Process and Apparatus for Purification of Acrylic Acid
US-2017326471-A1 · Nov 16, 2017 · US
US11891358B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11891358-B2 |
| Application number | US-202117916554-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 7, 2021 |
| Priority date | May 8, 2020 |
| Publication date | Feb 6, 2024 |
| Grant date | Feb 6, 2024 |
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A method for preparing a purified styrene composition with a styrene yield of at least 80%. The method comprises providing a crude composition containing styrene, and subjecting the crude composition to at least one crystallization step. The at least one crystallization step comprises at least one static crystallization stage and at least one dynamic crystallization stage.
Opening claim text (preview).
The invention claimed is: 1. A method for preparing a purified styrene composition with a styrene yield of at least 80%, the method comprising: providing a crude composition containing styrene; and subjecting the crude composition to at least one crystallization step to produce the purified styrene composition, the at least one crystallization step comprising at least one static crystallization stage and at least one dynamic crystallization stage. 2. The method of claim 1 , wherein the crude composition contains one or more impurities selected from the group consisting of: color inducing species, sulfur species, meta-xylenes, ortho-xylenes, ethylbenzene, phenylacetylene, cumene, n-propylbenzene, alpha-methylstyrene, ethyltoluene, organochlorinated, organo-nitrogenated species and arbitrary mixtures of two or more of the aforementioned impurities. 3. The method of claim 1 , wherein the at least one dynamic crystallization stage is a falling film crystallization stage or a suspension crystallization stage. 4. The method of claim 1 , wherein the at least one crystallization step comprises one to ten static crystallization stages and one to ten dynamic crystallization stages. 5. The method of claim 1 , wherein: providing the crude composition comprises subjecting a feed composition to at least one of: one or more distillation steps and one or more extractive distillation steps, and the crude composition is obtained as a head stream, as a side stream or as a bottom stream of one of the at least one of: one or more distillation steps and one or more extractive distillation steps. 6. The method of claim 1 , wherein the crude composition derives from a pygas, the crude composition being prepared by: distilling a pygas feed composition so as to obtain a C8-fraction and subjecting the C8-fraction to an extractive distillation in which the C8-fraction is treated with a polar solvent so as to obtain a styrene containing fraction as an overhead stream, as a side stream or as a bottom stream, which is used as the crude composition or which is processed into the crude composition, or distilling a pygas feed composition so as to obtain a C8-fraction, feeding the C8-fraction into a hydrogenation reactor so as to obtain a hydrogenated gas, subjecting the hydrogenated gas to an extractive distillation in which the hydrogenated gas is treated with a polar solvent so as to obtain a styrene containing fraction as an overhead stream, as a side stream or as a bottom stream, which is used as the crude composition or which is processed into the crude composition. 7. The method according to claim 1 , wherein the crude composition derives from an ethylbenzene and styrene containing stream produced in an ethyl-benzene/styrene monomer (EBSM) process or derives from a styrene containing stream produced by polystyrene pyrolysis. 8. The method of claim 1 , wherein the purified styrene composition has a styrene content of at least 99.00% by weight. 9. The method of claim 1 , wherein the purified styrene composition has a color of maximum 15 as defined by Pt—Co scale as per ASTM D5386. 10. The method of claim 1 , wherein the purified styrene composition comprises at least one of: less than 5 ppmw of total elemental sulfur as contained in mercaptans, disulfides and thiophenes, less than 20 ppmw of oxygenates, less than 40 ppmw of impurities selected from the group consisting of: phenylacetylene, mixed xylenes, ethylbenzene, cumene, ethyl-toluene, n-propylbenzene, and alpha-methylstyrene, a polymer content of less than 10 ppmw, and a total organic chlorine content of less than 2 ppmw. 11. The method of claim 1 , wherein: in the at least one crystallization step, a purified styrene composition and a styrene depleted mother liquor are obtained, and at most 50% by volume of the styrene depleted mother liquor is recycled to an optional distillation step.
by crystallisation; Purification or separation of the crystals · CPC title
by two or more of a fractionation, separation or rectification step · CPC title
Extractive distillation · CPC title
by indirect heat exchange · CPC title
by heating (B01D9/0022, B01D9/0027 take precedence) · CPC title
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