CN108203603A - Chlorinated paraffin continuous producing apparatus control pressurer system - Google Patents
Chlorinated paraffin continuous producing apparatus control pressurer system Download PDFInfo
- Publication number
- CN108203603A CN108203603A CN201810144178.1A CN201810144178A CN108203603A CN 108203603 A CN108203603 A CN 108203603A CN 201810144178 A CN201810144178 A CN 201810144178A CN 108203603 A CN108203603 A CN 108203603A
- Authority
- CN
- China
- Prior art keywords
- pressure
- chlorine
- liquid chlorine
- data processing
- processing module
- Prior art date
- Legal status (The legal status 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 status listed.)
- Pending
Links
- 239000012188 paraffin wax Substances 0.000 title claims abstract description 23
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 claims abstract description 50
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims abstract description 31
- 229910052801 chlorine Inorganic materials 0.000 claims abstract description 31
- 239000000460 chlorine Substances 0.000 claims abstract description 31
- 238000003860 storage Methods 0.000 claims abstract description 15
- 238000004519 manufacturing process Methods 0.000 claims abstract description 13
- 238000005660 chlorination reaction Methods 0.000 claims abstract description 4
- 238000001816 cooling Methods 0.000 claims description 7
- 230000001105 regulatory effect Effects 0.000 claims description 6
- 239000000523 sample Substances 0.000 claims description 6
- 238000004891 communication Methods 0.000 claims description 3
- 238000009826 distribution Methods 0.000 claims description 3
- 230000001934 delay Effects 0.000 claims 2
- 238000006243 chemical reaction Methods 0.000 abstract description 8
- 239000000463 material Substances 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 5
- 239000002994 raw material Substances 0.000 abstract description 5
- 230000003139 buffering effect Effects 0.000 abstract description 4
- 238000010924 continuous production Methods 0.000 abstract description 4
- 238000000034 method Methods 0.000 abstract description 3
- 239000004173 sunset yellow FCF Substances 0.000 description 6
- 230000001276 controlling effect Effects 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 230000036632 reaction speed Effects 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G73/00—Recovery or refining of mineral waxes, e.g. montan wax
- C10G73/38—Chemical modification of petroleum
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The chlorinated paraffin continuous producing apparatus control pressurer system of the present invention, liquid chlorine gasifier, Chlorine Buffer Vessel top are connected to the outlet valve of the inlet valve of liquid chlorine gasifier, liquid chlorine reservoir outlet by first pressure harvester, second pressure harvester, the first data processing module, the second data processing module；The third pressure acquisition device of every grade of chlorinating container of multistage chlorination reaction production line is all connected to the first data processing module of surge tank by data switching center；Chlorinating container at different levels, surge tank, liquid chlorine gasifier etc. pressure condition are monitored in real time, and it is converted into controlling liquid chlorine storage tank, liquid chlorine gasifier input and output material flow according to pressure condition by data processing module after digital signal, and stablize after buffered tank buffering and enter chlorinating containers at different levels, pressure can be accurately controlled, it is easy to operate, adapt to continuous production intelligentized control method demand；Consumption of raw materials is reduced, improves production efficiency, reaction effect is good, and product quality is stablized.
Description
Technical field
The present invention relates to a kind of chlorinated paraffin continuous producing apparatus control pressurer systems.
Background technology
Chlorinated paraffin is generally given birth to by chlorine, paraffin in reaction kettle by certain temperature, pressure condition reactive absorption
Production manufacture, chlorine feed need control pressure to adapt to production reaction speed when adding, and traditional mode of production mode by controlling chlorine manually
Gas feedstock transportation pressure, control is inaccurate, and low production efficiency when pressure is too small, raw material causes to waste when pressure is too big, pressure control
System is inconvenient, reaction is caused to be not thorough, wastage of material situations such as, unstable product quality, reaction effect is bad, cost input
It is high.
Invention content
The technical problem to be solved by the invention is to provide one kind can accurately control pressure, cut down the consumption of raw materials, and improve
The chlorinated paraffin continuous producing apparatus control pressurer system of production efficiency.
The chlorinated paraffin continuous producing apparatus control pressurer system of the present invention, including liquid chlorine storage tank, liquid chlorine storage tank passes through pipe
Road is connected with liquid chlorine gasifier, and liquid chlorine gasifier outlet is connected with Chlorine Buffer Vessel, it is characterised in that：Chlorine Buffer Vessel, liquid chlorine
Gasifier top side is separately installed with first pressure harvester, second pressure harvester, first pressure harvester,
Two pressure acquisition devices are connected separately with the first data processing module, the second data processing module, the second number of liquid chlorine gasifier
The inlet valve of liquid chlorine gasifier is connected to according to processing module, the first data processing module of Chlorine Buffer Vessel is connected to liquid chlorine storage tank
The outlet valve of discharge port；
Chlorine Buffer Vessel top middle portion is connected with chlorine by pipeline and distributes platform, and chlorine distribution platform is connected by multiple chlorine gas outlets
To the chlorinating containers at different levels of chlorinated paraffin production line, every grade of chlorinating container top side is equipped with third pressure acquisition dress
It puts, the third pressure acquisition device at the top of every grade of chlorinating container is all connected to the of Chlorine Buffer Vessel by data switching center
One data processing module；
The liquid chlorine reservoir outlet is provided with stop valve and regulating valve, the first data processing module be connected to simultaneously stop valve and
Regulating valve；
The second pressure harvester end of probe is stretched into inside liquid chlorine gasifier, the third pressure at the top of every grade of chlorinating container
Harvester end of probe is all stretched into inside corresponding chlorinating container；
Every grade of chlorinating container is provided with cooling device, and the 4th pressure is provided between every grade of chlorinating container and cooling device and is adopted
Acquisition means, the 4th pressure acquisition device and data switching center's communication connection；
The Chlorine Buffer Vessel pressure control range is 0.3~0.4MPa；
The Chlorine Buffer Vessel pressure control is 0.35MPa.
