GB1078660A - Steam sublimation of terephthalic acid - Google Patents
Steam sublimation of terephthalic acidInfo
- Publication number
- GB1078660A GB1078660A GB5303565A GB5303565A GB1078660A GB 1078660 A GB1078660 A GB 1078660A GB 5303565 A GB5303565 A GB 5303565A GB 5303565 A GB5303565 A GB 5303565A GB 1078660 A GB1078660 A GB 1078660A
- Authority
- GB
- United Kingdom
- Prior art keywords
- stream
- acid
- condenser
- steam
- terephthalic acid
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D7/00—Sublimation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/42—Separation; Purification; Stabilisation; Use of additives
- C07C51/43—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
Abstract
1,078,660. Purification of terephthalic add by sublimation. MOBIL OIL CORPORATION. Dec. 14, 1965 [Dec. 15, 1964], No. 53035/65. Heading BIB. Terephthalic acid is purified by entraining finely-divided particles of the impure acid in a gaseous stream containing steam, preferably superheated steam at 600‹F. to effect vaporization of a substantial portion of the acid, heating the stream (if necessary) to vaporize the acid completely, separating non-volatile solid impurites (ash) from the stream, cooling the stream to condense a substantial portion of the acid in the form of freely-flowing solid particles while retaining at least a major proportion of the more volatile material in the gaseous phase, and separating the purified acid particles from the stream. The process is particularly suitable for eliminating p-carboxybenzaldehyde from terephthalic acid produced by the partial oxidation of p-xylene. Ash is separated from the hot gaseous stream, containing vaporized acid, by passing the stream through a cyclone or a filter made of sintered stainless steel. The stream is then cooled in a condenser comprising one or more U-tubes 32 each surrounded by a heating-jacket 39 and provided, at the inlet end, with steam injectors. In operating this primary condenser, the mixture of acid vapour and gaseous carrier enters tube 32 from pipe 30 and is joined by two annular streams of steam (1) superheated steam at 650‹F. supplied through line 52 to the inner annular zone, and (2) saturated steam at 350‹F. supplied through conduit 58 into the outer annular zone. Saturated steam may also be injected into the condenser tube at one or more points downstream. The cooled stream is conveyed from the primary condenser to a cyclone separator maintained at about 500‹F. by an automatic control which governs the admission of saturated steam to the condenser. The partially purified particles of terephthalic acid withdrawn from the cyclone separator are re-sublimed in a second stage, and the desired product is removed from the cyclone separator of the condenser of this second stage. The vapours from the two cyclone separators, following the two primary condensers, are united and passed to a secondary condenser comprising a U-tube, into the inlet end of which demineralized water is sprayed. The amount of sprayed water is controlled to maintain a stream outlet temperature of 380‹F. whereby slightly impure terephthalic acid is condensed and the water is vaporized. The terephthalic acid is separted in a cyclone separator, and is returned to the first sublimation stage. The gaseous stream from the separator of the secondary condenser is passed to a tertiary condenser where a waterspray condenses the residual terephthalic acid. This acid is separated in a bag filter, and the steam passes on to a barometric jet condenser which produces sub-atmospheric pressure in the system. The condensation of the terephthalic acid may also be carried out in horizontal tubes.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US41848264A | 1964-12-15 | 1964-12-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1078660A true GB1078660A (en) | 1967-08-09 |
Family
ID=23658285
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB5303565A Expired GB1078660A (en) | 1964-12-15 | 1965-12-14 | Steam sublimation of terephthalic acid |
Country Status (5)
Country | Link |
---|---|
BE (1) | BE673809A (en) |
CH (1) | CH470336A (en) |
DE (1) | DE1493132C3 (en) |
FR (1) | FR1497466A (en) |
GB (1) | GB1078660A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109646987A (en) * | 2019-01-10 | 2019-04-19 | 合肥欧莱迪光电技术有限公司 | A kind of continuous feeding and discharging high vacuum small organic molecule purification special equipment |
-
1965
- 1965-12-14 GB GB5303565A patent/GB1078660A/en not_active Expired
- 1965-12-15 FR FR42461A patent/FR1497466A/en not_active Expired
- 1965-12-15 BE BE673809A patent/BE673809A/xx unknown
- 1965-12-15 CH CH1731565A patent/CH470336A/en not_active IP Right Cessation
- 1965-12-15 DE DE19651493132 patent/DE1493132C3/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109646987A (en) * | 2019-01-10 | 2019-04-19 | 合肥欧莱迪光电技术有限公司 | A kind of continuous feeding and discharging high vacuum small organic molecule purification special equipment |
CN109646987B (en) * | 2019-01-10 | 2024-03-26 | 合肥百思智能装备有限公司 | Continuous feeding and discharging high-vacuum organic micromolecule purifying special equipment |
Also Published As
Publication number | Publication date |
---|---|
FR1497466A (en) | 1967-10-13 |
CH470336A (en) | 1969-03-31 |
DE1493132C3 (en) | 1973-12-13 |
DE1493132A1 (en) | 1969-05-14 |
BE673809A (en) | 1966-06-15 |
DE1493132B2 (en) | 1973-05-17 |
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