CN1872845A - Method and equipment for preparing 2 - benzothiazole sulphenamide - Google Patents
Method and equipment for preparing 2 - benzothiazole sulphenamide Download PDFInfo
- Publication number
- CN1872845A CN1872845A CN 200510072366 CN200510072366A CN1872845A CN 1872845 A CN1872845 A CN 1872845A CN 200510072366 CN200510072366 CN 200510072366 CN 200510072366 A CN200510072366 A CN 200510072366A CN 1872845 A CN1872845 A CN 1872845A
- Authority
- CN
- China
- Prior art keywords
- mercaptobenzothiazole
- water
- preparation
- hydrogen peroxide
- amine
- 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.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 15
- GPNLWUFFWOYKLP-UHFFFAOYSA-N s-(1,3-benzothiazol-2-yl)thiohydroxylamine Chemical compound C1=CC=C2SC(SN)=NC2=C1 GPNLWUFFWOYKLP-UHFFFAOYSA-N 0.000 title abstract 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 46
- YXIWHUQXZSMYRE-UHFFFAOYSA-N 1,3-benzothiazole-2-thiol Chemical compound C1=CC=C2SC(S)=NC2=C1 YXIWHUQXZSMYRE-UHFFFAOYSA-N 0.000 claims abstract description 40
- 238000006243 chemical reaction Methods 0.000 claims abstract description 27
- 239000002994 raw material Substances 0.000 claims abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 24
- 238000002360 preparation method Methods 0.000 claims description 16
- -1 amine compound Chemical class 0.000 claims description 12
- PAFZNILMFXTMIY-UHFFFAOYSA-N cyclohexylamine Chemical compound NC1CCCCC1 PAFZNILMFXTMIY-UHFFFAOYSA-N 0.000 claims description 11
- 238000003756 stirring Methods 0.000 claims description 6
- 150000001412 amines Chemical class 0.000 claims description 5
- 238000009413 insulation Methods 0.000 claims description 4
- 239000002904 solvent Substances 0.000 claims description 3
- 238000010792 warming Methods 0.000 claims description 3
- 238000002425 crystallisation Methods 0.000 claims description 2
- 230000008025 crystallization Effects 0.000 claims description 2
- 238000001556 precipitation Methods 0.000 claims description 2
- 150000003141 primary amines Chemical class 0.000 claims description 2
- 150000003335 secondary amines Chemical class 0.000 claims description 2
- 238000000967 suction filtration Methods 0.000 claims description 2
- YBRBMKDOPFTVDT-UHFFFAOYSA-N tert-butylamine Chemical compound CC(C)(C)N YBRBMKDOPFTVDT-UHFFFAOYSA-N 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- 238000013019 agitation Methods 0.000 claims 1
- 239000007800 oxidant agent Substances 0.000 abstract description 2
- 230000001590 oxidative effect Effects 0.000 abstract description 2
- 125000002924 primary amino group Chemical class [H]N([H])* 0.000 abstract 1
- 125000000467 secondary amino group Chemical class [H]N([*:1])[*:2] 0.000 abstract 1
- 239000000047 product Substances 0.000 description 20
- 230000003647 oxidation Effects 0.000 description 7
- 238000007254 oxidation reaction Methods 0.000 description 7
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N diphenyl Chemical compound C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 4
- 239000012452 mother liquor Substances 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- WYKHSBAVLOPISI-UHFFFAOYSA-N 2-phenyl-1,3-thiazole Chemical compound C1=CSC(C=2C=CC=CC=2)=N1 WYKHSBAVLOPISI-UHFFFAOYSA-N 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 2
