CN108727296A - A kind of dioxygen oxidation one-step synthesis technique of rubber accelerator dibenzothiazyl disulfide - Google Patents
A kind of dioxygen oxidation one-step synthesis technique of rubber accelerator dibenzothiazyl disulfide Download PDFInfo
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- CN108727296A CN108727296A CN201710990775.1A CN201710990775A CN108727296A CN 108727296 A CN108727296 A CN 108727296A CN 201710990775 A CN201710990775 A CN 201710990775A CN 108727296 A CN108727296 A CN 108727296A
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- China
- Prior art keywords
- mbts
- rubber accelerator
- dioxygen oxidation
- dibenzothiazyl disulfide
- ammonia
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D277/00—Heterocyclic compounds containing 1,3-thiazole or hydrogenated 1,3-thiazole rings
- C07D277/60—Heterocyclic compounds containing 1,3-thiazole or hydrogenated 1,3-thiazole rings condensed with carbocyclic rings or ring systems
- C07D277/62—Benzothiazoles
- C07D277/68—Benzothiazoles with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached in position 2
- C07D277/70—Sulfur atoms
- C07D277/76—Sulfur atoms attached to a second hetero atom
- C07D277/78—Sulfur atoms attached to a second hetero atom to a second sulphur atom
Abstract
The present invention is a kind of dioxygen oxidation one-step synthesis technique of rubber accelerator dibenzothiazyl disulfide, is comprised the step of：(1) ammonia is molten；(2) ammonium salt purifies；(3) MBTS is aoxidized；(4) MBTS finished products.A kind of dioxygen oxidation one-step synthesis processing step of rubber accelerator dibenzothiazyl disulfide of the present invention is concise, and easy to operate, the waste water of generation is few.
Description
Technical field
The present invention relates to rubber accelerator synthesis technology field more particularly to a kind of rubber accelerator diphenyl disulfide and thiophenes
The dioxygen oxidation one-step synthesis technique of azoles.
Background technology
Rubber accelerator dibenzothiazyl disulfide (MBTS) plays very important effect in Vulcanization Process of Rubber, adds
Fast rubber is reacted with vulcanizing agent, improves production efficiency, MBTS is that indispensable one kind helps in rubber accelerator industry
Agent.
About the production technology of MBTS, both at home and abroad there are also report, it is using industry that main process synthetic method, which has,
The MBT of grade synthesis is raw material, is obtained using oxidizing, oxidant mainly has nitrous acid, oxygen, chlorine, permanganic acid
Potassium etc. produces a large amount of waste water though the above method has their own advantages, and serious pollution is generated to environment, and toxicity is big, peace
Full property is low；Chlorine method oxidative synthesis MBTS, poor product quality, chlorine toxicity is big, causes serious pollution to the environment.
Patent name is：A kind of preparation method Patent No. of rubber vulcanization accelerator dibenzothiazyl disulfide：
200810183218.X patent document, it was recently reported that at 55~65 DEG C, the mixture with hydrogen peroxide and sulfuric acid is oxidant, directly
Oxidation Vencide salt is connect, obtains product MBTS, the wastewater flow rate of this process product easy to operate, per ton is reachable
To 30 tons, Water purification brings certain difficulty, production cost high.
Patent name is：Prepared by the oxygen method 2 based on 2- mercaptan benzothiazole ammonia salts, 2- dithio-bis-benzothiazoles, specially
Sharp number is：200710016805.5 patent document, it was recently reported that after MBT ammonium hydroxide or liquefied ammonia dissolving, obtain ammonium salt solution mistake
Filter, oxygen is passed through under certain temperature and pressure for addition catalyst or the air reaction regular hour obtains MBTS products, this
Process, of high cost, product yield is low.Our factory uses fine work MBT to synthesize MBTS products by alkali soluble hydrogen peroxide oxidation at present,
This process is of high cost when preparing refined MBT, and the waste water ratio that hydrogen peroxide oxidation technique generates is more.
For this purpose, the present invention designs a kind of dioxygen oxidation one-step synthesis technique of rubber accelerator dibenzothiazyl disulfide,
Solve problem above.
Invention content
The present invention is to overcome the above deficiency, provides a kind of one step of dioxygen oxidation of rubber accelerator dibenzothiazyl disulfide
Synthesis technology comprises the step of：
(1) ammonia is molten：
Crude product MBT is delivered directly to by pipeline in the stills for air blowing for containing ammonium hydroxide, stirring makes it react 0.5~1h；
The molar ratio of crude product MBT and pure ammonia is 1:1.2~6, ammonia concn is 3~15%, reaction temperature control 60~
85℃；
(2) ammonium salt purifies：
The M-NH4 salt dissolved (M ammonium salts) is delivered directly to by pipeline in stills for air blowing, oxygen is passed through and is aoxidized,
Ammonium salt solution until obtaining clear is terminal, and the temperature of oxidation reaction is controlled at 40~70 DEG C；
(3) MBTS is aoxidized：
The ammonium salt solution of clear is delivered directly to by pipeline in high-pressure oxidizing kettle, dioxygen oxidation, oxidation are passed through
At 60~85 DEG C, oxidative pressure control detects reaction solution not in 0.2~0.5MPa, using cobalt oleate as indicator for temperature control
Greening is reaction end, obtains MBTS slurries；
(4) MBTS finished products：
MBTS slurries are separated by solid-liquid separation by dryer, the mother liquor of drying directly returns the molten process of ammonia and ammonium salt purification work
Sequence, the wet feed MBTS after drying are dried, and obtain qualified rubber accelerator MBTS.
