SU538721A2 - The method of automatic regulation of the rectification process - Google Patents

The method of automatic regulation of the rectification process

Info

Publication number
SU538721A2
SU538721A2 SU2091653A SU2091653A SU538721A2 SU 538721 A2 SU538721 A2 SU 538721A2 SU 2091653 A SU2091653 A SU 2091653A SU 2091653 A SU2091653 A SU 2091653A SU 538721 A2 SU538721 A2 SU 538721A2
Authority
SU
USSR - Soviet Union
Prior art keywords
automatic regulation
rectification process
composition
irrigation
target product
Prior art date
Application number
SU2091653A
Other languages
Russian (ru)
Inventor
Вадим Викторович Коровин
Владимир Викторович Гришечкин
Юрий Васильевич Шевелев
Владлен Исаакович Файнерман
Original Assignee
Предприятие П/Я М-5593
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 Предприятие П/Я М-5593 filed Critical Предприятие П/Я М-5593
Priority to SU2091653A priority Critical patent/SU538721A2/en
Application granted granted Critical
Publication of SU538721A2 publication Critical patent/SU538721A2/en

Links

Landscapes

  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Description

(54) СПОСОБ АВТОМАТИЧЕСКОГО РЕГУЛИРОВАНИЯ ПРОЦЕССА РЕКТИФИКАЦИИ(54) METHOD FOR AUTOMATIC REGULATION OF RECTIFICATION PROCESS

Изобретение относитс  к области автоматического регулировани  химических и нефтехимических процессов, в частности к способам автоматического регулировани  процесса ректификации .The invention relates to the field of automatic regulation of chemical and petrochemical processes, in particular, to methods of automatic regulation of the rectification process.

Известен способ автоматического регулировани  процесса ректификации по авт. св. ЛЬ 460879, согласно которому изменение подачи дистилл та и дополнительного потока продукта на орошение осуществл ют в зависимости от состава целевого продукта.There is a method of automatic regulation of the rectification process according to ed. St. LL 460879, according to which the change in the supply of distillate and additional flow of the product to irrigation is carried out depending on the composition of the target product.

Недостатком известного способа  вл етс  замедленна  реакци  системы регулировани  ректификационной колонны нри изменении состава сырь , что обуславливаетс  инерционностью объекта регулировани  при управлении по составу целевого продукта.The disadvantage of the known method is the delayed reaction of the distillation column control system at a change in the composition of the feedstock, which is caused by the inertia of the control object when controlling the composition of the target product.

Целью изобретени   вл етс  интенсификаци  процесса ректификации и стабилизации качества целевого продукта.The aim of the invention is to intensify the process of rectification and stabilize the quality of the target product.

Поставленна  цель достигаетс  тем, что соотношение компонентов орошени  измен ют в зависимости то состава сырь .This goal is achieved by changing the ratio of the components of irrigation depending on the composition of the raw material.

На чертеже представлена схема регулировани  процесса ректификации.The drawing shows a diagram of the regulation of the rectification process.

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

На верхнюю тарелку колонны 1 подают дистиллат , отбираемый из сборника орошени  2, и дополнительный компонент орошени , расходы которых регулируют клапанами 3 и 4, установленными соответственно на лини х подачи на орошение дистиллата и дополнительного продукта.A distillate taken from the irrigation collector 2 and an additional irrigation component are supplied to the top plate of the column 1, the costs of which are controlled by valves 3 and 4 installed respectively on the lines for supplying the distillate and the additional product to irrigation.

Клапаны получают управл ющее воздействие от регул тора соотношени  5, который св зан с анализатором 6 состава сырь . Измерение расходов продуктов осуществл ют расходомерами 7, 8.The valves receive a control action from the ratio controller 5, which is associated with the raw material composition analyzer 6. The measurement of product flow rates is carried out by flow meters 7, 8.

Данный способ автоматического регулировани  процесса ректификации позвол ет ускорить реакцию системы регулировани  колонны при изменении состава сырь , тем самым интенсифицировать процесс и получать целевой продукт стабильного качества.This method of automatic regulation of the rectification process allows us to accelerate the response of the column control system when the composition of the raw materials is changed, thereby intensifying the process and obtaining the target product of stable quality.

Claims (1)

Формула изобретени Invention Formula Способ автоматического регулировани  процесса , ректификации по авт. св. N° 460879, о тличающийс  тем, что, с целью интенсификации процесса и стабилизации качества целевого продукта, соотнощение компонентов орошени  измен ют в зависимости от состава сырь .A method of automatic control of the process, rectification according to ed. St. N ° 460879, similar to the fact that, in order to intensify the process and stabilize the quality of the target product, the ratio of the components of irrigation is changed depending on the composition of the raw material.
SU2091653A 1974-12-31 1974-12-31 The method of automatic regulation of the rectification process SU538721A2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU2091653A SU538721A2 (en) 1974-12-31 1974-12-31 The method of automatic regulation of the rectification process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU2091653A SU538721A2 (en) 1974-12-31 1974-12-31 The method of automatic regulation of the rectification process

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
SU460879 Addition

Publications (1)

Publication Number Publication Date
SU538721A2 true SU538721A2 (en) 1976-12-15

Family

ID=20605915

Family Applications (1)

Application Number Title Priority Date Filing Date
SU2091653A SU538721A2 (en) 1974-12-31 1974-12-31 The method of automatic regulation of the rectification process

Country Status (1)

Country Link
SU (1) SU538721A2 (en)

Similar Documents

Publication Publication Date Title
SU710522A3 (en) Method of conversion process control in consecutively joined reactors
SU538721A2 (en) The method of automatic regulation of the rectification process
SU460879A1 (en) Method for automatic regulation of the rectification process
GB1119790A (en) Method and apparatus for the automatic control of a continuous distillation process
SU757171A1 (en) Rectification-processes automatic control method
SU553983A1 (en) Method for automatic control of mixture separation process
SU500805A1 (en) Method for automatic control of the rectification process
SU652951A2 (en) Method of automatic control of liquid extraction process in column with sieve trays
SU1234395A1 (en) Method of controlling process of dimethyldioxane synthesis
SU844016A1 (en) Method of automatic control of processes of selective separation and cleaning of gas-liquid mixtures in column apparatus
SU735881A1 (en) Method of regulating gas-mixture separation process in fractionating column
SU1276349A1 (en) Method of controlling the process of separaion of isoprene-isoamylene fraction
SU487648A1 (en) The method of automatic control of the technological mode of the rectification process
SU541481A1 (en) Device for automatic control of the gas fractionation column process mode
SU549159A1 (en) The method of automatic regulation of the rectification process
SU397533A1 (en) VPTB
SU1583129A1 (en) Method of controlling process of separation of isopheneisoamylene fractions
SU783296A1 (en) Method of control of dimethyldioxane synthesis
SU1036360A1 (en) Method of automatic control of continuous action reactor
SU594988A1 (en) Fractionating process control method
SU541479A1 (en) Method for automatic control of the evaporation process
SU981306A1 (en) Method for automatically controlling exothermal reaction of hydrogenation of acetylene compounds
SU683764A1 (en) Automatic regulator of temperature at 'monitor' tray of fractionating column
SU542527A1 (en) Method for automatic control of liquid extraction process
SU388758A1 (en) METHOD FOR AUTOMATIC CONTROL OF RECTIFICATION COLUMN