Molecular sieve crystallization mother liquor treatment method
A treatment method and technology for crystallization mother liquor, applied in molecular sieve and alkali exchange phosphate, molecular sieve characteristic silicoaluminophosphate, distillation in boiler/distillate, etc. The effect of reducing labor intensity, avoiding leakage of harmful substances, and solving processing difficulties
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Embodiment 1
[0035] use figure 1 process shown. The crystallization mother liquor used is the filtrate obtained by filtration and separation after the synthesis of SAPO-34 molecular sieve. The triethylamine content of the template agent is 7.6%, and the total solid content of the mother liquor is about 9%. Set of steam heating, the working temperature is 39 ℃.
[0036] When starting to run, the vacuum pump will evacuate the decompression dehydration device system. After the vacuum reaches -0.091MPa, the liquid inlet valve will automatically open the liquid inlet, and the liquid inlet volume will be 250L / time; after the liquid inlet is completed, it will be heated with steam, and the steam pressure will be 0.17MPa, and start at the same time In-tank mixer.
[0037] The steam evaporated from the mother liquor is simply filtered by the aerosol dust collector and then enters the shell and tube condenser to condense to form a liquid. The condensate automatically enters the waste water storage...
Embodiment 2
[0043] According to the conditions and steps described in Example 1, the vacuum dehydration device obtains residues with a water content of 50-51%, and enters the vacuum belt dryer system for drying. Only the temperature of the heating zone is changed: the first zone is 130 ° C, the second Zone 100°C, third zone 40°C, other conditions are the same as in Example 1. The moisture content of the obtained discharged solid powder was 1.57%.
Embodiment 3
[0045] According to the conditions and steps described in Example 1, the vacuum dehydration device obtains a residue with a water content of 50-51%, and enters the vacuum belt dryer system for drying, only changing the heating temperature: the first zone 160 ° C, the second zone 160°C, 40°C in the third zone, other conditions are the same as in Example 1. The moisture content of the obtained discharged solid powder was 0.38%.
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