RU2006127130A - REACTOR NODE FOR DI AND / OR OLIGOMERIZATION OF ETHYLENE AND OTHER OLEFINS - Google Patents

REACTOR NODE FOR DI AND / OR OLIGOMERIZATION OF ETHYLENE AND OTHER OLEFINS Download PDF

Info

Publication number
RU2006127130A
RU2006127130A RU2006127130/15A RU2006127130A RU2006127130A RU 2006127130 A RU2006127130 A RU 2006127130A RU 2006127130/15 A RU2006127130/15 A RU 2006127130/15A RU 2006127130 A RU2006127130 A RU 2006127130A RU 2006127130 A RU2006127130 A RU 2006127130A
Authority
RU
Russia
Prior art keywords
reactor
circulation
ethylene
nozzles
reaction
Prior art date
Application number
RU2006127130/15A
Other languages
Russian (ru)
Inventor
Сергей Сергеевич Потапов (RU)
Сергей Сергеевич Потапов
Геннадий Петрович Белов (RU)
Геннадий Петрович Белов
шов Владимир Николаевич Кудр (RU)
Владимир Николаевич Кудряшов
Леонид Степанович Алехин (RU)
Леонид Степанович Алехин
Ильгиз Хабипович Мухитов (RU)
Ильгиз Хабипович Мухитов
Александр Васильевич Кустов (RU)
Александр Васильевич Кустов
Борис Михайлович Шурупов (RU)
Борис Михайлович Шурупов
Владимир Петрович Петров (RU)
Владимир Петрович Петров
Original Assignee
Некоммерческа организаци Учреждение Институт проблем химической физики Российской академии наук (статус государственного учреждени (ИПХФ РАН) (RU)
Некоммерческая организация Учреждение Институт проблем химической физики Российской академии наук (статус государственного учреждения (ИПХФ РАН)
Казанское открытое акционерное общество "Органический синтез" (ОАО "Казаньоргсинтез") (RU)
Казанское Открытое Акционерное Общество "Органический Синтез" (Оао "Казаньоргсинтез")
Закрытое акционерное общество "Инкор Инжиниринг" (ЗАО "Инкор Инжиниринг") (RU)
Закрытое акционерное общество "Инкор Инжиниринг" (ЗАО "Инкор Инжиниринг")
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 Некоммерческа организаци Учреждение Институт проблем химической физики Российской академии наук (статус государственного учреждени (ИПХФ РАН) (RU), Некоммерческая организация Учреждение Институт проблем химической физики Российской академии наук (статус государственного учреждения (ИПХФ РАН), Казанское открытое акционерное общество "Органический синтез" (ОАО "Казаньоргсинтез") (RU), Казанское Открытое Акционерное Общество "Органический Синтез" (Оао "Казаньоргсинтез"), Закрытое акционерное общество "Инкор Инжиниринг" (ЗАО "Инкор Инжиниринг") (RU), Закрытое акционерное общество "Инкор Инжиниринг" (ЗАО "Инкор Инжиниринг") filed Critical Некоммерческа организаци Учреждение Институт проблем химической физики Российской академии наук (статус государственного учреждени (ИПХФ РАН) (RU)
Priority to RU2006127130/15A priority Critical patent/RU2006127130A/en
Priority to EA200700954A priority patent/EA014758B1/en
Priority to CNA2007101929180A priority patent/CN101199943A/en
Priority to BRPI0703325-7A priority patent/BRPI0703325A/en
Publication of RU2006127130A publication Critical patent/RU2006127130A/en

Links

Classifications

    • 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
    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Claims (4)

