FIELD: chemical and petrochemical industries. SUBSTANCE: natural gas is processed under pressure by steam-oxygen or steam-air conversion of carbons to produce methanol, higher alcohols, and ammonia which involves catalytic steam pre-conversion of raw carbon in adiabatic reactor, decomposition of gas mixture obtained at steam conversion stage in tubular converter followed by secondary decomposition at oxygen stage in shaft reactor; specific area of heat-transfer surface in tubular converter is found from equation given in description of invention so as to maintain desired temperature conditions. Temperature of gas mixture obtained as result of oxygen conversion at outlet from intertube space is maintained between 600 and 670 c and that of source steam-carbon mixture at adiabatic reactor inlet, between 580 and 650 C. This increases service life of reaction tubes by three or four times. EFFECT: improved service life of reaction tubes. 2 cl, 1 dwg
Title | Year | Author | Number |
---|---|---|---|
CONVERTER FOR CATALYTIC CONVERSION OF HYDROCARBONS | 1997 |
|
RU2124938C1 |
METHOD OF HYDROGEN-CONTAINING GAS PRODUCTION | 0 |
|
SU1770266A1 |
METHOD OF PREPARING METHANOL | 1997 |
|
RU2117627C1 |
PROCESSING OF NATURAL GAS TO PRODUCE METHANOL | 1998 |
|
RU2135454C1 |
CONVERTER FOR TWO-STAGE CATALYTIC CONVERSION OF HYDROCARBONS | 1998 |
|
RU2131765C1 |
METHOD FOR OBTAINING AMMONIA | 2022 |
|
RU2796561C1 |
DEVICE FOR HYDROGEN GENERATION | 1998 |
|
RU2124928C1 |
METHOD OF HYDROGEN-CONTAINING GAS PRODUCTION | 0 |
|
SU1770264A1 |
METHOD OF AMMONIA PRODUCTION | 0 |
|
SU1770277A1 |
METHOD FOR PRODUCTION OF METHANOL | 1995 |
|
RU2099320C1 |
Authors
Dates
1999-12-10—Published
1999-03-15—Filed