CN1364759A - preparation of dialkyl dithio amino formate - Google Patents
preparation of dialkyl dithio amino formate Download PDFInfo
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- CN1364759A CN1364759A CN 01102237 CN01102237A CN1364759A CN 1364759 A CN1364759 A CN 1364759A CN 01102237 CN01102237 CN 01102237 CN 01102237 A CN01102237 A CN 01102237A CN 1364759 A CN1364759 A CN 1364759A
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Abstract
The preparation of dialkyl dithio amino formate includes: adding carbon disulfide to the mixture of sec-alkyl amine, water solution of sodium hydroxide, dichloro methane and ethanol solvent for reaction at 10-60 deg.c for 0.5-5 hr, further reaction at 50-100 deg.c for 1-12 hr, and separation of the product. The present invention has less material feeding time owing to the once addition of the raw material but carbon disulfide, less post-treatment time owing to less dichloro methane adding amount and high conversion rate.
Description
The present invention relates to the preparation of dialkyl dithio amino formate.
Oil product in use contacts the generation oxidizing reaction inevitably and goes bad with airborne oxygen and metallic surface, oil viscosity is increased, and acid number increases, and generates greasy filth and precipitation, and generation is corroded and wearing and tearing to metal parts.In oil product, add oxidation inhibitor, effectively inhibited oxidation reaction, the work-ing life of prolongation oil product, the use properties of raising oil product.
Dialkyl dithio amino formate uses in oil product, outstanding antioxidant property and good abrasion resistance and extreme pressure property are arranged, also have good oil soluble and characteristics such as ashless simultaneously, be widely used in turbine oil, hydraulic efficiency oil, gear oil, the multiple oil product of oil engine wet goods and the lubricating grease.
Dialkyl dithio amino formate generally is to be formed by dithiocarbonic anhydride and sodium hydroxide, secondary amine and methylene dichloride reaction in the prior art, and reaction generally in two steps.
US 5,015, and 368 example 1 discloses and adopted two step method to prepare the method for dialkyl dithio amino formate.The first step contains the dithiocarbonic anhydride adding in the mixture of Di-n-Butyl Amine, sodium hydroxide and water under about 63 ℃; In second step, elevated temperature to 88 ℃ adds methylene dichloride in the above-mentioned reaction mixture, lasts 4 hours, adds behind the methylene dichloride again in 85～88 ℃ of reactions 3 hours.Reaction is isolated liquid phase after finishing, and underpressure distillation obtains product again.Its nitrogen content is 6.5%, and sulphur content is 30.0%.
US 5,744, and 629 disclose the method for preparation than the dialkyl dithio amino formate of light colour.At first, the aqueous solution of sodium hydroxide and Di-n-Butyl Amine and dithiocarbonic anhydride are reacted in autoclave, controlled temperature was not higher than 15 ℃, reacts 0.5 hour, slowly splashes into excessive methylene dichloride again, and elevated temperature gradually, 75～80 ℃ of reactions 2 hours.After reaction finishes, carry out underpressure distillation in two steps, the first step, carrying out under 45～100 ℃ of temperature and under the pressure of 5～50kPa, be separated at 35～50 ℃ then, second step, isolated organic phase is carried out a underpressure distillation according to the condition of the first step again, finally can obtain ASlM color less than 2 product.
From above-mentioned introduction as can be seen, prior art generally is earlier with dithiocarbonic anhydride and sodium hydroxide and secondary amine reaction for some time, and then adds methylene dichloride and continue to react, wherein the time of drip dichloromethane longer, reaction process is more loaded down with trivial details.
The object of the present invention is to provide a kind of by changing the preparation method that order of addition(of ingredients) is saved the dialkyl dithio amino formate of operating time.
The structural formula of the said dialkyl dithio amino formate of the present invention is as follows:
Wherein R is C
2～C
10Alkyl, preferred normal-butyl.
Preparation method provided by the invention is in the mixture that contains secondary alkylamine, aqueous sodium hydroxide solution, methylene dichloride and etoh solvent, splash into dithiocarbonic anhydride in 10～60 ℃, after dropwising, kept this thermotonus 0.5～5 hour, be warming up to 50～100 ℃ again and continue reaction 1～12 hour, separated product promptly gets liquid dialkyl dithio amino formate compound.
