RU2016135740A - HEATING WALL REACTOR - Google Patents

HEATING WALL REACTOR Download PDF

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Publication number
RU2016135740A
RU2016135740A RU2016135740A RU2016135740A RU2016135740A RU 2016135740 A RU2016135740 A RU 2016135740A RU 2016135740 A RU2016135740 A RU 2016135740A RU 2016135740 A RU2016135740 A RU 2016135740A RU 2016135740 A RU2016135740 A RU 2016135740A
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RU
Russia
Prior art keywords
reactor
raw materials
catalyst
reactor according
unloading
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Application number
RU2016135740A
Other languages
Russian (ru)
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RU2706050C2 (en
RU2016135740A3 (en
Inventor
Владимир Васильевич Каданцев
Original Assignee
Владимир Васильевич Каданцев
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Application filed by Владимир Васильевич Каданцев filed Critical Владимир Васильевич Каданцев
Priority to RU2016135740A priority Critical patent/RU2706050C2/en
Publication of RU2016135740A publication Critical patent/RU2016135740A/en
Publication of RU2016135740A3 publication Critical patent/RU2016135740A3/ru
Application granted granted Critical
Publication of RU2706050C2 publication Critical patent/RU2706050C2/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J3/00Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
    • B01J3/03Pressure vessels, or vacuum vessels, having closure members or seals specially adapted therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical 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
    • B01J8/04Chemical 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
    • B01J8/0446Chemical 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 the flow within the beds being predominantly vertical

Claims (8)

1. Реактор с греющей стенкой, состоящий из обечайки реактора, греющей рубашки, штуцера ввода сырья, задвижки, верхнего штуцера ввода сырья в камеру форсунки, выводного патрубока для выхода продуктов реакции, байпаса подачи сырья, минуя греющую рубашку реактора, штуцера аварийного слива сырья из греющей рубашки, люка загрузки катализатора, выгружного лючка для выгрузки катализатора, люка выгружного чистки реактора, штуцера выхода газов, смотрового люка для осмотра и освидетельствования внутренней полости реактора без выгрузки катализатора.1. A reactor with a heating wall, consisting of a shell of the reactor, a heating shirt, a nozzle for introducing raw materials, a gate valve, an upper nozzle for introducing raw materials into the nozzle chamber, an outlet pipe for the exit of reaction products, a bypass for supplying raw materials, bypassing the heating jacket of the reactor, and an emergency discharge nozzle for raw materials from heating jacket, catalyst loading hatch, unloading hatch for unloading the catalyst, unloading hatch for cleaning the reactor, gas outlet fitting, inspection hatch for inspecting and examining the internal cavity of the reactor without unloading the catalyst but. 2. Реактор по п. 1, отличающийся тем, что предварительно нагретое сырье подается в греющую рубашку и, поднимаясь по винтовой спирали, нагревает внутреннюю полость реактора до температуры реакции на стадии выхода на режим или поддерживает температурный режим во время проведения каталитических процессов во всем объеме реактора.2. The reactor according to claim 1, characterized in that the preheated raw material is fed into the heating jacket and, rising in a spiral spiral, heats the internal cavity of the reactor to the reaction temperature at the stage of entering the regime or maintains the temperature regime during the catalytic processes in full the reactor. 3. Реактор по п. 1, отличающийся тем, что сырье из греющей рубашки реактора поступает в камеру форсунки, состоящую из трубы распорной, перегородки распылительной верхней, перегородки распылительной нижней и распорок, придающих жесткость конструкции и задающих вектору движения потока спиральную составляющую.3. The reactor according to claim 1, characterized in that the raw material from the heating jacket of the reactor enters the nozzle chamber, which consists of a spacer pipe, a spray upper partition, a spray lower partition, and struts that impart structural rigidity and give a spiral component to the flow vector. 4. Реактор по п. 1, отличающийся тем, что слой катализатора в реакторе разделен кольцевыми перегородками, регулирующими движение сырьевого потока вдоль оси реактора и препятствуя стеканию сырья по стенкам реактора.4. The reactor according to claim 1, characterized in that the catalyst layer in the reactor is divided by annular partitions that regulate the movement of the feed stream along the axis of the reactor and preventing the flow of raw materials along the walls of the reactor. 5. Реактор по п. 1, отличающийся тем, что слой катализатора лежит на слое керамических шаров, препятствующих выносу катализатора вместе с продуктами реакции, и сверху закрыт слоем керамических шаров, способствующих лучшему распределению сырья по площади реактора.5. The reactor according to claim 1, characterized in that the catalyst layer lies on a layer of ceramic balls that impede the removal of the catalyst together with the reaction products, and is covered by a layer of ceramic balls on top, contributing to a better distribution of raw materials over the reactor area. 6. Реактор по п. 1, отличающийся тем, что выгружной лючок для выгрузки катализатора расположен под углом 30° к оси реактора.6. The reactor according to claim 1, characterized in that the discharge door for discharging the catalyst is located at an angle of 30 ° to the axis of the reactor. 7. Реактор по п. 1, отличающийся тем, что контроль температуры и давления внутри реактора осуществляется с помощью термодатчика многозонного и манометра.7. The reactor according to claim 1, characterized in that the temperature and pressure inside the reactor are controlled using a multi-zone temperature sensor and a pressure gauge. 8. Реактор по п. 1, отличающийся тем, что канал термодатчика изготавливается таким образом, чтобы обеспечить защиту термодатчика от механических повреждений и минимизировать тепловые искажения в показаниях приборов, имеющий обтекатели, препятствующие стеканию сырья вдоль канала по направляющим трубам.8. The reactor according to claim 1, characterized in that the temperature sensor channel is manufactured in such a way as to protect the temperature sensor from mechanical damage and minimize thermal distortions in the instrument readings, having fairings that prevent the flow of raw materials along the channel along the guide pipes.
RU2016135740A 2016-09-02 2016-09-02 Isothermal reactor RU2706050C2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
RU2016135740A RU2706050C2 (en) 2016-09-02 2016-09-02 Isothermal reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
RU2016135740A RU2706050C2 (en) 2016-09-02 2016-09-02 Isothermal reactor

Publications (3)

Publication Number Publication Date
RU2016135740A true RU2016135740A (en) 2018-03-05
RU2016135740A3 RU2016135740A3 (en) 2018-06-27
RU2706050C2 RU2706050C2 (en) 2019-11-13

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RU2016135740A RU2706050C2 (en) 2016-09-02 2016-09-02 Isothermal reactor

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Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU1217786A1 (en) * 1984-08-16 1986-03-15 Павлодарский Ордена Трудового Красного Знамени Алюминиевый Завод Им.50-Летия Ссср Method of calcining aluminium hydroxide
SU1733072A1 (en) * 1990-08-07 1992-05-15 Институт Химии Присадок Ан Азсср Film-type reactor
EP1900424A1 (en) * 2006-09-11 2008-03-19 Methanol Casale S.A. Isothermal reactor
WO2012027822A1 (en) * 2010-09-03 2012-03-08 Greg Naterer Thermochemical reactors and processes for hydrolysis of cupric chloride

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Publication number Publication date
RU2706050C2 (en) 2019-11-13
RU2016135740A3 (en) 2018-06-27

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Effective date: 20200903