WO2018117820A1 - Procédé de préparation de propylène - Google Patents

Procédé de préparation de propylène Download PDF

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Publication number
WO2018117820A1
WO2018117820A1 PCT/NL2017/050845 NL2017050845W WO2018117820A1 WO 2018117820 A1 WO2018117820 A1 WO 2018117820A1 NL 2017050845 W NL2017050845 W NL 2017050845W WO 2018117820 A1 WO2018117820 A1 WO 2018117820A1
Authority
WO
WIPO (PCT)
Prior art keywords
process according
hydrocarbon feed
catalyst
framework
molecular sieve
Prior art date
Application number
PCT/NL2017/050845
Other languages
English (en)
Inventor
Raymond Paul Fletcher
Original Assignee
Inovacat B.V.
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 NL2018256A external-priority patent/NL2018256B1/en
Application filed by Inovacat B.V. filed Critical Inovacat B.V.
Priority to ES17832106T priority Critical patent/ES2897435T3/es
Priority to US16/470,321 priority patent/US11447432B2/en
Priority to EP17832106.3A priority patent/EP3558907B1/fr
Publication of WO2018117820A1 publication Critical patent/WO2018117820A1/fr

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • C07C4/02—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
    • C07C4/06—Catalytic processes
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
    • C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
    • C07C5/2702—Catalytic processes not covered by C07C5/2732 - C07C5/31; Catalytic processes covered by both C07C5/2732 and C07C5/277 simultaneously
    • 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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • C10G11/04—Oxides
    • C10G11/05—Crystalline alumino-silicates, e.g. molecular sieves
    • 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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/10—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with stationary catalyst bed
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2529/00—Catalysts comprising molecular sieves
    • C07C2529/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
    • C07C2529/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • C07C2529/064—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof containing iron group metals, noble metals or copper
    • C07C2529/072—Iron group metals or copper
    • 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
    • C10G2300/1081—Alkanes
    • 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
    • C10G2400/20—C2-C4 olefins

Definitions

  • the higher boiling fraction as obtained after isolation of propylene and possible other low boiling compounds from the cracked effluent is preferably recycled to the one or more fixed beds.
  • the high boiling fraction is contacted in admixture with the hydrocarbon feed with the heterogeneous cracking catalyst.
  • the higher boiling fraction is first subjected to an isomerization step before being recycled to the one or more fixed beds. It has been found that the propylene yield may increase when such an isomerisation step is performed. Isomerisation of especially the normal pentanes and normal hexanes to their branched isomers has been found to increase the propylene yield.
  • a suitable extraction process is an extractive distillation using one of the above described solvents and suitably sulfolane, N-formyl morpholine or N- methyl pyrrolidone, optionally in combination with a suitable co-solvent.
  • a packed bed reactor was provided consisting of the MFI catalyst obtained in Example 1.
  • a naphtha having a GC RON of 91.2 with 90% boiling point at 182°C consisting of 35 wt% paraffins, 12 wt% naphthenes, 31 wt% olefins and 22 wt% aromatics and 1.4 wt% normal pentane and 10.1 wt% iso-pentane was fed to the reactor at 1.4 g/min in 50 ml/min nitrogen at 500 °C.
  • the WHSV was 57 h-1.
  • the pressure at the reactor effluent was atmospheric.
  • the cracked effluent was analysed and the results presented as (in weight percentages) are provided in Table 1.

Landscapes

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

Abstract

L'invention concerne un procédé de préparation de propylène à partir d'une charge d'alimentation d'hydrocarbures comprenant du pentane par la mise en contact de la charge d'alimentation d'hydrocarbures avec un catalyseur de craquage hétérogène tel que présent dans un ou plusieurs lits fixes, ce qui permet d'obtenir un effluent craqué. Le catalyseur hétérogène comprend un composant matriciel et un tamis moléculaire comprenant une structure d'alumine, une structure de silice et une structure de métal choisi dans le groupe constitué par Zn, Fe, Ce, La, Y, Ga et/ou Zr. Le propylène est isolé de l'effluent craqué.
PCT/NL2017/050845 2016-12-21 2017-12-19 Procédé de préparation de propylène WO2018117820A1 (fr)

Priority Applications (3)

Application Number Priority Date Filing Date Title
ES17832106T ES2897435T3 (es) 2016-12-21 2017-12-19 Proceso para preparar propileno
US16/470,321 US11447432B2 (en) 2016-12-21 2017-12-19 Process to prepare propylene
EP17832106.3A EP3558907B1 (fr) 2016-12-21 2017-12-19 Procédé de préparation de propylène

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US201662437242P 2016-12-21 2016-12-21
US62/437,242 2016-12-21
NL2018256 2017-01-30
NL2018256A NL2018256B1 (en) 2016-12-21 2017-01-30 Process to prepare propylene

Publications (1)

Publication Number Publication Date
WO2018117820A1 true WO2018117820A1 (fr) 2018-06-28

Family

ID=58159494

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/NL2017/050845 WO2018117820A1 (fr) 2016-12-21 2017-12-19 Procédé de préparation de propylène

Country Status (1)

Country Link
WO (1) WO2018117820A1 (fr)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5171921A (en) 1991-04-26 1992-12-15 Arco Chemical Technology, L.P. Production of olefins
US5245102A (en) 1990-11-29 1993-09-14 Uop Isomerization with distillation and psa recycle streams
US20090099398A1 (en) 2007-10-16 2009-04-16 David A Wegerer Pentane Catalytic Cracking Process
US20150174565A1 (en) * 2012-07-26 2015-06-25 Chiyoda Corporation Zeolite catalysts, methods for producing zeolite catalysts, and methods for producing lower olefins
WO2016209074A1 (fr) * 2015-06-23 2016-12-29 Inovacat B.V. Procédé de préparation de propylène

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5245102A (en) 1990-11-29 1993-09-14 Uop Isomerization with distillation and psa recycle streams
US5171921A (en) 1991-04-26 1992-12-15 Arco Chemical Technology, L.P. Production of olefins
US20090099398A1 (en) 2007-10-16 2009-04-16 David A Wegerer Pentane Catalytic Cracking Process
US20150174565A1 (en) * 2012-07-26 2015-06-25 Chiyoda Corporation Zeolite catalysts, methods for producing zeolite catalysts, and methods for producing lower olefins
WO2016209074A1 (fr) * 2015-06-23 2016-12-29 Inovacat B.V. Procédé de préparation de propylène

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
B.R. WOOD ET AL., JOURNAL OF CATALYSIS, vol. 225, 2004, pages 300 - 306
J.I. VILLEGAS, ET AL.: "Isomerisation of n-butane to isobutane over Pt-modified Beta and ZSM-5 zeolite catalysts: Catalyst deactivation and regeneration", CHEMICAL ENGINEERING JOURNAL, vol. 120, no. 1-2, July 2006 (2006-07-01), Elsevier Sequoia, Lausanne, CH, pages 83 - 89, XP028035874, ISSN: 1385-8947, [retrieved on 20060701], DOI: 10.1016/j.cej.2006.03.011 *

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