CN108251157A - Chlorinated paraffin continuous producing apparatus - Google Patents
Chlorinated paraffin continuous producing apparatus Download PDFInfo
- Publication number
- CN108251157A CN108251157A CN201810144202.1A CN201810144202A CN108251157A CN 108251157 A CN108251157 A CN 108251157A CN 201810144202 A CN201810144202 A CN 201810144202A CN 108251157 A CN108251157 A CN 108251157A
- Authority
- CN
- China
- Prior art keywords
- chlorine
- chlorinating container
- chlorinating
- multistage
- wax
- 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 32
- 239000001993 wax Substances 0.000 claims abstract description 80
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims abstract description 70
- 239000000460 chlorine Substances 0.000 claims abstract description 70
- 229910052801 chlorine Inorganic materials 0.000 claims abstract description 70
- 238000006243 chemical reaction Methods 0.000 claims abstract description 31
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 claims abstract description 30
- 238000005660 chlorination reaction Methods 0.000 claims abstract description 25
- 238000003860 storage Methods 0.000 claims abstract description 17
- 239000000463 material Substances 0.000 claims abstract description 9
- 238000000034 method Methods 0.000 claims abstract description 9
- 239000000047 product Substances 0.000 claims description 40
- 238000007872 degassing Methods 0.000 claims description 21
- 239000011265 semifinished product Substances 0.000 claims description 8
- 238000001816 cooling Methods 0.000 claims description 7
- 230000008676 import Effects 0.000 claims description 6
- 238000004806 packaging method and process Methods 0.000 claims description 5
- 238000009826 distribution Methods 0.000 claims description 4
- 238000012856 packing Methods 0.000 claims description 4
- 238000011084 recovery Methods 0.000 claims description 4
- 239000002994 raw material Substances 0.000 abstract description 18
- 238000004519 manufacturing process Methods 0.000 abstract description 17
- 230000000694 effects Effects 0.000 abstract description 6
- 238000010924 continuous production Methods 0.000 abstract description 5
- 238000002309 gasification Methods 0.000 abstract description 2
- 239000006227 byproduct Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000004234 Yellow 2G Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 239000002151 riboflavin Substances 0.000 description 2
- 239000004173 sunset yellow FCF Substances 0.000 description 2
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000012795 verification Methods 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
- B01J19/0013—Controlling the temperature of the process
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The chlorinated paraffin continuous producing apparatus of the present invention, liquid chlorine distributes platform by chlorine after gasifier gasification and connects multiple chlorinating containers in liquid chlorine storage tank, multiple chlorinating containers are arranged in order setting and form multistage chlorination reactor, multistage chlorination reaction is connected with wax oil feed pipe, chlorine feed pipe, offgas outlet, electric control system, and pass through electric control system and liquid chlorine storage tank inlet valve electric control system is chain, multistage chlorinating container forms tinuous production, it is easy to operate, it can adapt to continuous production processes demand, using the input and output material mode of upper entering and lower leaving, product reaction is thorough, chlorine feed can recycle participation reaction by device for recovering tail gas, reaction effect is good, raw material availability is high, product quality is stablized, reduce cost consumption, improve production efficiency.
Description
Technical field
The present invention relates to a kind of chlorinated paraffin continuous producing apparatus.
Background technology
Chlorinated paraffin is generally given birth to by chlorine, paraffin in reaction kettle by certain temperature, pressure condition reactive absorption
Production manufacture, tradition gasification paraffin reaction kettle are produced for discontinuous, are all needed to interrupt reaction process after each reaction production, are opened reaction
Kettle is to discharge, and reaction process is intermittent reaction in reaction kettle, and cumbersome, the production cycle is long, low production efficiency, it is impossible to suitable
Answer continuous production processes demand；Intermittent reaction generally uses the input and output material mode gone out on enterprising, and product density is uneven, exists
Situations such as reaction is not thorough, wastage of material, quality is unstable, and reaction effect is bad, and cost input is high.
Invention content
It is easy to operate the technical problem to be solved by the invention is to provide a kind of production process is continuously uninterrupted, chlorination
Paraffin continuous producing apparatus.
