FIELD: chemistry.
SUBSTANCE: fluidised medium 22, preferably gas, is fed into the bottom part of a reactor 24 and goes to the upper part of the reactor 20, such that the fluidised medium 22 moves in the vertical fluidisation direction 26. Solid particles 28 in the fluidised layer 30 move in the horizontal direction 32 of transfer of solid particles from the inlet 34 of solid particles in the horizontal position upstream to the outlet 36 of solid particles in the horizontal position downstream. Solid particles 28 are collected in the collector 38 of solid particles, which is connected to the outlet 36 of solid particles.
EFFECT: increased carrying capacity of solid particles, reduced loss of unreacted product and improved economic characteristics.
52 cl, 1 tbl, 2 dwg, 1 ex
| Title | Year | Author | Number |
|---|---|---|---|
| COKING IN A FLUIDIZED BED TO OBTAIN FUEL GAS | 2015 |
|
RU2688547C2 |
| DESULPHURISATION IN REACTOR WITH TURBULENT FLUIDISATED LAYER | 2006 |
|
RU2384361C2 |
| METHOD OF CATALYTIC HYDROPYROLYSIS WITH BUBBLED LAYER USING LARGE PARTICLES OF CATALYST AND FINE PARTICLES OF BIOMASS CHARACTERIZING REACTOR WITH "ANTI-BRIDGING" | 2012 |
|
RU2643810C1 |
| CONTROLLING SULPHUR LEVEL BY PROPANE DEHYDROGENATION | 2014 |
|
RU2682670C1 |
| METHOD OF CONVERTING STREAM OF MATERIAL CONTAINING OXYGENATE | 2006 |
|
RU2387630C2 |
| METHOD OF FLUIDIZED-BED COKING | 1997 |
|
RU2186822C2 |
| BUBBLING BED CATALYTIC HYDROPYROLYSIS PROCESS UTILISING LARGER CATALYST PARTICLES AND SMALLER BIOMASS PARTICLES FEATURING ANTI-SLUGGING REACTOR | 2012 |
|
RU2611631C2 |
| FLUID INJECTION NOZZLE FOR FLUID BED REACTORS | 2015 |
|
RU2680484C2 |
| REACTOR FOR PROCESSING CHLORO-ORGANIC COMPOUND | 2001 |
|
RU2181072C1 |
| FLUID BED COKING PROCESS WITH DECOUPLED COKING ZONE AND STRIPPING ZONE | 2014 |
|
RU2664803C2 |
