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RU2002133093A - REACTOR FOR EXOTHERMAL OR ENDOTERMAL HETEROGENEOUS REACTIONS - Google Patents

REACTOR FOR EXOTHERMAL OR ENDOTERMAL HETEROGENEOUS REACTIONS

Info

Publication number
RU2002133093A
RU2002133093A RU2002133093/12A RU2002133093A RU2002133093A RU 2002133093 A RU2002133093 A RU 2002133093A RU 2002133093/12 A RU2002133093/12 A RU 2002133093/12A RU 2002133093 A RU2002133093 A RU 2002133093A RU 2002133093 A RU2002133093 A RU 2002133093A
Authority
RU
Russia
Prior art keywords
reactor
housing
heat exchanger
heat exchangers
plates
Prior art date
Application number
RU2002133093/12A
Other languages
Russian (ru)
Other versions
RU2265480C2 (en
Inventor
Эрманно Филиппи
Энрико РИЦЦИ
Мирко ТАРОЦЦО
Original Assignee
Метанол Казале С.А.
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 EP00109968A external-priority patent/EP1153653A1/en
Application filed by Метанол Казале С.А. filed Critical Метанол Казале С.А.
Publication of RU2002133093A publication Critical patent/RU2002133093A/en
Application granted granted Critical
Publication of RU2265480C2 publication Critical patent/RU2265480C2/en

Links

Claims (12)

