GB916882A - Method and apparatus for the continuous separation of sublimed products from hot carrier gases - Google Patents
Method and apparatus for the continuous separation of sublimed products from hot carrier gasesInfo
- Publication number
- GB916882A GB916882A GB266560A GB266560A GB916882A GB 916882 A GB916882 A GB 916882A GB 266560 A GB266560 A GB 266560A GB 266560 A GB266560 A GB 266560A GB 916882 A GB916882 A GB 916882A
- Authority
- GB
- United Kingdom
- Prior art keywords
- elements
- cooling
- heating
- stream
- oil
- 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
- 239000012159 carrier gas Substances 0.000 title 1
- 238000000034 method Methods 0.000 title 1
- 238000000926 separation method Methods 0.000 title 1
- 238000010438 heat treatment Methods 0.000 abstract 9
- 238000001816 cooling Methods 0.000 abstract 8
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 abstract 6
- 239000000126 substance Substances 0.000 abstract 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 abstract 3
- 239000007787 solid Substances 0.000 abstract 3
- LGRFSURHDFAFJT-UHFFFAOYSA-N Phthalic anhydride Natural products C1=CC=C2C(=O)OC(=O)C2=C1 LGRFSURHDFAFJT-UHFFFAOYSA-N 0.000 abstract 2
- JHIWVOJDXOSYLW-UHFFFAOYSA-N butyl 2,2-difluorocyclopropane-1-carboxylate Chemical compound CCCCOC(=O)C1CC1(F)F JHIWVOJDXOSYLW-UHFFFAOYSA-N 0.000 abstract 2
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 abstract 2
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 abstract 1
- 230000003197 catalytic effect Effects 0.000 abstract 1
- 238000004140 cleaning Methods 0.000 abstract 1
- 230000005494 condensation Effects 0.000 abstract 1
- 238000009833 condensation Methods 0.000 abstract 1
- 239000002826 coolant Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 238000002844 melting Methods 0.000 abstract 1
- 230000008018 melting Effects 0.000 abstract 1
- 238000012986 modification Methods 0.000 abstract 1
- 230000004048 modification Effects 0.000 abstract 1
- 230000003647 oxidation Effects 0.000 abstract 1
- 238000007254 oxidation reaction Methods 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/54—Preparation of carboxylic acid anhydrides
- C07C51/573—Separation; Purification; Stabilisation; Use of additives
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D7/00—Sublimation
- B01D7/02—Crystallisation directly from the vapour phase
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Crystallography & Structural Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
<PICT:0916882/III/1> <PICT:0916882/III/2> Sublimable solid substances such as maleic anhydride, phthalic anhydride and naphthalene are condensed as solids from a stream of gas containing said substances in gaseous form by passing said stream into contact successively with a plurality of heat exchange elements and alternately heating and cooling each of said elements so that whilst sublimate is condensing on some elements it is melting off other elements for removal. In Fig. 4 in addition to the elements 2 for both heating and cooling, elements 18 are provided for cooling only, their temperature being such as to result in the condensation of the substance in liquid form. Heating and cooling are provided by means of oil respectively circulated through a steam energized heater 11 and a cooler 13 by means of pumps 10 and 12. The cooling oil for the elements 18 is circulated by a pump 19 through an oil/air cooler 20. The elements 2 comprise banks of horizontal finned tubes through which the oil flows in a series/parallel manner (Figs. 1 and 2, not shown). The tubes can alternatively be connected in serpentine fashion, and where smooth, unfinned tubes are employed, they may be arranged vertically. The elements may be mounted on guide rails so as to be retractable for cleaning. Troughs 3 are provided to collect molten sublimate, these and the outlet tubes therefrom being provided with heating jackets which are supplied with oil from the heating circuit. In Fig. 5 the heating circuit is eliminated by the inclusion in the cooling circuit of heat exchangers 26 which may employ steam as the heating medium or may be heated electrically. In a further embodiment (not illustrated) heat exchangers 26 may themselves be eliminated by including electrical heating elements within the tubes making up elements 2. The cooler 22 in these modifications must be capable of removing the additional heat imparted to the cooling medium. In the above embodiments valves 8, 9 and valves 28 are individually controllable either manually or automatically on a time basis or on a temperature basis, i.e. when the cooling becomes inefficient due to deposited condensate.ALSO:Maleic anhydride and phthalic anhydride are condensed as solids from a stream of gas containing said substances, which may be derived from the catalytic oxidation of benzene or naphthalene, by passing said stream into contact successively with a plurality of heat exchange elements and alternately heating and cooling each of said elements so that whilst sublimate is condensing on some elements, it is being melted off other elements for removal. Naphthalene may be similarly recovered from a stream of gas. Suitable apparatus is described (see Group III).