The chlorinated paraffin continuous producing apparatus control pressurer system of the present invention, is monitored at different levels in real time by pressure acquisition device
Chlorinating container, surge tank, liquid chlorine gasifier etc. pressure condition, and be converted into after digital signal by data processing module according to
Pressure condition control liquid chlorine storage tank, liquid chlorine gasifier input and output material flow, and stablize after buffered tank buffering anti-into chlorinations at different levels
Kettle is answered, pressure can be accurately controlled, it is easy to operate, adapt to continuous production intelligentized control method demand；Consumption of raw materials is reduced, is improved
Production efficiency, reaction effect is good, and product quality is stablized.
Description of the drawings
Fig. 1 is chlorinated paraffin continuous producing apparatus control pressurer system planar structure schematic diagram of the embodiment of the present invention；
Fig. 2 is the reaction kettle planar structure signals at different levels of chlorinated paraffin continuous production control pressurer system equipment of the embodiment of the present invention
Figure.
Specific embodiment
As shown in the figure, a kind of chlorinated paraffin continuous producing apparatus control pressurer system, including liquid chlorine storage tank A-01, liquid chlorine storage
Tank A-01 is connected with liquid chlorine gasifier E-110 by pipeline, and liquid chlorine gasifier E-110 outlets are connected with Chlorine Buffer Vessel V-102,
It is characterized in that：Chlorine Buffer Vessel V-102, liquid chlorine gasifier E-110 top sides are separately installed with first pressure harvester
A-06, second pressure harvester A-05, first pressure harvester A-06, second pressure harvester A-05 are connected separately with
First data processing module, the second data processing module, the second data processing module of liquid chlorine gasifier E-110 are connected to liquid chlorine
The first data processing module of the inlet valve A-04 of gasifier E-110, Chlorine Buffer Vessel V-102 are connected to liquid chlorine storage tank A-01 and go out
The outlet valve of material mouth；
Chlorine Buffer Vessel V-102 top middle portions are connected with chlorine by pipeline and distribute platform V-103, and chlorine distribution platform V-103 passes through
Multiple chlorine gas outlets are connected to chlorinating container R-101~R-107 at different levels of chlorinated paraffin production line, every grade of chlorinating container R-
101~R-107 top sides are equipped with third pressure acquisition device A-111~A-117, every grade of chlorinating container R-101~R-
The third pressure acquisition device A-111~A-117 at 107 tops is connected to Chlorine Buffer Vessel V- by data switching center A-07
102 the first data processing module；, monitor chlorinating container at different levels, surge tank, liquid chlorine vaporizing in real time by pressure acquisition device
Device etc. pressure condition, and be converted into controlling liquid chlorine storage tank, liquid chlorine according to pressure condition by data processing module after digital signal
Gasifier input and output material flow, and stablize after buffered tank buffering and enter chlorinating containers at different levels, pressure can be accurately controlled.
Liquid chlorine storage tank A-01 discharge ports are provided with stop valve A-02 and regulating valve A-03, and the first data processing module connects simultaneously
Stop valve A-02 and regulating valve A-03 are connected to, liquid chlorine storage tank discharging flow can be adjusted according to each point pressure condition in time, it is necessary
When can directly close cut-out liquid chlorine reservoir outlet, it is easy to control.
Second pressure harvester A-05R end of probe is stretched into inside liquid chlorine gasifier E-110, every grade of chlorinating container R-
The end of probe of third pressure acquisition device A-111~A-117 at the top of 101~R-107 is all stretched into inside corresponding chlorinating container,
Monitoring data are accurate.
Every grade of chlorinating container A-111~A-117 is both provided with cooling device, every grade of chlorinating container A-111~A-117
Be provided with the 4th pressure acquisition device A-12~A-127 between cooling device, the 4th pressure acquisition device in data exchange
Heart communication connection, to control cooling device pressure.
The chlorinated paraffin continuous producing apparatus control pressurer system control Chlorine Buffer Vessel pressure limit of the present invention for 0.3~
0.4MPa；Chlorine Buffer Vessel pressure control in the present embodiment is 0.35MPa, and reaction effect is good.