Specifically, the inventive method adopts the synthesis under normal pressure container, once add aqueous sodium hydroxide solution, secondary amine, methylene dichloride and etoh solvent, slowly splash into (also can divide several times add) dithiocarbonic anhydride in 10～60 ℃ preferred 20～50 ℃ then, added afterreaction 0.5～5 hour, preferred 1～3 hour, so that dithiocarbonic anhydride reacts completely, be warming up to 50～100 ℃ again, preferred 50～80 ℃, continue reaction 1～12 hour, preferred 2～8 hours.After reaction finishes, add the gasoline extracting for a moment, isolate organic phase, normal, decompression steams gasoline and less water, is washed with water to neutrality again, can obtain the yellow transparent liquid product.
Said secondary alkylamine is the dialkylamine of carbon number 2～10, preferred Di-n-Butyl Amine.Because secondary alkylamine price is more expensive, boiling point is higher, reside in to be difficult in the product removing, thus should suitably increase the ratio of other raw material, so that secondary alkylamine is complete.The mol ratio of secondary alkylamine and sodium hydroxide can be 1: 1～1.8, preferred 1: 1～1.5.The mol ratio of secondary alkylamine and dithiocarbonic anhydride can be 1: 1～1.7, preferred 1: 1～1.4.The mol ratio of secondary alkylamine and methylene dichloride can be 1: 0.5～0.8, preferred 1: 0.5～0.7.Secondary alkylamine and alcoholic acid mass ratio can be 1: 0.15～1, preferred 1: 0.2～0.6.The mass concentration of aqueous sodium hydroxide solution can be 20～75%.Aqueous sodium hydroxide solution can prepare in advance, if preparation when reaction must treat that solution temperature adds other reactant again when reducing near room temperature.
Preparation method provided by the invention has saved the reinforced time, except that dithiocarbonic anhydride, the reinforced of other raw material once finished, saved the time of drip dichloromethane, simultaneously because the consumption phasor of methylene dichloride is less relatively, the step of distilled dichloromethane when also having saved aftertreatment, thus saved the operation time widely, and transformation efficiency is higher, and product performance meet the requirements.
The invention will be further described below by example.
Example 1
In being furnished with the 250ml there-necked flask of cooling tube, add 17.6g sodium hydroxide and 36.2g water, be made into aqueous sodium hydroxide solution (mass concentration 33%).Because sodium hydroxide is water-soluble to be the process of a large amount of heat releases, available cooling bath cooling for a moment, when treating that temperature is reduced to room temperature, add 51.6g Di-n-Butyl Amine, 18g ethanol, 17.7g methylene dichloride again, stir, slowly drip 31.6g dithiocarbonic anhydride, with cooling tube condensation evaporable dithiocarbonic anhydride and methylene dichloride, control reaction temperature is at 25 ℃.After dithiocarbonic anhydride adds, kept this thermotonus 1 hour.Then, be warming up to 50 ℃, reacted again 5 hours.After reaction finishes, add industrial naptha 70g, extracting 20 minutes is told pure water and solid sodium chloride with separating funnel, underpressure distillation again (vacuum tightness 650mmHg), steam to reactor temperature about about 150 ℃ no longer include gasoline and flow out till.Obtain light yellow transparent liquid at last, be product, productive rate 91%.Its nitrogen content is 6.6%, and sulphur content is 29.5%.
Example 2
In being furnished with the 250ml there-necked flask of cooling tube, add 25.6g sodium hydroxide and 36.2g water, be made into aqueous sodium hydroxide solution (mass concentration 41%).When treating that sodium hydroxide solution is room temperature, add 51.6g Di-n-Butyl Amine, 18g ethanol, 20.4g methylene dichloride again, stir, slowly drip 32.2g dithiocarbonic anhydride, with cooling tube condensation evaporable dithiocarbonic anhydride and methylene dichloride, control reaction temperature is at 40 ℃.After dithiocarbonic anhydride adds, kept this thermotonus 1 hour.Then, be warming up to 50 ℃, reacted again 5 hours.After reaction finishes, add industrial naptha 70g, tell pure water and solid sodium chloride with separating funnel after the extracting, pressure reducing and steaming gasoline and less water obtain light yellow transparent liquid again, are product, productive rate 92%.
