GB900108A - Improvements in or relating to the separation or partial separation of components ofa liquid medium - Google Patents
Improvements in or relating to the separation or partial separation of components ofa liquid mediumInfo
- Publication number
- GB900108A GB900108A GB392058A GB392058A GB900108A GB 900108 A GB900108 A GB 900108A GB 392058 A GB392058 A GB 392058A GB 392058 A GB392058 A GB 392058A GB 900108 A GB900108 A GB 900108A
- Authority
- GB
- United Kingdom
- Prior art keywords
- liquid
- cylinder
- pict
- iii
- melted
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B30/00—Crystallisation; Crystallising apparatus; Separating crystals from mother liquors ; Evaporating or boiling sugar juice
- C13B30/02—Crystallisation; Crystallising apparatus
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
Landscapes
- Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Developing Agents For Electrophotography (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
A crystallizable constituent is separated from a liquid in a number of successive crystallization stages, liquid from an intermediate stage passing to the preceding stage while solid from said intermediate stage is melted and passed to the following stage. A portion of the melted solid may pass back to the said intermediate stage as reflux. The process may be continuous or intermittent. As shown in Fig. 1, a liquid is fed from a valved inlet 15 to form a layer 13 in a rotary cylinder 1 which may be partially immersed in a cooling bath 20 and which has one or more helical blades 2 forming a spiral path along the inner periphery of the cylinder. During rotation of the cylinder, liquid passes to the left while the crystallizable constituent passes to the right in spiral flow, rising as a crystalline layer and returning as a liquid, optionally after being melted by an external heating element 21. In a modification (Figs. 4 and 5, not shown), the heating element is situated within the cylinder in the form of a rotary spiral scraper intermeshing with the <PICT:0900108/III/1> <PICT:0900108/III/2> <PICT:0900108/III/3> <PICT:0900108/III/4> blades 2. In a further modification (Figs. 7 and 8, not shown), the crystalline layer may form on a rotary hollow coil associated with a heated scraper within the rotary cylinder. In a further modification (Fig. 8, not shown), the hollow coil may be associated with a horizontally displaceable U- or V-shaped heated scraper having spaced apertures for return of melted solid. As shown in Figs. 10 and 11, the liquid and crystallizable constituent pass in opposite directions in a zig-zag path formed by wedge-shaped partitions 51 in a trough 50, one end of the trough being cooled by bath 20 while the other end is heated by one of heaters 21. Tipping to produce the desired flow and rocking to alternate the heating and cooling is effected by four hydraulically operated reciprocating rods 53, one at each corner of the trough.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB392058A GB900108A (en) | 1958-02-06 | 1958-02-06 | Improvements in or relating to the separation or partial separation of components ofa liquid medium |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB392058A GB900108A (en) | 1958-02-06 | 1958-02-06 | Improvements in or relating to the separation or partial separation of components ofa liquid medium |
Publications (1)
Publication Number | Publication Date |
---|---|
GB900108A true GB900108A (en) | 1962-07-04 |
Family
ID=9767382
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB392058A Expired GB900108A (en) | 1958-02-06 | 1958-02-06 | Improvements in or relating to the separation or partial separation of components ofa liquid medium |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB900108A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2102476A5 (en) * | 1970-08-05 | 1972-04-07 | Thirel Yves | Continuous boiling appts - for sugar refinery syrups |
CN109569012A (en) * | 2018-11-23 | 2019-04-05 | 衡阳市晋宏精细化工有限公司 | It can be quickly cooled to the crystallization making apparatus of type |
CN116440533A (en) * | 2023-06-19 | 2023-07-18 | 东莞市瑞辉新材料技术有限公司 | Bisphenol fluorene recrystallization separation device with circulation temperature control function |
-
1958
- 1958-02-06 GB GB392058A patent/GB900108A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2102476A5 (en) * | 1970-08-05 | 1972-04-07 | Thirel Yves | Continuous boiling appts - for sugar refinery syrups |
CN109569012A (en) * | 2018-11-23 | 2019-04-05 | 衡阳市晋宏精细化工有限公司 | It can be quickly cooled to the crystallization making apparatus of type |
CN116440533A (en) * | 2023-06-19 | 2023-07-18 | 东莞市瑞辉新材料技术有限公司 | Bisphenol fluorene recrystallization separation device with circulation temperature control function |
CN116440533B (en) * | 2023-06-19 | 2023-08-29 | 东莞市瑞辉新材料技术有限公司 | Bisphenol fluorene recrystallization separation device with circulation temperature control function |
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