CN2926233Y - Reactor for continuous chlorinated paraffin production - Google Patents
Reactor for continuous chlorinated paraffin production Download PDFInfo
- Publication number
- CN2926233Y CN2926233Y CN 200620040753 CN200620040753U CN2926233Y CN 2926233 Y CN2926233 Y CN 2926233Y CN 200620040753 CN200620040753 CN 200620040753 CN 200620040753 U CN200620040753 U CN 200620040753U CN 2926233 Y CN2926233 Y CN 2926233Y
- Authority
- CN
- China
- Prior art keywords
- reactor
- recycle stock
- outlet
- chlorine
- tail gas
- 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.)
- Expired - Lifetime
Links
Images
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The utility model relates to a reactor for producing the serialization chlorinated paraffin, which comprises a reactor main body, an ultraviolet lamp, a recycle stock outlet, a paraffin oil inlet, a reaction product outlet and a tail gas outlet. The utility model is characterized in that the reactor also comprises a recycle stock and chlorine inlet device; the ultraviolet lamp is arranged in the reactor; the paraffin oil inlet is positioned on the upper part of the reactor; the recycle stock outlet is positioned on the upper part of the reactor; the reaction product outlet is arranged on the superior reactor; the recycle stock and chlorine inlet device is positioned on the base of the reactor; and the tail gas outlet is arranged on the top of the reactor. The reactor of the present invention prepares the chlorinated paraffin; the chlorine enters the reactor from the recycle stock and chlorine inlet device on the reactor base; flows from bottom to top; simultaneously with the stock in the reaction kettle from bottom to top accelerats the circular flow; prevents the frit phenomenon causing of the chlorination local heat-liberation oversize; and thereby avoids production accidents.
Description
Technical field
The utility model relates to a kind of reactor that continuous chloroparaffin is produced that is used for.
Background technology
Clorafin is a kind of important industrial raw material, as being used for the extender plasticizer of polyvinyl chloride, and can also be as antithrombotics, tackifier, paint stablizer etc.
Because the importance of clorafin in industrial application, so the optimization of its production equipment and production method have caused that people pay close attention to widely.
Disclosed a kind of reactor that continuous chloroparaffin is produced that is used among the Chinese patent CN02148592.5, the inlet of raw material chlorine is arranged on the top of reactor, therefore, the chlorine skewness that feeds, local chlorination phenomenon is serious, and reactor bottom " imitation frosted glass " can't effectively solve, chlorine conversion is not high, the chlorine content of carrying secretly in the hydrogen chloride tail gas that reaction produces is also higher simultaneously, thereby has influenced a pair quality product of producing hydrochloric acid, and therefore industrial accident often takes place.
Summary of the invention
The utility model technical issues that need to address are to disclose a kind of reactor that continuous chloroparaffin is produced that is used for, to overcome the above-mentioned defective that prior art exists.
Reactor of the present utility model comprises reactor body, ultraviolet lamp, recycle stock outlet, recycle stock and chlorine access to plant, paraffin oil inlet, reacting product outlet and tail gas outlet.It is characterized in that, also comprise recycle stock and chlorine access to plant, said ultraviolet lamp is installed in the reactor, the paraffin oil inlet is arranged on the top of reactor, the recycle stock outlet is arranged on the top of reactor, reacting product outlet is arranged on the upper lateral part of reactor, and recycle stock and chlorine access to plant are arranged on the bottom of reactor, and the tail gas outlet is arranged on reactor head.
Adopt reactor made clorafin of the present utility model, chlorine is entered in the reactor by the recycle stock and the chlorine access to plant of reactor bottom, bottom-up flowing, circulate with the bottom-up quickening of material in reactor simultaneously, prevent the excessive grog phenomenon that causes of chlorination reaction localized heat release, thereby avoid taking place industrial accident.
Description of drawings
Fig. 1 is the structure of reactor synoptic diagram.
Fig. 2 is recycle stock and chlorine access to plant structural representation.
Embodiment
Referring to Fig. 1, reactor of the present utility model comprises reactor body 1, ultraviolet lamp, recycle stock outlet 102, recycle stock and chlorine access to plant 103, paraffin oil inlet 104, reacting product outlet 105 and tail gas outlet 106;
Said ultraviolet lamp is installed in the reactor, paraffin oil inlet 104 is arranged on the top of reactor, recycle stock outlet 102 is arranged on the top of reactor, reacting product outlet 105 is arranged on the upper lateral part of reactor, recycle stock and chlorine access to plant 103 are arranged on the bottom of reactor, and tail gas outlet 106 is arranged on reactor head.
Referring to Fig. 2, said recycle stock and chlorine access to plant 103 comprise T shape mixing tube 113 and nozzle 114, nozzle 114 is arranged on an end of T shape mixing tube 113, the intracavity inter-connection of jet exit and T shape mixing tube 113, and the other end of T shape mixing tube 113 is connected with reactor;
According to the preferred scheme of the utility model, said nozzle 114 is a laddertron, and height H is 250～350mm, and upper base L1 length is 40～60mm, and the length L of going to the bottom 2 is 80～120mm.
