Method for preparing hypophosphorous acid by using electrolytic method
A hypophosphorous acid and electrolysis technology, applied in the direction of electrolysis process, electrolysis components, etc., can solve the problems of large-scale industrial production restrictions, expensive precious metal electrodes, etc., and achieve the effects of easy large-scale industrial production, low price, and simple process.
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Embodiment 1
[0018] The anode material is graphite, and the electrode area is 40cm 2 , The cathode is a stainless steel electrode. Anion and cation exchange membranes were purchased from Shanghai Chemical Plant, and the membrane area used in electrolysis was 48cm 2 . The solution volume of each chamber of the six-chamber electrodialysis cell is 500ml. The initial solution of the anode chamber before electrolysis is 10g / L sulfuric acid, the raw material chamber is 500g / L sodium hypophosphite, the cathode chamber and its adjacent buffer chamber are both 10g / L sodium hydroxide, and the product chamber and its adjacent buffer chamber are both 10g / L hypophosphorous acid.
[0019] Under the conditions of working voltage of 10-15V and holding current of 3.0A, after continuous electrolysis for 6 hours, the concentration of hypophosphorous acid in the product chamber is 69.3g / L, and the calculated current efficiency at this time is 80.9%.
[0020] After 6H electrolysis under different current c...
Embodiment 2
[0029] The initial working conditions of the six-chamber electrodialysis cell are the same as in Example 1.
[0030] When the working current is 3A, the electrolysis time is 30H, the concentration of hypophosphorous acid in the product chamber is 178.6g / L, and the current efficiency is 55.3%.
[0031] The concentrations of the hypophosphorous acid solution in the product chamber obtained under different electrolysis times are shown in Table 2.
[0032] Table 2 Product concentration and current efficiency under different electrolysis time
[0033] Electrolysis time (H) Hypophosphorous acid concentration (g / L) Current efficiency (%)
[0034] 6 69.3 80.9
[0035] 12 101.9 77.4
[0036] 18 136.1 68.3
[0037] 24 169.1 60.5
[0038] 30 178.6 55.3
Embodiment 3
[0040] The initial working conditions of the six-chamber electrodialysis cell are the same as in Example 1.
[0041] When the working current is 3A, the electrolysis time is 30H, and the contents of sodium ion and sulfate ion in the product chamber are 50ug / L and 0.80g / L respectively.
[0042] The contents of sodium ions and sulfate ions in the product compartment obtained under different electrolysis times are shown in Table 3.
[0043] Table 3 Changes of sodium ion and sulfate ion content in hypophosphorous acid products with time
[0044] Electrolysis time (H) Sodium ion content (ug / L) Sulfate content (g / L)
[0045] 6 5 0.11
[0046] 12 13 0.36
[0047] 18 25 0.48
[0048] 24 40 0.76
[0049] 30 50 0.80
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