The chlorinated paraffin continuous producing apparatus of the present invention, it is characterised in that：Including liquid chlorine storage tank, liquid chlorine storage tank passes through pipeline
Liquid chlorine gasifier is connected with, liquid chlorine gasifier outlet is connected with Chlorine Buffer Vessel, and Chlorine Buffer Vessel top middle portion is connected by pipeline
Chlorine distribution platform is connected to, chlorine distribution platform is provided with multiple chlorine gas outlets, and each chlorine gas outlet is connected with chlorinating container, multiple
Chlorinating container is arranged in order setting and forms multistage chlorination reactor；
Chlorine feed pipe, wax oil feed pipe are connected separately at the top of every grade of chlorinating container, bottom is provided with discharge port, every grade of chlorine
Change reactor bottom discharge port and be consecutively connected to wax oil feed pipe at the top of subordinate's chlorinating container, positioned at primary level-one chlorination
Wax oil feed pipe is connected to wax oil storage tank at the top of reaction kettle, is connected positioned at last final stage chlorinating container bottom discharge mouth
To wax oil treater, wax oil treater is connected to finished product packing platform；Cooling device is provided with outside every grade of chlorinating container；
Offgas outlet, every grade of offgas outlet and chlorinating container offgas outlet company of subordinate are additionally provided at the top of every grade of chlorinating container
Logical, the offgas outlet of at least level-one chlorinating container is connected to tail gas recycle pipeline；
Every grade of chlorinating container is equipped with electric control system, the electric control systems of chlorinating containers at different levels summarize after connection with
Liquid chlorine storage tank inlet valve electric control system is chain；
Circulating pump is provided between every grade of chlorinating container and cooling device；
The multistage chlorination reaction bottom discharge port is connected directly to wax oil treater after summarizing simultaneously by pipeline；
The offgas outlet of other chlorinating containers at different levels leads to simultaneously in addition to level-one chlorinating container in the multistage chlorinating container
Piping is connected directly to tail gas recycle pipeline after summarizing；
The offgas outlet of at least level-one chlorinating container is connected with drain in the multistage chlorinating container；
In the multistage chlorinating container gas recovery import and Balance Air import are also associated at the top of final stage chlorinating container；
Every grade of chlorinating container is equipped with temperature measuring equipment in the multistage chlorinating container, and chlorinating container temperature measuring equipments at different levels lead to
Cross the inlet valve that electric control system is connected to liquid chlorine storage tank；
The drain is connected in multistage chlorinating container at the top of the chlorinating container of final stage chlorinating container previous stage；
The multistage chlorination reactor includes 7 grades of chlorinating containers；
The wax oil treater include thick chlorine wax groove, thick chlorine wax groove top feed mouth simultaneously with final stage chlorinating container bottom
Semi-finished product discharge port, multistage chlorinating container bottom discharge mouth pipeline summarize connection, thick chlorine wax groove is connected with the first degassing
Kettle, second degassing kettle, thick chlorine wax groove, first degassing kettle, second degassing bottom portion finished product discharge port be connected with simultaneously chlorine wax into
Product slot and product groove tank car, chlorine wax pan tank are connected to product packaging platform, and the pipeline of multistage chlorinating container bottom discharge mouth converges
Chlorine wax pan tank, product groove tank car always are connected directly to simultaneously, after part finished product chlorinated paraffin is by product packaging platform subpackage
Transport, another part finished product chlorinated paraffin are directly transported by product groove tank car；First degassing kettle, the second degassing kettle top portion are also logical
Piping is connected with degassing surge tank, and the tail gas in semi-finished product subtractive process is by the surge tank that deaerates through tail gas recycle pipeline
To device for recovering tail gas；Chlorine wax pan tank is connected with two-stage chlorine wax discharge pump.
The chlorinated paraffin continuous producing apparatus of the present invention, multistage chlorinating container arrangement setting are sequentially connected the multistage chlorine of composition
Change reactor, multistage chlorinating container forms tinuous production, easy to operate, can adapt to continuous production processes demand, uses
The input and output material mode of upper entering and lower leaving, product reaction is thorough, and chlorine feed can recycle participation reaction by device for recovering tail gas, instead
Answer effect good, raw material availability is high, and product quality is stablized, and reduces cost consumption, improves production efficiency；Through actual verification,
Tinuous production is formed using 7 grades of chlorinating containers, production capacity can reach 2t/h, and production efficiency is high and product quality is steady
It is fixed.
