CN205910584U - Polymerization production ESS and integrated controlling means that promptly keeps safety in production of DCS - Google Patents

Polymerization production ESS and integrated controlling means that promptly keeps safety in production of DCS Download PDF

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Publication number
CN205910584U
CN205910584U CN201620835389.6U CN201620835389U CN205910584U CN 205910584 U CN205910584 U CN 205910584U CN 201620835389 U CN201620835389 U CN 201620835389U CN 205910584 U CN205910584 U CN 205910584U
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China
Prior art keywords
ess
dcs
polymerization
emptying
production
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CN201620835389.6U
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Chinese (zh)
Inventor
朱江军
张俊平
周红燕
张良
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Shihezi Tianyu new solid chemical Co. Ltd.
Xinjiang Tianye Group Co Ltd
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SHIHEZI DEVELOPMENT ZONE TIANYE CHEMICAL Co Ltd
Xinjiang Tianye Group Co Ltd
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Application filed by SHIHEZI DEVELOPMENT ZONE TIANYE CHEMICAL Co Ltd, Xinjiang Tianye Group Co Ltd filed Critical SHIHEZI DEVELOPMENT ZONE TIANYE CHEMICAL Co Ltd
Priority to CN201620835389.6U priority Critical patent/CN205910584U/en
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P90/00Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
    • Y02P90/02Total factory control, e.g. smart factories, flexible manufacturing systems [FMS] or integrated manufacturing systems [IMS]

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Abstract

The utility model discloses a polymerization production ESS and integrated controlling means that promptly keeps safety in production of DCS, the reinforced -> reaction -> ejection of compact overall process of DCS control polymerization cauldron, after the integrated communication of ESS and DCS, with the cauldron temperature, the cauldron is pressed, the stirring electric current reaches relevant setting value, on -the -spot with assist the urgent terminator of behaviour's bench and is pressed one of five according to the knob and satisfy and to start the ESS device, add the terminator and open the unloading device according to the real -time condition of polymeric kettle and in time solve emergency, it increases self emptying trip valve and unloading governing valve switching button between ESS and DCS device newly to assist behaviour's bench, above -mentioned messenger's operation more can reach ideal emergency control, it disturbs to overcome the human factor, eradicate accident occurrence is rateed, the utility model discloses but wide application in the urgent safe operation controlling means of different polymerization and polymerization process.

Description

A kind of polymerization ess produces control device with the integrated emergency safety of dcs
Technical field
This utility model is related to a kind of polymerization ess and produces control device with the integrated emergency safety of dcs, especially to poly- The control device of safety operation emergent management when symphysis abnormal during producing.
Background technology
At present, known polrvinyl chloride suspension polymerisation production Technology is very ripe.Technical process is: by chlorine The raw materials such as vinyl monomer, deionized water, dispersant, initiator, auxiliary agent are pressed dcs setting program and are put into polymeric kettle, through certain bar The reacted slurry of part is to be packaged through stripping, centrifugation, drying to the laggard pump that puts in storage of qualified products etc..Adopting above-mentioned technical process more Dcs Distributed Control System controls, and ess is to participate in dcs to control polymerization emergency safety system together.Ess and the collecting and distributing control of dcs System processed is made up of hardware and software, and wherein hardware includes field control station, active station, engineer station, communication netting twine etc.;Software Including the dcs and ess configuration software of operating system platform and industrial controlling, ess used and dcs hardware configuration and software arrangements Have nothing in common with each other, after integrated communication, wherein ess as all-the-way tracking dcs control in several critical process indexs parameter value, with kettle Temperature, kettle pressure, stir current reach related setting value, urgent terminator button is pressed one of five satisfactions on live and auxiliary behaviour's platform Ess device can be started, add terminator and open atmospheric valve according to rear condition, solve polymerization emergency in time.As day This Yokogawa centum-cs3000 dcs Distributed Control System and rrosafe-rs ess safe emergency system also can be used for this and gather Vinyl chloride process units.Above-mentioned technology directly applies to technique and its control that polymeric kettle produces polrvinyl chloride, and subject matter is During former ess system malfunctions, dcs can not operate emergency blow-down device, so that security control is relatively difficult, is not only difficult to reach To preferable production status, and extreme influence is caused to live personal safety and Environmental security.
Content of the invention
The purpose of this utility model technology be to provide a kind of easy to operate, can real-time monitoring, beneficial to safety in production, be suitable for Polymeric kettle produces the control device of the integrated emergency safety of dcs and ess of polrvinyl chloride.
A kind of polymerization ess produces control device with the integrated emergency safety of dcs, controls adding of polymerization reaction kettle by dcs Material → reaction → discharging overall process.After ess and dcs integrated communication, setting value a value is reached with kettle temperature, kettle pressure reaches setting value b Value, stir current reach setting value c value, live emergency termination agent button is pressed, urgent terminator button is pressed on auxiliary behaviour's platform One of lower condition five meets condition and can start the integrated emergency safety of ess and produces control device, and ess starts and adds terminator dress Put and open emptying regulating valve and emptying stop valve according to polymeric kettle real-time condition, solve polymerization emergency in time, on State ess and dcs to control switching is to newly increase automatic emptying device on auxiliary behaviour's platform: emptying stop valve and emptying regulating valve are in ess With dcs control room switching push button, emptying device is started by dcs.
Because this utility model increased ess and dcs device on polymerization auxiliary operation platform, switching emptying device is put Empty stop valve and emptying regulating valve button, in ess emergency safety operating system failure, emptying device is cut rapidly by operator Change button incision dcs control system, emptying device is started by dcs, dcs can complete associative operation within the time the shortest, solution The drawbacks of former emptying device of having determined can only be operated by ess controls standard so that emptying manipulation more can reach desired Safety, so that Safe and steady operation it is ensured that and optimize operating procedure, also have simultaneously convenient to operation, mitigate labor strength, gram Take the impact to polymerization for the anthropic factor, minimizing or fundamentally prevent accident rate, achieve polymerization key work The automatically controlling, improve the advantages of parameter measure precision and control accuracy of sequence.This utility model can be widely applied to not Emergency safety operating control device with polyreaction and polymerization process.
Brief description
The utility model is described in further detail with reference to the accompanying drawings and examples.
Fig. 1 is the polrvinyl chloride process for suspension polymerization ess system flow schematic diagram of this utility model embodiment 1.
Fig. 2 is to increase ess on the auxiliary operation platform of this utility model embodiment 1 to switch emptying device button with dcs device Switch schematic diagram with dcs, ess.
In Fig. 1,1. nitrogen cylinder;2. nitrogen cylinder outlet automatic nitrogen-charging valve;3. terminator tank automatic nitrogen-charging valve;4. eventually Only agent tank;5. terminator adds groove;6. terminator enters kettle valve automatically;7. polymeric kettle;8. polymeric kettle emptying stop valve;9. it is polymerized Kettle is vented regulating valve.
In Fig. 2,10.dcs control system;11.dcs toggle bit;12. emptying device switching push buttons;13. ess toggle bits; 14. ess control systems.
Specific embodiment
1-2 referring to the drawings, this utility model embodiment 1 controls the charging → reaction → discharging of polymerization reaction kettle for dcs Process, wherein reaction end is to meet preset pressure value with pressure drop, you can judge that reaction terminates and adds terminator with end Only polyreaction.In polymerization kettle temperature reach setting value a value be 70 DEG C, kettle pressure reach setting value b value 1.4mpa, stir current Reaching setting value c value 30a is homophony parameter, and live emergency termination agent button is pressed, urgent terminator button quilt on auxiliary behaviour's platform Press either button to be pressed;Five conditions meet one of them, you can judge that polymerization exception ess starts and adds termination Agent is to terminate polyreaction.Ess emergency safety operating system is primarily directed to abnormal conditions start-stop in polymerization production process Agent adding apparatus.Ess system is made up of hardware and software with dcs Distributed Control System, and wherein hardware includes field control station, behaviour Stand, engineer station, communication netting twine etc.;Software includes ess the and dcs configuration software of operating system platform and industrial controlling, This technology directly applies to technique and its control device that polymeric kettle produces polrvinyl chloride.
Embodiment 2 difference from Example 1 is: in polymerization production process, ess and the integrated emergency safety of dcs produce control Device processed, increases switching emptying device emptying stop valve and emptying regulating valve between ess and dcs device on auxiliary operation platform and presses Button, can be respectively started emptying device by dcs and ess.
Preset temperature in above-described embodiment, pressure, current reference value can rule of thumb need to take multiple, concrete value with The size of reaction kettle device, response characteristic etc. have particularly important relation.
This utility model mainly has been made to improve to the hardware unit in emptying stage, other identical with prior art.

