Polyolefin manufacturing system including a membrane fractionation system for diluent recovery
US-9211523-B2 · Dec 15, 2015 · US
US2016016808A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016016808-A1 |
| Application number | US-201514702944-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 4, 2015 |
| Priority date | Jun 22, 2010 |
| Publication date | Jan 21, 2016 |
| Grant date | — |
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In a method for recovering volatile components from a solid material, a liquid phase is mechanically removed from the solid material. Subsequently, the solid material is dried by exposing the solid material to superheated steam circulating in a closed circuit. From the closed circuit excess steam that contains volatile components given off by the solid material is removed. The volatile components are separated from the excess steam by condensing the excess steam to a condensed phase and the volatile components are from the condensed phase by adding suitable ions to the condensed phase to crystallize the volatile components.
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What is claimed is: 1 . A method for recovering volatile components from a solid material, the method comprising the steps of: removing a liquid phase mechanically from the solid material; subsequently drying the solid material by exposing the solid material to superheated steam circulating in a closed circuit; removing from the closed circuit excess steam that contains volatile components given off by the solid material; separating the volatile components from the excess steam by condensing the excess steam to a condensed phase and recovering the volatile components from the condensed phase by adding suitable ions to the condensed phase to crystallize the volatile components. 2 . The method according to claim 1 , wherein the solid material is of organic origin and the volatile component is ammonia. 3 . The method according to claim 1 , wherein the solid material is of organic origin and is subjected to a biological pretreatment prior to drying. 4 . The method according to claim 3 , wherein the biological pretreatment is anaerobic.
Crystallisation (crystallisation directly from the vapour phase B01D7/02; making single crystals C30B {; crystallisation as part of the Bayer process also classified in C01F7/14}) · CPC title
Fractional distillation {or use of a fractionation or rectification column} · CPC title
Preparation of ammonia from nitrogenous organic substances · CPC title
Manure · CPC title
Separating volatiles, e.g. recovering solvents from dryer exhaust gases · CPC title
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