Description of the drawings
Fig. 1 is the liquid chlorine storage tank planar structure schematic diagram of chlorinated paraffin continuous producing apparatus of the embodiment of the present invention；
Fig. 2 is the multistage chlorinating container planar structure schematic diagram of chlorinated paraffin continuous producing apparatus of the embodiment of the present invention；
Fig. 3 is the wax oil treater planar structure schematic diagram of chlorinated paraffin continuous producing apparatus of the embodiment of the present invention.
Specific embodiment
As shown in the figure, a kind of chlorinated paraffin continuous producing apparatus, including liquid chlorine storage tank A01, liquid chlorine storage tank A01 passes through pipeline
Liquid chlorine gasifier E110 is connected with, liquid chlorine gasifier E110 outlets are connected with Chlorine Buffer Vessel by C1G101-65-L1RP pipelines
V102, Chlorine Buffer Vessel V102 top middle portions are connected with chlorine by C1G102-65-L1RP pipelines and distribute platform V103, chlorine point
Platform V103 is provided with multiple chlorine gas outlets, each chlorine gas outlet is connected with chlorinating container, multiple chlorinating container R101~
R107 is arranged in order setting and forms multistage chlorination reactor；Chlorine Buffer Vessel V102 bottoms are connected with chlorine blowdown drum V104, chlorine
Qi leel is also connected to chlorine blowdown drum V104 with platform V103 bottoms.
The multistage chlorination reactor of chlorinated paraffin continuous producing apparatus of the embodiment of the present invention includes 7 grades of chlorinating containers
Chlorine feed pipe, wax oil feed pipe are connected separately at the top of R101~R107, every grade of chlorinating container R101~R107, bottom is set
Be equipped with discharge port, every grade of chlorine feed pipe respectively with the chlorine gas outlet C1G103-65-L1RP of chlorine distribution platform V103~
C1G109-65-L1RP connections are connected to wax oil storage positioned at wax oil feed pipe at the top of primary level-one chlorinating container R101
Tank, bottom discharge mouth are connected to the wax oil feed pipe at the top of secondary chlorination reaction kettle R102, and so on, every grade of chlorinating container
Bottom discharge mouth is consecutively connected to wax oil feed pipe at the top of subordinate's chlorinating container, positioned at last final stage chlorinating container
R107 bottom discharge mouths A08 is connected to wax oil treater, and wax oil semi-finished product are by wax oil treater purification, wax oil treater essence
The finished product chlorinated paraffin connection that system is completed is delivered to finished product packing platform packed and transported；Multistage chlorinating container R101~R107 bottoms
Discharge port summarizes A09 by pipeline simultaneously and is connected directly to wax oil treater, in level-one chlorinating container R101 wax oil raw material with
After chlorine reaction, the wax oil semi-finished product for reacting completion are delivered directly to the further refinement treatment of wax oil treater, and unreacted is completed
Wax oil raw material enter in secondary chlorination reaction kettle R102 and continue to react with new chlorine, and so on, up to last
Final stage chlorinating container R107.
Cooling device E101~E107, every grade of chlorinating container are provided with outside every grade of chlorinating container R101~R107
Be provided with circulating pump P101~P107 between R101~R107 and corresponding cooling device E101~E107, by circulating pump P101~
P107 will wax oil feedstock transportation in every grade of chlorinating container to cooling device cool down after enter back into every grade of chlorinating container R101~
In R107 and chlorine reaction, reaction effect can be improved；Every grade of chlorinating container R101~R107 both sides external is connected with cooling
Water feed pipe and cooling water return pipe.