- 235000010290 biphenyl Nutrition 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- AFZSMODLJJCVPP-UHFFFAOYSA-N dibenzothiazol-2-yl disulfide Chemical compound C1=CC=C2SC(SSC=3SC4=CC=CC=C4N=3)=NC2=C1 AFZSMODLJJCVPP-UHFFFAOYSA-N 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- DEQZTKGFXNUBJL-UHFFFAOYSA-N n-(1,3-benzothiazol-2-ylsulfanyl)cyclohexanamine Chemical compound C1CCCCC1NSC1=NC2=CC=CC=C2S1 DEQZTKGFXNUBJL-UHFFFAOYSA-N 0.000 description 2
- 239000011541 reaction mixture Substances 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- YWWOEPOBDHZQEJ-UHFFFAOYSA-N s-(4-cyclohexyl-1,3-benzothiazol-2-yl)thiohydroxylamine Chemical compound C1=CC=C2SC(SN)=NC2=C1C1CCCCC1 YWWOEPOBDHZQEJ-UHFFFAOYSA-N 0.000 description 2
- 229910052938 sodium sulfate Inorganic materials 0.000 description 2
- 235000011152 sodium sulphate Nutrition 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- QAZLUNIWYYOJPC-UHFFFAOYSA-M sulfenamide Chemical compound [Cl-].COC1=C(C)C=[N+]2C3=NC4=CC=C(OC)C=C4N3SCC2=C1C QAZLUNIWYYOJPC-UHFFFAOYSA-M 0.000 description 2
- LIWQXTCHJDFLDP-UHFFFAOYSA-N 2-(1,3-thiazol-2-yl)benzenethiol Chemical compound SC1=CC=CC=C1C1=NC=CS1 LIWQXTCHJDFLDP-UHFFFAOYSA-N 0.000 description 1
- 101100493820 Caenorhabditis elegans best-1 gene Proteins 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 206010013786 Dry skin Diseases 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 1
- 239000005708 Sodium hypochlorite Substances 0.000 description 1
- 239000002390 adhesive tape Substances 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 238000005576 amination reaction Methods 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000007810 chemical reaction solvent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004949 mass spectrometry Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000005311 nuclear magnetism Effects 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 1
- 229960005076 sodium hypochlorite Drugs 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005486 sulfidation Methods 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 238000004073 vulcanization Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Images
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
This invention relates to method and equipment for preparing 2-benzothiazolesulfenamide by using mercaptobenzothiazole and primary amine or secondary amine as the raw materials and hydrogen peroxide as the oxidant. The equipment is added with a connecting pipe, so that condenser of the reactor is connected with the dropping pipe via the connecting pipe, and the reaction is performed in a reaction system that is isolated from outer space and forms pressure equilibrium in the reactor. The product yield is higher than 96% and the purity is 98.7-99.5%.
Description
Technical field
It is method and the device that oxygenant prepares the 2-[4-morpholinodithio sulphenamide that the present invention is specifically related to the hydrogen peroxide.
Background technology
The sulphenamide compounds is a kind of aftereffect thiofide commonly used, and its scorching quality is good, and vulcanization rate is fast, and slight, the no blooming of variable color in sulfidation can significantly improve the tensile modulus and the tensile strength of cross-linked rubber.Therefore be widely used in making in the goods such as tire, rubber overshoes, adhesive tape, cable.
