Recovery method for NMMO solvent in fibre production by solvent method
A recovery method and technology of a solvent method are applied in the recovery field of solvent N-methylmorpholine oxide, can solve problems such as unfavorable control cost, pollute the environment, large amount of water vapor, etc., achieve environmental protection and reduce production cost , the effect of saving energy consumption
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Embodiment 1
[0027] The recycling of the NMMO waste liquid collected from the coagulation bath and the drawing tank includes the following steps:
[0028] 1. The NMMO waste liquid a (concentration 25%, weight 811 kilograms) and waste liquid b (concentration 12%, weight 695 kilograms) reclaimed from coagulation bath and drawing tank are mixed by mixer (the mixing ratio of a, b waste liquid 6~5:4~5), the mixed waste liquid c (concentration 19%) is sent into the head tank.
[0029] 2. The waste liquid c passes through a mechanical filter to remove solid impurities and enters the clear liquid storage tank.
[0030] 3. Put the filtered liquid into the cationic resin exchange column at a flow rate of 3.2BV / h to remove metal ions and put the treated liquid into the clear liquid storage tank.
[0031] 4. Put the liquid after removing metal ions into the anion resin exchange column at a flow rate of 3.2BV / h to remove colored substances and decomposition products, and put the treated liquid into th...
Embodiment 2
[0036] The recovery treatment of the NMMO waste liquid recovered from the washing tank includes the following steps:
[0037] 1. Waste liquid a (concentration 0.05%, weight 645.8 kilograms) and waste liquid b (concentration 1.86%, weight 872.2 kilograms) containing NMMO from each washing tank are mixed through a mixer, and the concentration of NMMO waste liquid c after mixing is 0.82%.
[0038] 2. The waste liquid c enters the high-level tank after removing solid impurities through a mechanical filter.
[0039] 3. Put the filtered solvent into the cationic resin exchange column at a flow rate of 3.6BV / h and put the collected solution into the clear liquid storage tank.
[0040] 4. Pour the liquid in the clear liquid storage tank in step 3 into the anion resin exchange column at a flow rate of 3.6BV / h and put the collected liquid into the clear liquid storage tank.
[0041] 5. Pour the liquid in the clear liquid storage tank in step 4 into the reverse osmosis treatment tank f...
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