FIELD: chemical equipment.
SUBSTANCE: reactor is used for performing of non-adiabatic process. Reactor has at least one heat-transfer wall in form of tube. According to the invention, tube is made with constant external diameter of tube's wall and with internal diameter of wall being bigger in first section of tube than internal diameter of wall of tube in the second section along direction of flow of non-adiabatic reaction medium. Heat can be produced or it can be absorbed as a result of non-adiabatic process. Non-adiabatic reaction can be reforming with water vapor. Heat-transfer wall limits catalyst layer. Catalyst layer can be presented in fixed form.
EFFECT: improved characteristics of heat flow; prolonged service life.
5 cl, 3 dwg
| Title | Year | Author | Number |
|---|---|---|---|
| METHOD AND REACTOR FOR PERFORMING NON-ADIABATIC CATALYTIC REACTIONS | 2000 |
|
RU2261756C2 |
| PRODUCTION OF A SYNTHESIS GAS BY THE VAPOR REFORMING WITH USE OF THE CATALYZED EQUIPMENT | 1999 |
|
RU2220901C2 |
| SYNTHETIC GAS REGENERATION METHOD AND DEVICE | 2003 |
|
RU2354607C2 |
| SYNTHETIC GAS REGENERATION PROCESS AND DEVICE | 2003 |
|
RU2354608C2 |
| CATALYST TUBE FOR REFORMING | 2017 |
|
RU2750041C2 |
| COMPACT REFORMING REACTOR | 2006 |
|
RU2415073C2 |
| METHOD OF TWO-STAGE CATALYTIC CONVERSION OF HYDROCARBON RAW MATERIAL | 0 |
|
SU784148A1 |
| PLANT FOR PERFORMING ENDOTHERMIC AND EXOTHERMIC REACTIONS AND REFORMING UNIT | 1997 |
|
RU2185879C2 |
| CATALYTIC REACTOR | 2008 |
|
RU2371243C1 |
| METHOD OF OBTAINING SYNTHESIS-GAS | 2003 |
|
RU2342318C2 |
