Process for producing sulfinate with low content exogenous salt
A sulfinate, low-content technology, applied in the electrolysis process, electrolysis components, etc., can solve the problems of separation, difficulty in zinc salt, etc., and achieve the effect of inhibiting the formation of by-products
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Embodiment 1
[0038] Reaction of crystalline sodium dithionite containing exotic salts with formalin solution to form NaHMS
[0039]In a stirred tank, 880 g of 88% crystalline sodium dithionite (BASF AGHydrosulfite, the balance of foreign salts), ie 4.5 moles of sodium dithionite, was dissolved in about 3.6 L of water. At room temperature, 4.5 moles of formaldehyde (30% (w / w) in formalin) were added over 20 minutes while stirring. After the addition of 4.3 molar NaOH, sodium dithionite had been converted quantitatively (on-line UV spectroscopy) and the pH of the solution was 9.7. A total of 4.31 moles of NaHMS were formed. The corresponding NaHMS yield was 95%, based on the dithionite initially charged.
Embodiment 2
[0041] Sodium dithionite solution (electrolysis effluent) containing foreign salts reacts with formalin solution to form HMS
[0042] Add 2.24 moles of sodium dithionite and 0.6 moles of foreign salts (NaHSO 3 , Na 2 SO 3 ) of electrolytic wastewater. Add 50% NaOH to adjust the pH to pH>8 and pH<10. Then 2.3 moles of formaldehyde (30% (w / w) in formalin) were added over 20 minutes at room temperature while stirring. The final pH was adjusted to pH=11.5 by adding 50% (w / w) NaOH. Sodium dithionite has been converted quantitatively after addition (online UV spectroscopy). In total 2.21 moles of NaHMS were formed. The corresponding NaHMS yield was 98%, based on the initially charged dithionite.
Embodiment 3
[0044] Electrodialysis of NaHMS aqueous solution containing foreign salts
[0045] In the electrodialysis cell (Osmota100, 5 pairs of cells, the electrodes are composed of RA2 and expanded metal titanium, and the electrolyte is 5% (w / w) Na 2 CO 3 , cation exchanger CMX, anion exchanger ASV, film CMB) add the reaction solution to be purified, wherein in the dilution circuit contains 89g / L NaHMS and 116g / L NaHMS 2 SO 3 . At the start of the run, the product loop contained a very dilute salt solution (5.6 g / L NaHMS and 10.6 g / L NaHMS 2 SO 3 ). A current of I = 1.81 A was applied at T = 35°C while circulating both circuits through the pump. After the run, the following concentrations were present in the dilution loop: 5.4 g / L NaHMS and 120 g / L NaHMS 2 SO 3 . Concentrations in the product loop are 94g / L NaHMS and 27.3g / L NaHMS 2 SO 3 .
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