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CN109438340A - A kind of preparation process of the chloro- nicotinonitrile of 2- - Google Patents

A kind of preparation process of the chloro- nicotinonitrile of 2- Download PDF

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Publication number
CN109438340A
CN109438340A CN201811256986.3A CN201811256986A CN109438340A CN 109438340 A CN109438340 A CN 109438340A CN 201811256986 A CN201811256986 A CN 201811256986A CN 109438340 A CN109438340 A CN 109438340A
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CN
China
Prior art keywords
chloro
nicotinonitrile
added dropwise
temperature
organic base
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Pending
Application number
CN201811256986.3A
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Chinese (zh)
Inventor
齐鲲鹏
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Laohekou City Tianhe Technology Co Ltd
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Laohekou City Tianhe Technology Co Ltd
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Priority to CN201811256986.3A priority Critical patent/CN109438340A/en
Publication of CN109438340A publication Critical patent/CN109438340A/en
Pending legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D213/00Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members
    • C07D213/02Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members
    • C07D213/04Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom
    • C07D213/60Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom 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 to ring carbon atoms
    • C07D213/78Carbon atoms having three bonds to hetero atoms, with at the most one bond to halogen, e.g. ester or nitrile radicals
    • C07D213/84Nitriles
    • C07D213/85Nitriles in position 3
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/0234Nitrogen-, phosphorus-, arsenic- or antimony-containing compounds
    • B01J31/0235Nitrogen containing compounds
    • B01J31/0237Amines
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/0234Nitrogen-, phosphorus-, arsenic- or antimony-containing compounds
    • B01J31/0235Nitrogen containing compounds
    • B01J31/0237Amines
    • B01J31/0238Amines with a primary amino group
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/19Catalysts containing parts with different compositions

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Pyridine Compounds (AREA)

Abstract

The invention proposes a kind of preparation processes of the chloro- nicotinonitrile of 2-, processing step includes: that N- oxo niacinamide is dissolved in organic solvent, phosphorus oxychloride is added dropwise under the conditions of 15 ± 5 DEG C, it is added dropwise, organic base is added dropwise under the conditions of 10 ± 5 DEG C, it is added dropwise, in 10 ± 5 DEG C of 30 ± 10min of insulated and stirred, it is warming up to 35 ± 10 DEG C, keep the temperature 1 ± 0.5h, it is warming up to 55 ± 5 DEG C again, keep the temperature 1 ± 0.5h, it is warming up to 95~100 DEG C again, keep the temperature 4 ± 1h, heat preservation finishes to obtain chloride reaction solution, chloride reaction solution is evaporated under reduced pressure, until without the outflow of visible liquid, add water, temperature is controlled at 65 ± 5 DEG C, stir 2 ± 0.5h, it is cooled to 20 ± 5 DEG C, stir 30 ± 10min, the chloro- 3- cyano pyrrole of 2- is obtained by filtration Pyridine wet product, the organic base that the present invention is mixed by using two kinds improve the yield of the chloro- nicotinonitrile of 2- as catalyst to a certain extent.