N-cyclohexyl benzo thiazolesulfenamide (accelerator CBS) is the principal item of sulfenamide type accelerators, and present production method mainly contains four kinds of hypochlorite oxidation methods, dioxygen oxidation method, non-oxidation agent synthesis method, hydrogen peroxide oxidation process.Domestic preparation accelerator CBS hypochlorous sodium oxidation style is main, and the problem of existence is that main raw material hexahydroaniline and 2-benzothiazolyl mercaptan (captax) adopt big proportioning, and it is very difficult further to improve product yield; And wastewater treatment is relatively more difficult, and environmental pollution is more serious.Adopt hydrogen peroxide oxidation process to compare with sodium-hypochlorite process, the oxidation capacity under alkaline condition is suitable, and can alleviate environmental pollution, and solves inorganic salt problem in the mother liquor, is more promising CBS preparation method therefore.Propose with chlorine bleach, chlorine and hydrogen peroxide as oxygenant among the US2419283.Also need add a certain amount of sulfuric acid and caustic soda in the reaction, generate the sodium sulfate of byproduct.In its embodiment relevant with hydrogen peroxide, sulfuric acid and hydrogen peroxide mix the back and together add as oxygenant, obtain the sulphenamide product yield after reaction finishes and reach 93.5%, if remove sodium sulfate, product yield can only reach 79.5～85.3%.Li Ming newly wait (Li Mingxin etc. the rubber vulcanizing accelerator CBS new synthetic process. " Liaoning chemical industry ", 1996.26 (3): 26-27) also adopt hydrogen peroxide to make oxygenant and prepare sulfenamide type accelerators, its accelerator CBS once through yield is up to 81.2%, and mother liquor returns three yields continuously and reaches 95%.Disclose among the WO9313084 a kind of with simple be the method for oxidant production 2-[4-morpholinodithio sulphenamide with the hydrogen peroxide, obtaining the highest yield of product in the example is 94.8%.Purity is 99.1%, and fusing point is 100 ℃ (top grade product).
Summary of the invention
The object of the invention provides a kind of preparation method of accelerator CBS, and another object of the present invention provides the device of a kind of CBS of preparation, can obtain higher product yield.
The adding of (WO9313084) amine compound mainly is disposable adding mode in the prior art, because amination reaction is thermopositive reaction, the disposable adding of amine compound is easy to generate the gathering of reactant and intermediate product, is unfavorable for subsequent reactions; Simultaneously, also make temperature of reaction be difficult to control and stable, influence reaction effect.Therefore, the present invention proposes the mode that amine compound adds continuously in reaction process, can solve problems of the prior art effectively, and the productive rate of product is further improved.
As oxygenant, with 2-mercaptobenzothiazole (captax), its an alkali metal salt or its disulphide (altax) and primary amine or secondary amine reaction prepare the 2-[4-morpholinodithio sulphenamide with hydrogen peroxide in the present invention.Specifically: in the reactor that band stirs, add solvent and mercaptobenzothiazole earlier; Drip amine compound under 25～35 ℃ temperature, amine compound can be preferably hexahydroaniline for hexahydroaniline, TERTIARY BUTYL AMINE etc., and its dropping time is 30～40 minutes; Dropwise back insulation at least 15 minutes; Continue to be warming up to 40～85 ℃, stir down and drip aqueous hydrogen peroxide solution again, the dropping time is 3h～6h; Dropwised back insulation at least 30 minutes, and treated all to generate below the crystallization postcooling to 20 ℃, through precipitation, suction filtration, washing, dry desired product.
With respect to the consumption of sulfydryl phenyl thiazole, amine compound and hydrogen peroxide are preferably excessive among the present invention.Consider that based on economy and product selectivity two aspects the mol ratio of mercaptobenzothiazole and amine is 1: 1.15～2.5, be preferably 1: 1.35～2.1; The mol ratio of mercaptobenzothiazole and hydrogen peroxide is 1: 1.0～1.38, best 1: 1.1～1.3; Hydrogen peroxide adds with the form of the aqueous solution, and its concentration has certain requirement, crosses the low or too high selectivity that all can reduce product, and the mass percent concentration that suggestion is adopted is 7～30%; Reaction solvent can be water, triethylamine, ethanol, Virahol etc., be preferably water, but a large amount of water can reduce product yield, therefore, the total amount of the water in the reaction mixture should not surpass 1500g water/mole mercaptobenzothiazole, be preferably 1200g water/mole mercaptobenzothiazole, optimum is 900g water/mole mercaptobenzothiazole, and said here Total Water should be the summation that generates water in required water of reaction and the chemical reaction process.
