Process for secondary treating of waste alkali liquid during production of viscose fibers
A viscose fiber and secondary treatment technology is applied in the field of viscose fiber to achieve the effects of reducing environmental pollution, improving ecological benefits and low energy consumption
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Embodiment 1
[0026] A secondary treatment method for waste lye in viscose fiber production, comprising the following process steps:
[0027] A. Prepare waste lye and desalinated water with a sodium hydroxide concentration of 70g / L and a semi-fiber content of 60g / L after conventional pretreatment;
[0028] B. The temperature of the pretreated waste lye and desalinated water obtained in control step A is 20°C, and the pretreated waste lye and desalted water are transported to the diffusion dialysis membrane stack for diffusion dialysis. The pretreated spent lye The flow ratio with desalted water is 1:1;
[0029] C. After diffusion dialysis, the lye with low hemicellulose concentration is separated from the lye with high hemicellulose concentration, and the lye with low hemicellulose concentration is reused in production.
Embodiment 2
[0031] A secondary treatment method for waste lye in viscose fiber production, comprising the following process steps:
[0032] A. Prepare waste lye and desalinated water with a sodium hydroxide concentration of 90 g / L and a hemifiber content of 70 g / L after conventional pretreatment;
[0033] B. The temperature of the pretreated waste lye and desalinated water obtained in control step A is 35°C, and the pretreated waste lye and desalted water are transported to the diffusion dialysis membrane stack for diffusion dialysis. The pretreated spent lye The flow ratio with desalted water is 2:1;
[0034] C. After diffusion dialysis, the lye with low hemicellulose concentration is separated from the lye with high hemicellulose concentration, and the lye with low hemicellulose concentration is reused in production.
Embodiment 3
[0036] A secondary treatment method for waste lye in viscose fiber production, comprising the following process steps:
[0037] A. Prepare waste lye and desalinated water with a sodium hydroxide concentration of 80g / L and a hemifiber content of 65g / L after conventional pretreatment;
[0038] B. The temperature of the pretreated waste lye and demineralized water obtained in control step A is 27.5°C, and the pretreated waste lye and demineralized water are transported to the diffusion dialysis membrane stack for diffusion dialysis. The pretreated waste lye The flow ratio to desalted water is 1.5:1;
[0039] C. After diffusion dialysis, the lye with low hemicellulose concentration is separated from the lye with high hemicellulose concentration, and the lye with low hemicellulose concentration is reused in production.
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