It is additionally provided with offgas outlet at the top of every grade of chlorinating container R101~R107, every grade of offgas outlet and subordinate chlorination are anti-
Kettle offgas outlet is answered to connect, the offgas outlet of at least level-one chlorinating container is connected to tail gas recycle pipeline A02；Multistage chlorination
The offgas outlet of other chlorinating containers at different levels passes through simultaneously in addition to level-one chlorinating container R101 in reaction kettle R101~R107
Pipeline is connected directly to tail gas recycle pipeline after summarizing；The chlorine not reacted in upper level chlorinating container with wax oil raw material
The reaction was continued with wax oil raw material in into subordinate's chlorinating container, while does not react in upper level chlorinating container with chlorine
Wax oil raw material also enter in subordinate's chlorinating container, chlorine and wax oil raw material continue to continue in subordinate's chlorinating container anti-
Should, and so on, until final stage chlorinating container；And since wax oil raw material is from primary level-one chlorinating container,
Wax oil raw material is sufficient, can be with entering the abundant reactive absorption of chlorination in level-one chlorinating container, thus level-one chlorinating container
Device for recovering tail gas need not be connected directly to.
The offgas outlet of at least chlorinating container of one of them is connected in multistage chlorinating container R101~R107
Drain A03, this example set pipeline to be connected to drain A03, similary wax oil at the top of penultimate stage chlorinating container R106
Raw material is after the reaction of multistage chlorinating container, and wax oil raw material can react consumption completely with chlorine, and residual gas can be passed through directly
Drain direct emission.
Every grade of chlorinating container R101~R107 is also equipped with electric control system, the electrical control of chlorinating containers at different levels
System, which summarizes, to be connected to chain with the electric control system of liquid chlorine storage tank inlet valve after A07, can be precisely controlled chlorine feed and be added
Dosage and addition program, further improve reaction effect and product quality.
Gas recovery is also associated at the top of multistage chlorinating container R101~R107 final stage chlorinating container R107 therein
Import A04, chlorine therein returns the tail gas in tail gas recycle pipeline in A02 from A04 after processing, makes full use of chlorination former
Material, raw material availability is high, reduces wastage of material, saves production cost input.
Be also associated at the top of multistage chlorinating container R101~R107 final stage chlorinating container R107 therein Balance Air into
Mouth 06, and pass through Balance Air import A06 to ensure reaction process pressure balance, it improves product quality stability
Recycling wax oil charging is also associated at the top of multistage chlorinating container R101~R107 final stage chlorinating container R107 therein
Mouth A05, the wax oil semi-finished product that either reacted completion because can also contain a small amount of unreacted wax oil raw material in tail gas simultaneously are mixed
It is returned together in the tail gas in A02 in tail gas recycle pipeline through processing, wax oil therein from A05, makes full use of chlorizated raw material, it is former
Expect that utilization rate is high, reduce wastage of material, save production cost input.
Every grade of chlorinating container is equipped with temperature measuring equipment, chlorinating containers at different levels in multistage chlorinating container R101~R107
Temperature measuring equipment is connected to the inlet valve of liquid chlorine storage tank by electric control system, by chain control liquid chlorine inlet amount, further
Reaction process is precisely controlled, and can adapt to continuous production processes and intelligentized control method using needs.
Drain A03, which is connected in multistage chlorinating container R101~R107, is located at final stage chlorinating container R107 previous stages
Chlorinating container R106 at the top of, to reduce the mounting structure at the top of final stage chlorinating container R107, rationally utilize space.It is multistage
Potential difference is 30cm between chlorinating container R101~R107 kettles.
Wax oil treater is connected to positioned at last, wax oil treater is connected to finished product packing platform；Multistage chlorination is anti-
Answering kettle R101~R107 bottom discharges mouth, summarizing A09 by pipeline is connected directly to wax oil treater, level-one chlorination reaction simultaneously
In kettle R101 after wax oil raw material and chlorine reaction, the wax oil finished product for reacting completion is delivered directly to wax oil treater and further refines
Processing, the wax oil raw material that unreacted is completed, which enters in secondary chlorination reaction kettle R102, to be continued to react with new chlorine, successively
Analogize, until last final stage chlorinating container R107.