Preferably, the tail gas in step (1) reaction process can reuse after being absorbed by absorption kettle.
Preferably, the tail gas in step (2) reaction process can reuse after being absorbed by absorption kettle.
Further, the preparation of the ammonia concn uses the liquid dosage or step (3) that dryer is isolated in step (4)
The absorbing liquid of middle tail gas absorption kettle is prepared.
The beneficial effects of the invention are as follows：A kind of oxygen oxygen of rubber accelerator dibenzothiazyl disulfide of the present invention
It is concise to change one-step synthesis processing step, easy to operate, the waste water of generation is few, high income, specifically there is following advantage：
1) using crude product MBT as raw material, MBT technique subtractive processes is eliminated, technological process is shortened, it is simple for process to be easy to
Control, saves the time, reduces cost；
2) crude product MBT uses the ammonia solvent of low concentration instead of liquid caustic soda, and uses oxygen purification ammonium salt, dioxygen oxidation
MBTS will not introduce waste water, while the mother liquor dried is salt-free, does not generate brine waste；Mother liquor can direct circulation recycle, environment
It pollutes small；
3) gained MBTS good product qualities, yield is up to 94~98%, and up to 98~99%, fusing point can reach purity
171~176 DEG C.
Specific implementation mode
It is described in detail below with reference to the embodiment of the present invention.
A kind of dioxygen oxidation one-step synthesis technique of rubber accelerator dibenzothiazyl disulfide, comprises the step of：
(1) ammonia is molten：
Crude product MBT is delivered directly to by pipeline in the stills for air blowing for containing ammonium hydroxide, stirring makes it react 0.5~1h；
The molar ratio of crude product MBT and pure ammonia is 1:1.2~6, ammonia concn is 3~15%, reaction temperature control 60~
85℃；
(2) ammonium salt purifies：
The M-NH4 salt dissolved (M ammonium salts) is delivered directly to by pipeline in stills for air blowing, oxygen is passed through and is aoxidized,
Ammonium salt solution until obtaining clear is terminal, and the temperature of oxidation reaction is controlled at 40~70 DEG C；
(3) MBTS is aoxidized：
The ammonium salt solution of clear is delivered directly to by pipeline in high-pressure oxidizing kettle, dioxygen oxidation, oxidation are passed through
At 60~85 DEG C, oxidative pressure control detects reaction solution not in 0.2~0.5MPa, using cobalt oleate as indicator for temperature control
Greening is reaction end, obtains MBTS slurries；
(4) MBTS finished products：
MBTS slurries are separated by solid-liquid separation by dryer, the mother liquor of drying directly returns the molten process of ammonia and ammonium salt purification work
Sequence, the wet feed MBTS after drying are dried, and obtain qualified rubber accelerator MBTS.
Gained MBTS good product qualities, yield is up to 94~98%, and for purity up to 98~99%, fusing point can reach 171
~176 DEG C.
Preferably, the tail gas in step (1) reaction process can reuse after being absorbed by absorption kettle；
Preferably, the tail gas in step (2) reaction process can reuse after being absorbed by absorption kettle.
Further, the preparation of the ammonia concn uses the liquid dosage or step (3) that dryer is isolated in step (4)
The absorbing liquid of middle tail gas absorption kettle is prepared.
Principle：
Using crude product MBT as raw material, MBT technique subtractive processes are eliminated, shorten technological process, it is simple for process to be easy to control
System, saves the time, reduces cost；
Crude product MBT uses the ammonia solvent of low concentration instead of liquid caustic soda, and uses oxygen purification ammonium salt, dioxygen oxidation
MBTS will not introduce waste water, while the mother liquor dried is salt-free, does not generate brine waste；Mother liquor can direct circulation recycle, environment
It pollutes small.
The above is only a preferred embodiment of the present invention, it is noted that for the ordinary skill people of the art
For member, various improvements and modifications may be made without departing from the principle of the present invention, these improvements and modifications are also answered
It is considered as protection scope of the present invention.