The chlorinated paraffin continuous producing apparatus control pressurer system of the present invention, is monitored at different levels in real time by pressure acquisition device
Chlorinating container, surge tank, liquid chlorine gasifier etc. pressure condition, and be converted into after digital signal by data processing module according to
Pressure condition control liquid chlorine storage tank, liquid chlorine gasifier input and output material flow, and stablize after buffered tank buffering anti-into chlorinations at different levels
Kettle is answered, pressure can be accurately controlled, it is easy to operate, adapt to continuous production intelligentized control method demand；Consumption of raw materials is reduced, is improved
Production efficiency, reaction effect is good, and product quality is stablized.
Claims (6)
1. a kind of chlorinated paraffin continuous producing apparatus control pressurer system, including liquid chlorine storage tank, liquid chlorine storage tank is connected by pipeline
There is liquid chlorine gasifier, liquid chlorine gasifier outlet is connected with Chlorine Buffer Vessel, it is characterised in that：Chlorine Buffer Vessel, liquid chlorine gasifier
Top side is separately installed with first pressure harvester, second pressure harvester, first pressure harvester, second pressure
Harvester is connected separately with the first data processing module, the second data processing module, the second data processing of liquid chlorine gasifier
Module is connected to the inlet valve of liquid chlorine gasifier, and the first data processing module of Chlorine Buffer Vessel is connected to liquid chlorine reservoir outlet
Outlet valve；
Chlorine Buffer Vessel top middle portion is connected with chlorine by pipeline and distributes platform, and chlorine distribution platform is connected by multiple chlorine gas outlets
To the chlorinating containers at different levels of chlorinated paraffin production line, every grade of chlorinating container top side is equipped with third pressure acquisition dress
It puts, the third pressure acquisition device at the top of every grade of chlorinating container is all connected to the of Chlorine Buffer Vessel by data switching center
One data processing module.
2. chlorinated paraffin continuous producing apparatus control pressurer system according to claim 1, it is characterised in that：The liquid chlorine storage
Tank discharge port is provided with stop valve and regulating valve, and the first data processing module is connected to stop valve and regulating valve simultaneously.
3. chlorinated paraffin continuous producing apparatus control pressurer system according to claim 1, it is characterised in that：Second pressure
Force acquisition device end of probe is stretched into inside liquid chlorine gasifier, the third pressure acquisition device end of probe at the top of every grade of chlorinating container
It all stretches into inside corresponding chlorinating container.
4. chlorinated paraffin continuous producing apparatus control pressurer system according to claim 1, it is characterised in that：Every grade of chlorination is anti-
Kettle is answered to be provided with cooling device, the 4th pressure acquisition device, the 4th pressure are provided between every grade of chlorinating container and cooling device
Force acquisition device and data switching center's communication connection.
5. chlorinated paraffin continuous producing apparatus control pressurer system according to claim 1, it is characterised in that：The chlorine delays
Pressure tank control range is rushed as 0.3~0.4MPa.
6. chlorinated paraffin continuous producing apparatus control pressurer system according to claim 1, it is characterised in that：The chlorine delays
It is 0.35MPa to rush pressure tank control.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810144178.1A CN108203603A (en) | 2018-02-12 | 2018-02-12 | Chlorinated paraffin continuous producing apparatus control pressurer system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810144178.1A CN108203603A (en) | 2018-02-12 | 2018-02-12 | Chlorinated paraffin continuous producing apparatus control pressurer system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108203603A true CN108203603A (en) | 2018-06-26 |
Family
ID=62606506
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810144178.1A Pending CN108203603A (en) | 2018-02-12 | 2018-02-12 | Chlorinated paraffin continuous producing apparatus control pressurer system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108203603A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103849433A (en) * | 2013-03-26 | 2014-06-11 | 洛阳欧克迈自控工程有限公司 | Automatic production technology of chlorinated paraffin |
| CN103965963A (en) * | 2014-03-24 | 2014-08-06 | 辛集市三金化工有限公司 | Chlorinated paraffin production equipment and automatic control system |
| CN106989269A (en) * | 2017-05-23 | 2017-07-28 | 大连百傲化学股份有限公司 | A kind of industrial liquid chlorine is directly used in the device of chlorination reaction |
| CN208038383U (en) * | 2018-02-12 | 2018-11-02 | 丹阳市助剂化工厂有限公司 | Chlorinated paraffin continuous producing apparatus control pressurer system |
-
2018
- 2018-02-12 CN CN201810144178.1A patent/CN108203603A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103849433A (en) * | 2013-03-26 | 2014-06-11 | 洛阳欧克迈自控工程有限公司 | Automatic production technology of chlorinated paraffin |
| CN103965963A (en) * | 2014-03-24 | 2014-08-06 | 辛集市三金化工有限公司 | Chlorinated paraffin production equipment and automatic control system |
| CN106989269A (en) * | 2017-05-23 | 2017-07-28 | 大连百傲化学股份有限公司 | A kind of industrial liquid chlorine is directly used in the device of chlorination reaction |
| CN208038383U (en) * | 2018-02-12 | 2018-11-02 | 丹阳市助剂化工厂有限公司 | Chlorinated paraffin continuous producing apparatus control pressurer system |
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| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180626 |
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| RJ01 | Rejection of invention patent application after publication |