GB829021A - Improvements in separation of butadiene from hydrocarbons by extractive distillation - Google Patents

Improvements in separation of butadiene from hydrocarbons by extractive distillation

Info

Publication number
GB829021A
GB829021A GB33659/56A GB3365956A GB829021A GB 829021 A GB829021 A GB 829021A GB 33659/56 A GB33659/56 A GB 33659/56A GB 3365956 A GB3365956 A GB 3365956A GB 829021 A GB829021 A GB 829021A
Authority
GB
United Kingdom
Prior art keywords
butene
via line
butadiene
fractionator
line
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
Application number
GB33659/56A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Phillips Petroleum Co
Original Assignee
Phillips Petroleum Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Phillips Petroleum Co filed Critical Phillips Petroleum Co
Publication of GB829021A publication Critical patent/GB829021A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/04Purification; Separation; Use of additives by distillation
    • C07C7/05Purification; Separation; Use of additives by distillation with the aid of auxiliary compounds
    • C07C7/08Purification; Separation; Use of additives by distillation with the aid of auxiliary compounds by extractive distillation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (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

<PICT:0829021/III/1> In a process for separating butadiene from a mixture of hydrocarbons by extractive distillation the flow of the extractive solvent to the distillation zone, where butene-1 is being separated from the butadiene, is controlled in response to the butene-1 concentration determined at a selected position at the butadienerich end of the zone to maintain the butene-1 concentration below a predetermined maximum at that position. A feed stream comprising the effluent from a butane dehydrogenation zone, with substantially all the C3 and lighter hydrocarbons removed, is fed through line 1, which is controlled by ultra-violet controller 9, into fractionator 2 from which butene-2 and heavier material is removed via line 5. Butadiene and lighter material which leaves fractionator 2 by line 4 is led via line 13 into the 50th tray of a 100-tray distillation column 14, which is supplied with furfural through line 26. Butene-1, isobutane, isobutylene and some butene-2 leave column 14 via line 15, while the furfural stream, containing the butadiene, passes to stripper 21 via line 20. The stripped furfural is returned from stripper 21 to column 14 via line 26 through valve 34, which is controlled by recorder controller 32 which measures the flow at 33. Recorder controller 32 is regulated by an analytical recorder controller 31, e.g. of the infra-red type (see Group XL (b)) which continuously detects the butene-1 concentration on a selected tray below the feed inlet of column 14, e.g. the 24th. Butadiene, with minor amounts of butenes and acetylenes, leaves stripper 21 via line 22 and passes through line 38 to a 120-tray fractionator 37, from which butene-2 and heavier materials are removed via line 47. Butadiene and the lighter acetylenes pass from fractionator 37 via line 40 to accumulator 42, from which methylacetylene rich vapours are bled through valve 46. A controller 52, similar to 31, detects the butene-2 or total olefine content on a selected tray in fractionator 37 and controls valve 49 which determines whether the butadiene runs to storage via line 48 or to recycle via line 43. A modification for acetylene-rich vapours entering fractionator 37 is described in which an extra analytical recorder controller detecting the acetylenes content is used below, and in conjunction with, recorder 52. The Specification mentions several other solvents which may be used to replace the furfural.
GB33659/56A 1955-11-10 1956-11-05 Improvements in separation of butadiene from hydrocarbons by extractive distillation Expired GB829021A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US829021XA 1955-11-10 1955-11-10

Publications (1)

Publication Number Publication Date
GB829021A true GB829021A (en) 1960-02-24

Family

ID=22174184

Family Applications (1)

Application Number Title Priority Date Filing Date
GB33659/56A Expired GB829021A (en) 1955-11-10 1956-11-05 Improvements in separation of butadiene from hydrocarbons by extractive distillation

Country Status (1)

Country Link
GB (1) GB829021A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4515661A (en) * 1981-10-13 1985-05-07 Nippon Zeon Co. Ltd. Process for separating highly pure butene-1 and butene-2
WO2018001982A1 (en) * 2016-06-29 2018-01-04 IFP Energies Nouvelles Method for the production of butadiene from ethanol, incorporating extractive distillation

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4515661A (en) * 1981-10-13 1985-05-07 Nippon Zeon Co. Ltd. Process for separating highly pure butene-1 and butene-2
WO2018001982A1 (en) * 2016-06-29 2018-01-04 IFP Energies Nouvelles Method for the production of butadiene from ethanol, incorporating extractive distillation
FR3053331A1 (en) * 2016-06-29 2018-01-05 IFP Energies Nouvelles PROCESS FOR PRODUCING BUTADIENE FROM INTEGRATED ETHANOL WITH EXTRACTIVE DISTILLATION
CN109641815A (en) * 2016-06-29 2019-04-16 Ifp 新能源公司 It is integrated with the method by ethyl alcohol production butadiene of extractive distillation
US10654763B2 (en) 2016-06-29 2020-05-19 IFP Energies Nouvelles Process for producing butadiene from ethanol integrated with extractive distillation
CN109641815B (en) * 2016-06-29 2021-06-15 Ifp 新能源公司 Method for producing butadiene from ethanol integrated with extractive distillation

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