SU381379A1 - EUA ^ A; LH1110 - ^? HNeNeOKAYA - Google Patents

EUA ^ A; LH1110 - ^? HNeNeOKAYA

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Publication number
SU381379A1
SU381379A1 SU1468526A SU1468526A SU381379A1 SU 381379 A1 SU381379 A1 SU 381379A1 SU 1468526 A SU1468526 A SU 1468526A SU 1468526 A SU1468526 A SU 1468526A SU 381379 A1 SU381379 A1 SU 381379A1
Authority
SU
USSR - Soviet Union
Prior art keywords
mixture
refrigerant
temperature
hneneokaya
eua
Prior art date
Application number
SU1468526A
Other languages
Russian (ru)
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 SU1468526A priority Critical patent/SU381379A1/en
Application granted granted Critical
Publication of SU381379A1 publication Critical patent/SU381379A1/en

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  • Physical Or Chemical Processes And Apparatus (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

1one

Изобретение относитс  к способам регулировани  работы реакторов и может примен тьс  в процессах нефтеперерабатывающей, нефтехимической и Х имической промышленности .The invention relates to methods for regulating the operation of reactors and can be used in the processes of the petroleum refining, petrochemical and chemical industries.

Известен способ автоматического управлени  работой реакторов путем изменени  расхода одного из компонентов в зависимости от температуры смеси и стабилизации расхода хладагента. Однако указанный способ не обеспечивает требуемого выхода целевого продукта .There is a known method of automatically controlling the operation of reactors by changing the flow rate of one of the components depending on the temperature of the mixture and stabilizing the flow rate of the refrigerant. However, this method does not provide the desired yield of the target product.

Дл  увеличени  выхода целевого продукта предлагаетс  регулировать соотношение расходов компонентов с коррекцией по температуре смеси на выходе из реакторов и расход хладагента в зависимости от разности температур смеси на выходе из реакторов и хладагента на входе реакторов.In order to increase the yield of the target product, it is proposed to adjust the ratio of the flow rates of the components with correction for the mixture temperature at the reactor outlet and the coolant flow rate depending on the temperature difference of the mixture at the reactor outlet and the refrigerant at the reactor inlet.

На чертеже показана схема реализации описываемого способа.The drawing shows the implementation of the described method.

Способ осуществл ют следующим образом.The method is carried out as follows.

Сигналы с датчиков расхода 1 и 2, установленных на лини х подачи сырь  и раствора карбамида в реакторы, поступают в регул тор соотношени  3, выход которого св зан с клапаном 4, расположенным на линии подачиThe signals from flow sensors 1 and 2, installed on the lines of supply of raw materials and urea solution to the reactors, enter the ratio controller 3, the output of which is connected to valve 4 located on the supply line

раствора карбамида. На регул тор соотношени  подают корректирующий сигнал от датчика температуры 5 реакционной смеси на выходе из последнего реактора через программное устройство 6. Регул тор 7 разности температур , на который поступает переменна  с суммирующего блока 8, получаема  в результате вычитани  сигналов с датчиков температур 5 и 5 реакционной смеси и хладагента, управл ет регулирующим клапаном 10, установленным на линии подачи охлаждающей воды.urea solution. The ratio controller is supplied with a correction signal from the temperature sensor 5 of the reaction mixture at the outlet of the last reactor through the software device 6. The temperature difference controller 7, which is variable from the summing unit 8, is obtained by subtracting the signals from the temperature sensors 5 and 5 of the reaction mixture mixture and refrigerant, controls the control valve 10 installed in the cooling water supply line.

Предмет изобретени Subject invention

Способ автоматического управлени  работой реакторов путем 1изменени  расходов компонентов и хладагента, отличающийс  тем, что, с целью увеличени  выхода целевого продукта , регулируют соотношение расходов компонентов с коррекцией но температуре смесн на выходе из реакторов и расход хладагента в зависимости от разности температур смеси на выходе из реакторов и .хладагента на входе реакторов.A method of automatically controlling the operation of reactors by changing the flow rates of components and refrigerant, characterized in that, in order to increase the yield of the target product, the ratio of the flow rates of components with correction at the reactor outlet temperature and refrigerant flow is controlled depending on the temperature difference of the mixture at the reactor outlet and coolant at the reactor inlet.

SU1468526A 1970-08-14 1970-08-14 EUA ^ A; LH1110 - ^? HNeNeOKAYA SU381379A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU1468526A SU381379A1 (en) 1970-08-14 1970-08-14 EUA ^ A; LH1110 - ^? HNeNeOKAYA

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU1468526A SU381379A1 (en) 1970-08-14 1970-08-14 EUA ^ A; LH1110 - ^? HNeNeOKAYA

Publications (1)

Publication Number Publication Date
SU381379A1 true SU381379A1 (en) 1973-05-22

Family

ID=20456369

Family Applications (1)

Application Number Title Priority Date Filing Date
SU1468526A SU381379A1 (en) 1970-08-14 1970-08-14 EUA ^ A; LH1110 - ^? HNeNeOKAYA

Country Status (1)

Country Link
SU (1) SU381379A1 (en)

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