1. Реактор (1) для проведения экзотермических или эндотермических гетерогенных реакций, имеющий наружный корпус (2) по существу цилиндрической формы, концы которого закрыты соответственно крышкой и днищем (2а, 2b), снабженными по меньшей мере одним патрубком (3, 4, 7), диаметр отверстия которого меньше диаметра корпуса (2), и по меньшей мере один теплообменник (9), погруженный в удерживаемый в корпусе (2) каталитический слой (10), отличающийся тем, что в качестве теплообменника (9) используется состоящий из пластин (14) теплообменник, размеры поперечного сечения которого позволяют установить его в корпус через отверстие патрубка (3, 4, 7).1. A reactor (1) for conducting exothermic or endothermic heterogeneous reactions, having an outer casing (2) of essentially cylindrical shape, the ends of which are closed respectively by a cover and a bottom (2a, 2b), equipped with at least one pipe (3, 4, 7 ), the opening diameter of which is smaller than the diameter of the housing (2), and at least one heat exchanger (9) immersed in the catalytic layer (10) held in the housing (2), characterized in that it consists of plates as a heat exchanger (9) (14) heat exchanger, cross-sectional dimensions The cross sections of which allow it to be installed in the housing through the nozzle opening (3, 4, 7). 2. Реактор (1) по п.1, отличающийся тем, что в пластинах (14) теплообменника (9) имеются каналы (14а), проходящие параллельно оси корпуса (2) реактора.2. The reactor (1) according to claim 1, characterized in that the plates (14) of the heat exchanger (9) have channels (14a) running parallel to the axis of the reactor vessel (2). 3. Реактор (1) по п.2, отличающийся тем, что пластины (14) теплообменника (9) имеют две примыкающие друг к другу стенки (14’, 14”), образующие расположенные между ними каналы (14а), которые проходят параллельно оси корпуса (2) реактора.3. The reactor (1) according to claim 2, characterized in that the plates (14) of the heat exchanger (9) have two adjacent walls (14 ', 14 ”), forming channels (14a) located between them, which run in parallel axis of the reactor vessel (2). 4. Реактор (1) по п.2, отличающийся тем, что в корпусе (2) установлено множество теплообменников (9), которые соединены с трубой (6), по которой в них подается теплообменная текучая среда.4. The reactor (1) according to claim 2, characterized in that a plurality of heat exchangers (9) are installed in the housing (2), which are connected to a pipe (6) through which a heat-exchange fluid is supplied to them. 5. Реактор (1) по п.2, отличающийся наличием по меньшей мере у одного из теплообменников (9) крепежных устройств (18, 19).5. The reactor (1) according to claim 2, characterized in the presence of at least one of the heat exchangers (9) mounting devices (18, 19). 6. Реактор (1) по п.1, отличающийся тем, что в пластинах (14) теплообменника (9) имеются каналы (14а), которые проходят перпендикулярно оси корпуса (2) реактора.6. The reactor (1) according to claim 1, characterized in that in the plates (14) of the heat exchanger (9) there are channels (14a) that extend perpendicular to the axis of the reactor vessel (2). 7. Реактор (1) по п.6, отличающийся тем, что пластины (14) теплообменника (9) имеют две примыкающие друг к другу стенки (14’, 14”), образующие расположенные между ними каналы (14а), которые проходят перпендикулярно оси корпуса(2) реактора.7. The reactor (1) according to claim 6, characterized in that the plates (14) of the heat exchanger (9) have two adjacent walls (14 ', 14 ”), forming channels (14a) located between them, which extend perpendicularly axis of the reactor vessel (2). 8. Реактор (1) по п.6, отличающийся тем, что в корпусе (2) установлено множество теплообменников (9), которые соединены с трубой (6), по которой в них подается теплообменная текучая среда.8. The reactor (1) according to claim 6, characterized in that a plurality of heat exchangers (9) are installed in the housing (2), which are connected to a pipe (6) through which a heat-exchange fluid is supplied to them. 9. Реактор (1) по п.6, отличающийся тем, что теплообменники (9) расположены в радиальных плоскостях внутри каталитического слоя (10).9. The reactor (1) according to claim 6, characterized in that the heat exchangers (9) are located in radial planes inside the catalytic layer (10). 10. Реактор (1) по п.6, отличающийся наличием по меньшей мере у одного из теплообменников (9) крепежных устройств (18, 19).10. The reactor (1) according to claim 6, characterized in the presence of at least one of the heat exchangers (9) mounting devices (18, 19). 11. Способ изготовления реактора (1), предназначенного для проведения экзотермических или эндотермических гетерогенных реакций, отличающийся тем, что восстанавливают по существу цилиндрический корпус существующего реактора, закрытый на концах соответственно крышкой и днищем, снабженными по меньшей мере одним патрубком, диаметр отверстия которого меньше диаметра корпуса, корпус (2) заполняют по меньшей мере одним каталитическим слоем (10) и в корпус устанавливают погружаемый по меньшей мере в один каталитический слой (10) по меньшей мере один пластинчатый теплообменник (9) по любому из предыдущих пунктов.11. A method of manufacturing a reactor (1) intended for conducting exothermic or endothermic heterogeneous reactions, characterized in that the substantially cylindrical body of the existing reactor is restored, closed at the ends with a lid and a bottom, equipped with at least one nozzle, the opening diameter of which is less than the diameter the housing, the housing (2) is filled with at least one catalytic layer (10) and at least one immersed in at least one catalytic layer (10) is installed in the housing n plate heat exchanger (9) according to any one of the preceding paragraphs. 12. Реактор (1) для проведения экзотермических или эндотермических гетерогенных реакций, имеющий наружный корпус (2) по существу цилиндрической формы и множество теплообменников (9), погруженных в удерживаемый в корпусе (2) каталитический слой (10), отличающийся тем, что в качестве теплообменников (9) используются теплообменники, состоящие из пластин (14), которые имеют по существу форму плоского параллелепипеда и установлены в радиальных плоскостях внутри каталитического слоя (10).12. A reactor (1) for conducting exothermic or endothermic heterogeneous reactions, having an outer casing (2) of a substantially cylindrical shape and a plurality of heat exchangers (9) immersed in a catalytic layer held in the casing (2), characterized in that As heat exchangers (9) heat exchangers are used, consisting of plates (14), which are essentially in the form of a flat parallelepiped and are installed in radial planes inside the catalytic layer (10).
RU2002133093/12A 2000-05-11 2001-05-10 Reactor for realization of the exothermic or endothermic heterogeneous reactions and a method of its production RU2265480C2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP00109968A EP1153653A1 (en) 2000-05-11 2000-05-11 Reactor for exothermic or endothermic heterogeneous reactions
EP00109968.8 2000-05-11

Publications (2)

Publication Number Publication Date
RU2002133093A true RU2002133093A (en) 2004-04-20
RU2265480C2 RU2265480C2 (en) 2005-12-10

Family

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Family Applications (1)

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RU2002133093/12A RU2265480C2 (en) 2000-05-11 2001-05-10 Reactor for realization of the exothermic or endothermic heterogeneous reactions and a method of its production

Country Status (15)

Country Link
US (2) US6982066B2 (en)
EP (4) EP1153653A1 (en)
CN (1) CN1281304C (en)
AR (1) AR033532A1 (en)
AT (1) ATE368511T1 (en)
AU (2) AU6591701A (en)
BR (1) BR0110625B1 (en)
CA (1) CA2407907C (en)
DE (1) DE60129686T2 (en)
DK (1) DK1284813T3 (en)
GC (1) GC0000361A (en)
MX (1) MXPA02011102A (en)
RU (1) RU2265480C2 (en)
UA (1) UA74376C2 (en)
WO (1) WO2001085331A1 (en)

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