Wax oil treater includes thick chlorine wax groove V401, and thick chlorine wax groove V401 top feeds mouth is anti-with final stage chlorination simultaneously
The pipeline of kettle R107 bottoms semi-finished product discharging port A 08, multistage chlorinating container R101~R107 bottom discharge mouths is answered to summarize A09 companies
It connects, thick chlorine wax groove V401 is connected with the first degassing kettle R402, the second degassing kettle R402B, thick chlorine wax groove V401, the first degassing
Kettle R402, the second degassing kettle R402B bottoms finished product discharge port are connected with chlorine wax pan tank V403 and product groove tank car A102 simultaneously,
Chlorine wax pan tank V403 is connected to A101 product packaging platforms, and the pipeline of multistage chlorinating container R101~R107 bottom discharge mouths converges
Total A09 is also connected directly to chlorine wax pan tank V403, product groove tank car A102 simultaneously, and part finished product chlorinated paraffin passes through product packet
It is transported after dress platform subpackage, another part finished product chlorinated paraffin is directly transported by product groove tank car；First degassing kettle R402, second
Degassing surge tank V405 is also connected with by pipeline at the top of degassing kettle R402, the tail gas in semi-finished product subtractive process is slow by deaerating
It rushes tank V405 and is transported to device for recovering tail gas through tail gas recycle pipeline A103；Chlorine wax pan tank V403 is connected with two-stage chlorine wax finished product
Pump P-401A, P-401B.
The chlorinated paraffin continuous producing apparatus of the present invention, multistage chlorinating container arrangement setting are sequentially connected the multistage chlorine of composition
Change reactor, multistage chlorinating container forms tinuous production, easy to operate, can adapt to continuous production processes demand, uses
The input and output material mode of upper entering and lower leaving, product reaction is thorough, and chlorine feed can recycle participation reaction by device for recovering tail gas, instead
Answer effect good, raw material availability is high, and product quality is stablized, and reduces cost consumption, improves production efficiency.
Claims (9)
1. a kind of chlorinated paraffin continuous producing apparatus, it is characterised in that：Including liquid chlorine storage tank, liquid chlorine storage tank is connected with by pipeline
Liquid chlorine gasifier, liquid chlorine gasifier outlet are connected with Chlorine Buffer Vessel, and Chlorine Buffer Vessel top middle portion is connected with chlorine by pipeline
Qi leel matches platform, and chlorine distribution platform is provided with multiple chlorine gas outlets, and each chlorine gas outlet is connected with chlorinating container, and multiple chlorinations are anti-
Kettle is answered to be arranged in order setting and forms multistage chlorination reactor；
Chlorine feed pipe, wax oil feed pipe are connected separately at the top of every grade of chlorinating container, bottom is provided with discharge port, every grade of chlorine
Change reactor bottom discharge port and be consecutively connected to wax oil feed pipe at the top of subordinate's chlorinating container, positioned at primary level-one chlorination
Wax oil feed pipe is connected to wax oil storage tank at the top of reaction kettle, is connected positioned at last final stage chlorinating container bottom discharge mouth
To wax oil treater, wax oil treater is connected to finished product packing platform；Cooling device is provided with outside every grade of chlorinating container；
Offgas outlet, every grade of offgas outlet and chlorinating container offgas outlet company of subordinate are additionally provided at the top of every grade of chlorinating container
Logical, the offgas outlet of at least level-one chlorinating container is connected to tail gas recycle pipeline；
Every grade of chlorinating container is equipped with electric control system, the electric control systems of chlorinating containers at different levels summarize after connection with
Liquid chlorine storage tank inlet valve electric control system is chain；
Circulating pump is provided between every grade of chlorinating container and cooling device.
2. chlorinated paraffin continuous producing apparatus according to claim 1, it is characterised in that：The multistage chlorination reaction bottom goes out
Material mouth is connected directly to wax oil treater after summarizing simultaneously by pipeline.
3. chlorinated paraffin continuous producing apparatus according to claim 1, it is characterised in that：It is removed in the multistage chlorinating container
The offgas outlet of other outer chlorinating containers at different levels of level-one chlorinating container is connected directly to tail gas after summarizing simultaneously by pipeline
Recovery channel.
4. chlorinated paraffin continuous producing apparatus according to claim 1, it is characterised in that：In the multistage chlorinating container extremely
The offgas outlet of rare level-one chlorinating container is connected with drain.
5. chlorinated paraffin continuous producing apparatus according to claim 1, it is characterised in that：End in the multistage chlorinating container
Gas recovery import and Balance Air import are also associated at the top of grade chlorinating container.
