Method of crystallization
The present invention proposes a crystallization process comprising the steps of feeding a slurry solution in which a terephthalic acid solution or a part of the terephthalic acid is precipitated to a crystallization vessel, precipitating the terephthalic acid in the crystallization vessel, generating a slurry containing crystals and solvent, discharging the slurry, and further comprising the steps of introducing the slurry in a tangential the direction of a hydrocyclone, returning the slurry flowing out as a downward swirling flow from a lower part of the hydrocyclone to the vessel, and discharging the slurry overflowing from the upper part of the hydrocyclone. According to the present invention, crystals of large particle size is obtained and a stable driving ranging long term can be achieved because any adhesion or accumulation of the terephthalic acid crystals does not appear at all in the crystallization vessel.
1. A crystallization process including the steps of feeding a terephthalic acid solution or a slurry solution in which a part of the terephthalic acid is precipitated to a crystallization vessel, precipitating the terephthalic acid in the crystallization vessel, generating a slurry containing crystals and solvent, and discharging the slurry, and comprising the further steps of:
(i) introducing the slurry discharged from the crystallization vessel to a hydrocyclone, in a tangential direction of the hydrocyclone,
(ii) returning all amount of the concentrated slurry flowing out as a downward swirling flow from a lower part of the hydrocyclone directly to the crystallization vessel, and
(iii) discharging the slurry overflowing from an upper part of the hydrocyclone, wherein the concentration of crystals in said slurry overflowing from said upper part of said hydrocyclone is 5% or less.
2. The crystallization process according to claim 1 , wherein said precipitating the terephthalic acid in the crystallization vessel is conducted with cooling by flash vaporization of solvent.
3. The crystallization process according to claim 2 , wherein crystals and mother liquor product are separated from each other after supplying said slurry overflowing from the upper part of said hydrocyclone to a separating means.
4. The crystallization process according to claim 1 , wherein, prior to the feeding of the terephthalic acid solution or the slurry solution in which the part of the terephthalic acid is precipitated to the crystallization vessel, the process further comprises the steps of:
dissolving a crude product of terephthalic acid obtained by oxidizing paraxylene with a molecular oxygen in liquid phase in hot water, thereby forming an aqueous solution of crude terephthalic acid, and
catalytically hydrogenating the aqueous solution of the crude terephthalic acid by contacting with group VIII noble metal catalyst in the presence of hydrogen, and thereafter cooling the resultant solution,
wherein a first mother liquor product in which most of the terephthalic acid has been separated as crystals as first crystallization products, is fed to said crystallization vessel, and
wherein second crystallization products are recovered from the slurry including second crystallization products obtained in the crystallization vessel by further cooling the mother liquor.
5. The crystallization process according to claim 4 , wherein said slurry solution of terephthalic acid including the second crystallization products is provided by a mother liquor substitution method.
6. The crystallization process according to claim 1 , wherein crystals and mother liquor product are separated from each other after supplying said slurry overflowing from the upper part of said hydrocyclone to a separating means.
7. The crystallization process according to claim 6 , wherein, prior to the feeding of the terephthalic acid solution or the slurry solution in which the part of the terephthalic acid is precipitated to the crystallization vessel, the process further comprises the steps of:
dissolving a crude product of terephthalic acid obtained by oxidizing paraxylene with a molecular oxygen in liquid phase in hot water, thereby forming an aqueous solution of crude terephthalic acid, and
catalytically hydrogenating the aqueous solution of the crude terephthalic acid by contacting with group VIII noble metal catalyst in the presence of hydrogen, and thereafter cooling the resultant solution,
wherein a first mother liquor product in which most of the terephthalic acid has been separated as crystals as first crystallization products, is fed to said crystallization vessel, and
wherein second crystallization products are recovered from the slurry including second crystallization products obtained in the crystallization vessel by further cooling the mother liquor.
8. The crystallization process according to claim 7 , wherein said slurry solution of terephthalic acid including the second crystallization products is provided by a mother liquor substitution method.
9. The crystallization process according to claim 3 , wherein, prior to the feeding of the terephthalic acid solution or the slurry solution in which the part of the terephthalic acid is precipitated to the crystallization vessel, the process further comprises the steps of:
dissolving a crude product of terephthalic acid obtained by oxidizing paraxylene with a molecular oxygen in liquid phase in hot water, thereby forming an aqueous solution of crude terephthalic acid, and
catalytically hydrogenating the aqueous solution of the crude terephthalic acid by contacting with group VIII noble metal catalyst in the presence of hydrogen, and thereafter cooling the resultant solution,
wherein a first mother liquor product in which most of the terephthalic acid has been separated as crystals as first crystallization products, is fed to said crystallization vessel, and
wherein second crystallization products are recovered from the slurry including second crystallization products obtained in the crystallization vessel by further cooling the mother liquor.
10. The crystallization process according to claim 9 , wherein said slurry solution of terephthalic acid including the second crystallization products is provided by a mother liquor substitution method.
11. The crystallization process according to claim 2 , wherein, prior to the feeding of the terephthalic acid solution or the slurry solution in which the part of the terephthalic acid is precipitated to the crystallization vessel, the process further comprises the steps of:
dissolving a crude product of terephthalic acid obtained by oxidizing paraxylene with a molecular oxygen in liquid phase in hot water, thereby forming an aqueous solution of crude terephthalic acid, and
catalytically hydrogenating the aqueous solution of the crude terephthalic acid by contacting with group VIII noble metal catalyst in the presence of hydrogen, and thereafter cooling the resultant solution,
wherein a first mother liquor product in which most of the terephthalic acid has been separated as crystals as first crystallization products, is fed to said crystallization vessel, and
wherein second crystallization products are recovered from the slurry including second crystallization products obtained in the crystallization vessel by further cooling the mother liquor.
12. The crystallization process according to claim 11 , wherein said slurry solution of terephthalic acid including the second crystallization products is provided by a mother liquor substitution method.
13. The crystallization process according to claim 3 , wherein said slurry overflowing from the upper part of said hydrocyclone is passed through a cooling process and thereafter supplied to said separating means.
14. The crystallization process according to claim 3 , wherein the concentration of crystals in said slurry overflowing from said upper outlet of said hydrocyclone is 1% or less.
15. A crystallization process including the steps of feeding a terephthalic acid solution or a slurry solution in which a part of the terephthalic acid is precipitated to a crystallization vessel, precipitating the terephthalic acid in the crystallization vessel, generating a slurry containing crystals and solvent, and discharging the slurry, and comprising the further steps of:
(i) introducing the slurry discharged from the crystallization vessel to a hydrocyclone, in a tangential direction of the hydrocyclone,
(ii) returning the concentrated slurry flowing out as a downward swirling flow from a lower part of the hydrocyclone directly from the hydrocyclone to the crystallization vessel, and
(iii) discharging the slurry overflowing from an upper part of the hydrocyclone, wherein the concentration of crystals in said slurry overflowing from said upper part of said hydrocyclone is 5% or less.