SA518391110B1 - Olefin Hydration Process Using Oscillatory Baffled Reactor - Google Patents

Olefin Hydration Process Using Oscillatory Baffled Reactor

Info

Publication number
SA518391110B1
SA518391110B1 SA518391110A SA518391110A SA518391110B1 SA 518391110 B1 SA518391110 B1 SA 518391110B1 SA 518391110 A SA518391110 A SA 518391110A SA 518391110 A SA518391110 A SA 518391110A SA 518391110 B1 SA518391110 B1 SA 518391110B1
Authority
SA
Saudi Arabia
Prior art keywords
internal
single pass
mixed
fluid conduit
process fluid
Prior art date
Application number
SA518391110A
Other languages
Arabic (ar)
Inventor
عرجة عبير
الدين ام شيخ كريم
زو وي
Original Assignee
شركه الزيت العربية السعودية
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 US14/879,601 external-priority patent/US10155707B2/en
Application filed by شركه الزيت العربية السعودية filed Critical شركه الزيت العربية السعودية
Publication of SA518391110B1 publication Critical patent/SA518391110B1/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/03—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by addition of hydroxy groups to unsaturated carbon-to-carbon bonds, e.g. with the aid of H2O2
    • C07C29/04—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by addition of hydroxy groups to unsaturated carbon-to-carbon bonds, e.g. with the aid of H2O2 by hydration of carbon-to-carbon double bonds
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053—Details of the reactor
    • B01J19/006—Baffles
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053—Details of the reactor
    • B01J19/0066—Stirrers
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053—Details of the reactor
    • B01J19/0073—Sealings
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18—Stationary reactors having moving elements inside
    • B01J19/1806—Stationary reactors having moving elements inside resulting in a turbulent flow of the reactants, such as in centrifugal-type reactors, or having a high Reynolds-number
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18—Stationary reactors having moving elements inside
    • B01J19/185—Stationary reactors having moving elements inside of the pulsating type
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
    • C07C31/02—Monohydroxylic acyclic alcohols
    • C07C31/12—Monohydroxylic acyclic alcohols containing four carbon atoms
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00761—Details of the reactor
    • B01J2219/00763—Baffles
    • B01J2219/00765—Baffles attached to the reactor wall
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/582—Recycling of unreacted starting or intermediate materials

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

A butanol production system and method for producing refined mixed butanols includes an internal baffle single pass reactor having an internal fluid conduit defined by an internal wall. The internal fluid conduit contains a process fluid comprising water, mixed butenes and mixed butanols, to form a crude product. Internal flow baffles are located along a length of the internal fluid conduit. Baffled cells are defined at an outer diameter by the internal wall and at ends by the internal flow baffles. A separation system separates water and mixed butenes from the crude product to produce refined mixed butanols. An oscillator assembly is coupled to the internal baffle single pass reactor and has a reciprocating oscillator head selectively movable in a back and forth linear motion, and in communication with the process fluid such that the process fluid undergoes a general sinusoidal movement along the internal baffle single pass reactor. Fig 1a.
SA518391110A 2015-10-09 2018-03-13 Olefin Hydration Process Using Oscillatory Baffled Reactor SA518391110B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US14/879,601 US10155707B2 (en) 2012-09-05 2015-10-09 Olefin hydration process using oscillatory baffled reactor
PCT/US2016/056015 WO2017062783A1 (en) 2015-10-09 2016-10-07 Olefin hydration process using oscillatory baffled reactor

Publications (1)

Publication Number Publication Date
SA518391110B1 true SA518391110B1 (en) 2021-12-21

Family

ID=57200114

Family Applications (1)

Application Number Title Priority Date Filing Date
SA518391110A SA518391110B1 (en) 2015-10-09 2018-03-13 Olefin Hydration Process Using Oscillatory Baffled Reactor

Country Status (6)

Country Link
EP (1) EP3359514A1 (en)
JP (2) JP2018531255A (en)
KR (1) KR102073112B1 (en)
CN (1) CN108349856A (en)
SA (1) SA518391110B1 (en)
WO (1) WO2017062783A1 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109179321B (en) * 2018-11-09 2023-11-10 沈阳航空航天大学 Online methanol reformer utilizing engine tail gas by adopting baffling separation mechanism
CN113145007B (en) * 2021-05-26 2023-03-10 昆明珑瑞一焰气体产品配送服务有限公司 Device for mixing and conveying natural gas and additive

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH523711A (en) * 1967-06-13 1972-06-15 Ceskoslovenska Akademie Ved Device for the contact of at least two liquid phases
DE69206759T2 (en) * 1991-10-26 1996-05-02 Bp Chem Int Ltd Process for the production of polyolefins
GB9313442D0 (en) * 1993-06-30 1993-08-11 Bp Chem Int Ltd Method of mixing heterogegeous systems
JP4834811B2 (en) * 2004-09-06 2011-12-14 徳島県 Method for producing formic acid
GB0523245D0 (en) * 2005-11-15 2005-12-21 Nitech Solutions Ltd Improved apparatus and method for applying oscillatory motion
JP4886324B2 (en) * 2006-03-02 2012-02-29 出光興産株式会社 Secondary reactor for butanol production
GB0614810D0 (en) * 2006-07-25 2006-09-06 Nitech Solutions Ltd Improved apparatus and method for maintaining consistently mixed materials
US8696192B2 (en) * 2007-05-10 2014-04-15 Fluid-Quip, Inc. Multiple helical vortex baffle
CN101486659B (en) * 2009-02-24 2013-02-27 中国药科大学 Alpha 1-adrenalin receptor antagonist, and preparation and medical use thereof
JP2012005382A (en) * 2010-06-23 2012-01-12 Equos Research Co Ltd Biomass hydrolyzing device
US9187388B2 (en) * 2012-09-05 2015-11-17 Saudi Arabian Oil Company Olefin hydration process using oscillatory baffled reactor

Also Published As

Publication number Publication date
EP3359514A1 (en) 2018-08-15
KR102073112B1 (en) 2020-02-04
CN108349856A (en) 2018-07-31
WO2017062783A1 (en) 2017-04-13
KR20180059541A (en) 2018-06-04
JP2018531255A (en) 2018-10-25
JP2020164535A (en) 2020-10-08

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