FIELD: engines and pumps.
SUBSTANCE: reactor is intended for chemical reactions in three-phase sludge system, features free zone above sludge zone, and diametre making at least 0.5 m, preferably, 1 m, more preferably, over 2 m, and height making at least 5 m, preferably at least 10 m. Proposed reactor comprises gas feed appliances arranged nearby reactor housing base, gas discharge appliances arranged nearby reactor housing top part, fluid discharge appliances and multiple vertical pipes in the sludge zone. Pipes diametre varies from 1 cm to 200 cm, their full girth varies from 1400 to 4000 cm/m2.
EFFECT: sufficient amount of vertical pipes in reactor housing suppresses formation of gas flows through fluid and circular motions in sludge, thus preventing large-scale return mixing of gas and fluid phases.
12 cl, 3 dwg, 1 ex
| Title | Year | Author | Number |
|---|---|---|---|
| GAS DISTRIBUTOR FOR REACTOR | 2005 |
|
RU2365407C2 |
| CATALYST STRUCTURE | 2005 |
|
RU2381062C2 |
| FILTERING SYSTEM WITH FILTERING DEVICE THAT RETRACTS IN JACKET | 2005 |
|
RU2363532C2 |
| METHOD AND DEVICE FOR FUNCTIONING OF BUBBLE REACTION COLUMN WITH THREE-PHASE REACTION METHOD FOR FISHER- TROPSCH SYNTHESIS | 1997 |
|
RU2189857C2 |
| REACTOR WITH AIR-FLUIDISED BED, THREE-PHASE REACTOR AND PROCEDURES FACILITATING THEIR OPERATIONS (VERSIONS) | 2006 |
|
RU2391132C2 |
| METHOD FOR PROVISION OF THREE-PHASE SLURRY REACTOR FUNCTIONING | 2006 |
|
RU2380150C2 |
| METHOD OF CONTINUOUSLY CONDUCTING MULTIPHASE CATALYTIC CONVERSION REACTION | 1993 |
|
RU2108146C1 |
| CATALYST SYSTEMS USED IN FISCHER-TROPSCH SYNTHESIS AND USE THEREOF | 2006 |
|
RU2412926C2 |
| METHOD OF PREPARING LIQUID AND OPTIONALLY GAS PRODUCTS FROM GASEOUS REACTANTS | 1998 |
|
RU2201800C2 |
| FISCHER-TROPSCH PROCESS WITH MULTI-STAGE COLUMN-TYPE BUBBLE REACTOR | 1997 |
|
RU2178443C2 |
