ES193894A1 - PROCEDURE FOR THE CONVERSION OF LIQUID HYDROCARBONS IN AROMATIC HYDROCARBONS AND GASES CONTAINING OLEFINS - Google Patents

PROCEDURE FOR THE CONVERSION OF LIQUID HYDROCARBONS IN AROMATIC HYDROCARBONS AND GASES CONTAINING OLEFINS

Info

Publication number
ES193894A1
ES193894A1 ES0193894A ES193894A ES193894A1 ES 193894 A1 ES193894 A1 ES 193894A1 ES 0193894 A ES0193894 A ES 0193894A ES 193894 A ES193894 A ES 193894A ES 193894 A1 ES193894 A1 ES 193894A1
Authority
ES
Spain
Prior art keywords
hydrocarbons
reactor
conversion
aromatic hydrocarbons
procedure
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
ES0193894A
Other languages
Spanish (es)
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.)
PETROCARBON Ltd
Original Assignee
PETROCARBON Ltd
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
Priority claimed from GB19653/49A external-priority patent/GB679194A/en
Application filed by PETROCARBON Ltd filed Critical PETROCARBON Ltd
Publication of ES193894A1 publication Critical patent/ES193894A1/en
Expired legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10C—WORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
    • C10C1/00—Working-up tar
    • C10C1/20—Refining by chemical means inorganic or organic compounds
    • 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
    • C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/14—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils in pipes or coils with or without auxiliary means, e.g. digesters, soaking drums, expansion means

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)
  • Materials Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

Procedimiento para la conversión de hidrocarburos líquidos en hidrocarburos aromáticos y gases conteniendo olefinas cuyos hidrocarburos a convertir tienen puntos de ebullición entre los 50 y los 400ºC. y están constituidos en su totalidad o en su parte principal por hidrocarburos no aromáticos caracterizado por el hecho de comprender el paso del material de partida hidrocarburo vaporizado conteniendo una apropiada cantidad de un agente que puede en las condiciones reinantes de presión y temperatura preferentemente oxidar carbón depositado durante la conversión a través de un reactor a una temperatura entre los 600 y los 850ºC. y a una presión entre la aproximadamente atmosférica y la manométrica de 10 atmósferas y con un espaciado de velocidades entre 0 05 y 2 0 litros siendo líquido el material de partida por hora por litro de volumen del reactor estando rellena la parte inicial o sección destiladora del reactor con trozos formados de adecuado material refractario y la parte siguiente o aromatizadora del reactor no conteniendo material alguno de relleno.Procedure for the conversion of liquid hydrocarbons into aromatic hydrocarbons and gases containing olefins whose hydrocarbons to be converted have boiling points between 50 and 400ºC. and they are constituted in its entirety or in its main part by non-aromatic hydrocarbons characterized by the fact of comprising the passage of the vaporized hydrocarbon starting material containing an appropriate amount of an agent that can preferably oxidize deposited carbon under the prevailing conditions of pressure and temperature during conversion through a reactor at a temperature between 600 and 850 ° C. and at a pressure between approximately atmospheric and gauge of 10 atmospheres and with a velocity spacing between 0.05 and 2.0 liters, the starting material being liquid per hour per liter of reactor volume, the initial part or distillation section of the reactor being filled with pieces formed of suitable refractory material and the next or aromatizing part of the reactor containing no filler material.

ES0193894A 1949-07-26 1950-07-13 PROCEDURE FOR THE CONVERSION OF LIQUID HYDROCARBONS IN AROMATIC HYDROCARBONS AND GASES CONTAINING OLEFINS Expired ES193894A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB19653/49A GB679194A (en) 1949-07-26 1949-07-26 Process for the conversion of liquid hydrocarbons into olefin-containing gases and aromatic hydrocarbons

Publications (1)

Publication Number Publication Date
ES193894A1 true ES193894A1 (en) 1951-05-01

Family

ID=10132928

Family Applications (1)

Application Number Title Priority Date Filing Date
ES0193894A Expired ES193894A1 (en) 1949-07-26 1950-07-13 PROCEDURE FOR THE CONVERSION OF LIQUID HYDROCARBONS IN AROMATIC HYDROCARBONS AND GASES CONTAINING OLEFINS

Country Status (2)

Country Link
BE (1) BE497121A (en)
ES (1) ES193894A1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1068245B (en) * 1959-11-05 Imperial Chemical Industries Limited, London Process for the production of practically acetylene-free ethylene and propylene by non-catalytic cracking of petroleum hydrocarbons by means of superheated steam

Also Published As

Publication number Publication date
BE497121A (en)

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