SU629955A1 - Gas cleaning and drying absorbent - Google Patents
Gas cleaning and drying absorbentInfo
- Publication number
- SU629955A1 SU629955A1 SU762392348A SU2392348A SU629955A1 SU 629955 A1 SU629955 A1 SU 629955A1 SU 762392348 A SU762392348 A SU 762392348A SU 2392348 A SU2392348 A SU 2392348A SU 629955 A1 SU629955 A1 SU 629955A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- gas cleaning
- absorbent
- minus
- drying
- drying absorbent
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/1493—Selection of liquid materials for use as absorbents
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treating Waste Gases (AREA)
Description
39,75 вес. % N-метилпирролидона, 59,75 вес. % Д ЭТИ ле гликол и 0,5 :зес. % воды. Услови опыта по примеру 1.39.75 weight. % N-methylpyrrolidone, 59,75 weight. % D THIS le glycol and 0.5: hz. % water. The conditions of the experiment in example 1.
Дри температуре абсорбци 40, 20, О и минус 20° С получают еоответствен-но температуры точки росы осушенного газа: минус 14,5, минус 24,9, минус 35, минус 45,7° С.A dry absorption temperature of 40, 20, O and minus 20 ° C is obtained according to the dew point temperature of the dried gas: minus 14.5, minus 24.9, minus 35, minus 45.7 ° C.
Предлагаемый абсорбент при 0° С обеспечивает точку росы осушенного газа в зависимости от содержани диэтиленгликол минус 29 и минус 35° С, в то врем как из:ве спный С0|р|бент - минус 25,9° С. СтепеНь .«олверсии сероводорода .в серу при иасышении абсорбепта двуокисью серы составл ет 99,72%.The proposed absorbent at 0 ° C provides the dew point of the dried gas depending on the content of diethylene glycol minus 29 and minus 35 ° C, while from: a cold C0 | p | bent - minus 25.9 ° C. StepperS. . in sulfur, with absorption of sulfur dioxide absorbed is 99.72%.
Таким образам, иснользо-вание предлагаемого абсорбента позВОл ет повысить степень осушки газа, исключить применение низкокип щи.х добавок к абсорбенту с целью у.меньшени потерь, а также одновременио с осушкой и ОЧИСТКОЙ газа от сероорганических сосдипений, углезодородов Сз-Cg и HoS получать серу.Thus, the use of the proposed absorbent allows to increase the degree of gas drying, to eliminate the use of low-boiling additives to the absorbent to reduce losses, and also to dry and clean the gas from organic sulfur from Cs-Cg and HoS carbon. sulfur.
Ф о р м у л а изобретен и Formula is invented and
Абсорбент дл осуШКИ и очистки газа от кислых примесей и сероорганических соединений на основе N-метилпирролидона, отличающийс тем, что, с целью повышени степени осушки и уменьшени потерь абсорбента, он дополпительно содержит диэтиленгликоль при следуюшем соотnonjewHH комлонентов, вес. %:Absorbent for drying and gas purification from acidic impurities and organic sulfur-based compounds based on N-methylpyrrolidone, characterized in that, in order to increase the degree of drying and reduce the loss of absorbent, it additionally contains diethylene glycol at the next ratio of fresh HH, weight %:
N-Метилпирролидон40-80N-Methylpyrrolidone 40-80
Диэтиленгликоль20-60Diethylene glycol 20-60
ИеточИНки информации, The details of the information,
ирин тые во внимание дри экспертизе:Irritations taken into consideration:
1.Коуль А. Л., Ризснфельд Ф. С. Очистка газа. М., 1968, с. 285-287.1. Cole A. L., Riznfeld F. S. Gas purification. M., 1968, p. 285-287.
2.Патент США .Yg 3324627, ЛЩИ В 01 D 53/00, 1967.2. US Patent .Yg 3324627, BENDING IN 01 D 53/00, 1967.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU762392348A SU629955A1 (en) | 1976-08-01 | 1976-08-01 | Gas cleaning and drying absorbent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU762392348A SU629955A1 (en) | 1976-08-01 | 1976-08-01 | Gas cleaning and drying absorbent |
Publications (1)
Publication Number | Publication Date |
---|---|
SU629955A1 true SU629955A1 (en) | 1978-10-30 |
Family
ID=20672692
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU762392348A SU629955A1 (en) | 1976-08-01 | 1976-08-01 | Gas cleaning and drying absorbent |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU629955A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4479811A (en) * | 1982-01-19 | 1984-10-30 | Veb Chemieanlagenbaukombinat Leipzig-Grimma | Method for the drying and removal of hydrocarbons from gases |
-
1976
- 1976-08-01 SU SU762392348A patent/SU629955A1/en active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4479811A (en) * | 1982-01-19 | 1984-10-30 | Veb Chemieanlagenbaukombinat Leipzig-Grimma | Method for the drying and removal of hydrocarbons from gases |
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