SU364337A1 - METHOD FOR PROCESSING INDUSTRIAL GASES - Google Patents

METHOD FOR PROCESSING INDUSTRIAL GASES

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Publication number
SU364337A1
SU364337A1 SU1482756A SU1482756A SU364337A1 SU 364337 A1 SU364337 A1 SU 364337A1 SU 1482756 A SU1482756 A SU 1482756A SU 1482756 A SU1482756 A SU 1482756A SU 364337 A1 SU364337 A1 SU 364337A1
Authority
SU
USSR - Soviet Union
Prior art keywords
gases
industrial gases
processing industrial
gas
oxygen
Prior art date
Application number
SU1482756A
Other languages
Russian (ru)
Inventor
С. Г. Солюс Г. Д. Конюх
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 filed Critical
Priority to SU1482756A priority Critical patent/SU364337A1/en
Application granted granted Critical
Publication of SU364337A1 publication Critical patent/SU364337A1/en

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  • Treating Waste Gases (AREA)

Description

Изобретение относитс  к химической технологии , в частности к обработке промышленных газов.This invention relates to chemical technology, in particular to the treatment of industrial gases.

Известные способы обработки промышленных газов, например выход ш,их газов предпри тии , путем непосредственпого сжпганн  газа с подачей теплоносител  не обеспечивают необходимой эффективности и получени  азота и ипертиых газов.The known methods of treating industrial gases, for example, the output of gas and their gases by an enterprise, by directly squeezing gas with a coolant supply, do not provide the necessary efficiency and the production of nitrogen and second gases.

С целью устранени  указанных недостатков по предлагаемому способу производ т выжигание окиси углерода и кислорода прн темнературе 500-700°С с последуюш,им извлечением из газа углекислоты и его осушкой.In order to eliminate the above disadvantages of the proposed method, carbon monoxide and oxygen are burned at a temperature of 500-700 ° C with subsequent extraction of carbon dioxide from the gas and drying it.

Иутем дожигани  окиси углерода и кислорода , извлечени  механических примесей, а также ЗОз и НоО можио получить требуемый инертный газ или азот.By the post-combustion of carbon monoxide and oxygen, the extraction of mechanical impurities, as well as of the POF and Ho, it is possible to obtain the required inert gas or nitrogen.

Промышленные газы содовых нроизводств или известково-обжигательиых печей имеют примерно следуюпдий химический состав в %: Содовое производство Производство известиIndustrial gases of soda production or lime kilns have about the following chemical composition in%: Soda production Lime production

АзотNitrogen

62,5 62.5

93,5 26,5 4,2 1,0 1,193.5 26.5 4.2 1.0 1.1

Углекислый газ Окись углерода 4,55Carbon Dioxide Carbon Monoxide 4.55

3 - Кислород , 003 - Oxygen, 00

Выжигание кислорода и окиси углерода ведетс  ;в аппаратах полото типа, футерованных ша.мотом или другим огнеупорным материалом , с насадкой из кирпича, железной «ли медной стружки, или без насадки пр/, температуре 700°С.The burning of oxygen and carbon monoxide is carried out; in apparatus of a hollow type, lined with a shaft or other refractory material, with a nozzle made of brick, iron or copper shavings, or without nozzle pr /, a temperature of 700 ° C.

Механические прнмеси и SO извлекаютс  обычпыми способами путем промывки водой в полых скрубберах. Осушка от влаги ведетс  в аппаратах с иасадкой из силикагел  или других влагоу,1авл 1ваюш,их продуктов, отход идее тепло регенерируетс  в противотоке п o6bi4iioi i аппаратуре.Mechanical mixtures and SO are extracted by conventional methods by rinsing with water in hollow scrubbers. Moisture drying is carried out in apparatuses with silica gel or other moisture showers, 1st person, their products, waste, the idea of heat is regenerated in countercurrent n o6bi4iioii equipment.

Дл  запуска ттановки, а также дл  выравнивани  колебаний но содержанию в отход ших газах окиси углерода и кислорода к аппарату автоматически подвод тс  горючий гдэ и .In order to start the installation, as well as to equalize the fluctuations, the content of carbon monoxide and oxygen in the exhaust gases is automatically supplied to the apparatus with combustible gas.

П р е д .м е 1 изобретени PREd. M e 1 invention

Способ обработки промышлеппых газон, папрпмер выход ш,пх газов предпри тий, нуте .м непосредствепного сжигани  газа с подачей теплоносптел , отличающийс  тем, что, с целью повышепп  эффективности способа li обеспечени  получени  азота н инертных газов , пронзвод т выжигание окиси углерода и кислорода при температуре 500-700 С с последуюпдим 1 3влечепием из газа углекислоты н его осхшкой.The method of treating industrial lawn, paprpmer exit w, fx gases of enterprises, chickens with direct combustion of gas with supply of heat-spraying, characterized in that, in order to improve the efficiency of the process of providing nitrogen and inert gases, the burning of carbon monoxide and oxygen is carried out temperature of 500–700 ° C, followed by 1–3 impurity from carbon dioxide gas and its osshshkoy.

SU1482756A 1970-10-08 1970-10-08 METHOD FOR PROCESSING INDUSTRIAL GASES SU364337A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU1482756A SU364337A1 (en) 1970-10-08 1970-10-08 METHOD FOR PROCESSING INDUSTRIAL GASES

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU1482756A SU364337A1 (en) 1970-10-08 1970-10-08 METHOD FOR PROCESSING INDUSTRIAL GASES

Publications (1)

Publication Number Publication Date
SU364337A1 true SU364337A1 (en) 1972-12-28

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
SU1482756A SU364337A1 (en) 1970-10-08 1970-10-08 METHOD FOR PROCESSING INDUSTRIAL GASES

Country Status (1)

Country Link
SU (1) SU364337A1 (en)

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