ES348810A1 - Un procedimiento para separar un efluente de producto de conversion hidrocarbonado de fase mixta. - Google Patents

Un procedimiento para separar un efluente de producto de conversion hidrocarbonado de fase mixta.

Info

Publication number
ES348810A1
ES348810A1 ES348810A ES348810A ES348810A1 ES 348810 A1 ES348810 A1 ES 348810A1 ES 348810 A ES348810 A ES 348810A ES 348810 A ES348810 A ES 348810A ES 348810 A1 ES348810 A1 ES 348810A1
Authority
ES
Spain
Prior art keywords
separation zone
phase
separating
liquid phase
gas 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
Application number
ES348810A
Other languages
English (en)
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.)
Universal Oil Products Co
Original Assignee
Universal Oil Products 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 Universal Oil Products Co filed Critical Universal Oil Products Co
Publication of ES348810A1 publication Critical patent/ES348810A1/es
Expired legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
    • C10G49/22—Separation of effluents
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G5/00—Recovery of liquid hydrocarbon mixtures from gases, e.g. natural gas
    • C10G5/06—Recovery of liquid hydrocarbon mixtures from gases, e.g. natural gas by cooling or compressing
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G7/00—Distillation of hydrocarbon oils

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Pressure Vessels And Lids Thereof (AREA)

Abstract

Un procedimiento para separar un efluente de producto de conversión hidrocarbonado de fase mixta, que contiene hidrocarburos que hierven por encima de aproximadamente 566ºC, que comprende las operaciones de: (a) separar dicho efluente en una primera zona de separación a una temperatura superior a aproximadamente 371ºC y una presión manométrica superior a aproximadamente 68 atmósferas, para proporcionar una primera fase de vapor y una primera fase líquida , (b) enfriar dicha primera fase de vapor, introducirla en una segunda zona de separación a una temperatura inferior a aproximadamente 60º C y una presión sustancialmente igual a la de dicha primera zona de separación y separar en ella una segunda fase de vapor rica en hidrógeno y una segunda fase líquida que comprende principalmente propano e hidrocarburos normalmente líquidos más pesados © introducir al menos una parte de dicha primera fase líquida, a una presión manométrica inferior a aproximadamente 13,6 atmósferas, en una tercera zonade separación, en un punto situado bajo una capa de malla que se extiende a través de una parte superior de dicha tercera zona de separación y separar en ella una tercera fase de vapor y una tercera fase líquida que contiene hidrocarburos que hierven por encima de 566ºC (d) introducir dicha tercera fase líquida en una cuarta zona de separación, a una temperatura superior a aproximadamente 371ºC y una presión inferior a la atmosférica y separar en ella una fracción residual que contiene hidrocarburos que hierven por encima de aproximadamente 566ºC y una fracción de gasoil pesado que hierve por debajo de aproximadamente 566ºC y (e) introducir una parte de dicha fracción de gasoil pesado en dicha tercera zona de separación , en un punto situado por encima de dicha capa de malla
ES348810A 1966-12-30 1967-12-29 Un procedimiento para separar un efluente de producto de conversion hidrocarbonado de fase mixta. Expired ES348810A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US606107A US3371030A (en) 1966-12-30 1966-12-30 Black oil conversion product separation process

Publications (1)

Publication Number Publication Date
ES348810A1 true ES348810A1 (es) 1969-03-16

Family

ID=24426564

Family Applications (1)

Application Number Title Priority Date Filing Date
ES348810A Expired ES348810A1 (es) 1966-12-30 1967-12-29 Un procedimiento para separar un efluente de producto de conversion hidrocarbonado de fase mixta.