Claims (1)

1. a kind of polymerization ess and the integrated emergency safety of dcs produce control device, are controlled the charging of polymerization reaction kettle by dcs → reaction → discharging overall process, after ess and dcs integrated communication, setting value a value is reached with kettle temperature, kettle pressure reaches setting value b value, Stir current reaches setting value c value, live emergency termination agent button is pressed, urgent terminator button is pressed bar on auxiliary behaviour's platform One of part five meets condition and can start ess integrated emergency safety production control device, and ess starts addition terminator device simultaneously Open emptying regulating valve and emptying stop valve according to polymeric kettle real-time condition, solve polymerization emergency, its feature in time It is to newly increase automatic emptying device switching push button between ess and dcs control device on auxiliary behaviour's platform, as ess emergency safety behaviour When making the system failure, emptying device switching push button is cut dcs control system rapidly by operator, starts emptying device by dcs.
CN201620835389.6U 2016-08-04 2016-08-04 Polymerization production ESS and integrated controlling means that promptly keeps safety in production of DCS Active CN205910584U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620835389.6U CN205910584U (en) 2016-08-04 2016-08-04 Polymerization production ESS and integrated controlling means that promptly keeps safety in production of DCS

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620835389.6U CN205910584U (en) 2016-08-04 2016-08-04 Polymerization production ESS and integrated controlling means that promptly keeps safety in production of DCS

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CN205910584U true CN205910584U (en) 2017-01-25

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110631125A (en) * 2019-09-18 2019-12-31 鲁西化工集团股份有限公司煤化工二分公司 Emptying control system and method of high back pressure system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110631125A (en) * 2019-09-18 2019-12-31 鲁西化工集团股份有限公司煤化工二分公司 Emptying control system and method of high back pressure system

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CP03 Change of name, title or address
CP03 Change of name, title or address

Address after: North Road 832000 the Xinjiang Uygur Autonomous Region Shihezi Development Zone No. 36

Co-patentee after: Xinjiang Tianye (Group) Co., Ltd.

Patentee after: Shihezi Tianyu new solid chemical Co. Ltd.

Address before: No. 36 North Third East Road, Shihezi Development Zone, the Xinjiang Uygur Autonomous Region Province

Co-patentee before: Xinjiang Tianye (Group) Co., Ltd.

Patentee before: SHIHEZI DEVELOPMENT ZONE TIANYE CHEMICAL CO., LTD.