MX358364B - Hidrodesulfuración selectiva de gasolina de fcc menos de 100 ppm de azufre. - Google Patents

Hidrodesulfuración selectiva de gasolina de fcc menos de 100 ppm de azufre.

Info

Publication number
MX358364B
MX358364B MX2015002230A MX2015002230A MX358364B MX 358364 B MX358364 B MX 358364B MX 2015002230 A MX2015002230 A MX 2015002230A MX 2015002230 A MX2015002230 A MX 2015002230A MX 358364 B MX358364 B MX 358364B
Authority
MX
Mexico
Prior art keywords
naphtha fraction
naphtha
medium
heavy
fraction
Prior art date
Application number
MX2015002230A
Other languages
English (en)
Other versions
MX2015002230A (es
Inventor
G Podrebarac Gary
Original Assignee
Catalytic Distillation Tech
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 Catalytic Distillation Tech filed Critical Catalytic Distillation Tech
Publication of MX2015002230A publication Critical patent/MX2015002230A/es
Publication of MX358364B publication Critical patent/MX358364B/es

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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
    • C10G65/06—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps at least one step being a selective hydrogenation of the diolefins
    • 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
    • B01D3/009—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping in combination with chemical reactions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/32—Selective hydrogenation of the diolefin or acetylene 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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • 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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/14—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural parallel stages only
    • C10G65/16—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural parallel stages only including only refining steps
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1037—Hydrocarbon fractions
    • C10G2300/104—Light gasoline having a boiling range of about 20 - 100 °C
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1037—Hydrocarbon fractions
    • C10G2300/1044—Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/201—Impurities
    • C10G2300/202—Heteroatoms content, i.e. S, N, O, P
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/4087—Catalytic distillation
    • 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
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/02—Gasoline

Landscapes

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

Abstract

Se revela un proceso para reducir el contenido de azufre de una corriente de hidrocarburo. Una nafta craqueada de pleno intervalo es puesta en contacto con un catalizador de hidrogenación para convertir por lo menos una porción de los dienos y mercaptanos a tioéteres y para hidrogenar por lo menos una porción de los dienos. La nafta craqueada de pleno intervalo es fraccionada a una fracción de nafta ligera, una fracción de nafta media y una fracción de nafta pesada. La fracción de nafta pesada es hidrodesulfurada. La fracción de nafta media es mezclada con hidrógeno y gasoil para formar una mezcla, la cual es puesta en contacto con un catalizador de hidrodesulfuración para producir una fracción de nafta media que tiene una concentración de azufre reducida. Luego, las fracciones de nafta ligera, pesada y media pueden ser recombinadas para formar un producto hidrodesulfurado que tiene un contenido de azufre de menos de 10 ppm en algunas modalidades.
MX2015002230A 2012-08-21 2013-07-23 Hidrodesulfuración selectiva de gasolina de fcc menos de 100 ppm de azufre. MX358364B (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US201261691452P 2012-08-21 2012-08-21
PCT/US2013/051679 WO2014031274A1 (en) 2012-08-21 2013-07-23 Selective hydrodesulfurization of fcc gasoline to below 10 ppm sulfur

Publications (2)

Publication Number Publication Date
MX2015002230A MX2015002230A (es) 2015-05-08
MX358364B true MX358364B (es) 2018-08-15

Family

ID=50147063

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2015002230A MX358364B (es) 2012-08-21 2013-07-23 Hidrodesulfuración selectiva de gasolina de fcc menos de 100 ppm de azufre.

Country Status (13)

Country Link
US (2) US9631149B2 (es)
EP (1) EP2888341B1 (es)
KR (1) KR101663916B1 (es)
CN (1) CN103627435B (es)
AR (1) AR092371A1 (es)
BR (1) BR112015003750B1 (es)
CA (1) CA2883131C (es)
EA (1) EA026212B1 (es)
MX (1) MX358364B (es)
PH (1) PH12015500354B1 (es)
SG (1) SG11201501303XA (es)
WO (1) WO2014031274A1 (es)
ZA (1) ZA201501052B (es)

Families Citing this family (19)

