FIELD: catalysts. SUBSTANCE: product - aluminium oxide is regenerated by air supply at first for charge superheater and for the second contacting stage, then in proportion to burning-out of polymeric deposition for the first stage of reactor. Temperature rise in superheater and reactor is limited by supply of low-temperature steam to these position. Process is carried out without deviation and cleaning the charge superheater being worked with high air steam relation and high oxygen concentration in the second stage of reactor. EFFECT: reduced regeneration period and energy consumption, decreased losses of hydrocarbon and secured afterburning of product of incomplete burning in regeneration gases which are blowing-out in atmosphere. 2 cl, 1 dwg
Title | Year | Author | Number |
---|---|---|---|
METHYLPHENYLCARBINOL DEHYDRATION CATALYST REGENERATION METHOD | 1999 |
|
RU2160633C1 |
METHOD FOR REGENERATION OF METHYL PHENYL CARBINOL DEHYDRATION CATALYST | 1999 |
|
RU2161532C1 |
METHOD OF REACTIVATION OF THE ALUMINA CATALYZER DEHYDRATION OF METHYLPHENYLCARBINOL | 2005 |
|
RU2285559C1 |
STYRENE PRODUCTION PROCESS | 1995 |
|
RU2106334C1 |
METHOD OF PRODUCING STYRENE | 2019 |
|
RU2721773C1 |
METHOD FOR ACTIVATING A CATALYST BASED ON GAMMA-ALUMINIUM OXIDE FOR PRODUCING STYRENE | 2021 |
|
RU2760678C1 |
METHOD FOR RECOVERY OF HYDROCARBONACEOUS SOLVENT FROM RECYCLED SOLVENT IN PRODUCTION OF SYNTHETIC RUBBER | 1991 |
|
RU2039756C1 |
METHOD OF ISOLATION OF AROMATIC HYDROCARBONS FROM NONCONDENSED GASES IN STYRENE PRODUCTION | 1991 |
|
RU2024472C1 |
METHOD FOR REGENERATION OF CATALYST USED FOR PRODUCTION OF ISOPRENE FROM 4,4-DIMETHYL-1,3-DIOXAN | 2002 |
|
RU2235592C1 |
METHOD FOR PROCESSING RESIDUAL OF METHYLPHENYLCARBINOL DEHYDRATION INTO STYRENE | 0 |
|
SU1740363A1 |
Authors
Dates
1994-09-15—Published
1991-11-25—Filed