Country Status (13)

Country Link
US (1) US3371030A (es)
AT (1) AT285007B (es)
BE (1) BE708519A (es)
DK (1) DK130648B (es)
ES (1) ES348810A1 (es)
FI (1) FI49986C (es)
FR (1) FR1567989A (es)
GB (1) GB1199740A (es)
IL (1) IL29217A (es)
NL (1) NL152921B (es)
NO (1) NO116511B (es)
OA (1) OA02564A (es)
SE (1) SE338390B (es)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1276877A (en) * 1968-10-28 1972-06-07 Universal Oil Prod Co Process for the conversion and desulfurization of oil
US3594309A (en) * 1968-10-28 1971-07-20 Universal Oil Prod Co Conversion and desulfurization of hydrocarbonaceous black oils
US3617502A (en) * 1968-10-28 1971-11-02 Universal Oil Prod Co Desulfurization and conversion of hydrocarbonaceous black oils
US3537985A (en) * 1968-12-23 1970-11-03 Phillips Petroleum Co Fractionation process
US3546099A (en) * 1969-02-26 1970-12-08 Universal Oil Prod Co Method for separating the effluent from a hydrocarbon conversion process reaction zone
US4159935A (en) * 1978-08-30 1979-07-03 Uop Inc. Conversion of hydrocarbonaceous black oils
US4159937A (en) * 1978-08-30 1979-07-03 Uop Inc. Mixed-phase reaction product effluent separation process
GB8807807D0 (en) * 1988-03-31 1988-05-05 Shell Int Research Process for separating hydroprocessed effluent streams

Also Published As

Publication number Publication date
FR1567989A (es) 1969-05-23
NL6717794A (es) 1968-07-01
SE338390B (es) 1971-09-06
IL29217A (en) 1971-01-28
DK130648B (da) 1975-03-17
OA02564A (fr) 1970-05-05
GB1199740A (en) 1970-07-22
DK130648C (es) 1975-08-25
NO116511B (es) 1969-04-08
FI49986B (es) 1975-07-31
AT285007B (de) 1970-10-12
FI49986C (fi) 1975-11-10
BE708519A (es) 1968-05-02
US3371030A (en) 1968-02-27
DE1645828A1 (de) 1970-07-30
NL152921B (nl) 1977-04-15

Similar Documents

Publication Publication Date Title
US2301240A (en) Purification of acetylene prepared by thermal or electrical methods
US2325379A (en) Distillation process
ES347843A1 (es) Un procedimiento para separar un fluido saliente de pro- ducto de conversion, en fase mixta y caliente.
US2398689A (en) Azeotropic styrene distillation
ES348810A1 (es) Un procedimiento para separar un efluente de producto de conversion hidrocarbonado de fase mixta.
GB1340764A (en) Quenching process for pyrolytically cracked hydrocarbons
US3575818A (en) Manufacture of absolute ethanol using pentane as azeotroping agent
ES372921A1 (es) Un procedimiento para la conversion y desulfuracion de un material de carga sulfuroso, hidrocarburado.
US2322881A (en) Solvent treating
US2316126A (en) Method of producing toluene
US2870226A (en) Production and recovery of aromatic hydrocarbons
GB1308735A (en) Method of extracting aromatic hydrocarbons
US2341282A (en) Purification of methyl methacrylate
GB1164372A (en) Method of Separating Aromatic Hydrocarbons from Mixtures Containing Them.
US2411808A (en) Separation of hydrocarbons from water miscible liquids by distillation and washing
ES395783A1 (es) Un procedimiento para la obtencion de anhidrido maleico pu-ro.
US2264928A (en) Production of optically active piperitone
JPS5740423A (en) Production of cumene and/or polyisopropylbenzene
US2704272A (en) Separation of organic mixtures
US2459432A (en) Separation of cineoles from hydrocarbons of similar boiling range by azeotropic distillation with phenols
US3201492A (en) Separation of hydrocarbons possessing volatility differences
US2979542A (en) Production of dichlorbutenes
US3637486A (en) Steam distilling pyrolysis gasoline
GB918003A (en) Process for the continuous fractional distillation of coal tar
GB1331778A (en) Hydrogenation of residual petroleum fractions