Description

A kind of preparation process of the chloro- nicotinonitrile of 2-
Technical field
The present invention relates to the preparations of dynamic chemical intermediate preparation technical field more particularly to a kind of chloro- nicotinonitrile of 2- Technique.
Background technique
2- chlorine apellagrin is important fine-chemical intermediate, in a variety of drugs, insecticide, fungicide and herbicide Mesosome raw material, the chloro- nicotinonitrile of 2- are then the key intermediates for preparing 2- chlorine apellagrin.
The common route of the synthesis chloro- nicotinonitrile of 2- obtains N- oxo by hydrogen peroxide oxidation for nicotinonitrile at present Niacinamide, N- oxo niacinamide obtain the chloro- nicotinonitrile of 2- through superchlorination, need in reaction process using a large amount of organic base As catalyst, currently used organic base is triethylamine, therefore this method is easy to produce a large amount of nitrogenous effluent, is produced to environment Raw harm, increases the difficulty of scale wastewater treatment.
Simultaneously using triethylamine as catalyst when, reaction generation the chloro- nicotinonitrile of 2- yield be not also it is very high, because This needs to improve the yield of reaction using new catalyst.
Summary of the invention
In view of this, the invention proposes a kind of preparation processes of chloro- nicotinonitrile of the 2- using new catalyst.
The technical scheme of the present invention is realized as follows: the present invention provides a kind of preparation works of the chloro- nicotinonitrile of 2- Skill, preparation method includes: that N- oxo niacinamide is dissolved in organic solvent to obtain N- oxo nicotinamide soln, at 15 ± 5 DEG C Under the conditions of phosphorus oxychloride is added dropwise into N- oxo nicotinamide soln, be added dropwise, to N- oxo niacinamide under the conditions of 10 ± 5 DEG C Organic base is added dropwise in solution, is added dropwise, makes N- oxo nicotinamide soln in 10 ± 5 DEG C of 30 ± 10min of insulated and stirred, is warming up to 35 ± 10 DEG C, 1 ± 0.5h is kept the temperature, then be warming up to 55 ± 5 DEG C, keeps the temperature 1 ± 0.5h, then be warming up to 95~100 DEG C, keeps the temperature 4 ± 1h, Heat preservation finishes to obtain chloride reaction solution, is evaporated under reduced pressure to chloride reaction solution, until without the outflow of visible liquid, adds water, controls Temperature processed stirs 2 ± 0.5h at 65 ± 5 DEG C, is cooled to 20 ± 5 DEG C, stirs 30 ± 10min, the chloro- 3- cyano pyrrole of 2- is obtained by filtration Pyridine wet product.
On the basis of above technical scheme, it is preferred that the organic base includes main organic base and secondary organic base, the master Organic base includes one of diethylamine and triethylamine, and the pair organic base includes in di-n-propylamine, Tri-n-Propylamine and n-butylamine One kind.
On the basis of above technical scheme, it is preferred that calculated with mass percent for 100%, the N- oxo nicotinoyl Amine: organic solvent: phosphorus oxychloride: organic base: the mass ratio of water is 1: (5-10): (2-4): (1.1-1.5): (2-5).
On the basis of above technical scheme, it is preferred that the organic solvent is in chloroform, methylene chloride or dichloroethanes One kind.
Still more preferably, the temperature of the vacuum distillation is 50~70 DEG C, and pressure is 2~8KPa.
On the basis of above technical scheme, it is preferred that the time that phosphorus oxychloride is added dropwise is 2 ± 0.5h.
On the basis of above technical scheme, it is preferred that the time that organic base is added dropwise is 1 ± 0.5h.
The preparation process of the chloro- nicotinonitrile of 2- of the invention has the advantages that compared with the existing technology
The present invention is used as catalyst using two kinds of organic base mixing, has been surprisingly found that, compared to using for single variety catalyst Better yield can be obtained, its alkalinity is different due to different organic bases, in the different interruptions of catalysis reaction, can produce Raw different reaction mechanism, to realize different reaction changing effects, inventor obtains preferably by multiple orthogonal experiment Embodiment makees catalyst using triethylamine compared to conventional, and different catalysts mixed system of the invention can be different degrees of Raising reaction yield.
Specific embodiment
Below in conjunction with embodiment of the present invention, the technical solution in embodiment of the present invention is carried out clearly and completely Description, it is clear that described embodiment is only some embodiments of the invention, rather than whole embodiments.Base Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts all Other embodiments shall fall within the protection scope of the present invention.
Embodiment 1:
It weighs 50g chloroform to be added in 250ml three-necked flask, weighs 10gN- oxo niacinamide and be added in three-necked flask, 15 ± 5 DEG C are cooled to, weighing 20g phosphorus oxychloride control time for adding is that 1.5h is added dropwise in three-necked flask, is added dropwise, then drop Temperature weighs 10g triethylamine and 1g Tri-n-Propylamine is uniformly mixed to 10 ± 5 DEG C, and control time for adding is that 0.5h is added dropwise to three mouthfuls of burnings It in bottle, is added dropwise, maintains the temperature at 5 DEG C and continue to stir 20min, be warming up to 25 DEG C, insulated and stirred 30min, then be warming up to 50 DEG C, insulated and stirred 30min, then 95 DEG C are warming up to, insulated and stirred 3h, heat preservation finishes to obtain chloride reaction solution, by chloride Reaction solution is transferred in revolving bottle, and for control temperature at 50 DEG C, pressure is 2Kpa progress rotary evaporation, until flowed out without obvious liquid, It measures 20ml water and revolving bottle is added, be warming up to 60 DEG C, the solution in revolving bottle be transferred in 250ml three-necked flask, heat preservation is stirred 1.5h is mixed, is cooled to 15 DEG C, stirs 20min, filters, obtains the chloro- nicotinonitrile wet product of 2-.
Embodiment 2:
It weighs 80g methylene chloride to be added in 250ml three-necked flask, weighs 10gN- oxo niacinamide and be added to three mouthfuls of burnings In bottle, 15 ± 5 DEG C are cooled to, weighing 30g phosphorus oxychloride control time for adding is that 2h is added dropwise in three-necked flask, it is added dropwise, It is cooled to 10 ± 5 DEG C again, weighs 8g diethylamine and 5g di-n-propylamine is uniformly mixed, control time for adding is that 1h is added dropwise to three mouthfuls of burnings It in bottle, is added dropwise, maintains the temperature at 10 DEG C and continue to stir 30min, be warming up to 35 DEG C, insulated and stirred 1h, then be warming up to 55 DEG C, insulated and stirred 1h, then 97 DEG C are warming up to, insulated and stirred 4h, heat preservation finishes to obtain chloride reaction solution, by chloride reaction solution It is transferred in revolving bottle, for control temperature at 60 DEG C, pressure is that 5Kpa carries out rotary evaporation, until flowing out without obvious liquid, is measured Revolving bottle is added in 40ml water, is warming up to 65 DEG C, the solution in revolving bottle is transferred in 250ml three-necked flask, insulated and stirred 2h, 20 DEG C are cooled to, 30min is stirred, filters, obtains the chloro- nicotinonitrile wet product of 2-.
Embodiment 3:
It weighs 100g dichloroethanes to be added in 250ml three-necked flask, weighs 10gN- oxo niacinamide and be added to three mouthfuls of burnings In bottle, 15 ± 5 DEG C are cooled to, weighing 40g phosphorus oxychloride control time for adding is that 2.5h is added dropwise in three-necked flask, is dripped Finish, then be cooled to 10 ± 5 DEG C, weigh 7g triethylamine and 8g n-butylamine is uniformly mixed, control time for adding is that 1.5h is added dropwise to three It in mouth flask, is added dropwise, maintains the temperature at 15 DEG C and continue to stir 40min, be warming up to 45 DEG C, insulated and stirred 1.5h, then rise Temperature is to 60 DEG C, insulated and stirred 1.5h, then is warming up to 100 DEG C, insulated and stirred 5h, and heat preservation finishes to obtain chloride reaction solution, by chlorine Compound reaction solution is transferred in revolving bottle, and control temperature is at 70 DEG C, and pressure is that 8Kpa carries out rotary evaporation, until without obvious liquid flow Out, it measures 50ml water and revolving bottle is added, be warming up to 70 DEG C, the solution in revolving bottle is transferred in 250ml three-necked flask, keep the temperature 2.5h is stirred, is cooled to 25 DEG C, stirs 40min, filters, obtains the chloro- nicotinonitrile wet product of 2-.
Comparative example:
It weighs 30g phosphorus oxychloride to be added in 250ml three-necked flask, is cooled to 15 ± 5 DEG C, weigh 10gN- oxo nicotinoyl Amine is slowly added into three-necked flask in 1h, and addition finishes, and weighs 4g triethylamine, three-necked flask is slowly dropped in 1h It is interior, it is added dropwise, insulated and stirred 1h, stirring finishes, and is warming up to 35 DEG C, insulated and stirred 1h, then be warming up to 55 DEG C, insulated and stirred 1h, then 95 DEG C are warming up to, insulated and stirred 4h, heat preservation finishes to obtain chloride reaction solution, and chloride reaction solution is transferred to revolving In bottle, keeping temperature is 95~100 DEG C, and pressure is that 20Kpa is rotated, and when obvious liquid does not flow out, stops revolving, to 35ml water is added in revolving bottle, is warming up to 65 DEG C, insulated and stirred 30min, is cooled to 25 DEG C, insulated and stirred 30min, filters, obtains To the chloro- nicotinonitrile wet product of 2-.
By above embodiments and the chloro- nicotinonitrile wet product drying of comparative example 2- obtained, weighing, and carry out related object Quality detection, correlated results are as follows:
Project Embodiment 1 Embodiment 2 Embodiment 3 Comparative example
Yield/g 8.85 8.92 9.09 8.64
Yield/% 90.8 91.5 93.2 88.6
Related substance/% 99.5 99.6 99.3 99.1
Above embodiments are not difficult to find out with comparative example data, the chloro- 3- of 2- being prepared using process of the invention Cyanopyridine yield is improved.
The foregoing is merely better embodiments of the invention, are not intended to limit the invention, all of the invention Within spirit and principle, any modification, equivalent replacement, improvement and so on be should all be included in the protection scope of the present invention.