Method of the present invention is preferably in one to outer closure, internally forms in the reaction system of internal recycle to carry out.Its advantage is: on the one hand, hydrogen peroxide can produce the part decomposition in the dropping process for a long time, seal by system, can further improve the utilization ratio of hydrogen peroxide, particularly can obviously reduce the mol ratio (amine of the prior art is than about 1: 3) of sulfydryl phenyl thiazole and amine compound.
Carry out in closed system for realization response, the present invention provides the device of a kind of CBS of preparation again.Comprise reactor 1, condenser 2, minim pipette 3, it is characterized in that condenser 2 is connected by a pipe connecting 4 with minim pipette 3, when amine compound or hydrogen peroxide after minim pipette splashes into reaction flask, the a small amount of volatilization gas that produces is by the prolong cooling for reflux, but still have the part volatilization gas to enter pipe connecting, feed minim pipette through pipe connecting and continue to participate in reaction, at this moment, reaction system is complete closed to external world, has formed a circulation path in system inside and has reached a kind of reaction pressure balance.
Among the present invention, the liquid that obtains after the filtration can also be participated in new preparation process whole or in part, and repeated multiple times, still can obtain high yield, highly purified CBS product.
The present invention adopts the mode of continuous adding amine compound, and product yield is compared with prior art further improved, and again in conjunction with enclosed appts provided by the invention, a yield of product can reach more than 96% product purity 98.7%～99.5%.
Description of drawings
The synoptic diagram of Fig. 1 CBS preparation facilities provided by the invention
Embodiment
In a 1000ml reaction flask that agitator, reflux cooler, thermometer and measurement instrument be housed, add the 2-sulfydryl phenyl thiazole (captax, 0.5 mole) and the 220 gram water of 87.5 grams 95.8%, stir also and be warming up to 35 ℃ behind the thorough mixing; 78 gram hexahydroaniline (0.75 mole) are added dropwise in the reaction mixture gradually, and hexahydroaniline dropwised at 35 minutes; Be incubated 15 minutes; Be warmed up to 48 ℃ again, under the violent stirring, drip 0.65 mole of aqueous hydrogen peroxide solution of 17.5%, the dropping time of aqueous hydrogen peroxide solution is 4.8 hours; Insulation also continues to stir 30 minutes.When being cooled to below 20 ℃, throw out is leached, with hexahydroaniline aqueous solution Returning utilization, the filter cake deionized water wash obtains 125.6 products that restrain 50～60 ℃ of dryings.Through element, infrared, nuclear-magnetism and mass spectroscopy, prove that product is a N cyclohexyl 2 benzothiazole sulfenamide.Product yield is 95.4%, purity 99.4%, fusing point 99.5-103.3 ℃ (top grade product).
With embodiment 1 way, adopt the apparatus structure of accompanying drawing 1, make in the system that is reflected at sealing and carry out.The yield of cyclohexyl-benzothiazole sulphenamide that obtain this moment is 96.45%, purity 99.3%, fluxing point 99.0-103.5 ℃.
With embodiment 2 ways, the mother liquor 237g among the embodiment 2 is added in the reaction flask as solution, the amount of hexahydroaniline is 17g in the mother liquor by analysis, the water yield is 220g, newly adds hexahydroaniline 61g.The yield of cyclohexyl-benzothiazole sulphenamide that obtain this moment is 97.3%, purity 99.1%, fluxing point 99.0-103.8 ℃.
Comparative Examples 1
With embodiment 1 way, difference is that the N-cyclohexyl that obtains-phenyl thiazole sulphenamide yield is 94.1% with in the disposable adding reaction flask of hexahydroaniline, purity 99.2%, fusing point 99.0-102.8 ℃.