According to the preferred scheme of the present invention, the height of reactor body 1 and the ratio of diameter are: highly: diameter=2.5～6: 1 according to utility model.
Claims (4)
1. one kind is used for the reactor that continuous chloroparaffin is produced, comprise reactor body (1), ultraviolet lamp, recycle stock outlet (102), paraffin oil inlet (104), reacting product outlet (105) and tail gas go out (106), it is characterized in that, also comprise recycle stock and chlorine access to plant (103), said ultraviolet lamp is installed in the reactor, paraffin oil inlet (104) is arranged on the top of reactor, recycle stock outlet (102) is arranged on the top of reactor, reaction product goes out the upper lateral part that (105) are arranged on reactor, recycle stock and chlorine access to plant (103) are arranged on the bottom of reactor, and tail gas outlet (106) is arranged on reactor head.
2. reactor according to claim 1, it is characterized in that, said recycle stock and chlorine access to plant (103) comprise T shape mixing tube (113) and nozzle (114), nozzle (114) is arranged on an end of T shape mixing tube (113), the intracavity inter-connection of jet exit and T shape mixing tube (113), the other end of T shape mixing tube (113) is connected with reactor.
3. reactor according to claim 2 is characterized in that, said nozzle (114) is a laddertron, and height H is 250～350mm, and upper base L1 length is 40～60mm, and the length L of going to the bottom 2 is 80～120mm.
4. according to claim 1,2 or 3 described reactors, it is characterized in that the height of reactor body (1) and the ratio of diameter are: highly: diameter=2.5～6: 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620040753 CN2926233Y (en) | 2006-04-03 | 2006-04-03 | Reactor for continuous chlorinated paraffin production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620040753 CN2926233Y (en) | 2006-04-03 | 2006-04-03 | Reactor for continuous chlorinated paraffin production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2926233Y true CN2926233Y (en) | 2007-07-25 |
Family
ID=38280474
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620040753 Expired - Lifetime CN2926233Y (en) | 2006-04-03 | 2006-04-03 | Reactor for continuous chlorinated paraffin production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2926233Y (en) |
-
2006
- 2006-04-03 CN CN 200620040753 patent/CN2926233Y/en not_active Expired - Lifetime
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101632909B (en) | Ball dropper used for drop ball forming of oxide | |
| JP5359082B2 (en) | Trichlorosilane production apparatus and trichlorosilane production method | |
| KR20100085852A (en) | Apparatus for producing trichlorosilane and method for producing trichlorosilane | |
| CN104971668B (en) | A kind of device and method of continuous preparing chlorinated polyvinyl chloride by gas-solid phase method | |
| CN101801899A (en) | Process for the selective oxidation of methane | |
| CN100371426C (en) | Continuous chloroparaffin production apparatus | |
| CN102060269B (en) | Fluidized bed oxygen permeable membrane reactor and method for producing synthesis gas containing hydrogen | |
| CN2926233Y (en) | Reactor for continuous chlorinated paraffin production | |
| CN101229915A (en) | Method for producing hydrogen peroxide by anthraquinone process | |
| CN1424381A (en) | Devices for continuously producing chlorinated paraffin | |
| CN113716526A (en) | Combustion reactor for producing high-purity electronic grade hydrogen bromide and equipment thereof | |
| CN100420731C (en) | Coal hydrogenation reaction device and its industrial application | |
| CN104108683B (en) | A kind of stable chlorine dioxide reactor | |
| CN101486466A (en) | Fluid bed reactor for producing trichlorosilane and gas distributor thereof | |
| CN217068844U (en) | Multistage atomization photocatalytic chlorination efficient reaction tower for producing chlorinated ethylene carbonate | |
| CN202909706U (en) | Efficient gas-liquid reactor | |
| CN215917355U (en) | Reaction device for synthesizing nano calcium carbonate by using carbon dioxide | |
| CN206168211U (en) | A reactor and smoke treatment device for flue gas is handled | |
| CN104338419B (en) | A kind of hydrogen chloride combined absorbing tower | |
| CN210065673U (en) | Ultraviolet light catalytic reaction system for chlorinated paraffin production | |
| CN201305577Y (en) | Continuous chlorcosane production device provided with liquid seal device | |
| CN202785646U (en) | Hydrogen sulfide generator for hydrogen sulfide production | |
| CN104986940A (en) | Glass fusing device and fusing method thereof for prolonging service life | |
| CN201362599Y (en) | Fluidized bed reactor for producing trichlorosilane | |
| CN1169608C (en) | Self-cleaning gas-liquid reactor with three-phase spray bed |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20070725 |
|
| EXPY | Termination of patent right or utility model |