blowing process. The process adopts the methods of oxidation, blowing, absorption and distillation to extract bromine from bittern (high-concentration bittern is called bittern). The specific process steps are:

[0030] 1) Choose bittern with a bromine content of 1000-2500ppm as the raw material, adjust the ph value with acid liquid before the raw bittern enters the blowing tower, and adjust the ph to 2-3.5 through a mixer;

[0031] 2) Oxidation stage: the bittern is pumped into the high-efficiency gas-liquid and liquid-liquid mixing mixer 2 with the bittern pump 1, the acid concentration is 10-13%, the pH is controlled at 2.0-3.5, and the chlorine mixing rate is 110-130%. In mixer 2, bittern is fully contacted with chlorine gas, and the oxidation rate is above 90%.

[0032] 3) Blow-out stage: the oxi...

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Abstract

The invention discloses a bittern bromine-blowing process comprising oxidation, blowout, absorption and distillation. A blowout tower and a mixer are used in the process. The process comprises the steps of selecting bittern of which the bromine content is 1000-2500ppm as a raw material, and adjusting the pH value to 2-3.5 before the bittern raw material is fed into the blowout tower; and performing a bittern oxidation stage and a blowout stage on the bittern, then feeding the bittern into an absorption tower to perform concurrent flow gas liquid contact with absorption completed liquid, and performing absorption operation, wherein the bromine content of the absorption completed liquid is 80-100g/L. The bromine is extracted from the mother solution (bittern) of sea salt production by adopting the oxidation and blowout method, and the blowout tower and the mixer are used in the process, so that the bromine extraction process is scientific, the yield of the bromine is 2.5 times that of a water vapor distillation method, and the power consumption of the process is 60% of that of an intermediate bittern bromine-blowing process. The total extraction rate is over 85%. The process initiates the process equipment parameters of high bromine content, high viscosity and high specific gravity raw material condition, and is used for design and production.

Description

technical field [0001] The invention relates to a bromine extraction technology, in particular to a bittern bromine blowing process, which adopts oxidation and blowing methods to extract bromine from the mother liquor (brine) produced by sea salt, and is also applicable to other bromine-containing ( 1000-2500ppm) raw material to extract bromine. Background technique [0002] Bromine is an important chemical raw material, mainly used in energy, automobiles, medicine, pesticides, dyes, flame retardants, fire extinguishing agents, refrigerants, photosensitive materials, etc. [0003] Bromine is mainly taken from seawater and concentrated seawater (including underground brine). The bromine content of seawater is 65ppm; the bromine content of underground brine in Shandong, China is 200ppm; the dead sea of ​​Israel is 3000-10000ppm; India is 3000-5000ppm; the shallow sea of ​​Ukraine is 600-1000ppm; the deep brine of the United States is 2000-3000ppm. [0004] The world's bromin...

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Application Information

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IPC IPC(8): C01B7/09
Inventor 王伟安彦平李学德马海永袁泽民徐默谦李翠敏
Owner 唐山三友盐化有限公司
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