CN202185176U - Extraction kettle for extracting and purifying 2-sulfydryl benzothiazole by solvent method - Google Patents
Extraction kettle for extracting and purifying 2-sulfydryl benzothiazole by solvent method Download PDFInfo
- Publication number
- CN202185176U CN202185176U CN2011202265526U CN201120226552U CN202185176U CN 202185176 U CN202185176 U CN 202185176U CN 2011202265526 U CN2011202265526 U CN 2011202265526U CN 201120226552 U CN201120226552 U CN 201120226552U CN 202185176 U CN202185176 U CN 202185176U
- Authority
- CN
- China
- Prior art keywords
- kettle
- mercapto benzothiazole
- film forming
- toluene
- forming chamber
- 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 - Fee Related
Links
Images
Landscapes
- Extraction Or Liquid Replacement (AREA)
Abstract
An extraction kettle for extracting and purifying 2-sulfydryl benzothiazole by a solvent method is disclosed, and comprises a kettle body (4). An agitating device (3) is arranged at the top of the kettle body (4), an atomizer (2) is arranged in the upper part of the kettle body (4) and a filter screen (6) is arranged in the lower part of the kettle body. A mother liquid cavity (9) is formed between the filer screen (6) and the bottom of the kettle. A mother liquid outlet (7) and 2-sulfydryl benzothiazole outlet (8) are arranged at the bottom of the kettle body. In the utility model, synthesized high temperature liquid (180-220 DEG C) coarse 2-sulfydryl benzothiazole is pressed from a high pressure kettle to a sealed extraction kettle with nitrogen and sprayed to powder in the atomizer sprayer to be directly contacted with methylbenzene (normal temperature) for high-low temperature interchanging extraction so as to improve the solubility of resin in methylbenzene and stabilize the fineness of 2-sulfydryl benzothiazole. In addition, the high-low temperature interchanging extraction technology not only improves the extraction precision, but also solves the problem on explosion of mixture of methylbenzene steam and air so as to achieve the technological innovation from open manual operation to sealed operation.
Description
Technical field
The utility model belongs to the purification technique field of 2-mercapto benzothiazole, is specifically related to a kind of extraction kettle that is used for solvent extraction purification 2-mercapto benzothiazole.
Background technology
Thiofide 2-mercapto benzothiazole (MBT) is widely used a kind of universal promoter in the rubber industry, is the maximum product of at present domestic and international thiofide volume of production and marketing, also is simultaneously the primary raw material of producing other promoter.High-load MBT still produces the primary raw material of cephalosporin analog antibiotic medicine.But the MBT purity that high pressure is synthesized is low, contains plurality of impurities (being referred to as resin), can not directly use.Therefore, the refining purification process of MBT becomes a very important step in its production.The production method of present domestic rubber vulcanization accelerant MBT has two kinds: the one, and the soda acid WATER-WASHING METHOD; The 2nd, solvent extraction.The soda acid WATER-WASHING METHOD is present domestic the most frequently used process for refining and purifying, accounts for dominant position.This method will consume a large amount of strong acid, highly basic and water, produces product per ton and can produce the high concentration saliferous organic basic waste water more than 45 tons, the post processing difficulty.Solvent extraction is present more novel process for refining and purifying.Along with the increasing of environmental protection dynamics, refining purification technique of solvent extraction and non-aqueous technique more and more receive people's attention.The solvent that existing solvent method uses is main with toluene mainly.Shortcomings such as but this technology is the opened type manually-operated, and extractant evaporates in the air, has severe operational environment, and labour intensity is big.
The utility model content
The purpose of the utility model is to solve the above-mentioned technical problem that exists in the prior art, and a kind of extraction kettle that is used for thiofide 2-mercapto benzothiazole totally enclosed type production system is provided.
For realizing above-mentioned purpose, the technical scheme that the utility model adopts is following:
The extraction kettle that is used for solvent extraction purification 2-mercapto benzothiazole of the utility model; Comprise kettle; Be provided with agitating device at the kettle top, be provided with atomizer, be provided with screen pack in the kettle bottom on kettle top; Constitute the mother liquor chamber between at the bottom of screen pack and the still, autoclave body bottom is provided with mother liquor outlet and the outlet of 2-mercapto benzothiazole.
Described atomizer comprises the atomizer housing, is provided with the atomizer shower nozzle in case top, and shower nozzle is provided with toluene feed mouth and 2-mercapto benzothiazole charging aperture; Housing top is provided with the oxygen content test port, and housing sidewall is provided with vacuum orifice, adds nitrogen mouth and venting, and housing bottom is provided with discharging opening.
