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
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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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