FIELD: oil refining. SUBSTANCE: stable gas condensate is heated and delivered for rectification at a pressure of 2-3 kg/cm2, a temperature at the top of 160-170 C and a temperature of the column still of 250-260 C. The resulting fraction of hydrocarbon with a boiling temperature of 250-260 C is taken out from the distilling part of the column in the amount of 2-20 wt. -% and delivered for absorption at 145-155 C. The liquid hydrocarbon fraction is produced by cooling the vapor product from rectification stage to 150-160 C and using it as absorbent at a weight ratio of hydrocarbon fraction to absorbents of (1.3-3.0) to 1. The fraction of vapor-liquid mixture in the column is divided into two flows in a weight relation of 1 to 4-20. The smaller flow is delivered for absorption while the larger one is used for refluxing at the rectification stage. Absorption is carried out at a pressure of 1-1,8 kg/сm2. EFFECT: higher efficiency. 9 cl, 1 dwg, 1 tbl
Title | Year | Author | Number |
---|---|---|---|
METHOD OF PRODUCTION OF MOTOR FUELS FROM GAS CONDENSATE | 1992 |
|
RU2030446C1 |
METHOD OF PRODUCING MOTOR FUEL | 1992 |
|
RU2010836C1 |
METHOD FOR PREPARING LINEAR PRIMARY MONOALCOHOLS | 2002 |
|
RU2291848C2 |
METHOD OF PROCESSING LIQUID PYROLYSIS PRODUCTS INTO AROMATIC HYDROCARBONS | 2004 |
|
RU2266944C1 |
PLANT AND METHOD FOR PRODUCING HIGH-OCTANE NUMBER GASOLINE FRACTIONS AND AROMATIC HYDROCARBONS (OPTIONS) | 1994 |
|
RU2069227C1 |
METHOD OF PRODUCING HIGH-OCTANE GASOLINE FRACTIONS AND AROMATIC HYDROCARBONS | 2019 |
|
RU2708071C1 |
METHOD OF PRODUCING HIGH-OCTANE GASOLINE FRACTIONS AND AROMATIC HYDROCARBONS | 2019 |
|
RU2708620C1 |
METHOD FOR HYDROFORMYLATION OF OLEFINS C6-C9 IN ALCOHOLS C7-C10 | 2015 |
|
RU2602239C1 |
METHOD FOR TREATMENT AND UTILIZATION OF LIGHT PYROLYSIS RESIN | 2005 |
|
RU2278143C1 |
METHOD FOR PROCESSING OF LIGHT HYDROCARBON MATERIALS | 1992 |
|
RU2041918C1 |
Authors
Dates
1995-03-10—Published
1991-09-30—Filed