GB815961A - Improvements in separating into its constituents the reaction mixture derived from the cyclo-octatetraene synthesis - Google Patents
Improvements in separating into its constituents the reaction mixture derived from the cyclo-octatetraene synthesisInfo
- Publication number
- GB815961A GB815961A GB35181/57A GB3518157A GB815961A GB 815961 A GB815961 A GB 815961A GB 35181/57 A GB35181/57 A GB 35181/57A GB 3518157 A GB3518157 A GB 3518157A GB 815961 A GB815961 A GB 815961A
- Authority
- GB
- United Kingdom
- Prior art keywords
- water
- steam
- pipe
- octatetraene
- reaction mixture
- 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
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C13/00—Cyclic hydrocarbons containing rings other than, or in addition to, six-membered aromatic rings
- C07C13/02—Monocyclic hydrocarbons or acyclic hydrocarbon derivatives thereof
- C07C13/26—Monocyclic hydrocarbons or acyclic hydrocarbon derivatives thereof with an eight-membered ring
- C07C13/267—Monocyclic hydrocarbons or acyclic hydrocarbon derivatives thereof with an eight-membered ring with a cyclo-octatriene or cyclo-octatetraene ring
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/34—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
- B01D3/38—Steam distillation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
- B01J19/0013—Controlling the temperature of the process
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/04—Purification; Separation; Use of additives by distillation
- C07C7/05—Purification; Separation; Use of additives by distillation with the aid of auxiliary compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
- B01J2219/00103—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor in a heat exchanger separate from the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00162—Controlling or regulating processes controlling the pressure
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2601/00—Systems containing only non-condensed rings
- C07C2601/18—Systems containing only non-condensed rings with a ring being at least seven-membered
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Water Supply & Treatment (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
<PICT:0815961/III/1> The components of a reaction mixture from the cyclo-octatetraene synthesis which contains solid and liquid substances are separated by steam distillation by leading steam into a column of water at a short distance below the surface so that a steam-water zone is formed above the water and introducing the mixture into this zone so that liquid constituents are vaporized while the solids fall downwardly through the non-turbulent water below the point of entry of steam and can be sluiced out. Steam, for example at 1-10 atmospheres, is introduced by pipe 5 and annular pipe 9 provided with holes round the top and positioned just below the surface of water in a vessel 4 having a conical bottom contained in a vessel 1, the water level being fixed by overflow pipe 2. The reaction mixture is introduced from above by pipe 10. Solids fall downwardly through the non-turbulent water into vessel 1 and thence into sluice 3. Due to the freedom from turbulence the solids are not deposited on the wall and no incrustations are formed. Vapours pass by pipe 6 to condenser 7 and are separated in separator 8 into an upper organic layer containing cyclo-octatetraene drawn off into storage tank 16 and a lower aqueous layer which, since it may contain organic constituents is preferably returned to the steam distillation. Reduced pressure, e.g. 300-760 tons, may be used but atmospheric pressure is preferred.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEB42501A DE1032217B (en) | 1956-11-16 | 1956-11-16 | Process and device for the decomposition of liquid and solid reaction products |
Publications (1)
Publication Number | Publication Date |
---|---|
GB815961A true GB815961A (en) | 1959-07-01 |
Family
ID=6966751
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB35181/57A Expired GB815961A (en) | 1956-11-16 | 1957-11-12 | Improvements in separating into its constituents the reaction mixture derived from the cyclo-octatetraene synthesis |
Country Status (3)
Country | Link |
---|---|
CH (1) | CH364246A (en) |
DE (1) | DE1032217B (en) |
GB (1) | GB815961A (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4171265A (en) | 1974-10-02 | 1979-10-16 | Saint-Gobain Industries | Suppression of pollution in mineral fiber manufacture |
CN113398721B (en) * | 2021-05-24 | 2022-10-04 | 太原科技大学 | Acetylene, chloroethylene and overflow water recycling system and method |
-
1956
- 1956-11-16 DE DEB42501A patent/DE1032217B/en active Pending
-
1957
- 1957-11-07 CH CH5239657A patent/CH364246A/en unknown
- 1957-11-12 GB GB35181/57A patent/GB815961A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
CH364246A (en) | 1962-09-15 |
DE1032217B (en) | 1958-06-19 |
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