SU767024A1 - Method of waste gas purification from ammonia - Google Patents
Method of waste gas purification from ammonia Download PDFInfo
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- SU767024A1 SU767024A1 SU742020386A SU2020386A SU767024A1 SU 767024 A1 SU767024 A1 SU 767024A1 SU 742020386 A SU742020386 A SU 742020386A SU 2020386 A SU2020386 A SU 2020386A SU 767024 A1 SU767024 A1 SU 767024A1
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- USSR - Soviet Union
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- ammonia
- gas
- waste gas
- gas purification
- coke
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- Treating Waste Gases (AREA)
Description
(54) СПОСОБ ОЧИСТКИ КОКСОВОГО ГАЗА ОТ АММИАКА(54) METHOD FOR CLEANING COKE GAS FROM AMMONIA
1one
Известен способ очистки коксового газа от аммиака путем косвенного нагрева в камерах, где пары аммиака нагревают до 1000°С и обо-; грев йедут топочными газами, сжигаемыми в специальных каналах. Продукты разложени не содержат окислов азота 1 .A known method of cleaning coke oven gas from ammonia by indirect heating in chambers, where ammonia vapors are heated to 1000 ° C and both; They are heated by flue gases burned in special channels. The decomposition products do not contain nitrogen oxides 1.
Недостатком известного способа вл ютс высокие -затраты тепла из-за потерь при теплопередаче через стенку.The disadvantage of this method is the high heat consumption due to heat transfer losses through the wall.
. Наиболее близким по технической сущности Q .и достигаемому результату вл етс способ очиртки коксового газа от аммиак;а пиролизом аммиака путем контактировани коксового газа с высокотемпературным газовым потоком горени топлива 2.15. The closest in technical essence Q. and the achieved result is a method of cleaning coke gas from ammonia, and ammonia pyrolysis by contacting coke gas with a high-temperature gas stream of fuel combustion 2.15
Недостатком известного способа вл етс наличие вредных примесей в отход ншх газах.The disadvantage of this method is the presence of harmful impurities in the waste gases.
Целью изобретени вл етс устранение содержани вредных примесей в отход щих газах.The aim of the invention is to eliminate the content of harmful impurities in the exhaust gases.
Поставленна цель достигаетс тем, что в 20 предлагаемом способе очистки коксового гай от аммиака пиролизом аммиака путем контактировани коксового газа с высокотемпературным газовым потоком горени топлива, коксовый газ, содержащий аммиак, контактирует с газовым потоком при 950-1100°С вне камеры говрни топлива.The goal is achieved by the fact that in 20 of the proposed method of purifying a coke oven from ammonia by ammonia pyrolysis by contacting coke oven gas with a high-temperature gas stream of burning fuel, the coke oven gas containing ammonia is in contact with the gas stream at 950-1100 ° C outside the chamber.
П р и м е р. В камеру горени подают npj родныи газ 0,45 м/ч с воздухом (козффициент избытка воздуха 1,1); в газах, выход щи: из топочного устройства, содержание окислов азота - 0,2 т/нм. В газы - продукты горени (температура 1000° С) - подают вне камеры горени аммиак в количестве 10 г/ч. Содержание окислов азота в выход щих газах - 0,2 г/нм, содержание аммиака - следыPRI me R. Npj native gas of 0.45 m / h with air is supplied to the combustion chamber (an air excess factor of 1.1); in gases, escaping: from the furnace device, the content of nitrogen oxides is 0.2 t / nm. To the gases — products of combustion (temperature 1000 ° C) —– ammonia is supplied in the amount of 10 g / h outside the combustion chamber. The content of nitrogen oxides in the exhaust gases is 0.2 g / nm, the content of ammonia is traces
Использование предлагаемого способа терми ческого разложени аммиака по .сравнению с известным способом обеспечивает снижение содержани окислов азота при очистке отход щи газов, что позвол ет снизить расходы на устано ку оборудовани дл очистки газов.The use of the proposed method of thermal decomposition of ammonia in comparison with a known method provides a reduction in the content of nitrogen oxides during the purification of waste gases, which reduces the cost of installation of equipment for the purification of gases.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU742020386A SU767024A1 (en) | 1974-04-30 | 1974-04-30 | Method of waste gas purification from ammonia |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU742020386A SU767024A1 (en) | 1974-04-30 | 1974-04-30 | Method of waste gas purification from ammonia |
Publications (1)
Publication Number | Publication Date |
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SU767024A1 true SU767024A1 (en) | 1980-09-30 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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SU742020386A SU767024A1 (en) | 1974-04-30 | 1974-04-30 | Method of waste gas purification from ammonia |
Country Status (1)
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SU (1) | SU767024A1 (en) |
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1974
- 1974-04-30 SU SU742020386A patent/SU767024A1/en active
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