GB960943A - Fractionation method - Google Patents
Fractionation methodInfo
- Publication number
- GB960943A GB960943A GB16985/62A GB1698562A GB960943A GB 960943 A GB960943 A GB 960943A GB 16985/62 A GB16985/62 A GB 16985/62A GB 1698562 A GB1698562 A GB 1698562A GB 960943 A GB960943 A GB 960943A
- Authority
- GB
- United Kingdom
- Prior art keywords
- solvent
- stream
- heat
- constant
- variable
- 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
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/42—Regulation; Control
- B01D3/4211—Regulation; Control of columns
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/11—Purification; Separation; Use of additives by absorption, i.e. purification or separation of gaseous hydrocarbons with the aid of liquids
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
In the separation of butadiene from a selective solvent such as furfural, in which it is dissolved, by stripping, heat is recovered from the hot stripped solvent by controlling the level of liquid in the stripper removing a variable flow stream of solvent, dividing the solvent into a constant flow stream and a smaller variable flow stream and recovering heat from the constant stream. The heat may be used in the reboiler of a fractionator such as that used to separate butadiene from acetylenes in the hydrocarbon stream stripped from the solvent. The variable solvent stream may be cooled and recombined with the cooled constant stream or may be recombined and further heat recovered e.g. to heat a hydrocarbon feed stream to an absorber where butadiene is dissolved in the solvent. In the latter case the flow of solvent through the heat exchanger is kept constant by means of a variable by-pass.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11875161A | 1961-05-08 | 1961-05-08 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB960943A true GB960943A (en) | 1964-06-17 |
Family
ID=22380521
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB16985/62A Expired GB960943A (en) | 1961-05-08 | 1962-05-03 | Fractionation method |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB960943A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0043023A1 (en) * | 1980-06-27 | 1982-01-06 | Raphael Katzen Associates International, Inc. | Hydrous alcohol distillation method and apparatus |
-
1962
- 1962-05-03 GB GB16985/62A patent/GB960943A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0043023A1 (en) * | 1980-06-27 | 1982-01-06 | Raphael Katzen Associates International, Inc. | Hydrous alcohol distillation method and apparatus |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DK113979B (en) | Apparatus for determining the location of the boundary level between two separated components in a separation centrifuge. | |
GB948180A (en) | Process for the separation of an organic mixture containing hydrocarbons by means of extractive distillation | |
DK106685C (en) | Apparatus for regenerating insulating oils. | |
GB960943A (en) | Fractionation method | |
GB1255570A (en) | Process for separating a mixture of c5 hydrocarbons into its constituents | |
DK110023C (en) | Process for separating aromatic hydrocarbons from hydrocarbon mixtures by extractive fractionation. | |
DK114992B (en) | Method for regulating an iodine oil refining process depending on the vanadium content of the starting material or intermediates. | |
DK112040B (en) | Process by continuously extracting fat or apparatus for performing the process. | |
DK105331C (en) | Process for recovering pure or almost pure aromatic hydrocarbons from hydrocarbon mixtures. | |
GB939470A (en) | The separation of olefinic hydrocarbons from mixtures containing the same | |
GB951500A (en) | Selective separation of hydrocarbon mixtures | |
GB908079A (en) | Extraction of phenols from neutral hydrocarbon oils | |
GB1150308A (en) | Process for the Separation of Mixtures of Organic Compounds. | |
GB958898A (en) | Method of separating aromatic from non-aromatic hydrocarbons | |
NL6502144A (en) | ||
FR1302196A (en) | Process and apparatus for extracting cashew nut oil and for separating the fruits from these nuts | |
GB1384948A (en) | Method of recovering pure aromatics from mixtures thereof with non- aromatics | |
GB1002562A (en) | A method of separating immiscible of difficulty miscible liquids and apparatus for performing the same | |
GB1090176A (en) | Process for the separation of low boiling aliphatic dienes from mono-olefines and paraffins or mono-olefines from paraffins | |
GB936990A (en) | Separation of low boiling point impurities from hydrocarbons | |
GB910215A (en) | Process for the separation of wax containing mixtures | |
GB933680A (en) | Separation of a mixture of 1, 5-and 1, 8-dinitronaphthalenes into its two components | |
JPS5225806A (en) | Method and appapatus for the desalting of crude oil | |
JPS56145230A (en) | Separation of styrene | |
DK114074B (en) | Method for maintaining a constant hydrocarbon content in the raffinate stream by regulating a hydrocarbon oil refining process. |