Method for production of quaternary ammonium hydroxide
A technology of quaternary ammonium base and halogenated quaternary ammonium salt, which is applied in chemical instruments and methods, electrolytic organic production, electrolytic components, etc., and can solve problems such as difficulty in completely isolating halogen gas and oxidation degradation of anion exchange membranes
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Embodiment 1
[0130] According to the following formulation, a paste mixture (polymerizable composition) for forming an anion exchange membrane was prepared.
[0131] The recipe of the paste mixture:
[0132] Chloromethylstyrene 50 parts by weight
[0133] Styrene 50 parts by weight
[0134] Divinylbenzene 21.4 parts by weight
[0135] Di-tert-butyl peroxide (radical polymerization initiator) 7.14 parts by weight
[0136] Styrene-butadiene copolymer (base resin) 14.3 parts by weight
[0137] Next, as a skeleton base material, a calendered high-density polyethylene net of the following specifications was prepared.
[0138] High density polyethylene net:
[0139] Commodity name: NBC Industrial System Nipp Qiangli Net
[0140] Thickness: 150μm
[0141] Number of meshes: 200 per 1 square meter
[0142] The pre-prepared paste mixture is coated on the skeleton substrate, and then a polyester film (release film) is coated, and then the paste mixture is polymerized to obtain the original film of the anion exchang...
Embodiment 2
[0153] Use the anion exchange membrane A and cation exchange membrane C used in Example 1, except for installing figure 2 The effective membrane area of the setup shown is 2dm 2 Except for the electrolysis device of, electrolysis was performed in the same manner as in Example 1. (The anion exchange membrane A is set so that the surface crosslinking layer is located on the anode side.)
[0154] That is, in figure 2 0.5 equivalent of sulfuric acid is circulated in the anode chamber 11 of the electrolysis device shown, 0.5 equivalent of hydrochloric acid is circulated in the chamber 7 between the cation exchange membrane C and the anion exchange membrane A on the anode side, and the anion exchange membrane A and the cathode side Circulate 2.5 equivalents of tetramethylammonium chloride aqueous solution in the chamber between the cation exchange membrane C (stock solution chamber 5), and circulate pure water in the cathode chamber 9, with a current density of 30A / dm 2 , The temper...
Embodiment 3
[0157] The anion exchange membrane A was prepared in the same manner as in Example 1, except that it was immersed in a 1.0-N dimethylamine aqueous solution for 3 hours to form a surface crosslinked layer on one side of the original membrane.
[0158] The exchange capacity of the surface crosslinked layer at this time was 0.008 meq / g dry film. In addition, the ion exchange capacity of the anion exchange membrane A before electrolysis is 1.2 meq / g dry membrane, the rupture strength of the Mullen type is 1.0 MPa or more, and the water permeability is 0 ml / (m 2 ·Hour·0.1MPa).
[0159] Except for the use of the above-mentioned anion exchange membrane A, the electrolysis operation was continuously carried out in exactly the same manner as in Example 2. As a result, the ion exchange capacity of the anion exchange membrane A after 1 year of continuous operation was 1.0 meq / g dry membrane. The breaking strength of the formula is 0.9MPa, and the water permeability is 0ml / (m 2 ·Hour·0.1MPa). ...
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