GB788712A - Improvements in or relating to distillation apparatus - Google Patents

Improvements in or relating to distillation apparatus

Info

Publication number
GB788712A
GB788712A GB19437/56A GB1943756A GB788712A GB 788712 A GB788712 A GB 788712A GB 19437/56 A GB19437/56 A GB 19437/56A GB 1943756 A GB1943756 A GB 1943756A GB 788712 A GB788712 A GB 788712A
Authority
GB
United Kingdom
Prior art keywords
stripper
chamber
vortex
riser
liquid
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
GB19437/56A
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.)
Bataafsche Petroleum Maatschappij NV
Original Assignee
Bataafsche Petroleum Maatschappij NV
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 Bataafsche Petroleum Maatschappij NV filed Critical Bataafsche Petroleum Maatschappij NV
Publication of GB788712A publication Critical patent/GB788712A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G7/00Distillation of hydrocarbon oils
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/06Flash distillation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14Fractional distillation or use of a fractionation or rectification column
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14Fractional distillation or use of a fractionation or rectification column
    • B01D3/16Fractionating columns in which vapour bubbles through liquid
    • B01D3/18Fractionating columns in which vapour bubbles through liquid with horizontal bubble plates
    • B01D3/20Bubble caps; Risers for vapour; Discharge pipes for liquid

Abstract

<PICT:0788712/III/1> <PICT:0788712/III/2> In a distillation apparatus comprising a vortex chamber V having one or more tangential inlets 18 for distilland and a stripper S below and communicating with the vortex chamber, there is provided a separating plate 36 between the stripper and the vortex chamber and having a central opening 37 connected to a riser 38 while the annular space 39 around the riser communicates with the stripper by at least one downcomer duct 43 which passes through the separating plate and is arranged to deliver liquid into the stripper. This arrangement prevents entrainment of liquid flowing into the stripper in the stripper gas and/or vapour rising from the stripper. The diameter of the opening 37 is preferably between 0.4 and 0.7 of the diameter of the stripper. The radially disposed vortex breakers 47 have an upper edge 49 sloping down from the top of the riser to the shell of the vortex chamber. Each chamber formed by the vortex breakers may have its own downcomer to the stripper or the lower edge 48 terminates above the plate 36 so that each chamber communicates with the downcomer 43. If the vortex chamber is a flash chamber operated under reduced pressure, flanges 40 and 41 are provided on the riser to prevent liquid creeping up the side. Vapours leave the vortex chamber through the collar 19 and may be led to a conventional rectifying column or a catalytic cracking plant. In an example a topped crude oil was introduced at 390 DEG C. into the chamber V operating at a pressure of 43 mm. of mercury, and for comparative purposes under similar conditions in a similar apparatus having vortex breakers but without a separating plate. In the latter case, vapours leaving the chamber V had 3.2 per cent of the liquid leaving the base of the stripper entrained therein, whereas in the apparatus of the invention the vapours contained only 1.85 per cent of the liquid.
GB19437/56A 1955-06-24 1956-06-22 Improvements in or relating to distillation apparatus Expired GB788712A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US788712XA 1955-06-24 1955-06-24

Publications (1)

Publication Number Publication Date
GB788712A true GB788712A (en) 1958-01-08

Family

ID=22146706

Family Applications (1)

Application Number Title Priority Date Filing Date
GB19437/56A Expired GB788712A (en) 1955-06-24 1956-06-22 Improvements in or relating to distillation apparatus

Country Status (4)

Country Link
DE (1) DE1019278B (en)
FR (1) FR1154236A (en)
GB (1) GB788712A (en)
NL (2) NL208277A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113801688A (en) * 2021-10-15 2021-12-17 辽宁宝来生物能源有限公司 Decompression tower for removing solid content in catalytic slurry oil
WO2022263868A1 (en) * 2021-06-16 2022-12-22 Daviti Khomasuridze Tornado plate

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022263868A1 (en) * 2021-06-16 2022-12-22 Daviti Khomasuridze Tornado plate
CN113801688A (en) * 2021-10-15 2021-12-17 辽宁宝来生物能源有限公司 Decompression tower for removing solid content in catalytic slurry oil
CN113801688B (en) * 2021-10-15 2022-06-24 辽宁宝来生物能源有限公司 Decompression tower for removing solid content in catalytic slurry oil

Also Published As

Publication number Publication date
NL208277A (en)
DE1019278B (en) 1957-11-14
FR1154236A (en) 1958-04-03
NL95446C (en)

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