1. Реакторный узел для ди- и/или олигомеризации этилена и других олефинов, выполненный в виде вертикального реактора колонного типа без внешней охлаждающей трубчатой рубашки, снабженный патрубками для ввода в реакционное пространство сырья и компонентов катализатора, турбулизаторами реакционной массы, размещенными в реакционном пространстве, датчиками температуры, давления и расхода реагентов и продуктов на входе и выходе, устройством для отбора проб, а также циркуляционным контуром, включающим холодильники и циркуляционные насосы для охлаждения и прокачки реакционной массы через реактор сверху - вниз, отличающийся тем, что он дополнительно снабжен выносным циркуляционным контуром, включающим циркуляционный насос и теплообменник-холодильник.1. The reactor unit for the di- and / or oligomerization of ethylene and other olefins, made in the form of a vertical column reactor without an external cooling tube jacket, equipped with nozzles for introducing into the reaction space of raw materials and catalyst components, reaction mass turbulators located in the reaction space, sensors of temperature, pressure and consumption of reagents and products at the inlet and outlet, a device for sampling, as well as a circulation circuit, including refrigerators and circulation pumps for cooling and pumping the reaction mixture through the reactor from the top - down, characterized in that it is further provided with external circulation loop comprising a circulation pump and a heat exchanger cooler. 2. Реакторный узел по п.1, отличающийся тем, что патрубки для ввода в реактор этилена и водорода размещены в 2-6 точках, разнесенных по высоте реактора на расстоянии 1-8 м друг от друга через группу 4 или 8 патрубков, размещенных касательно к оси реактора под углом 45-60° через каждые 90-60-45° соответственно по окружности обечайки.2. The reactor assembly according to claim 1, characterized in that the nozzles for introducing ethylene and hydrogen into the reactor are located at 2-6 points spaced along the height of the reactor at a distance of 1-8 m from each other through a group of 4 or 8 nozzles placed relative to to the axis of the reactor at an angle of 45-60 ° every 90-60-45 °, respectively, around the circumference of the shell. 3. Реакторный узел по п.1, отличающийся тем, что основание реактора выполнено конусообразным.3. The reactor unit according to claim 1, characterized in that the base of the reactor is conical. 4. Реакторный узел по п.1, отличающийся тем, что патрубки возврата охлажденного реакционного циркуляционного потока размещены в 2-4 точках, разнесенных по высоте реактора на расстоянии 1-15 м от верхней точки возврата циркулирующей жидкой фазы в реактор.4. The reactor assembly according to claim 1, characterized in that the return pipes of the cooled reaction circulation stream are located at 2-4 points spaced along the height of the reactor at a distance of 1-15 m from the upper return point of the circulating liquid phase to the reactor.
RU2006127130/15A 2006-07-27 2006-07-27 REACTOR NODE FOR DI AND / OR OLIGOMERIZATION OF ETHYLENE AND OTHER OLEFINS RU2006127130A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
RU2006127130/15A RU2006127130A (en) 2006-07-27 2006-07-27 REACTOR NODE FOR DI AND / OR OLIGOMERIZATION OF ETHYLENE AND OTHER OLEFINS
EA200700954A EA014758B1 (en) 2006-07-27 2007-05-25 Catalytic system for ethylene dimerization and method
CNA2007101929180A CN101199943A (en) 2006-07-27 2007-07-27 Ethylene dimerization catalysis system, ethylene dimerization method, dimerization device and reactor unit
BRPI0703325-7A BRPI0703325A (en) 2006-07-27 2007-07-27 catalytic system for ethylene dimerization, ethylene dimerization process, dimerization reactor plant and unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
RU2006127130/15A RU2006127130A (en) 2006-07-27 2006-07-27 REACTOR NODE FOR DI AND / OR OLIGOMERIZATION OF ETHYLENE AND OTHER OLEFINS

Publications (1)

Publication Number Publication Date
RU2006127130A true RU2006127130A (en) 2008-02-10

Family

ID=39153847

Family Applications (1)

Application Number Title Priority Date Filing Date
RU2006127130/15A RU2006127130A (en) 2006-07-27 2006-07-27 REACTOR NODE FOR DI AND / OR OLIGOMERIZATION OF ETHYLENE AND OTHER OLEFINS

Country Status (4)

Country Link
CN (1) CN101199943A (en)
BR (1) BRPI0703325A (en)
EA (1) EA014758B1 (en)
RU (1) RU2006127130A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2825653C1 (en) * 2019-12-18 2024-08-28 Ифп Энержи Нувелль Gas-liquid oligomerisation reactor with successive zones of different diameters

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3079813A2 (en) 2013-12-13 2016-10-19 Saudi Basic Industries Corporation Catalyst compositions for selective dimerization of ethylene
WO2015155666A2 (en) * 2014-04-07 2015-10-15 Saudi Basic Industries Corporation Freeze-drying of organoaluminum co-catalyst compositions and transition metal complex catalyst compositions
US10414699B2 (en) * 2016-05-27 2019-09-17 Chevron Phillips Chemical Company Lp Process improvements in selective ethylene oligomerizations
FR3074493B1 (en) * 2017-12-05 2019-12-13 IFP Energies Nouvelles METHOD FOR DIMERIZATION OF ETHYLENE COMPRISING A STEP OF TREATMENT OF THE REACTIONAL EFFLUENT
FR3083235B1 (en) * 2018-06-29 2021-12-03 Ifp Energies Now CASCADE OLIGOMERIZATION PROCESS OF AGITATED LIQUID GAS REACTORS WITH STAGE INJECTION OF ETHYLENE
CN111408408B (en) * 2019-01-04 2023-04-11 中国石油化工股份有限公司 Catalyst composition, preparation method thereof and application thereof in reaction for synthesizing 1-butene through selective dimerization of ethylene

