REACTOR FOR CATALYTIC PROCESSES
FIELD: designs of reactors for conducting the catalytic processes, in particular, reforming of gasolines; may be used in petroleum and petrochemical industries. SUBSTANCE: reactor has cylindrical body accommodating coaxially installed perforated tube plugged from one end and connected with its other...
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Main Authors | , , , , , , , |
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Format | Patent |
Language | English |
Published |
20.01.1998
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Edition | 6 |
Subjects | |
Online Access | Get full text |
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Abstract | FIELD: designs of reactors for conducting the catalytic processes, in particular, reforming of gasolines; may be used in petroleum and petrochemical industries. SUBSTANCE: reactor has cylindrical body accommodating coaxially installed perforated tube plugged from one end and connected with its other end to branch pipe. Two-layer troughs are located over generating line of body and forming gap between layers. Gap is plugged at trough end faces. Gap value is determined by expression (0.1-0.2)R, where R is trough radius. Perforation of trough adjacent to catalytic layer occupies 20-40%, and perforation of the second layer is 2-5% of the trough exposed surface. Perforation of the second layer of trough is made symmetrically to area of segments confined by radii from 180 to 90 deg. EFFECT: higher efficiency. 3 cl, 3 dwgv |
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AbstractList | FIELD: designs of reactors for conducting the catalytic processes, in particular, reforming of gasolines; may be used in petroleum and petrochemical industries. SUBSTANCE: reactor has cylindrical body accommodating coaxially installed perforated tube plugged from one end and connected with its other end to branch pipe. Two-layer troughs are located over generating line of body and forming gap between layers. Gap is plugged at trough end faces. Gap value is determined by expression (0.1-0.2)R, where R is trough radius. Perforation of trough adjacent to catalytic layer occupies 20-40%, and perforation of the second layer is 2-5% of the trough exposed surface. Perforation of the second layer of trough is made symmetrically to area of segments confined by radii from 180 to 90 deg. EFFECT: higher efficiency. 3 cl, 3 dwgv |
Author | SAFIN R.JU NABERZHNEV V.V DOLMATOV V.L MINNULLIN M.N NAVALIKHIN P.G SAKHAROV V.D SAJFULLIN N.R KALIMULLIN M.M |
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Notes | Application Number: RU19960113893 |
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Snippet | FIELD: designs of reactors for conducting the catalytic processes, in particular, reforming of gasolines; may be used in petroleum and petrochemical... |
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SubjectTerms | CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY PERFORMING OPERATIONS PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL THEIR RELEVANT APPARATUS TRANSPORTING |
Title | REACTOR FOR CATALYTIC PROCESSES |
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