US 5,409,505 AGranted

Method and apparatus for crystallization of organic matter

AssigneeTsukishima Kikai Co., Ltd.

InventorsMinoru Morita, Keizo Takegami

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Abstract

Adiabatic self-evaporation cooling of a refrigerant is performed in a crystallizer for a treated organic matter which contains the refrigerant and is fed into the crystallizer. Crystals produced by the adiabatic self-evaporation cooling are withdrawn from the crystallize. An evaporated vapor is introduced from the crystallizer into an absorber so as to be contacted with a concentrated solution transformed from a generator for condensation in the absorber. A condensate is introduced from the absorber into the generator, the refrigerant is evaporated in the generator, an evaporated vapor is introduced from the generator to the condenser, the evaporated vapor is condensed in the condenser, a condensate is supplied from the condenser to the crystallizer and the concentrated solution is circulated between the absorber and the generator by returning the concentrated solution, in which the concentration of an absorbent is increased by the generator to the absorber.

A method for crystallization of an organic matter in which an organic matter is adiabatically cooled and crystallized, comprising the steps of:

(a) supplying an organic matter to be crystallized and a refrigerant solvent for the organic matter to a crystallizer which is maintained at a reduced pressure, mixing the organic matter with the refrigerant solvent, while preforming adiabatic self-evaporation of the refrigerant solvent wherein the refrigerant solvent is evaporated to form an evaporated vapor, said adiabatic self-evaporation taking place in the reduced pressure in the crystallizer, and crystallizing the organic matter by removing crystallization heat as a result of the adiabatic self-evaporation;
(b) withdrawing crystals produced in the crystallizer and recovering said crystals by separating said crystals from the liquid component by means of a solid-liquid separator;
(c) introducing the evaporated vapor from the crystallizer into an absorber in which the evaporated vapor is directly contacted with a concentrated liquid absorbent solution returned from the generator of step (d) to cause absorption of the evaporated vapor in the returned concentrated liquid absorbent solution and thereby condensing the evaporated vapor to form an absorbed condensate;
(d) introducing the absorbed condensate from the absorber from step (c) into a generator and evaporating the refrigerant solvent in the absorbed condensate to recover evaporated refrigerant solvent and form a concentrated liquid absorbent solution;
(e) introducing the evaporated refrigerant solvent from the generator into a condenser and condensing the same;
(f) supplying the condensate from the condenser in step (e) to the crystallizer as the refrigerator solvent;
and
(g) introducing concentrated liquid absorbent solution formed in step (d) into the absorber and contacting the concentrated liquid absorbent solution with the evaporated vapor from the crystallizer in the absorber and condensing the evaporated vapor by raising a boiling point of the resulting mixture and a condensing temperature due to the contact.

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Abstract

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