Described atomizer shower nozzle comprises head body, is provided with the toluene feed tube that is communicated with the toluene feed mouth on head body top, and the toluene feed tube is communicated with the toluene film forming chamber; On the sidewall of head body, be provided with the 2-mercapto benzothiazole feed tube that is communicated with 2-mercapto benzothiazole charging aperture; 2-mercapto benzothiazole feed tube is communicated with 2-mercapto benzothiazole film forming chamber; Toluene liquid film forming chamber bottom is connected with 2-mercapto benzothiazole film forming chamber bottom, and the head body bottom is provided with mixture export.
Described toluene film forming chamber is cylindric.
Described 2-mercapto benzothiazole film forming chamber is cylindric.
Described toluene film forming chamber bottom is a conically shaped with the place of being connected, 2-mercapto benzothiazole film forming chamber bottom.
Outside kettle, be provided with chuck, chuck is provided with cooling water inlet and cooling water outlet.
High-temperature liquid state after the utility model will synthesize (180-220 ℃) crude 2-mercapto benzene a pair of horses going side by side thiazole in autoclave with in nitrogen pressure to the airtight extraction kettle; Directly carry out high low temperature at atomizer shower nozzle internal spraying Cheng Fenyu toluene (normal temperature) and exchange extraction; Thereby improved the solubility of resin in toluene, and stablized the fineness of 2-mercapto benzothiazole.High in addition low temperature exchanges cold abstraction technique and has not only improved the extraction precision, has also thoroughly solved the blast problem of toluene steam and air mixture, has realized the technological innovation of being shifted to closed-loop operation by uncovered type manually-operated fully.
Description of drawings
Fig. 1 is the structural representation of the utility model.
Fig. 2 is the structural representation of the atomizer in the utility model.
Fig. 3 is the structural representation of atomizer in the utility model.
The specific embodiment
The extraction kettle that is used for solvent extraction purification 2-mercapto benzothiazole of the utility model is as shown in Figure 1; Comprise kettle 4; Be provided with agitating device 3 at kettle 4 tops, be provided with atomizer 2, be provided with 300 order screen packs 6 in the kettle bottom on kettle 4 tops; Constitute mother liquor chamber 9 between at the bottom of screen pack 6 and the still, autoclave body bottom is provided with mother liquor outlet 7 and 2-mercapto benzothiazole outlet 8.
Described atomizer is as shown in Figure 2, comprises atomizer housing 18, is provided with atomizer shower nozzle 16 at housing 18 tops, and shower nozzle 16 is provided with toluene feed mouth 15 and 2-mercapto benzothiazole charging aperture 14; Housing top is provided with oxygen content test port 13, is used to test oxygen content in the atomizer.Housing sidewall is provided with vacuum orifice 12, adds nitrogen mouth 11 and venting 17, and housing 18 bottoms are provided with discharging opening 19.
Described atomizer shower nozzle is as shown in Figure 3, comprises head body 16-1, is provided with the toluene feed tube 16-3 that is communicated with toluene feed mouth 15 on head body 16-2 top, and toluene feed tube 16-1 is communicated with toluene film forming chamber 16-5; Described toluene film forming chamber 16-5 is cylindric.On the sidewall of head body 16-2, be provided with the 2-mercapto benzothiazole feed tube 16-1 that is communicated with 2-mercapto benzothiazole charging aperture 14; 2-mercapto benzothiazole feed tube 16-1 is communicated with 2-mercapto benzothiazole film forming chamber 16-4, and described 2-mercapto benzothiazole film forming chamber 16-4 is cylindric.Toluene liquid film forming chamber 16-5 bottom is connected with 2-mercapto benzothiazole film forming chamber 16-4 bottom, and described toluene film forming chamber 16-5 bottom is a conically shaped with the place of being connected, 2-mercapto benzothiazole film forming chamber 16-4 bottom.Head body 16-2 bottom is provided with mixture export 16-7.
