SU480642A1 - The method of automatic control of the process of cleaning tail gas from nitrogen oxides - Google Patents

The method of automatic control of the process of cleaning tail gas from nitrogen oxides

Info

Publication number
SU480642A1
SU480642A1 SU1968334A SU1968334A SU480642A1 SU 480642 A1 SU480642 A1 SU 480642A1 SU 1968334 A SU1968334 A SU 1968334A SU 1968334 A SU1968334 A SU 1968334A SU 480642 A1 SU480642 A1 SU 480642A1
Authority
SU
USSR - Soviet Union
Prior art keywords
nitrogen oxides
tail gas
automatic control
cleaning tail
reactor
Prior art date
Application number
SU1968334A
Other languages
Russian (ru)
Inventor
Дмитрий Григорьевич Подошвин
Владимир Антонович Демкович
Гарий Владимирович Болтянский
Павел Александрович Егоров
Сергей Петрович Савичев
Владимир Михайлович Гурьев
Борис Федорович Егоров
Original Assignee
Ленинградское Специализированное Пусконаладочное Управление Треста "Севзапмонтажавтоматика"
Череповецкий Азотно-Туковый Завод
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 Ленинградское Специализированное Пусконаладочное Управление Треста "Севзапмонтажавтоматика", Череповецкий Азотно-Туковый Завод filed Critical Ленинградское Специализированное Пусконаладочное Управление Треста "Севзапмонтажавтоматика"
Priority to SU1968334A priority Critical patent/SU480642A1/en
Application granted granted Critical
Publication of SU480642A1 publication Critical patent/SU480642A1/en

Links

Landscapes

  • Treating Waste Gases (AREA)

Description

оптимальным расходом природного газа дл  поддержани  нормальной восстановительной среды в зоне реакции с учетом изменени  процесса абсорбции и изменени  содержани  окислов азота и кислорода в хвостовых газах. Было подтверждено, что определенное положение нижней границы температурного пол  зоны реакции реактора каталитической очистки  вл етс  показателем оптимального разложени  окислов азота, содержащихс  в хвостовых газах на входе в реактор.optimal consumption of natural gas to maintain a normal reducing environment in the reaction zone, taking into account changes in the absorption process and changes in the content of nitrogen oxides and oxygen in the tail gases. It was confirmed that a certain position of the lower limit of the temperature field of the catalytic cleaning reactor reaction zone is an indicator of the optimal decomposition of nitrogen oxides contained in the tail gas at the entrance to the reactor.

Верхн   граница температурного пол  стабилизируетс  регул тором температуры после реактора.The upper limit of the temperature field is stabilized by a post-reactor temperature controller.

Предмет изобретени Subject invention

1. Способ автоматического регулировани  процесса очистки хвостовых газов от окислов1. Method for automatic regulation of the process of cleaning tail gases from oxides

XdocmodineXdocmodine

НитрозныеNitrous

Ло5адочныи 5оздуLoader 5ozda

азота в реакторе каталитической очистки производства слабой азотной кислоты под давлением путем воздействи  па подачу природного газа в реактор и добавочного воздуха на установку абсорбции, отличающийс  тем, что, с целью оптимального управлени  процессом и сокращени  расхода газа, подачу газа в реактор осуществл ют по соотношению расходов газа и добавочного воздуха на установку абсорбции с коррекцией по разности температур хвостовых газов и минимальной температуры температурного пол  зоны реакции реактора.Nitrogen in a catalytic purification reactor for the production of weak nitric acid under pressure by affecting the supply of natural gas to the reactor and the additional air to an absorption unit, characterized in that, in order to optimally control the process and reduce the gas flow, the gas is supplied to the reactor gas and additional air to the installation of absorption with the correction of the temperature difference of the tail gases and the minimum temperature of the temperature field of the reaction zone of the reactor.

2. Способ ио п. 1, отличающийс  тем, что задание регул тору коррекции по перепаду температур устанавливают в пределах 10-20С, преимущественно 15+ГС.2. The method of clause 1, characterized in that the setting of the temperature differential correction controller is set in the range of 10-20 ° C, preferably 15 + HS.

SU1968334A 1973-10-26 1973-10-26 The method of automatic control of the process of cleaning tail gas from nitrogen oxides SU480642A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU1968334A SU480642A1 (en) 1973-10-26 1973-10-26 The method of automatic control of the process of cleaning tail gas from nitrogen oxides

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU1968334A SU480642A1 (en) 1973-10-26 1973-10-26 The method of automatic control of the process of cleaning tail gas from nitrogen oxides

Publications (1)

Publication Number Publication Date
SU480642A1 true SU480642A1 (en) 1975-08-15

Family

ID=20567105

Family Applications (1)

Application Number Title Priority Date Filing Date
SU1968334A SU480642A1 (en) 1973-10-26 1973-10-26 The method of automatic control of the process of cleaning tail gas from nitrogen oxides

Country Status (1)

Country Link
SU (1) SU480642A1 (en)

Similar Documents

Publication Publication Date Title
US4374105A (en) Purification of fuel gases
DE3687656D1 (en) REDUCTION OF NITROGEN-BASED POLLUTANTS BY USE OF OXYGEN-BASED HYDROCARBON SOLVENTS WITH URINE SOLUTIONS.
GB1033235A (en) A process for the production of gases containing sulphur dioxide
GB1510256A (en) Process for the manufacture of betamethylthiopropionaldehyde
DE69009077D1 (en) Treatment of nitrogen oxides.
EP2753416B1 (en) A process for incinerating nh3 and a nh3 incinerator
CA1172428A (en) Process for reacting hydrogen sulphide with oxygen
US4405593A (en) Process of decreasing the sulfur content of exhaust gases obtained during the recovery of sulfur
SU480642A1 (en) The method of automatic control of the process of cleaning tail gas from nitrogen oxides
US4219536A (en) Nitric acid process and disposal of waste liquids containing ammonium nitrites
FR2675794B1 (en) PROCESS FOR PRODUCING SULFUR FROM AT LEAST ONE ACID GAS CONTAINING H2S AND A GASEOUS OR LIQUID FUEL EFFLUENT AND THERMAL REACTOR FOR USE IN CARRYING OUT SAID PROCESS.
EP0217567B1 (en) Process and apparatus for treating sulphur dioxide-containing gas
US4003987A (en) Waste stream treatment
SU1680619A1 (en) Method for controlling catalytic purification of nitrose gases in production of weak nitric acid
SU676561A1 (en) Method of producing ferric chloride solutions
SU128453A1 (en) The method of regulating the process of acid absorption in the production of weak nitric acid
SU445618A1 (en) Method for automatic control of nitric acid production process
CA1206323A (en) Process for sulfuric acid regeneration
GB1411106A (en) Process for reducing the nitrogen oxide-s- content of a gas comprising oxygen and one or more nitrogen oxides
SU893856A1 (en) Device for automatic control of sulphur production process
ES479231A1 (en) Process for the catalytic oxidation of sulphur dioxide to form sulphur trioxide.
SU548621A1 (en) Method for automatic temperature control of a tubular furnace
SU1278349A1 (en) Method for controlling process of absorption in production of methanol formalin
SU611876A1 (en) Method of regulating process of hydrogen sulfide gas burning in furnace
SU1548181A1 (en) Method of controlling the process of oxidative dehydrogenation of n-butylenes