6. chlorinated paraffin continuous producing apparatus according to claim 1, it is characterised in that：It is every in the multistage chlorinating container
Grade chlorinating container is equipped with temperature measuring equipment, and chlorinating container temperature measuring equipments at different levels are connected to liquid chlorine by electric control system and store up
The inlet valve of tank.
7. chlorinated paraffin continuous producing apparatus according to claim 4, it is characterised in that：The drain is connected to multistage chlorine
Change in reaction kettle and be located at the top of the chlorinating container of final stage chlorinating container previous stage.
8. chlorinated paraffin continuous producing apparatus according to claim 1, it is characterised in that：The multistage chlorination reactor includes
There are 7 grades of chlorinating containers.
9. chlorinated paraffin continuous producing apparatus according to claim 1, it is characterised in that：The wax oil treater includes thick chlorine
Wax groove, thick chlorine wax groove top feed mouth simultaneously with final stage chlorinating container bottom semi-finished product discharge port, multistage chlorination reaction
The pipeline of bottom portion discharge port summarizes connection, and thick chlorine wax groove is connected with the first degassing kettle, the second degassing kettle, thick chlorine wax groove,
First degassing kettle, the second degassing bottom portion finished product discharge port are connected with chlorine wax pan tank and product groove tank car, chlorine wax finished product simultaneously
Slot is connected to product packaging platform, and the pipeline of multistage chlorinating container bottom discharge mouth summarizes also while is connected directly to chlorine wax finished product
Slot, product groove tank car, by being transported after product packaging platform subpackage, another part finished product chlorinated paraffin leads to part finished product chlorinated paraffin
Product groove tank car is crossed directly to transport；First degassing kettle, the second degassing kettle top portion are also connected with degassing surge tank by pipeline, half into
Tail gas in product subtractive process is by the surge tank that deaerates through tail gas recycle pipeline to device for recovering tail gas；Chlorine wax pan tank connects
It is connected to two-stage chlorine wax discharge pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810144202.1A CN108251157A (en) | 2018-02-12 | 2018-02-12 | Chlorinated paraffin continuous producing apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810144202.1A CN108251157A (en) | 2018-02-12 | 2018-02-12 | Chlorinated paraffin continuous producing apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108251157A true CN108251157A (en) | 2018-07-06 |
Family
ID=62744485
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810144202.1A Pending CN108251157A (en) | 2018-02-12 | 2018-02-12 | Chlorinated paraffin continuous producing apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108251157A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108905862A (en) * | 2018-08-27 | 2018-11-30 | 天津金牛电源材料有限责任公司 | A kind of electrolyte automatic preparation system and its preparation method |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB815454A (en) * | 1956-11-05 | 1959-06-24 | Diamond Alkali Co | Improvements in or relating to chlorinated paraffins |
| 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 |
| CN106281457A (en) * | 2016-08-03 | 2017-01-04 | 安徽中缘新材料科技有限公司 | Chlorinated paraffin production line |
| CN208038384U (en) * | 2018-02-12 | 2018-11-02 | 丹阳市助剂化工厂有限公司 | Chlorinated paraffin continuous producing apparatus |
-
2018
- 2018-02-12 CN CN201810144202.1A patent/CN108251157A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB815454A (en) * | 1956-11-05 | 1959-06-24 | Diamond Alkali Co | Improvements in or relating to chlorinated paraffins |
| 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 |
| CN106281457A (en) * | 2016-08-03 | 2017-01-04 | 安徽中缘新材料科技有限公司 | Chlorinated paraffin production line |
| CN208038384U (en) * | 2018-02-12 | 2018-11-02 | 丹阳市助剂化工厂有限公司 | Chlorinated paraffin continuous producing apparatus |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108905862A (en) * | 2018-08-27 | 2018-11-30 | 天津金牛电源材料有限责任公司 | A kind of electrolyte automatic preparation system and its preparation method |
| CN108905862B (en) * | 2018-08-27 | 2023-11-07 | 天津金牛电源材料有限责任公司 | Automatic electrolyte preparation system and preparation method thereof |
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Application publication date: 20180706 |