SU715478A1 - Method of control of hydrocarbon raw material catalytic reforming process - Google Patents

Method of control of hydrocarbon raw material catalytic reforming process Download PDF

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Publication number
SU715478A1
SU715478A1 SU782564622A SU2564622A SU715478A1 SU 715478 A1 SU715478 A1 SU 715478A1 SU 782564622 A SU782564622 A SU 782564622A SU 2564622 A SU2564622 A SU 2564622A SU 715478 A1 SU715478 A1 SU 715478A1
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SU
USSR - Soviet Union
Prior art keywords
raw material
control
catalytic reforming
reforming process
hydrocarbon raw
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Application number
SU782564622A
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Russian (ru)
Inventor
Фаиг Мамедали Оглы Абдуллаев
Мовсум Алмамед Оглы Мехтиев
Виктор Львович Левин
Алиман Багир Оглы Алиев
Донмаз Джамшид Оглы Джафаров
Original Assignee
Научно-Исследовательский И Проектный Институт По Комплексной Автоматизации Нефтяной И Химической Промышленности
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Priority to SU782564622A priority Critical patent/SU715478A1/en
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Publication of SU715478A1 publication Critical patent/SU715478A1/en

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Description

(54) СПОСОБ РЕГУЛИРОВАНИЯ ПРОЦЕССА КАТАЛИТИЧЕСКОГО РИФОРМИНГА УГЛЕВОДОРОДОВ(54) METHOD FOR REGULATING THE PROCESS OF CATALYTIC REFORMING OF HYDROCARBONS

Выходной сигнал экстремального регул тора 12 поступает на клапан 13, ycTajHtOBленный на трубопроводе 5 подачи топлива в печь 4. Дл  предотвращени  повышени  темйература сырь  на входе в реактор 1 выше граничного значени  предназначено выключгиощев 14. Выключающее рёЛе сравнивают текущее значение температуры с заданным значением тёййературы , поступающим по линии 15, и при увеличении ее выше заданного значени  стабилизирует выход экстремального регул тора 12 на посто нном значении.The output signal of the extreme controller 12 is fed to the valve 13, ycTajHtOBenny on the fuel supply pipe 5 to the furnace 4. To prevent an increase in the temperature of the raw material at the inlet of the reactor 1 above the limit value, the off-set point 14 is compared to the specified temperature value on line 15, and increasing it above a predetermined value stabilizes the output of the extreme regulator 12 at a constant value.

Реализаци  описываемого, способа может обеспечить максимальное соотношение между концентрацией ароматических углеводородов в продуктах реакции и концентрацией нафтеновых углеводородов в сырье, что соответствует максимальной конверсии нафтенов .The implementation of the described method can provide the maximum ratio between the concentration of aromatic hydrocarbons in the reaction products and the concentration of naphthenic hydrocarbons in the feed, which corresponds to the maximum conversion of naphthenes.

Claims (1)

1. Авторское свидетельство СССР 20 487104, кл. С 10 G 11/00, 1979 (прототип ) .1. USSR author's certificate 20 487104, cl. C 10 G 11/00, 1979 (prototype).
SU782564622A 1978-01-02 1978-01-02 Method of control of hydrocarbon raw material catalytic reforming process SU715478A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU782564622A SU715478A1 (en) 1978-01-02 1978-01-02 Method of control of hydrocarbon raw material catalytic reforming process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU782564622A SU715478A1 (en) 1978-01-02 1978-01-02 Method of control of hydrocarbon raw material catalytic reforming process

Publications (1)

Publication Number Publication Date
SU715478A1 true SU715478A1 (en) 1980-02-15

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Family Applications (1)

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SU782564622A SU715478A1 (en) 1978-01-02 1978-01-02 Method of control of hydrocarbon raw material catalytic reforming process

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SU (1) SU715478A1 (en)

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