Claims (4)
1. a kind of dioxygen oxidation one-step synthesis technique of rubber accelerator dibenzothiazyl disulfide, which is characterized in that including
Step has：
(1) ammonia is molten：
Crude product MBT is delivered directly to by pipeline in the stills for air blowing for containing ammonium hydroxide, stirring makes it react 0.5~1h；
The molar ratio of crude product MBT and pure ammonia is 1:1.2~6, ammonia concn is 3~15%, and reaction temperature is controlled at 60~85 DEG C；
(2) ammonium salt purifies：
The M-NH4 salt dissolved is delivered directly to by pipeline in stills for air blowing, oxygen is passed through and is aoxidized, until being clarified
Transparent ammonium salt solution is terminal, and the temperature of oxidation reaction is controlled at 40~70 DEG C；
(3) MBTS is aoxidized：
The ammonium salt solution of clear is delivered directly to by pipeline in high-pressure oxidizing kettle, dioxygen oxidation, oxidizing temperature are passed through
At 60~85 DEG C, oxidative pressure control detects reaction solution not greening in 0.2~0.5MPa, using cobalt oleate as indicator for control
For reaction end, MBTS slurries are obtained；
(4) MBTS finished products：
MBTS slurries are separated by solid-liquid separation by dryer, the mother liquor of drying directly returns the molten process of ammonia and ammonium salt purification process,
Wet feed MBTS after drying is dried, and obtains qualified rubber accelerator MBTS.
2. a kind of dioxygen oxidation one-step synthesis work of rubber accelerator dibenzothiazyl disulfide according to claim 1
Skill, which is characterized in that the tail gas in step (1) reaction process can reuse after being absorbed by absorption kettle.
3. a kind of dioxygen oxidation one-step synthesis of rubber accelerator dibenzothiazyl disulfide according to claim 1 or 2
Technique, which is characterized in that the tail gas in step (2) reaction process can reuse after being absorbed by absorption kettle.
4. a kind of dioxygen oxidation one-step synthesis work of rubber accelerator dibenzothiazyl disulfide according to claim 3
Skill, which is characterized in that the preparation of the ammonia concn uses the liquid dosage or step (3) that dryer is isolated in step (4)
The absorbing liquid of middle tail gas absorption kettle is prepared.
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Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4307236A (en) * | 1979-11-02 | 1981-12-22 | Akzona Incorporated | Process for the preparation of dithiazole-disulfides |
| CN101215272A (en) * | 2008-01-16 | 2008-07-09 | 天津市科迈化工有限公司 | Method of producing rubber vulcanization accelerator DM |
| CN101717378A (en) * | 2009-11-16 | 2010-06-02 | 天津市科迈化工有限公司 | Method for synthesizing rubber vulcanization accelerator DM by oxygen oxidization |
| CN102167686A (en) * | 2011-03-17 | 2011-08-31 | 郑州大学 | Method for preparing 2,2'-dibenzothiazyl disulfide by catalyzing oxidation through molecular oxygen |
| CN102350350A (en) * | 2011-08-29 | 2012-02-15 | 科迈化工股份有限公司 | Catalysts used in production of promoter 2,2'-dithiobisbenzothiazole, and preparation method thereof |
| CN102367237A (en) * | 2011-09-20 | 2012-03-07 | 科迈化工股份有限公司 | Method for producing medical DM by taking oxygen as oxidizing agent |
| CN105175353A (en) * | 2015-10-15 | 2015-12-23 | 内蒙古科迈化工有限公司 | Method for performing ammonolysis on oxygen to obtain rubber accelerator MBT by oxidization-synthesis |
| CN107163002A (en) * | 2017-06-16 | 2017-09-15 | 蔚林新材料科技股份有限公司 | A kind of method that oxygen method prepares rubber vulcanization accelerator DM |
-
2017
- 2017-10-23 CN CN201710990775.1A patent/CN108727296A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4307236A (en) * | 1979-11-02 | 1981-12-22 | Akzona Incorporated | Process for the preparation of dithiazole-disulfides |
| CN101215272A (en) * | 2008-01-16 | 2008-07-09 | 天津市科迈化工有限公司 | Method of producing rubber vulcanization accelerator DM |
| CN101717378A (en) * | 2009-11-16 | 2010-06-02 | 天津市科迈化工有限公司 | Method for synthesizing rubber vulcanization accelerator DM by oxygen oxidization |
| CN102167686A (en) * | 2011-03-17 | 2011-08-31 | 郑州大学 | Method for preparing 2,2'-dibenzothiazyl disulfide by catalyzing oxidation through molecular oxygen |
| CN102350350A (en) * | 2011-08-29 | 2012-02-15 | 科迈化工股份有限公司 | Catalysts used in production of promoter 2,2'-dithiobisbenzothiazole, and preparation method thereof |
| CN102367237A (en) * | 2011-09-20 | 2012-03-07 | 科迈化工股份有限公司 | Method for producing medical DM by taking oxygen as oxidizing agent |
| CN105175353A (en) * | 2015-10-15 | 2015-12-23 | 内蒙古科迈化工有限公司 | Method for performing ammonolysis on oxygen to obtain rubber accelerator MBT by oxidization-synthesis |
| CN107163002A (en) * | 2017-06-16 | 2017-09-15 | 蔚林新材料科技股份有限公司 | A kind of method that oxygen method prepares rubber vulcanization accelerator DM |
Non-Patent Citations (1)
| Title |
|---|
| 魏伟涛: "粗品MBT（M）氧气氧化一步合成橡胶促进剂MBTS（DM）", 《中国橡胶》 * |
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Application publication date: 20181102 |