The operation principle of the utility model is following: before charging; Close mother liquor outlet 7 and 2-mercapto benzothiazole outlet 8 on toluene feed mouth 15,2-mercapto benzothiazole charging aperture 14 and the extraction kettle on the atomizer; Vacuumize through vacuum orifice on the atomizer; Make in the extraction kettle vacuum to-0.085MPa, charge into through the nitrogen mouth that adds on the atomizer that vacuum is-0.02 MPa in nitrogen to the atomizer then.Open toluene feed mouth 15 and 2-mercapto benzothiazole charging aperture 14 then successively; Extractant toluene gets into through toluene feed tube 16-3; Form the annular film through toluene film forming chamber 16-5, treat that extracting substance 2-mercapto benzothiazole gets into through 2-mercapto benzothiazole feed tube 16-1, forms circular membrane through 2-mercapto benzothiazole film forming chamber 16-4; Two circular membrane cross in connection place of liquid film forming chamber, and mixing material fully extracts through discharging opening entering extraction kettle after the atomizing in atomizer.Mixing material stirs further mixed dissolution through agitating device 3 in extraction kettle, mother liquor (mixed liquor of toluene and resin) gets into mother liquor chamber 9 through screen pack 6, discharges through mother liquor outlet 7; The 2-mercapto benzothiazole is discharged through 2-mercapto benzothiazole outlet 8.
Claims (7)
1. extraction kettle that is used for solvent extraction purification 2-mercapto benzothiazole; Comprise kettle (4); It is characterized in that: be provided with agitating device (3) at kettle (4) top, be provided with atomizer (2), be provided with screen pack (6) in the kettle bottom on kettle (4) top; Constitute mother liquor chamber (9) between at the bottom of screen pack (6) and the still, autoclave body bottom is provided with mother liquor outlet (7) and 2-mercapto benzothiazole outlet (8).
2. the extraction kettle that is used for solvent extraction purification 2-mercapto benzothiazole according to claim 1; It is characterized in that: described atomizer comprises atomizer housing (18); Be provided with atomizer shower nozzle (16) at housing (18) top, shower nozzle (16) is provided with toluene feed mouth (15) and 2-mercapto benzothiazole charging aperture (14); Housing top is provided with oxygen content test port (13), and housing sidewall is provided with vacuum orifice (12), adds nitrogen mouth (11) and venting (17), and housing (18) bottom is provided with discharging opening (19).
3. the extraction kettle that is used for solvent extraction purification 2-mercapto benzothiazole according to claim 2; It is characterized in that: described atomizer shower nozzle comprises head body (16-1); Be provided with the toluene feed tube (16-3) that is communicated with toluene feed mouth (15) on head body (16-2) top, toluene feed tube (16-1) is communicated with toluene film forming chamber (16-5); On the sidewall of head body (16-2), be provided with the 2-mercapto benzothiazole feed tube (16-1) that is communicated with 2-mercapto benzothiazole charging aperture (14); 2-mercapto benzothiazole feed tube (16-1) is communicated with 2-mercapto benzothiazole film forming chamber (16-4); Toluene liquid film forming chamber (16-5) bottom is connected with 2-mercapto benzothiazole film forming chamber (16-4) bottom, and head body (16-2) bottom is provided with mixture export (16-7).
4. the extraction kettle that is used for solvent extraction purification 2-mercapto benzothiazole according to claim 2 is characterized in that: described toluene film forming chamber (16-5) is cylindric.
5. the extraction kettle that is used for solvent extraction purification 2-mercapto benzothiazole according to claim 2 is characterized in that: described 2-mercapto benzothiazole film forming chamber (16-4) is cylindric.
6. the extraction kettle that is used for solvent extraction purification 2-mercapto benzothiazole according to claim 2 is characterized in that: described toluene film forming chamber (16-5) bottom is a conically shaped with the place of being connected, 2-mercapto benzothiazole film forming chamber (16-4) bottom.
