GB851026A - A process for the purification of solid materials - Google Patents
A process for the purification of solid materialsInfo
- Publication number
- GB851026A GB851026A GB976459A GB976459A GB851026A GB 851026 A GB851026 A GB 851026A GB 976459 A GB976459 A GB 976459A GB 976459 A GB976459 A GB 976459A GB 851026 A GB851026 A GB 851026A
- Authority
- GB
- United Kingdom
- Prior art keywords
- substance
- pressure
- adiabatic expansion
- carrier gas
- steam
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
Solid substances, e.g. disilylbenzene, are purified by a sublimation process wherein the substance is distilled in the presence of an inert carrier gas and the gaseous overheads are allowed to expand adiabatically into a region where the pressure is such that, as a result of the adiabatic expansion, the temperature falls to a value not higher than the temperature of solidification, Steam, nitrogen, hydrogen, and helium are p mentioned as suitable carrier gases.ALSO:Solid substances, e.g. phenthiazine, diphenylamine, p-hydroxy diphenylamine, acridine, anthracene, terphenyl (1 : 2 and 1 : 3 diphenyl benzene), naphthalene, 2,21-bis-(p-hydroxyphenyl propane), rosin acids such as abietic acid, high molecular weight coal tar products, and dicyclopentadienyl iron, are purified by subjecting the substance to distillation in the presence of an inert carrier gas, and allowing the gaseous overheads, comprising the normally solid substance in the gaseous state and the carrier gas, to expand substantially adiabatically into a region where the pressure is such that, as a result of adiabatic expansion, the temperature falls to a value not higher than the temperature at which the substance solidifies. Substantially adiabatic expansion comprises expansion which is at least 60% of the theoretical adiabatic expansion. Steam, nitrogen, hydrogen, helium, or alcohol vapour when appropriate may be used as the inert carrier gas. The adiabatic expansion may be attained by providing a constriction such as a converging-diverging nozzle between the heating vessel and the condensing chamber. The pressure in the heating vessel is generally above atmospheric but in some cases may be sub-atmospheric. A substance which removes chemically the impurities in the substance under treatment may be present, e.g. when treating phenothiazine about 1% of iron powder, based on the phenothiazine, may be added to the charge in order to remove iodine impurities. In an example, impure phenothiazine and a small proportion of iron powder are heated to 280 DEG C. and then superheated steam at 300 DEG C. is passed through the charge. A pressure in the vessel of 45 p.s.i.g. is maintained. The steam and distillate are cooled adiabatically by expanding through a nozzle into a condenser, maintained at atmospheric pressure. Solid phenothiazine is deposited.ALSO:Solid substances, e.g. selenium, are purified by a sublimation process in which the substance is distilled in the presence of an inert carrier gas such as steam, nitrogen, hydrogen, helium or alcohol vapour and the gaseous overheads comprising the said solid substance in the gaseous state and the carrier gas, allowed to expand adiabatically into a region where the pressure is such that, as a result of the adiabatic expansion, the temperature falls to a value not higher than the temperature at which the substance solidifies. The adiabatic expansion may be attained by providing a constriction such as a converging-diverging nozzle between the heating vessel and the condensing chamber. The pressure in the heating vessel may be above or below atmospheric.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB976459A GB851026A (en) | 1959-03-20 | 1959-03-20 | A process for the purification of solid materials |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB976459A GB851026A (en) | 1959-03-20 | 1959-03-20 | A process for the purification of solid materials |
Publications (1)
Publication Number | Publication Date |
---|---|
GB851026A true GB851026A (en) | 1960-10-12 |
Family
ID=9878341
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB976459A Expired GB851026A (en) | 1959-03-20 | 1959-03-20 | A process for the purification of solid materials |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB851026A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2362214A1 (en) * | 1976-08-16 | 1978-03-17 | Hori Fumio | METHOD AND APPARATUS FOR OBTAINING MAGNESIUM AND CALCIUM IN THEIR PURE METAL FORM |
-
1959
- 1959-03-20 GB GB976459A patent/GB851026A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2362214A1 (en) * | 1976-08-16 | 1978-03-17 | Hori Fumio | METHOD AND APPARATUS FOR OBTAINING MAGNESIUM AND CALCIUM IN THEIR PURE METAL FORM |
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