Novel alkali recovery technology during viscose fiber production
A viscose fiber and new process technology, applied in alkali metal compounds, alkali metal oxides/hydroxides, inorganic chemistry, etc., to achieve stable operation, low energy consumption, and no power consumption
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Embodiment 1
[0036] A new alkali recovery process in the production of viscose fiber, the pretreated waste alkali and desalted water are transported to the membrane module through the pump at a flow ratio of 1:1 to the diffusion dialysis membrane unit, and the waste alkali that flows out Through the anode chamber of electrodialysis, the dilute lye passes through the cathode chamber as electrolyte, reclaims the concentrated alkali that the cathode chamber obtains, the described spent lye sodium hydroxide concentration after pretreatment is 50g / L, and semi-fiber content is 50g / L.
Embodiment 2
[0038] A new alkali recovery process in the production of viscose fiber. The pretreated waste alkali and desalted water are transported to the membrane module through the pump at a flow ratio of 2:1 to the diffusion dialysis membrane unit, and the waste alkali that flows out Through the anode chamber of electrodialysis, the dilute lye passes through the cathode chamber as electrolyte, and reclaims the concentrated alkali obtained in the cathode chamber. The sodium hydroxide concentration of the pretreated waste lye is 200g / L, and the semi-fiber content is 150g / L.
[0039] The spent lye and demineralized water enter the diffusion dialysis membrane unit in a cross-flow manner.
[0040] The process operates at a temperature of 45°C.
[0041] The gauge pressure of the pump is 0.08Mpa.
Embodiment 3
[0043] A new alkali recovery process in the production of viscose fiber. The pretreated waste alkali and desalted water are transported to the membrane module through the pump at a flow ratio of 1.5:1 to the diffusion dialysis membrane unit, and the waste alkali that flows out Through the anode chamber of electrodialysis, the dilute lye passes through the cathode chamber as electrolyte, and the concentrated alkali obtained in the cathode chamber is reclaimed. The pretreated waste lye sodium hydroxide concentration is 80g / L, and the semi-fiber content is 20g / L.
[0044] The spent lye and demineralized water enter the diffusion dialysis membrane unit in a cross-flow manner.
[0045] The temperature of the electrodialysis is 15°C.
[0046] The gauge pressure of the pump is 0.03Mpa.
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