FIELD: oil and gas industry.
SUBSTANCE: reactor contains a vertical cylindrical body (1), inlet tubes (11) and circulating catalyst outlet tubes (10), raw material feed lines (8) and a contact gas tube (16), a raw material vapor distributor (2) at the bottom of the housing (1), grids (3) with a free-flowing section that increases along the reactor's height, separating the fluidized layer zone into sections (4) and the contact gas purification cyclones (5) from the catalyst dust in the upper part of the housing (1) with the dust descent risers (13) equipped with valves (14) for returning the trapped catalyst to the fluidized layer. At the same time, tubes (7), (6) are installed along the height of the housing (1), connected to devices for measuring temperature and pressure differences respectively, nipples (7), (6) are installed in groups with tubes (7), (6) in horizontal plane. At that, the groups are set according to the height of the housing (1) in such a way that the group of lower tubes(7), (6) is located at or above the raw material vapor distributor (2), and the upper tube group (7), (6) is at or below the inlet of the contact gas into the cyclones (5). Simultaneously, in the fluidized catalyst layer, the groups of tubes (7), (6) are installed above and below the lower grids (3), and between these grids one or more groups of tubes (7), (6) are installed. One or more grids (3) are located between said groups of tubes (7), (6). A method for diagnosing reactor failures is also provided, wherein temperature and pressure differences are measured between the tubes groups (7), (6) in the fluidized layer sections (4) and the amount of catalyst in the sections is determined.
EFFECT: increase of dehydrogenation indicators, decrease of catalyst offsetting from the reactor.
31 cl, 6 dwg
Title | Year | Author | Number |
---|---|---|---|
REACTOR FOR DEHYDROGENATION OF PARAFFIN HYDROCARBONS C-C | 2015 |
|
RU2601002C1 |
REACTOR FOR DEHYDROGENATION OF C-C PARAFFIN HYDROCARBONS | 1999 |
|
RU2156161C1 |
REACTOR FOR DEHYDROGENATION OF PARAFFINIC HYDROCARBONS C-C | 2005 |
|
RU2301107C1 |
DISTRIBUTOR CATALYST AND TRANSPORT GAS FOR THE REACTOR - RECLAIMER SYSTEM OF THE C-C PARAFFIN HYDROCARBON DEHYDROGENATION PLANTS WITH THE FLUIDIZED BED | 2017 |
|
RU2652195C1 |
DISTRIBUTOR OF THE CATALYST FOR THE REACTOR-RECLAIMER SYSTEM OF C-C PARAFFIN HYDROCARBON DEHYDRATION OF WITH FLUIDIZED BED | 2017 |
|
RU2652198C1 |
PLANT FOR DEHYDROGENATION OF PARAFFINS OR ISOPARAFFINS C-C IN CHROMIA-ALUMINA CATALYST FLUIDISED BED | 2015 |
|
RU2591159C1 |
REACTOR SYSTEM FOR CHEMICAL PROCESSES IN THE FLUIDIZED BED OF THE CATALYST | 2021 |
|
RU2773697C1 |
METHOD FOR REGENERATION OF CHROMIUM ALUMINA CATALYST AND REGENERATOR FOR ITS IMPLEMENTATION | 2020 |
|
RU2746425C1 |
PLANT FOR DEHYDROGENATION OF PARAFFIN HYDROCARBONS C-C | 1998 |
|
RU2129111C1 |
DEVICE FOR PREPARATION OF CATALYST IN PROCESSES OF DEHYDROGENATION OF PARAFFIN HYDROCARBONS C-C | 2019 |
|
RU2719490C1 |
Authors
Dates
2017-07-19—Published
2016-06-09—Filed