Claims (7)

1. a kind of preparation process of the chloro- nicotinonitrile of 2-, which is characterized in that the preparation method includes: by N- oxo nicotinoyl Amine, which is dissolved in organic solvent, obtains N- oxo nicotinamide soln, is added dropwise under the conditions of 15 ± 5 DEG C into N- oxo nicotinamide soln Phosphorus oxychloride is added dropwise, and organic base is added dropwise into N- oxo nicotinamide soln under the conditions of 10 ± 5 DEG C, is added dropwise, makes N- Oxo nicotinamide soln is warming up to 35 ± 10 DEG C in 10 ± 5 DEG C of 30 ± 10min of insulated and stirred, keeps the temperature 1 ± 0.5h, then be warming up to 55 ± 5 DEG C, 1 ± 0.5h is kept the temperature, then be warming up to 95~100 DEG C, keeps the temperature 4 ± 1h, heat preservation finishes to obtain chloride reaction solution, to chlorine The vacuum distillation of compound reaction solution adds water until without the outflow of visible liquid, controls temperature at 65 ± 5 DEG C, stirs 2 ± 0.5h, drop Temperature stirs 30 ± 10min, the chloro- nicotinonitrile wet product of 2- is obtained by filtration to 20 ± 5 DEG C.
2. a kind of preparation process of the chloro- nicotinonitrile of 2- as described in claim 1, which is characterized in that the organic base packet Main organic base and secondary organic base are included, the main organic base includes one of diethylamine and triethylamine, and the pair organic base includes One of di-n-propylamine, Tri-n-Propylamine and n-butylamine.
3. a kind of preparation process of the chloro- nicotinonitrile of 2- as described in claim 1, which is characterized in that with mass percent Calculate for 100%, the N- oxo niacinamide: organic solvent: phosphorus oxychloride: organic base: the mass ratio of water is 1: (5-10): (2-4)∶(1.1-1.5)∶(2-5)。
4. a kind of preparation process of the chloro- nicotinonitrile of 2- as described in claim 1, which is characterized in that the organic solvent For one of chloroform, methylene chloride or dichloroethanes.
5. a kind of preparation process of the chloro- nicotinonitrile of 2- as described in claim 1, which is characterized in that the vacuum distillation Temperature be 50~70 DEG C, pressure be 2~8KPa.
6. a kind of preparation process of the chloro- nicotinonitrile of 2- as described in claim 1, which is characterized in that phosphorus oxychloride is added dropwise Time be 2 ± 0.5h.
7. a kind of preparation process of the chloro- nicotinonitrile of 2- as described in claim 1, which is characterized in that organic base is added dropwise Time is 1 ± 0.5h.
CN201811256986.3A 2018-10-25 2018-10-25 A kind of preparation process of the chloro- nicotinonitrile of 2- Pending CN109438340A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117443319A (en) * 2023-10-25 2024-01-26 老河口市天和科技有限公司 Production process of 2-chloro-3-cyanopyridine

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59144759A (en) * 1983-02-07 1984-08-18 Yuki Gosei Yakuhin Kogyo Kk Preparation of 2-chloronicotinic acid
CN101108824A (en) * 2007-08-17 2008-01-23 黑龙江省石油化学研究院 Method for synthesizing 2- chlorine -3- cyanogen radical pyridine with 3- cyanogen radical pyridine
CN101117332A (en) * 2006-08-04 2008-02-06 浙江医药股份有限公司新昌制药厂 Preparation method of 2-chloronicotinic acid

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59144759A (en) * 1983-02-07 1984-08-18 Yuki Gosei Yakuhin Kogyo Kk Preparation of 2-chloronicotinic acid
CN101117332A (en) * 2006-08-04 2008-02-06 浙江医药股份有限公司新昌制药厂 Preparation method of 2-chloronicotinic acid
CN101108824A (en) * 2007-08-17 2008-01-23 黑龙江省石油化学研究院 Method for synthesizing 2- chlorine -3- cyanogen radical pyridine with 3- cyanogen radical pyridine

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
陈建辉,等: "2-氯烟酸的合成", 《精细化工中间体》 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117443319A (en) * 2023-10-25 2024-01-26 老河口市天和科技有限公司 Production process of 2-chloro-3-cyanopyridine
CN117443319B (en) * 2023-10-25 2024-04-09 老河口市天和科技有限公司 Production process of 2-chloro-3-cyanopyridine

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Application publication date: 20190308