Method of preparing 2-vinylpyridine

专利摘要:
Verfahren zur katalytischen, selektiven Herstellung von 2-Vinylpyridin aus Acetylen und Acrylnitril mit Hilfe von Cyclopentadienyl-Cobalt-Katalysatoren bzw. π-Allyl-Cobald-Katalysatoren bei erhöhter Temperatur unter Verwendung einer mit Acetylen gesättigten Lösung des Nitrils in inerten Lösungsmitteln, wobei die Acrylnitrilkonzentration bis zu 2 Mol/1 beträgt und die Umsetzung bei Temperaturen oberhalb von 140°C bis 180°C während einer Reaktionsdauer von höchstens 50 Minuten durchgeführt wird.
公开号:SU888817A3
申请号:SU792809608
申请日:1979-09-13
公开日:1981-12-07
发明作者:Беннеманн Хельмут；Самсон Марк
申请人:Штудиенгезельшафт Коле Мбх(Фирма)；
IPC主号:

专利说明:

(3) METHOD OF OBTAINING 2-V11NILPYRIDINE
The invention relates to an improved, improved, method for producing 2-vinylpyridine, which is used as a component of adhesion agents in the tire industry and as a comonomer in the manufacture of acrylic fibers. A known method for producing 2-vinyl pyridine from acetylene and acrylonitrile in the presence of cyclopentadienylcobalt catalysts. At a nitrile concentration of 2.1 mol / l, a temperature of 100 ° C and a contact time of k h, 75% of the desired product 1} is obtained. The disadvantage of this method is the relatively low yield of the product. The aim of the invention is to increase the yield of the target product. To achieve this, when carrying out the method of producing 2-vinylpyridine, which involves the interaction of acetylene with acrylonitrile, the process is carried out at 1 0 -80 ° C, the concentration of acrylonitrile OT 0.1 to 2 mol / L and contact less than 50 min. When choosing a temperature, 150-1bO is preferred. The reaction time is from 5 to 50 minutes, but it can also be below 5 minutes, up to the order of seconds, if appropriate devices are used, such as hydraulic pipes. The reaction time is preferably from 15 to 30 minutes. The concentration of acrylinitrile lies in the range from about 0.1 mol / L to 2 mol / L or also higher. The concentration of acrylnitrile is preferably at or above 1 mol / L. The solvents used are those that are inert with respect to the reaction reagents in the specified temperature range. Such are aliphatic solvents and in particular aromatic solvents such as benzene or toluene.
3
The process is carried out in a pressure vessel with a good mixing device so that during the conversion the solution is saturated with acetylene. At the same time, the pressure of acetylene lies between 5 and 20 atm, preferably between 8 and 17 atm.
Suitable catalysts are heat-resistant cobalt compounds that contain at least one cyclopentadienyl bound to cobalt, such as bis-cyclopentadienylcobalt (cobaltocene), cyclopentadienylcobalt-cyclooctadiene, cyclopentadienylcobalt-dicarbonyl, but also J-allyco-boiled compounds
 The method can be carried out periodically or continuously, either in a cascade of boilers with agitators, or in a hydraulic pipe, and the outflow stream should be rapidly cooled. The catalyst is used in the form of pre-prepared cobalt compounds, but it can also be obtained in the reaction mixture.
These conditions allow an increase in the yield to 93.
1Trimer 1-0.12 g (o, 52 mmol of cyclopentadienylcobaltcycloocta- (1,5) -diene is dissolved in 2 + 1, 6 ml of toluene and mixed with 14.05 g (2b4.8 mmol) of acrylonitrile, and the resultant 259.1 ml of a 1.02 M nitrile solution, including a catalyst. It is absorbed at 20 ° C in a 500 ml autoclave of special steel with a metal stirrer. At 7 bar, the acetylene solution is saturated and heated for 15 minutes to 150 ° C and the pressure rises by siphoning acetylene. The spent acetylene is quickly replenished. After 30 minutes of contact time, the vessel operating under pressure It is brought to 30 ° C with external cooling for 1 O min.
233 g of the crude product is removed from the autoclave and the volatile constituents are condensed at 0.2 Torr, with 1.90 g of residue remaining. According to gas chromatographic analysis, the condensate in the amount of 230.0 g contains 8.13 g of acrylonitrile and 10.88 g of 2-vinylpyridine.
Output, counting on converted acrylonitrile 93 2-vinylpyridine.
Catalyst consumption: 200 mol pyridine / g At Cobalt.
7. 4
Example 2. The process is carried out according to Example 1, but cobaltocene is used as a catalyst.
Load 0.2 g (1.06 mmol) of cobaltocene, 13.05 g (246 mmol) of acrinitrile, 209.9 g (242 ml) of toluene, to obtain a 0.95 M solution.
Reaction temperature, contact time at 148C 50 min.
Reaction unloading, g 231.20.
Condensate (0.2 torr), g 227.70
Residue, g. 3.05
Result (according to gas chromatographic analysis);
6.25 g of unconverted acrylonitrile
10.44 g 2-B1 /,: nilpyridine
Output, counting on converted acrylonitrile, 78% 2-vinylpyridine.
Catalyst consumption: 94 mol pyridine / g At Cobalt.
Example 3. The process is carried out according to Example 1, but J-cyclopentadienyl dicarbonyl cobalt is used as a catalyst.
Load 0.135 g (0.86 mmol) I (CO), 20.7 g (390.6 mmol) of acrylonitrile, 203.5 g (234 ml) of toluene, and a 1.50 M solution is obtained.
The reaction temperature is 155 ° C, howling contact at 30 minutes.
Reaction unloading, g 229.5 Condensate (0.2 Torr), g 228.3 Residue, g 0.7
Result (according to gas chromatographic analysis): 15.12 g of unconverted acrylonitrile 8.89 g of 2-8 vinylpyridine. Output, calculated on converted acrylonitrile 80.4 2-vinylpyridine. Catalyst consumption: 98 mol pyridine / g At Cobalt.
Example 4. The process is carried out according to Example 1, but J-cyclopentadienyl- (1-exo-trichloromethylclopentadienecobalt,
About, 245 g (O, 797 mmol) of ZG-C5H5CoC5H / C1 2 ,, 13, b5 g (257.6 mmolT of acrylonitrile and 206.4 g (237 ml) of toluene are charged, a 1.02 M solution is obtained.
The reaction temperature is 150 ° C, the contact time at 150 ° C is 30 minutes.
Reaction unloading, g223,6
Condensate (0.2 torr), g222.8

