SU413182A1 - - Google Patents
Info
- Publication number
- SU413182A1 SU413182A1 SU1477494A SU1477494A SU413182A1 SU 413182 A1 SU413182 A1 SU 413182A1 SU 1477494 A SU1477494 A SU 1477494A SU 1477494 A SU1477494 A SU 1477494A SU 413182 A1 SU413182 A1 SU 413182A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- soda
- carbon dioxide
- amount
- oxidate
- concentration
- Prior art date
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- Physical Or Chemical Processes And Apparatus (AREA)
Description
1one
Изобретение относнтс к области автоматического унравлепи .нроцессами химических производств, где реакци сонровождаетс выделением .газа, и может найти применение в химической и нефтеперерабатывающей промышленности , например, нри содовом омылеНИИ оксидата.The invention relates to the field of automatic control of chemical production processes, where the reaction is generated by the release of gas, and can be used in the chemical and petroleum refining industry, for example, at the saponate of the oxidation of oxidate.
Известен способ авто.матического регулировани процесса омылени -путем изменени подачи соды в зависимости от расходов и концентрации оксидата и соды.There is a known method of automatic regulation of the saponification process — by varying the supply of soda depending on the flow rate and concentration of the oxidate and soda.
Однако известный способ автоматического регулировани не обеснечивает оптимального ведени .нроцесса.However, the known method of automatic regulation does not discredit the optimal management of the process.
С целью онтимизации Нроцесса ino предлагаемому Способу расход соды корректируют по концентрации выделившегос углекислого газа.In order to optimize the Nano process ino to the proposed Method, the consumption of soda is adjusted by the concentration of carbon dioxide emitted.
На чертеже представлена схема реализации способа.The drawing shows a diagram of the implementation of the method.
Работа схемы ,ествл етс следующим образом.The operation of the circuit is as follows.
В реактор 1 подают оксидат, количество которого автоматически поддерживаетс регул торо .м расхода 2 с клапаном 3. Туда же подают соду, количество и коНЦентрадию ко2An oxidate is supplied to the reactor 1, the amount of which is automatically maintained by the flow rate regulator 2 with the valve 3. Soda, the amount and concentration of carbon 2 are also supplied there.
торой Измер ют расходомером 4 и концептратомером 5, и воздух дл отдува углекислого газа из реакционной смеси. Воздух подают через расходомер 6 и анализатор 7 углекпслого газа (дл определенн коннептрадии углекислого газа). Весовое количество соды, идушей па омыление, измер ют вычислительным блоком 8, а количество выделившегос углекислого газа вычислительным блоком 9.The torus is measured by a flow meter 4 and a concept meter 5, and an air for venting carbon dioxide from the reaction mixture. Air is supplied through the flow meter 6 and the analyzer 7 of the carbon dioxide gas (for certain carbon dioxide). The weight amount of soda, as indicated by saponification, is measured by the computing unit 8, and the amount of carbon dioxide released by the computing unit 9.
При уменьшении расхода оксидата или его кислотного числа нарушаетс лропорцнональпость между количеством израсходованной соды и количеством выделившегос углекислого газа. Сигиал рассогласовани поступаетWhen reducing the consumption of oxidate or its acid number, the proportionality between the amount of soda consumed and the amount of carbon dioxide emitted is disturbed. Sigal mismatch arrives
на прибор 10, воздействующий па регулпрующий клапан 11, уменьшаюппп подачу соды.The device 10, acting on the regulating valve 11, reduces the supply of soda.
Предмет изобретен и The subject is invented and
Способ автоматического регулировани процесса омыленн нутем изменени нодачн соды в зависи.мости от расходов и концентрации оксидата и соды, о т л и ч а ю HI, и и с тем, что, с целью оптимизации нроцесса, расход содыThe method of automatic regulation of the process of saponification of nodal soda changes depending on the cost and concentration of the oxidate and soda, about t h and h HI, and with the fact that, in order to optimize the process, soda consumption
корре.ктируют по количеству выделпвн егоси углекислого газа.korp.ktiruyut by the amount of vyppvn its axis of carbon dioxide.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU1477494A SU413182A1 (en) | 1970-09-14 | 1970-09-14 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU1477494A SU413182A1 (en) | 1970-09-14 | 1970-09-14 |
Publications (1)
Publication Number | Publication Date |
---|---|
SU413182A1 true SU413182A1 (en) | 1974-01-30 |
Family
ID=20457592
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU1477494A SU413182A1 (en) | 1970-09-14 | 1970-09-14 |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU413182A1 (en) |
-
1970
- 1970-09-14 SU SU1477494A patent/SU413182A1/ru active
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