FIELD: chemistry.
SUBSTANCE: apparatus for carrying out gas-phase catalytic chemical reaction of obtaining HCN contains catalyst/current-collector 1, located coaxially inside reactor 2 and having in essence circular transverse section. Catalyst/current-collector 1 is surrounded by non-electroconducting cylinder. Catalyst/current-collector 1 is inductionally heated by means of alternating magnetic field, generated by surrounding it induction coil 3, to temperature sufficient for carrying out chemical reaction. Intensity of energy release by induction coil 3 is measured along length of cylindrical catalyst/current-collector 1. Apparatus can be additionally equipped with gas-proof cylinder for gas flow in axial direction through catalyst/current-collector 1, or gas-permeable cylinder for gas flow in radial direction through catalyst/current-collector 1.
EFFECT: increase of efficient length of conducting tract in object from metal of platinum group; minimisation of temperature fluctuations in catalyst and minimisation of flow changes in it; reduction of capital investment and production expenditures.
25 cl, 32 ex, 8 dwg, 4 tbl
Title | Year | Author | Number |
---|---|---|---|
METHOD OF INDUCTION INITIATION OF CHEMICAL REACTION | 1998 |
|
RU2193918C2 |
REACTOR FOR PRODUCING HYDROGEN CYANIDE USING ANDRUSSOV'S METHOD | 2008 |
|
RU2470860C2 |
CATALYTIC REACTOR WITH INDUCTION HEATING | 1998 |
|
RU2193917C2 |
METHOD OF PRODUCING HYDROGEN CYANIDE | 2012 |
|
RU2603656C2 |
METHOD OF PRODUCING HYDROGEN CYANIDE THROUGH CATALYTIC OXIDATION IN AMMONIA MEDIUM | 2008 |
|
RU2454277C2 |
METHOD FOR CONVERSION OF AMMONIA | 1990 |
|
RU2033835C1 |
THREE-DIMENSIONAL NETWORK FOR CATALYTIC REACTIONS | 1995 |
|
RU2095135C1 |
AMMONIA CONVERSION METHOD | 1997 |
|
RU2119889C1 |
PLATINOID TRAP FOR GAS MIX | 2008 |
|
RU2392048C2 |
METHOD FOR OXIDISING AMMONIA AND SYSTEM SUITABLE THEREFOR | 2014 |
|
RU2646643C2 |
Authors
Dates
2008-11-27—Published
2003-03-11—Filed