FIELD: coke industry. SUBSTANCE: in order to remove tar and naphthalene particles, coke gas is cooled in cooler to 20-35 C and treated in Venturi scrubber with absorption oil, which is fed in amount 0.3-0.5 kg/cu.m through nozzles at flow rate 10-25 m/s. Gas velocity in Venturi scrubber neck is maintained between 20 and 45 m/s. EFFECT: reduced investment and operation expenses. 2 cl, 1 tbl
Title | Year | Author | Number |
---|---|---|---|
METHOD OF TREATING COKE-OVEN GAS | 0 |
|
SU1824423A1 |
METHOD OF CLEANING COKING GAS FROM HYDROGEN SULFIDE | 0 |
|
SU1717619A1 |
METHOD OF COOLING AND PURIFYING COKE GAS FROM NAPTHALENE | 0 |
|
SU857239A1 |
METHOD OF TREATING COKE GAS TO RECOVER BENZENE HYDROCARBONS AND NAPHTHALENE | 2003 |
|
RU2257946C1 |
METHOD OF COOLING COKE GAS AND REMOVING NAPHTHALENE FROM THE LATTER | 0 |
|
SU1244169A1 |
METHOD FOR PURIFYING COKING GAS FROM HYDROGEN SULFIDE | 0 |
|
SU1135750A1 |
METHOD OF REMOVING BENZOL HYDROCARBONS AND NAPHTHALENE | 0 |
|
SU1357425A1 |
METHOD OF PURIFYING COKE GAS FROM HYDROGEN SULFIDE | 0 |
|
SU1333698A1 |
METHOD OF CLEANING COKE-OVEN GAS | 0 |
|
SU1263707A1 |
METHOD OF COKE GAS HYDROGEN SULFIDE ABSORPTION AUTOMATIC CONTROL | 1990 |
|
RU2023485C1 |
Authors
Dates
1999-07-10—Published
1994-10-05—Filed