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Solid-waste-discharge-free membrane method total halogenated caustic production method

A membrane method and brine technology, applied in the direction of alkali metal chloride, alkali metal halide purification, electrolysis process, etc., can solve the problems of incapable of high-concentration brine, difficult salt mud treatment, denitrification treatment, etc., to save salt consumption, brine The effect of reducing the cost of denitration and high filtration accuracy

Inactive Publication Date: 2019-10-25
安徽星奇达膜科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, domestic chlor-alkali enterprises only use the membrane method for denitrification of light brine, but not for denitrification of high-concentration brine (NaCl>260g / L).
Therefore, for brine denitrification, this requires that the saturated brine mined from the ground must first be added with water to reduce the NaCl content in it, and then increase the NaCl content through the denitrification process, which is inefficient
In addition, the content of calcium and magnesium ions in brine is relatively high, and domestic chlor-alkali enterprises mainly use the two-alkali method to remove them, by adding NaOH, Na 2 CO 3 , the reaction produces Mg(OH) 2 , CaCO 3 The solid matter is then trapped in the concentrated solution through the membrane, and then the salt mud is pressed out through the filter press, and the salt mud is sent to the outside for treatment, but the subsequent treatment of the salt mud is becoming more and more difficult

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] The content of NaCl in the brine mined from the mine is 300g / L, SO 4 2- Content 12g / L, Ca 2+ Content 0.65g / L, Mg 2+ content of 0.07g / L, pump it directly into the baffle tank, add 2.1g / L of sodium carbonate, 0.35g / L of sodium hydroxide, and 20mg / L of sodium hypochlorite into the baffle tank, and then flow into the reaction tank for refining reaction; Among them, the Mg in the salt 2+ , Ca 2+ Respectively with NaOH, Na 2 CO 3 The reaction produces Mg(OH) 2 , CaCO 3 The solid matter and crude brine after refined reaction are sent to the organic tubular membrane system. The organic tubular membrane system is composed of 2 sets of membrane stacks. Each set of membrane stacks is connected in series with 5 organic tubular membrane modules with a diameter of 10 inches and a length of 4m. The tubular membrane channel is 5mm, the pore size is 30nm, and the membrane material is polyvinylidene fluoride; the control operating pressure is 0.3MPa, the membrane surface flow rat...

Embodiment 2

[0035] The content of NaCl in the brine mined from the mine is 295g / L, SO 4 2- Content 18g / L, Ca 2+ Content 1.32g / L, Mg 2+ content of 0.18g / L, directly pumped into the baffle tank, metered into the baffle tank 4g / L of sodium carbonate, 0.9g / L of sodium hydroxide, 30mg / L of sodium hypochlorite, and then flowed into the reaction barrel for refining reaction; Mg in salt 2+ , Ca 2+ Respectively with NaOH, Na 2 CO 3 The reaction produces Mg(OH) 2 , CaCO 3 The solid matter and crude brine after refined reaction are fed into the organic tubular membrane system. The organic tubular membrane system is composed of 4 sets of membrane stacks. Each set of membrane stacks is connected in series with 6 organic tubular membrane modules with a diameter of 10 inches and a length of 4m. The tubular membrane channel is 8mm, the pore size is 50nm, and the membrane material is polyvinylidene fluoride. The organic tubular membrane controls the operating pressure to 0.35MPa, the membrane sur...

Embodiment 3

[0039] The content of NaCl in the brine mined from the mine is 295g / L, SO 4 2- Content 13g / L, Ca 2+ Content 0.86g / L, Mg 2+ Content 0.1g / L, directly pumped into the baffle tank, metered into the baffle tank 2.7g / L of sodium carbonate, 0.53g / L of sodium hydroxide, 20mg / L of sodium hypochlorite, and then flowed into the reaction tank for refining reaction; Among them, Mg in salt 2+ , Ca 2+ Respectively with NaOH, Na 2 CO 3 The reaction produces Mg(OH) 2 , CaCO 3 The solid matter and crude brine after refined reaction are sent to the organic tubular membrane system. The organic tubular membrane system is composed of a set of membrane stacks. Each set of membrane stacks is connected in series with 4 organic tubular membrane modules with a diameter of 8 inches and a length of 3m. The tubular membrane channel is 5mm, the pore size is 30nm, and the membrane material is polyvinylidene fluoride. The operating pressure is controlled to 0.3MPa, the membrane surface flow velocity ...

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PUM

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Abstract

The invention relates to a solid-waste-discharge-free membrane method total halogenated caustic production method. The solid-waste-discharge-free membrane method total halogenated caustic production method comprises the following steps that brine is sent to an organic tubular membrane system for filtration after refining reaction, and the filtered permeate is divided into two parts, and one part of the permeate is denitrated to obtain low nitrate brine and high nitrate brine; the other part of the permeate is mixed with the low nitrate brine obtained in the step S1 to obtain first brine; and the first brine is adsorbed and then caustic soda and light slat brine are prepared through an ion membrane alkali produced system. According to the solid-waste-discharge-free membrane method total halogenated caustic production method, an alkali resistant nanofiltration membrane is used for denitrating the brine directly. Compared with a traditional process that water is added firstly for dilutionand then salt is dissolved to saturation, salt consumption, steam consumption and water consumption are saved, and the denitration cost is greatly reduced. In addition, the high nitrate brine is injected into wells with Mg(OH)2 and CaCO3 mud to solve the outlet problem of the high nitrate brine and the subsequent difficulties of treating the salt mud.

Description

technical field [0001] The invention belongs to the technical field of brine refining, and in particular relates to a membrane-based all-halogen soda production method without solid waste discharge. Background technique [0002] At present, the domestic chlor-alkali industry mainly adopts the ion-exchange membrane method to make alkali, and uses saturated brine as raw material to electrolyze to produce sodium hydroxide and other products. OH - The insoluble matter produced by the reaction is deposited on the ionic membrane, which seriously affects the life of the ionic membrane. Therefore, brine refining is extremely important in the production process of ionic membrane alkali production. [0003] The domestic traditional primary brine refining process based on the "barrel reactor + Doyle clarifier + sand filter" process route has been basically eliminated. At present, domestic chlor-alkali enterprises mainly use the following two membrane filtration processes: Gore membran...

Claims

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Application Information

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IPC IPC(8): C01D3/14C01D3/06C25B1/46
CPCC01D3/06C01D3/14C25B1/46
Inventor 石风强尹燕亓庆珺
Owner 安徽星奇达膜科技有限公司
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