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US9476000B2 (en) * 2013-07-10 2016-10-25 Uop Llc Hydrotreating process and apparatus
US9399741B2 (en) * 2013-10-09 2016-07-26 Uop Llc Methods and apparatuses for desulfurizing hydrocarbon streams
FR3030563B1 (fr) * 2014-12-18 2018-06-29 IFP Energies Nouvelles Procede d'adoucissement en composes du type sulfure d'une essence olefinique
US10308883B2 (en) * 2015-10-07 2019-06-04 Axens Process for desulfurizing cracked naphtha
FR3049955B1 (fr) 2016-04-08 2018-04-06 IFP Energies Nouvelles Procede de traitement d'une essence
FR3057578B1 (fr) 2016-10-19 2018-11-16 IFP Energies Nouvelles Procede d'hydrodesulfuration d'une essence olefinique.
JP2020513472A (ja) * 2016-11-23 2020-05-14 ハルドール・トプサー・アクチエゼルスカベット 炭化水素の脱硫方法
WO2018096063A1 (en) * 2016-11-23 2018-05-31 Haldor Topsøe A/S Process for desulfurization of hydrocarbons
CN106590739B (zh) * 2016-12-26 2018-07-13 中国石油大学(北京) 一种催化裂化汽油深度脱硫的方法
US10752847B2 (en) 2017-03-08 2020-08-25 Saudi Arabian Oil Company Integrated hydrothermal process to upgrade heavy oil
US10703999B2 (en) 2017-03-14 2020-07-07 Saudi Arabian Oil Company Integrated supercritical water and steam cracking process
TWI756504B (zh) 2017-12-29 2022-03-01 大陸商中國石油化工科技開發有限公司 一種蠟油加氫裂化方法和系統
JP2021526177A (ja) * 2018-05-30 2021-09-30 ハルドール・トプサー・アクチエゼルスカベット 炭化水素の脱硫のための方法
WO2019229049A1 (en) * 2018-05-30 2019-12-05 Haldor Topsøe A/S Process for desulfurization of hydrocarbons
US10774276B2 (en) * 2018-10-09 2020-09-15 Saudi Arabian Oil Company Multi-stage fractionation of FCC naphtha with post treatment and recovery of aromatics and gasoline fractions
US10526552B1 (en) * 2018-10-12 2020-01-07 Saudi Arabian Oil Company Upgrading of heavy oil for steam cracking process
US11292973B2 (en) * 2019-11-01 2022-04-05 Exxonmobil Chemical Patents Inc. Process and system for upgrading a hydrocarbon feed
US20240124788A1 (en) * 2022-10-17 2024-04-18 Lummus Technology Llc Selective treatment of fcc gasoline for removal of sulfur, nitrogen, and olefin compounds while maximizing retention of aromatic compounds
US11866660B1 (en) * 2022-11-09 2024-01-09 Saudi Arabian Oil Company Process and catalyst formulation for cracking crude oil

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US5597476A (en) 1995-08-28 1997-01-28 Chemical Research & Licensing Company Gasoline desulfurization process
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Also Published As

Publication number Publication date
PH12015500354A1 (en) 2015-04-20
BR112015003750A8 (pt) 2019-08-06
US20140054198A1 (en) 2014-02-27
ZA201501052B (en) 2016-01-27
CN103627435B (zh) 2016-04-27
CN103627435A (zh) 2014-03-12
SG11201501303XA (en) 2015-05-28
EP2888341A4 (en) 2016-04-27
BR112015003750A2 (pt) 2017-07-04
WO2014031274A1 (en) 2014-02-27
US20170226433A1 (en) 2017-08-10
EA201590419A1 (ru) 2015-07-30
MX2015002230A (es) 2015-05-08
EA026212B1 (ru) 2017-03-31
CA2883131A1 (en) 2014-02-27
US10280376B2 (en) 2019-05-07
CA2883131C (en) 2019-01-08
PH12015500354B1 (en) 2015-04-20
KR20150052100A (ko) 2015-05-13
BR112015003750B1 (pt) 2020-04-07
KR101663916B1 (ko) 2016-10-07
EP2888341B1 (en) 2019-12-18
AR092371A1 (es) 2015-04-15
EP2888341A1 (en) 2015-07-01
US9631149B2 (en) 2017-04-25

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