CONVERTER SYSTEM WITH MAXIMUM REACTION SPEED FOR EXOTHERMIC REACTIONS Russian patent published in 2010 - IPC C01B3/04 B01J8/06 

Abstract RU 2398733 C2

FIELD: chemistry.

SUBSTANCE: conversion method for ammonia synthesis involves: supply of a gaseous, reagent-rich stream containing a mixture of hydrogen and nitrogen at supply temperature into the heat exchange channel of a heat exchange reaction zone for heating the reagent-rich stream to temperature equal to that at the input, where the heat exchange reaction zone has a shell and tube heat exchanger, the heat exchange channel is an inter-tube channel through the heat exchanger, and the reaction channel has several tubes containing a catalyst, supply of a preheated reagent-rich stream at temperature equal to that at the input into a counterflow reaction channel containing a catalyst for exothermic conversion of the reagent gas into the obtained gas with formation of a product-rich reagent gas and obtained gases mixture, where the reaction channel contains several successive alternating zones containing a catalyst and zones which limit the reaction, indirect transfer of heat from the reaction channel to the heat exchange channel at a rate sufficient for keeping temperature of the mixture of gases below equilibrium temperature, and tapping the output stream rich in ammonia from the output of the reaction channel at outlet temperature. A converter for realising the said method is also proposed.

EFFECT: method and converter enable to control temperature of exothermic reactions on the length of the of the reactor, which enables use of less catalyst volume and increase conversion.

23 cl, 13 dwg, 1 ex

Similar patents RU2398733C2

Title Year Author Number
METHOD FOR OBTAINING DIMETHYL ETHER 2011
  • Juul Dal' Per
  • Shtal' Khenrik Otto
RU2572557C2
AMMONIA SYNTHESIS REACTOR WITH SPLIT-FLOW AND TUBULAR NOZZLE 2015
  • Blokhin Dmitrij Aleksandrovich
RU2608092C2
REACTOR FOR IMPLEMENTATION OF HETEROGENEOUS CATALYTICAL REACTIONS 2007
  • Sergeev Stanislav Petrovich
  • Majdurov Nikolaj Petrovich
  • Krasnushkina Natalija Valer'Evna
  • Nikiforov Faddej Faddeevich
  • Fomenko Aleksej Alekseevich
  • Shustov Vladimir Anatol'Evich
RU2366499C2
0
SU187740A1
REACTOR FOR EXOTHERMIC GASEOUS-PHASE REACTION AND A METHOD TO PERFORM THE EXOTHERMIC GASEOUS-PHASE REACTION 1991
  • Otto Stakhl[Dk]
RU2031702C1
CATALYTIC REACTOR AND METHOD OF REALIZATION OF HIGHLY EXOTHERMIC REACTIONS 1998
  • Kirillov V.A.
  • Kuzin N.A.
  • Shigarov A.B.
  • Danilova M.M.
RU2139135C1
METHOD AND REACTOR FOR PERFORMING NON-ADIABATIC CATALYTIC REACTIONS 2000
  • Tomsen Seren Gide
RU2261756C2
0
SU295319A1
METHOD FOR PRODUCING HYDROGEN-RICH FLOW, METHOD FOR ELECTRIC CURRENT GENERATION, METHOD OF HYDROFINING, DEVICE FOR HYDROGEN-RICH FLOW CREATION 2004
  • Malkhotra Avinash
  • Gosnell Dzhejms Khanlan
RU2343109C2
METHOD FOR EXOTHERMIC AND ENDOTHERMIC CATALYTIC PROCESSES FOR PARTIAL CONVERSION OF HYDROCARBONS AND REACTOR SET THEREFOR 2015
  • Nizamiev Almaz Lutovich
  • Nurullin Rinnat Galeevich
  • Gureev Mikhail Viktorovich
  • Gortyshov Yurij Fedorovich
  • Gureev Viktor Mikhajlovich
  • Nizamiev Lut Burganovich
  • Shvetsov Mikhail Viktorovich
  • Malyshkin Denis Anatolevich
  • Kalachev Ivan Fedorovich
RU2588617C1

RU 2 398 733 C2

Authors

Singkh Shashi P.

Mann Dehvid P.

Pisut Anant

Dates

2010-09-10Published

2005-11-02Filed