Example 3
In being furnished with the 250ml there-necked flask of cooling tube, add 17.6g sodium hydroxide and 36.2g water, be made into aqueous sodium hydroxide solution (mass concentration 33%).When treating that sodium hydroxide solution is room temperature, add 51.6g Di-n-Butyl Amine, 25.8g ethanol, 23.8g methylene dichloride again, stir, slowly drip 33.4g dithiocarbonic anhydride, with cooling tube condensation evaporable dithiocarbonic anhydride and methylene dichloride, control reaction temperature is at 25 ℃.After dithiocarbonic anhydride adds, kept this thermotonus 2 hours.Then, be warming up to 70 ℃, reacted again 3 hours.After reaction finishes, add industrial naptha 70g, tell pure water and solid sodium chloride with separating funnel after the extracting, pressure reducing and steaming gasoline and less water obtain light yellow transparent liquid again, are product, productive rate 91%.
Example 4
Adopt ASTMD-2272 rotary oxygen bomb method that the example product is carried out oxidation test, measure oxidation induction period.Base oil is selected the HVIS 150SN of Dalian Petrochemical Industry Company, add 0.5% example product and with the trade mark be the external like product of VL-7723 (productions of Vanderbilt company) with comparison under the dosage, the result is as follows:
| Additive | Dosage, % | Inductive phase, min. |
| Example 1 | ????0.5 | ????31 |
| Example 2 | ????0.5 | ????35 |
| Example 3 | ????0.5 | ????30 |
| ????VL-7723 | ????0.5 | ????31 |
The explanation of this example adopts the dialkyl dithio amino formate of the inventive method preparation and external like product to have essentially identical performance.
Claims (7)
1. the preparation method of dialkyl dithio amino formate, comprise: in the mixture that contains secondary alkylamine, aqueous sodium hydroxide solution, methylene dichloride and etoh solvent, add dithiocarbonic anhydride in 10～60 ℃, reacted 0.5～5 hour, be warming up to 50～100 ℃ and continue reaction 1～12 hour, separated product.
2. preparation method according to claim 1 is characterized in that, splashes into or divide at 20～50 ℃ to add dithiocarbonic anhydride several times, adds afterreaction 1～3 hour, is warming up to 50～80 ℃ again, continues reaction 2～8 hours.
3. preparation method according to claim 1 is characterized in that, said secondary alkylamine is the dialkylamine of carbon number 2～10.
4. according to claim 1 or 3 described preparation methods, it is characterized in that said secondary alkylamine is a Di-n-Butyl Amine.
5. preparation method according to claim 1, it is characterized in that, the mol ratio of secondary alkylamine and sodium hydroxide is 1: 1～1.8, the mol ratio of secondary alkylamine and dithiocarbonic anhydride is 1: 1～1.7, the mol ratio of secondary alkylamine and methylene dichloride is 1: 0.5～0.8, and secondary alkylamine and alcoholic acid mass ratio are 1: 0.15～1.
6. preparation method according to claim 5, it is characterized in that, the mol ratio of secondary alkylamine and sodium hydroxide is 1: 1～1.5, the mol ratio of secondary alkylamine and dithiocarbonic anhydride is 1: 1～1.4, the mol ratio of secondary alkylamine and methylene dichloride is 1: 0.5～0.7, and secondary alkylamine and alcoholic acid mass ratio are 1: 0.2～0.6.
7. preparation method according to claim 1 is characterized in that, the mass concentration of aqueous sodium hydroxide solution is 20～75%.