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEG26358A DE1084239B (en) | 1959-02-11 | 1959-02-11 | Method and device for the continuous separation of sublimation products from hot carrier gases |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB916882A true GB916882A (en) | 1963-01-30 |
Family
ID=7122899
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB266560A Expired GB916882A (en) | 1959-02-11 | 1960-01-25 | Method and apparatus for the continuous separation of sublimed products from hot carrier gases |
Country Status (3)
| Country | Link |
|---|---|
| DE (1) | DE1084239B (en) |
| FR (1) | FR1245875A (en) |
| GB (1) | GB916882A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4765966A (en) * | 1986-02-03 | 1988-08-23 | Ultra-Centrifuge Nederland N.V. | Sublimation apparatus |
| WO2011100081A1 (en) | 2010-02-12 | 2011-08-18 | Exxonmobil Chemical Patents Inc. A Corporation Of The State Of Delaware | Processes utilizing switch condensers |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1196578B (en) * | 1962-02-27 | 1965-07-08 | Leybold Hochvakuum Anlagen | Freeze-drying process with recovery of volatile components |
| US4066420A (en) | 1976-05-07 | 1978-01-03 | Dr. C. Otto & Comp. G.M.B.H. | Process for the gasification of solid fuels |
| CA1091678A (en) * | 1977-06-24 | 1980-12-16 | Chevron Research And Technology Company | Process for recovering maleic anhydride by condensation |
| SE425215B (en) * | 1980-09-12 | 1982-09-13 | Jacob Weitman | SET AND DEVICE FOR TREATING A HEATED CONTAMINATED GAS |
| DE3512930A1 (en) * | 1985-04-11 | 1986-10-16 | GEA Luftkühlergesellschaft Happel GmbH & Co, 4630 Bochum | Desublimation unit |
| DE4427872C1 (en) * | 1994-08-06 | 1996-02-01 | Gea Luftkuehler Happel Gmbh | Process for separating a vaporous product from a carrier gas |
| DE19703681A1 (en) * | 1997-01-31 | 1998-08-06 | Linde Ag | Method and device for removing condensable components from gases and / or gas mixtures |
| DE112005003542A5 (en) * | 2005-04-19 | 2008-02-28 | Creaphys Gmbh | Vacuum apparatus and method for gas phase processing a substance |
-
1959
- 1959-02-11 DE DEG26358A patent/DE1084239B/en active Pending
-
1960
- 1960-01-15 FR FR815778A patent/FR1245875A/en not_active Expired
- 1960-01-25 GB GB266560A patent/GB916882A/en not_active Expired
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4765966A (en) * | 1986-02-03 | 1988-08-23 | Ultra-Centrifuge Nederland N.V. | Sublimation apparatus |
| WO2011100081A1 (en) | 2010-02-12 | 2011-08-18 | Exxonmobil Chemical Patents Inc. A Corporation Of The State Of Delaware | Processes utilizing switch condensers |
| US20130001448A1 (en) * | 2010-02-12 | 2013-01-03 | Exxonmobil Chemical Patents Inc. | Processes Utilizing Switch Condensers |
Also Published As
| Publication number | Publication date |
|---|---|
| DE1084239B (en) | 1960-06-30 |
| FR1245875A (en) | 1960-11-10 |
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