7. according to any described extraction kettle that is used for solvent extraction purification 2-mercapto benzothiazole of claim 1-6, it is characterized in that: outside kettle, be provided with chuck (5), chuck (5) is provided with cooling water inlet (10) and cooling water outlet (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202265526U CN202185176U (en) | 2011-06-30 | 2011-06-30 | Extraction kettle for extracting and purifying 2-sulfydryl benzothiazole by solvent method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202265526U CN202185176U (en) | 2011-06-30 | 2011-06-30 | Extraction kettle for extracting and purifying 2-sulfydryl benzothiazole by solvent method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202185176U true CN202185176U (en) | 2012-04-11 |
Family
ID=45916655
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011202265526U Expired - Fee Related CN202185176U (en) | 2011-06-30 | 2011-06-30 | Extraction kettle for extracting and purifying 2-sulfydryl benzothiazole by solvent method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202185176U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102327702A (en) * | 2011-06-30 | 2012-01-25 | 鹤壁市恒瑞橡塑材料有限公司 | Extraction kettle for extracting and purifying 2-mercapto benzothiazole through solvent process |
| CN107158744A (en) * | 2016-03-08 | 2017-09-15 | 神华集团有限责任公司 | Extraction tower, extract and separate system and coal tar extraction process |
-
2011
- 2011-06-30 CN CN2011202265526U patent/CN202185176U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102327702A (en) * | 2011-06-30 | 2012-01-25 | 鹤壁市恒瑞橡塑材料有限公司 | Extraction kettle for extracting and purifying 2-mercapto benzothiazole through solvent process |
| CN102327702B (en) * | 2011-06-30 | 2013-12-11 | 鹤壁市恒瑞橡塑材料有限公司 | Extraction kettle for extracting and purifying 2-mercapto benzothiazole through solvent process |
| CN107158744A (en) * | 2016-03-08 | 2017-09-15 | 神华集团有限责任公司 | Extraction tower, extract and separate system and coal tar extraction process |
| CN107158744B (en) * | 2016-03-08 | 2019-05-03 | 神华集团有限责任公司 | Extraction tower, extraction and separation system and coal tar extraction process |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105524014B (en) | Purification method of rubber vulcanization accelerator 2-mercaptobenzothiazole | |
| CN202185176U (en) | Extraction kettle for extracting and purifying 2-sulfydryl benzothiazole by solvent method | |
| CN102516806A (en) | Method for extracting capsorubin and capsaicine by utilizing continuous countercurrent ultrasonic extracting machine | |
| CN101671374A (en) | Novel process for extracting D-glucosamine hydrochloride | |
| CN102850292A (en) | Totally enclosed clean production system for rubber vulcanization accelerator 2-mercaptobenzothiazole | |
| CN102327702B (en) | Extraction kettle for extracting and purifying 2-mercapto benzothiazole through solvent process | |
| CN102936025B (en) | Micro and nano-grade active light calcium carbonate automated production system | |
| CN104649898A (en) | Method and device for producing 2-naphthol and coproducing 2,3 acid by solvent method continuous carbonization | |
| CN202185177U (en) | Atomizer for extracting and purifying 2-sulfydryl benzothiazole by solvent method | |
| CN202133259U (en) | Stereo spiral dryer | |
| CN215310346U (en) | Pentaerythritol solvent recovery tower | |
| CN102295620A (en) | Co-production synthesizing technology of rubber vulcanization promoter NS | |
| CN204619973U (en) | A kind of reactor for the production of inositol | |
| CN202036956U (en) | Premixing device | |
| CN202186953U (en) | Totally closed-type production system for thiofide 2-mercapto benzothiazole | |
| CN102249970A (en) | Process for synthesizing doripenem lateral chain | |
| CN106635112A (en) | Hydrothermal liquidization system and hydrothermal liquidization method for biomass | |
| CN106542953A (en) | A kind of preparation method of lycopene crystal | |
| CN202942707U (en) | Three-leg type jacket suction filter | |
| CN102602940B (en) | Method for producing high-performance white carbon black and succinic acid by comprehensively utilizing white spirit lees | |
| CN207811280U (en) | Circulating ammonia coupled reaction is filtered, washed, drying system | |
| CN101723806B (en) | Method for extracting borneol by using supercritical CO2 fluid turbulences | |
| CN207085365U (en) | A kind of resin alambique | |
| CN205599244U (en) | Traditional chinese medicine concentrate granulator | |
| CN205613387U (en) | High -efficient reation kettle with damping device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: HENAN HENGRUI RUBBER-PLASTIC TECHNOLOGY CO., LTD.. Free format text: FORMER OWNER: HEBI HENGRUI RUBBER-PLASTIC TECHNOLOGY CO., LTD.. Effective date: 20121101 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20121101 Address after: Hebi City, Henan province Xunxian County 456250 Li Yang Zhen Yang Di Cun Patentee after: HENAN HENGRUI RUBBER PLASTIC SCIENCE AND STOCK CO., LTD. Address before: Hebi City, Henan province Xunxian County 456250 Li Yang Zhen Yang Di Cun Patentee before: Hebi Hengrui Rubber Plastic Material Co.,Ltd. |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Extraction kettle for extracting and purifying 2-mercapto benzothiazole through solvent process Effective date of registration: 20130918 Granted publication date: 20120411 Pledgee: Bank of China Limited by Share Ltd Hebi branch Pledgor: HENAN HENGRUI RUBBER PLASTIC SCIENCE AND STOCK CO., LTD. Registration number: 2013990000684 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120411 Termination date: 20170630 |