权利要求:
Claims (3)
[1]
Residue, g0.6 Result (according to chromatographic analysis): 9.73 g of unconverted acrylonitrile 6.37 g of 2-vinylpyridine Yield, calculated for converted acrylonitrile, 2-vinylpyridine. Catalyst consumption: 7b mol of pyridine / g At Cobalt. Example 5. The process is carried out as described in Example 1, but J-cyclopentadienyl- (1-exo-cyanomethylene cyclopentadiene-cobalt is used as a catalyst. Load is 0.206 g (0.897 mmol) J-CjHjCoCjHfCH CN, 16.25 g (goiter, 6 mmol) acrylnitrile and 209.6 (2 + 1 ml) toluene, get 1.17 M solution. Reaction temperature 155 ° C, contact time at 30 minutes. Reaction discharge, g 236.75 Condensate (0.2 Torr), g 232, 6 Residue, gk, Q Result (according to gas chromatographic analysis): 7.27 g of unconverted acrylonitrile 13.7 g of 2-vinylpyridine. Output, calculated on converted acrylonitrile, 77 2-vinylpyridine. Alizator: k6 mol pyridine / g At Coba Example 6. 0.2 g (0.9 mmol of methylheptadienylbutadiene cobalt at -30 ° C. is dissolved in 233 ml of toluene and mixed with 0.05 g (O, 9 mmol) of pentadiene monomer tion. Heated to 20 ° C, 19.2 g (Zb2.3 mmol of acrylonitrile (a 1, + M solution of acrylonitrile in toluene is obtained) and then carried out as in Example 1. The reaction temperature is 155 ° C, contact time at 155 ° From 30 min. Reaction discharge, g 227.9 Condensate (0.2 Torr), g 225.8 Residue, g 1.85 Result (according to gas chromatographic analysis): 12.69 g of unconverted acrylonitrile and 9.7 g of 2-vinylpyridine. Output, counting on converted acrylonitrile, 75.2 2-vinylpyridine. Catalyst consumption: 103 mol pyridine / g At Cobalt. Example 7. The process is carried out according to Example 1, but 1-indenylcyclooctadiene-1, 5-cobalt is used as a catalyst. 0.1 (92 g (0.529 mmol) indenylcobalt-COO, 26.20 g 76 (, 3 mmol) acrylonitrile {1, b5 and), 231.25 g of toluene are charged. Reaction temperature lAO C, contact time at 20 min. Reaction unloading, g 271.15 Condensate (0.2 torr), g 268.3 Residue, g2, 6 Result (according to gas chromatographic analysis): 16.79 g of unconverted acrylonitrile and 16, t g of 2-vinylpyridine. Output, counting on converted acrylonitrile, 88% 2-vinylpyridine. Catalyst consumption: 29 mol pyridine / g At Cobalt. Example 8. 101.4 mg (0.3595 mmol) of l-indenylcobalt-COO are dissolved in 151 i8 g of toluene and mixed with 19.0 (358.5 mmol) of acrylonitrile, and 200 ml of a 1.79 M nitrile solution are obtained, including catalyst. At 20 ° C, this solution is loaded into a 500 ml autoclave from special steel. The solution is saturated with acetylene at 7 bar. Heat up to for 12 minutes, and the pressure (by reaching acetylene to 18.5 bar) is increased and kept constant. After 17 minutes of reaction time, 105.5 mg (0.37 mmol) of indenyl-cobalt-C00, dissolved in 29.9 g of toluene, are dosed over 6 minutes. After 18 minutes of reaction time at 145 ° C, cool the pressure vessel for 10 minutes to 25 ° C. Reaction time tl min, reaction temperature 145 ° C, reaction unloading 210.7 g; condensate (0.2 torr) 206.6 g residue 2.9 g. Result (according to gas chromatographic analysis): 9.31 g of unconverted acrylonitrile and 15, g of 2-vinylpyridine; Output, counting on converted acrylonitrile, 79 2-vinylpyridine. Catalyst consumption 197 mol pyridine / g At Cobalt. Example 9- Preparation of 2-vinylilyridine with trimethylsilylcyclopentenyl (cyclooct-1, 5-diene) -cobal as catalyst. A load of 0.222 g (0.730 mmol) e ,, SiCpCoCOD, 15.55 g (293.0 mm1l) of krylnitrile (1.13 M), 208, b5 g of oluol. The reaction temperature is 150 ° C, (less than 30 minutes. Reaction of reaction P. And pv.T7 ka 233.55 g, condensate (0.2 Torr) 231 g, residue 2.0 g. Result (according to gas chromatographic analysis): 9.51 g of acryl nitrile (unconverted), 10.9 g of 2-vinylpyridine., Yield, calculated for unconverted acrylonitrile, 91% of 2-vinylpyridine; catalyst consumption, mole pyridine / g At Cobalt. Example 10. Preparation of 2-vinylpyridine with JT-cyclopentadadienyl- (O1, sb-bipyridyl) -cobalt as a catalyst. Loading 0.150 g (O, 536 mmol) CpCobipy; 16.60 g (315.1 mmol) of acrylonitrile (1.21 M); 209.25 g of toluene. Reaction temperature vre m reaction 15 min. Reaction unloading 233.50 g, condensate (0.2 Torr) 229.8 g, residue 1.5 g. Result (according to gas chromatographic analysis): 10.55 g of acryl nitrile (unconverted) and 3.82 g 2-vinylpyridine. The yield, calculated on converted acr14lnitrile, 81 2-vinylpyridine, consumption of catalyst is 17 mol of pyridine / g At Cobalt. elevated temperature and when using a solution of nitrile, sat acetylene, inert solvents, characterized in that, in order to increase the yield of the product, the process is carried out at an acrylonitrile concentration of from 0.1 to 2 mol / l and at a temperature of 1t-l8oc for up to 50 minutes.
[2]
2. Method pop. 1, distinguished by the fact that the process temperature is 150-160.C.
[3]
3. A method according to claims 1 and 2, characterized in that the reaction time is 15-30 minutes. C. C. method according to claims 1 to 3, of which is acrylonitrile with a concentration of about 1 mol / l. 5. The method according to PP.-1-4, about tl and c by using cobaltocene as a catalyst. Sources of information taken into account in the examination 1. US patent number 00b149, cl. 260-290, 1977 (prototype).

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引用文献:

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法律状态:

优先权:

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申请号 | 申请日 | 专利标题

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DE2840460A|DE2840460C2|1978-09-16|1978-09-16|Catalytic process for the production of 2-vinylpyridine from acetylene and acrylonitrile|

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