Pressure driven flow crystallizer
US-10155786-B2 · Dec 18, 2018 · US
US10173147B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10173147-B2 |
| Application number | US-201514738033-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 12, 2015 |
| Priority date | Jun 12, 2014 |
| Publication date | Jan 8, 2019 |
| Grant date | Jan 8, 2019 |
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The present invention further relates to a process for removing a target product from a liquid phase P comprising the target product.
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The invention claimed is: 1. An apparatus ( 1 ) for separation of a target product from a liquid phase P comprising the target product, comprising a plurality of primary spaces ( 3 ) for a heat transfer medium W and a plurality of cooling disks ( 103 ), each primary space located within each cooling disk, lines having surfaces which conduct the heat transfer medium W, a first feed unit ( 5 a ) and a first removal unit ( 5 b ) for the heat transfer medium W, a plurality of secondary spaces ( 7 ) for the liquid phase P, a second feed unit ( 9 ) for the liquid phase P, a plurality of crystallization surfaces ( 13 ), each crystallization surface located within each cooling disk, and each crystallization surface divides each primary space from the secondary spaces ( 7 ), a second removal unit ( 15 ) for the target product, and a plurality of application units ( 11 ) for distributing a liquid phase P 0 essentially directly to the crystallization surfaces ( 13 ) and the surfaces of lines that conduct the heat transfer medium W, wherein one or more of the plurality of application units ( 11 ) are arranged for each cooling disk. 2. The apparatus ( 1 ) according to claim 1 , wherein each application unit ( 11 ) comprises a pipeline system having nozzles for distributing the liquid phase P 0 over each crystallization surface ( 13 ) of each cooling disk ( 103 ) and the surfaces of lines that conduct the heat transfer medium W. 3. The apparatus ( 1 ) according to claim 1 , wherein the liquid phase P 0 comprises at least one of the liquid phase P and a liquid phase P 1 comprising a solvent. 4. The apparatus ( 1 ) according to claim 1 , further comprising a heat exchanger ( 19 ) for the heat transfer medium W, arranged upstream of the first feed unit ( 5 a ). 5. The apparatus ( 1 ) according to claim 1 , wherein the apparatus ( 1 ) is a cooling disk crystallizer.
by change of the physical state, e.g. crystallisation · CPC title
Selection of auxiliary, e.g. for control of crystallisation nuclei, of crystal growth, of adherence to walls; Arrangements for introduction thereof · CPC title
cooling by heat exchange (by evaporation of components of the mixture to be separated B01D9/0013; refrigeration machines F25B) · CPC title
by indirect heat exchange · CPC title
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