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| CNB01102237XA CN1159294C (en) | 2001-01-18 | 2001-01-18 | Preparation of dialkyl dithio amino formate |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20140371483A1 (en) * | 2013-06-18 | 2014-12-18 | China Petroleum & Chemical Corporation | Process for preparing methylene bis-(dialkylamino-dithioformate) in one step |
| CN104557644A (en) * | 2013-10-09 | 2015-04-29 | 中国石油化工股份有限公司 | Method for preparing dialkyl dithiocarbamate by utilization of continuous flow tubular reactor |
| CN105001137A (en) * | 2015-08-13 | 2015-10-28 | 新乡市瑞丰新材料股份有限公司 | Method for preparing dialkyl dithio carbamic acid ester |
| CN105503676A (en) * | 2014-09-25 | 2016-04-20 | 中国石油化工股份有限公司 | Safe production method for low-chroma methylene bis(dialkyldithioformamide) |
| CN106146370A (en) * | 2016-08-04 | 2016-11-23 | 西北矿冶研究院 | Synthesis method of dialkyl dithiocarbamate |
| CN106966934A (en) * | 2017-04-07 | 2017-07-21 | 新乡市瑞丰新材料股份有限公司 | A kind of preparation method of dialkyl dithio amino formate |
| CN107200703A (en) * | 2016-03-18 | 2017-09-26 | 中国石油化工股份有限公司 | The method that Keywords dibutyl dithiocarbamate is prepared using supergravity reactor |
| CN108017566A (en) * | 2016-10-28 | 2018-05-11 | 中国石油化工股份有限公司 | A kind of purification process of lube oil additive mixed liquor |
-
2001
- 2001-01-18 CN CNB01102237XA patent/CN1159294C/en not_active Expired - Lifetime
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104230775A (en) * | 2013-06-18 | 2014-12-24 | 中国石油化工股份有限公司 | Method for preparing dialkyl aminodithioformic acid by using one-step method |
| US9006482B2 (en) * | 2013-06-18 | 2015-04-14 | China Petroleum & Chemical Corporation | Process for preparing methylene bis-(dialkylamino-dithioformate) in one step |
| US20140371483A1 (en) * | 2013-06-18 | 2014-12-18 | China Petroleum & Chemical Corporation | Process for preparing methylene bis-(dialkylamino-dithioformate) in one step |
| CN104557644B (en) * | 2013-10-09 | 2017-09-22 | 中国石油化工股份有限公司 | The method that dialkyl dithio amino formate is prepared using continuous flow tubular reactor |
| CN104557644A (en) * | 2013-10-09 | 2015-04-29 | 中国石油化工股份有限公司 | Method for preparing dialkyl dithiocarbamate by utilization of continuous flow tubular reactor |
| CN105503676A (en) * | 2014-09-25 | 2016-04-20 | 中国石油化工股份有限公司 | Safe production method for low-chroma methylene bis(dialkyldithioformamide) |
| CN105001137A (en) * | 2015-08-13 | 2015-10-28 | 新乡市瑞丰新材料股份有限公司 | Method for preparing dialkyl dithio carbamic acid ester |
| CN107200703A (en) * | 2016-03-18 | 2017-09-26 | 中国石油化工股份有限公司 | The method that Keywords dibutyl dithiocarbamate is prepared using supergravity reactor |
| CN107200703B (en) * | 2016-03-18 | 2019-06-04 | 中国石油化工股份有限公司 | The method for preparing Keywords dibutyl dithiocarbamate using supergravity reactor |
| CN106146370A (en) * | 2016-08-04 | 2016-11-23 | 西北矿冶研究院 | Synthesis method of dialkyl dithiocarbamate |
| CN108017566A (en) * | 2016-10-28 | 2018-05-11 | 中国石油化工股份有限公司 | A kind of purification process of lube oil additive mixed liquor |
| CN108017566B (en) * | 2016-10-28 | 2020-06-02 | 中国石油化工股份有限公司 | Purification method of lubricating oil additive mixed solution |
| CN106966934A (en) * | 2017-04-07 | 2017-07-21 | 新乡市瑞丰新材料股份有限公司 | A kind of preparation method of dialkyl dithio amino formate |
| CN106966934B (en) * | 2017-04-07 | 2019-01-15 | 新乡市瑞丰新材料股份有限公司 | A kind of preparation method of dialkyl dithio amino formate |
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