Post-treatment method for washing, drying and calcining SAPO (silicoaluminophosphate) molecular sieve
A molecular sieve and drying technology, applied in the direction of molecular sieve catalyst, molecular sieve and alkali-exchanged phosphate, molecular sieve characteristic silicoaluminophosphate, etc. The effect of dust pollution and low comprehensive energy consumption
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Embodiment 1
[0023] The SAPO molecular sieve mother liquor A of 500Kg after the crystallization is first filtered with a belt filter section 1, and the mother liquor B is separated, and then washed twice at the second section 2 of the belt filter and the third section 3 of the belt filter. The third section 3 of the belt filter is washed with desalted water E, and the obtained secondary washing liquid C is returned to the second section 2 of the belt filter for washing, and the primary washing liquid is filtered to achieve the purpose of recycling, and finally in the belt filter The filter cake F is formed at the end of the machine; then the filter cake F is dried at 400°C using the rotary flash drying device 4 to form a dry molecular sieve fine powder G with a particle size of 6-12 microns; the dry molecular sieve fine powder G passes through a bag filter 5 After collection, use the rotary kiln 6 to roast the molecular sieve fine powder G. The roasting temperature is 550°C, the roasting ti...
Embodiment 2
[0025] The SAPO molecular sieve mother liquor A of 1200Kg after the crystallization is first filtered with a belt filter section 1, and the mother liquor B is separated, and then washed twice in the second section 2 of the belt filter and the third section 3 of the belt filter. The third section 3 of the belt filter is washed with desalted water E, and the obtained secondary washing liquid C is returned to the second section 2 of the belt filter for washing, and the primary washing liquid is filtered to achieve the purpose of recycling, and finally in the belt filter The filter cake F is formed at the end of the machine; then the filter cake F is dried at 600°C using the rotary flash drying device 4 to form a dry molecular sieve fine powder G with a particle size of 8-13 microns; the dry molecular sieve fine powder G passes through a bag filter 5 After collection, use the rotary kiln 6 to roast the molecular sieve fine powder G. The roasting temperature is 700°C, the roasting t...
Embodiment 3
[0027] The SAPO molecular sieve mother liquor A of 800Kg after crystallization is first filtered with belt filter one section 1, and mother liquor B is separated, and then washed twice at belt filter two section 2 and belt filter three section 3, wherein The third section 3 of the belt filter is washed with desalted water E, and the obtained secondary washing liquid C is returned to the second section 2 of the belt filter for washing, and the primary washing liquid is filtered to achieve the purpose of recycling, and finally in the belt filter The filter cake F is formed at the end of the machine; then the filter cake F is dried at 500°C using a rotary flash drying device 4 to form a dry molecular sieve fine powder G with a particle size of 2-16 microns; the dry molecular sieve fine powder G passes through a bag filter 5 After collection, use the rotary kiln 6 to roast the molecular sieve fine powder G. The roasting temperature is 620°C, the roasting time is 5 hours, and the re...
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