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU992501A1 (en) * 1981-05-28 1983-01-30 Предприятие П/Я А-3134 Process for preparing butene-1
EP0135441B1 (en) * 1983-09-20 1986-11-05 Institut Français du Pétrole Process for the synthesis of butene-1 by dimerisation of ethylene
SU1759824A1 (en) * 1987-01-04 1992-09-07 Грозненский филиал Охтинского научно-производственного объединения "Пластполимер" Method of producing butene-1
EP0516852A4 (en) * 1990-12-07 1993-04-21 Okhtinskoe Nauchno-Proizvodstvennoe Obieninenie "Plastopolimer" Method of obtaining butene-i
SU1809593A1 (en) * 1991-05-21 1996-03-27 Научно-производственное акционерное общество "Спектр ЛК" Method of pentaerythritol synthesis

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2825653C1 (en) * 2019-12-18 2024-08-28 Ифп Энержи Нувелль Gas-liquid oligomerisation reactor with successive zones of different diameters
RU2825652C1 (en) * 2019-12-18 2024-08-28 Ифп Энержи Нувелль Gas-liquid oligomerisation reactor containing transverse internal elements

Also Published As

Publication number Publication date
BRPI0703325A (en) 2008-03-11
EA014758B1 (en) 2011-02-28
EA200700954A1 (en) 2008-04-28
CN101199943A (en) 2008-06-18

Similar Documents

Publication Publication Date Title
RU2006127130A (en) REACTOR NODE FOR DI AND / OR OLIGOMERIZATION OF ETHYLENE AND OTHER OLEFINS
CN105050992A (en) Olefin hydration process using oscillatory baffled reactor
RU2010132705A (en) CATALYST FEEDING SYSTEMS AND WAYS OF THEIR APPLICATION
CN103030622B (en) Method for preparing glyceride carbonate by using loop reaction device
CN201841013U (en) 1-hexene synthesis reation kettle
RU2015123993A (en) A FLOW-FLOW REACTOR WITH A PSEU-LIQUID CATALYST LAYER FOR OLEFIN DEGHODATION
KR100997570B1 (en) Multiphase polymerization reactor
RU2013135413A (en) HEAT EXCHANGER FOR COOLING HOT GASES AND HEAT EXCHANGE SYSTEM
CN103030505B (en) MTP (methanol to propylene) method
RU91755U1 (en) VORTEX HEAT EXCHANGE FOR GAS CONDENSATION
CN102502697A (en) Method for recovering ammonia in morpholine solution
CN217612958U (en) Purification device for medical intermediate
RU2017134410A (en) SOLID COOLANT COOLING DEVICE, DESIGNED FOR PRECISE TEMPERATURE CONTROL, SUITABLE FOR APPLICATION IN THE ENDOTHERMAL OR EXOTHERMAL PROCESS
CN108129300A (en) A kind of novel preparation method of acetylsalicylic acid
CN205313484U (en) Gas hydrate preparation facilities
CN103816847A (en) Combined reactor and application thereof
RU2007130790A (en) METHOD FOR POLYMERIZATION OF VINYL MONOMERS
RU2294320C2 (en) Method of alkylation of benzene and alkylator for realization of this method
JPH01128955A (en) Continuous production of isobutyric acid
RU2006138522A (en) REACTOR
CN1166449C (en) Coupling equipment of reaction and separation
RU2539984C1 (en) Reactor with stationary layer of catalyst
CN217015376U (en) High-efficiency fractionating column
CN214469621U (en) Heat dissipation system for ethylene oligomerization reactor
RU198299U1 (en) Multilayer Catalytic Reactor

Legal Events

Date Code Title Description
FA92 Acknowledgement of application withdrawn (lack of supplementary materials submitted)

Effective date: 20090226

FA92 Acknowledgement of application withdrawn (lack of supplementary materials submitted)

Effective date: 20090226