[go: up one dir, main page]

SU642585A1 - Method of low-temperature scrubbing of gas from moisture and carbon dioxide - Google Patents

Method of low-temperature scrubbing of gas from moisture and carbon dioxide

Info

Publication number
SU642585A1
SU642585A1 SU772509767A SU2509767A SU642585A1 SU 642585 A1 SU642585 A1 SU 642585A1 SU 772509767 A SU772509767 A SU 772509767A SU 2509767 A SU2509767 A SU 2509767A SU 642585 A1 SU642585 A1 SU 642585A1
Authority
SU
USSR - Soviet Union
Prior art keywords
gas
carbon dioxide
low
moisture
temperature
Prior art date
Application number
SU772509767A
Other languages
Russian (ru)
Inventor
Борис Тимофеевич Маринюк
Иван Петрович Усюкин
Игорь Анатольевич Яковлев
Михаил Иванович Дьячков
Юрий Николаевич Петров
Николай Павлович Берсенев
Original Assignee
Московский Ордена Трудового Красного Знамени Институт Химического Машиностроения
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Московский Ордена Трудового Красного Знамени Институт Химического Машиностроения filed Critical Московский Ордена Трудового Красного Знамени Институт Химического Машиностроения
Priority to SU772509767A priority Critical patent/SU642585A1/en
Application granted granted Critical
Publication of SU642585A1 publication Critical patent/SU642585A1/en

Links

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

(54) СПОСОБ НИЗКСТЕМПЕРАТУРНОЙ ОЧИСТКИ ГАЗОВ ОТ ВЛАГИ И УГЛЕКИСЛОТЫ(54) METHOD FOR LOW-TEMPERATURE PURIFICATION OF GASES FROM MOISTURE AND CARBON

жидкую сус тензию фильтруют дл  QTделени  твердой фазы из жидкого холодильного агента. Холодильный еигент возвращаю на вход теплообменника в-газообразном или жидком виде.the liquid slurry is filtered to QT separate the solid phase from the liquid refrigerant. Refrigerant is returned to the inlet of the heat exchanger in gaseous or liquid form.

Технико- экономическа  эффективность от применени  предлагаемого способа состоит в том, что процесс очистки мож о вести непрерывно в течение неограниченного периода времени в одном аппарате . Кроме того, этот способ позвол ет совместить системы очистки и теплообмена в окном аппарате, причём глубина охлаждени  ограничена исключительно температурой затвердевани  вспомогательного холодильного агента, Формула .изобретени Technical and economic efficiency from the application of the proposed method consists in the fact that the cleaning process can be carried out continuously for an unlimited period of time in one apparatus. In addition, this method makes it possible to combine cleaning and heat exchange systems in a window of the apparatus, and the cooling depth is limited solely by the solidification temperature of the auxiliary refrigerant, the Invention Formula

Оюсоб низкотемпературной очистки газов от вЛаги и углекислоты путем охлаждени  скоростного потока загр зненного газа до температуры конденсации и замерзани  примесей, о т л и ч а ющ и и с   тем, что, с целью обеспечени  непрерывной очистки, в поток газа ввод т газообразный холодильный агент с температурой конденсации выше О С и температурой затвердевани  ниже температуры затвердевани  углекислоты пр данном давлении и конденсируют его с образованием пленки и суспензии, которую отдел ют от воздуха, фильтруют, а чистый холодильный агент направл ют на рециркул цию.Discharge of low-temperature gas cleaning from lags and carbon dioxide by cooling the high-speed flow of contaminated gas to the temperature of condensation and freezing of impurities, so that with a view to ensure continuous cleaning, a gaseous refrigerant is introduced into the gas flow with a condensation temperature above 0 C and a solidification temperature below the solidification temperature of carbon dioxide, at a given pressure and condense it to form a film and suspension, which is separated from the air, filtered, and the clean refrigerant apravl was recirculated.

Источники информации, прин тые во ;внимание при экспертизе:Sources of information taken into consideration; during examination:

1, Патент Англии } 917286, кл, 8 (2) F, 1963,1, Patent of England} 917286, class, 8 (2) F, 1963,

SU772509767A 1977-07-11 1977-07-11 Method of low-temperature scrubbing of gas from moisture and carbon dioxide SU642585A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU772509767A SU642585A1 (en) 1977-07-11 1977-07-11 Method of low-temperature scrubbing of gas from moisture and carbon dioxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU772509767A SU642585A1 (en) 1977-07-11 1977-07-11 Method of low-temperature scrubbing of gas from moisture and carbon dioxide

Publications (1)

Publication Number Publication Date
SU642585A1 true SU642585A1 (en) 1979-01-15

Family

ID=20718891

Family Applications (1)

Application Number Title Priority Date Filing Date
SU772509767A SU642585A1 (en) 1977-07-11 1977-07-11 Method of low-temperature scrubbing of gas from moisture and carbon dioxide

Country Status (1)

Country Link
SU (1) SU642585A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2718943C2 (en) * 2015-12-03 2020-04-15 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Method of liquefying stream of contaminated co2 containing hydrocarbons

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2718943C2 (en) * 2015-12-03 2020-04-15 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Method of liquefying stream of contaminated co2 containing hydrocarbons

Similar Documents

Publication Publication Date Title
RU94042251A (en) Process of removal of elementary sulphur present in gas
DK160084C (en) METHOD AND APPARATUS FOR WASTE CLEANING
CN110180317A (en) System and method that is a kind of while removing carbon dioxide in flue gas and sulfur dioxide
ATE228637T1 (en) METHOD AND DEVICE FOR THE LOW TEMPERATURE SEPARATION OF AIR
US6257018B1 (en) PFC recovery using condensation
ATE258819T1 (en) METHOD AND DEVICE FOR PURIFYING GASES USING HEAT EXCHANGERS
SU642585A1 (en) Method of low-temperature scrubbing of gas from moisture and carbon dioxide
SU1006378A1 (en) Gas hydrate desalination plant
KR880001511B1 (en) Air separation process with turbine exhaust desuper heat
US3793806A (en) Low temperature removal of mercury from gas streams
US2842941A (en) Method for purification of carbon dioxide
US3275403A (en) Removal of carbon dioxide and hydrogen sulfide from gaseous mixtures
US5122358A (en) Process for the purification of exhaust gases
CN210544174U (en) System for simultaneously removing carbon dioxide and sulfur dioxide in flue gas
US3994691A (en) Apparatus for the recovery of sulphuric acid from industrial waste gases
SU851036A1 (en) Air separation method
SU1537986A1 (en) Heating/refrigerating unit
JPS56100603A (en) Method and apparatus for recovery of hydrocarbon in gas
GB1114947A (en) Process and apparatus for drying and/or purifying gases
SU925938A1 (en) Process for producing urea
SU908836A1 (en) Apparatus for utilizing gases
SU947039A1 (en) Apparatus for producing yellow phosphorus
SU830087A1 (en) Method of condensation of moisture in gas flow
SU65386A1 (en) The method of purification of coke oven gas from nitrogen oxides
RU2100056C1 (en) Method of trapping nitrogen oxides