Adopt the step identical with embodiment 1, with phenylbenzene thiazolyl-2,2-disulphide replacement 2-mercaptobenzothiazole.With 166 gram phenylbenzene thiazolyls-2,2-disulphide (0.5 mole), 0.68 mole of hexahydroaniline and 450 gram water are brought in the reaction, and are heated to 48 ℃.Under this temperature and in 4.5 hours, 105 gram aqueous hydrogen peroxide solutions (0.56 mole) are added drop-wise in the reaction system.The product yield 94.6% that finally obtains, purity 98.7%, 99.2～103.1 ℃ of fusing points.
Comparative Examples 2
Adopt the way identical with embodiment 4, difference is in the disposable adding reaction flask of amine aqueous solution.Can obtain 93.8% yield, purity 99.1%, 99.3～103.6 ℃ of fusing points.
Claims (11)
1. a method for preparing the 2-[4-morpholinodithio sulphenamide is a raw material with mercaptobenzothiazole and primary amine, secondary amine, and hydrogen peroxide is an oxygenant, it is characterized in that carrying out as follows:
1) under the agitation condition solvent and mercaptobenzothiazole are joined in the reactor;
2) drip amine compound continuously under 25～35 ℃ of temperature, the mol ratio of mercaptobenzothiazole and amine is 1: 1.15～2.5, and the dropping time is 30～40 minutes;
3) dropwise back insulation at least 15 minutes;
4) continue to be warming up to 40～85 ℃, stir down and drip aqueous hydrogen peroxide solution, the mol ratio of mercaptobenzothiazole and hydrogen peroxide is 1: 1.0～1.38, and the dropping time is 3～6 hours;
5) dropwised the back temperature at least 30 minutes;
6) treat all to generate below the crystallization postcooling to 20 ℃ precipitation, suction filtration, washing, dry desired product.
2. method according to claim 1 is characterized in that amine compound is hexahydroaniline, TERTIARY BUTYL AMINE.
3. preparation method according to claim 2, the mol ratio that it is characterized in that mercaptobenzothiazole and amine is 1: 1.35～2.1.
4. preparation method according to claim 3, the mol ratio that it is characterized in that mercaptobenzothiazole and hydrogen peroxide is 1: 1.1～1.3.
5. preparation method according to claim 4, the mass percent concentration that it is characterized in that hydrogen peroxide is 7～30%.
6. preparation method according to claim 5 is characterized in that solvent is a water.
7. preparation method according to claim 6, the summation that generates water in water that it is characterized in that reacting required and the chemical reaction process is no more than 1500g water/mole mercaptobenzothiazole.
8. preparation method according to claim 7, the summation that generates water in water that it is characterized in that reacting required and the chemical reaction process is no more than 1200g water/mole mercaptobenzothiazole.
9. preparation method according to claim 8, the summation that generates water in water that it is characterized in that reacting required and the chemical reaction process is no more than 900g water/mole mercaptobenzothiazole.
10. the preparation method one of described according to claim 1 to 9, it is characterized in that reacting one to outer closure, internally form in the pressure balanced reaction system and carry out.
