FIELD: process engineering.
SUBSTANCE: invention relates to has phase catalytic process equipment to be used in chemical, petrochemical and other industries exploiting gas phase catalytic reactions. Reactor comprises housing, catalyst table, initial components feed branch pipe, reaction products discharge branch pipe, inner housing communicated with reaction products discharge branch pipe. Heat pipe zone is arranged between aforesaid housings and/or inside inner housing, heat pipe ends being located under catalyst table. Space between housings and inner housing are filled with catalyst. Initial components feed branch pipe communicated with reactor inner space. Reaction gases passages are made in inner reactor bottom in catalyst table zone.
EFFECT: possibility for multistage processes in one reactor at various temperatures and with different catalysts.
23 cl, 1 dwg
| Title | Year | Author | Number |
|---|---|---|---|
| CATALYST AND METHOD FOR COMBINED TREATMENT OF LOW-OCTANE HYDROCARBON FRACTIONS AND ALIPHATIC ALCOHOLS AND/OR DIMETHYL EHTER | 2010 |
|
RU2429910C1 |
| METHOD AND DEVICE FOR OBTAINING OF HIGH-OCTANE GASOLINE BY COMBINED PROCESSING OF HYDROCARBON FRACTIONS AND OXYGEN-CONTAINING ORGANIC RAW MATERIAL | 2014 |
|
RU2567534C1 |
| CATALYST AND METHOD OF PRODUCING HIGH-OCTANE GASOLINE WITH LOW CONTENT OF BENZENE AND DURENE | 2010 |
|
RU2440189C1 |
| CONVECTOR FOR GAS-PHASE CATALYTIC PROCESSES | 2009 |
|
RU2417834C1 |
| CONVECTOR FOR GAS PHASE CATALYTIC PROCESSES AND GAS PHASE CATALYTIC PROCESS CONVECTOR THERMAL ELEMENT | 2009 |
|
RU2419485C1 |
| HIGH-OCTANE GASOLINE PRODUCTION PROCESS | 2005 |
|
RU2284343C1 |
| CONVERTER AND ELEMENT OF CONVERTER HEAT PIPE | 2011 |
|
RU2466786C2 |
| METHOD OF CARRYING OUT CATALYTIC ENDOTHERMIC REACTION | 2011 |
|
RU2462502C1 |
| CATALYST AND METHOD FOR AROMATISATION OF C-C GASES, LIGHT HYDROCARBON FRACTIONS OF ALIPHATIC ALCOHOLS, AS WELL AS MIXTURES THEREOF | 2014 |
|
RU2544017C1 |
| REACTOR FOR GAS-PHASE CATALYTIC REACTIONS (VERSIONS) | 2010 |
|
RU2456069C1 |