11. realize the device of claim 10 preparation 2-[4-morpholinodithio sulphenamide, comprise reactor (1), condenser (2), minim pipette (3), it is characterized in that condenser (2) is connected by a pipe connecting (4) with minim pipette (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100723660A CN100404518C (en) | 2005-05-31 | 2005-05-31 | Method and equipment for preparing 2 - benzothiazole sulphenamide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100723660A CN100404518C (en) | 2005-05-31 | 2005-05-31 | Method and equipment for preparing 2 - benzothiazole sulphenamide |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1872845A true CN1872845A (en) | 2006-12-06 |
| CN100404518C CN100404518C (en) | 2008-07-23 |
Family
ID=37483467
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2005100723660A Expired - Fee Related CN100404518C (en) | 2005-05-31 | 2005-05-31 | Method and equipment for preparing 2 - benzothiazole sulphenamide |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100404518C (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102796060A (en) * | 2012-08-28 | 2012-11-28 | 山东邹平开元化工石材有限公司 | Production technique of vulcanization accelerator CZ |
| CN103508978A (en) * | 2013-09-30 | 2014-01-15 | 科迈化工股份有限公司 | Method for producing rubber vulcanization accelerator CZ with two-dropping method |
| CN103508977A (en) * | 2013-09-30 | 2014-01-15 | 科迈化工股份有限公司 | Method for producing rubber vulcanization accelerator CZ by adopting double-dripping method using hydrogen peroxide as oxidizing agent |
| CN104193697A (en) * | 2014-09-15 | 2014-12-10 | 河南省开仑化工有限责任公司 | Novel oxidation method of rubber vulcanization accelerator CZ (C13H16N2S2) |
| CN104610193A (en) * | 2014-12-29 | 2015-05-13 | 内蒙古科迈化工有限公司 | Preparation method of rubber vulcanizing accelerator TBBS |
| CN106699685A (en) * | 2016-12-22 | 2017-05-24 | 蔚林新材料科技股份有限公司 | Method for preparing N-cyclohexyl-2-benzothiazole sulfonamide serving as rubber vulcanization accelerator |
| CN108727299A (en) * | 2017-10-23 | 2018-11-02 | 科迈化工股份有限公司 | A kind of synthesis technology of vulcanization accelerator N- tertiary butyls -2- benzothiazole sulfonamides |
| CN110523332A (en) * | 2019-09-16 | 2019-12-03 | 山东尚舜化工有限公司 | A kind of device and method of continuous production aniline fluid bed |
| CN110627740A (en) * | 2019-09-30 | 2019-12-31 | 山东尚舜化工有限公司 | Novel environment-friendly production method of accelerator CBS without waste salt and wastewater |
| CN112625003A (en) * | 2020-12-30 | 2021-04-09 | 蔚林新材料科技股份有限公司 | N-cyclohexyl-2-benzothiazole sulfonamide and synthesis process thereof |
| CN113636986A (en) * | 2021-10-14 | 2021-11-12 | 科迈化工股份有限公司 | Process for synthesizing accelerator CBS by MBTS air oxidation |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2126336A1 (en) * | 1991-12-21 | 1993-07-08 | Ludwig Eisenhuth | Process for producing benzothiazolyl-2-sulphenamides |
| CN1069489A (en) * | 1992-08-28 | 1993-03-03 | 沈阳化工学院 | A kind of reparation technology of thiofide |
-
2005
- 2005-05-31 CN CNB2005100723660A patent/CN100404518C/en not_active Expired - Fee Related
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102796060A (en) * | 2012-08-28 | 2012-11-28 | 山东邹平开元化工石材有限公司 | Production technique of vulcanization accelerator CZ |
| CN103508978A (en) * | 2013-09-30 | 2014-01-15 | 科迈化工股份有限公司 | Method for producing rubber vulcanization accelerator CZ with two-dropping method |
| CN103508977A (en) * | 2013-09-30 | 2014-01-15 | 科迈化工股份有限公司 | Method for producing rubber vulcanization accelerator CZ by adopting double-dripping method using hydrogen peroxide as oxidizing agent |
| CN104193697A (en) * | 2014-09-15 | 2014-12-10 | 河南省开仑化工有限责任公司 | Novel oxidation method of rubber vulcanization accelerator CZ (C13H16N2S2) |
| CN104610193A (en) * | 2014-12-29 | 2015-05-13 | 内蒙古科迈化工有限公司 | Preparation method of rubber vulcanizing accelerator TBBS |
| CN106699685A (en) * | 2016-12-22 | 2017-05-24 | 蔚林新材料科技股份有限公司 | Method for preparing N-cyclohexyl-2-benzothiazole sulfonamide serving as rubber vulcanization accelerator |
| CN108727299A (en) * | 2017-10-23 | 2018-11-02 | 科迈化工股份有限公司 | A kind of synthesis technology of vulcanization accelerator N- tertiary butyls -2- benzothiazole sulfonamides |
| CN110523332A (en) * | 2019-09-16 | 2019-12-03 | 山东尚舜化工有限公司 | A kind of device and method of continuous production aniline fluid bed |
| CN110523332B (en) * | 2019-09-16 | 2021-07-02 | 山东尚舜化工有限公司 | Equipment and method for continuously producing vulcanization accelerator CBS |
| CN110627740A (en) * | 2019-09-30 | 2019-12-31 | 山东尚舜化工有限公司 | Novel environment-friendly production method of accelerator CBS without waste salt and wastewater |
| CN112625003A (en) * | 2020-12-30 | 2021-04-09 | 蔚林新材料科技股份有限公司 | N-cyclohexyl-2-benzothiazole sulfonamide and synthesis process thereof |
| CN112625003B (en) * | 2020-12-30 | 2023-11-28 | 蔚林新材料科技股份有限公司 | N-cyclohexyl-2-benzothiazole sulfenamide and synthesis process thereof |
| CN113636986A (en) * | 2021-10-14 | 2021-11-12 | 科迈化工股份有限公司 | Process for synthesizing accelerator CBS by MBTS air oxidation |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100404518C (en) | 2008-07-23 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100404518C (en) | Method and equipment for preparing 2 - benzothiazole sulphenamide | |
| CN106745246B (en) | A kind of method for preparing vanadic sulfate | |
| WO2018000404A1 (en) | Method for preparing taurine | |
| CN104945286A (en) | Method for compounding high-purity sulfuric acid esters | |
| CN101717379B (en) | Production method of rubber vulcanizing accelerator CBS | |
| CN106866466A (en) | A kind of method for synthesizing N-acetylsulfanilyl chloride as sulfonating agent with sulfur trioxide | |
| CN117986162B (en) | Preparation method of ethyl sulfonyl chloride | |
| CN105037295A (en) | Method for producing sulfenamide rubber vulcanization accelerator | |
| CN106083672B (en) | A kind of synthetic method of β-mercaptopropionic acid | |
| CN110330468A (en) | A kind of synthetic method of 4,4 '-dithio morpholines | |
| CN102367238A (en) | Method for synthesizing accelerator N,N-dicyclohexyl-2-benzothiazole sulfenamide | |
| CN101906082A (en) | Method for synthesizing TBBS (Tertiarybutyl Benzothiazole Sulfenamide) by mechanically applying mother solution | |
| CN104230844A (en) | Preparation method of vulcanization accelerator CZ | |
| CN115650243B (en) | Method for separating and recovering fluorine and silicon in fluorine-containing silicon slag in one step | |
| CN106316981A (en) | Preparation method of N-cyclohexyl-2-benzothiazolesulfenamide | |
| CN110143922A (en) | A kind of synthetic method of 1,1 '-dicaprolactam disulfides | |
| CN114195736B (en) | Preparation method of 2-amino-5-bromo-1, 3, 4-thiadiazole | |
| CN108912019A (en) | The method that one kind recycling mantoquita and ethyl alcohol from D, L- Su Shi-D-4-methylsulfonylphserine serine ethyl ester mother liquor | |
| CN106185835B (en) | A kind of method that vulcanized sodium is prepared using starch low-temperature reduction | |
| CN104230764A (en) | Preparation method of 2-acrylamide-2-methyl propanesulfonic acid | |
| CN110156691A (en) | A kind of preparation method of curing dicaprolactam | |
| CN1310880C (en) | Improved process for preparing 2-sodium naphthalenesulfonate in production of beta-naphthol | |
| CN110256318A (en) | A kind of clean method for producing of tetra-benzyl thiram disulfide | |
| CN118063354B (en) | Synthesis method of high-purity p-toluenesulfonyl chloride | |
| CN108727298A (en) | It is a kind of using 2- benzothiazolyl mercaptans and tert-butylamine as the clean synthesis process of Material synthesis vulcanization accelerator TBSI |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080723 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |