Background technology
2,3-two chloro-5-trichloromethylpyridines and 2-chloro-5-trichloromethylpyridine are two important agricultural chemicals synthetic intermediates, wherein 2, and 3-two chloro-5-trichloromethylpyridines can further be fluoridized and obtain 2,3-two chloro-5-trifluoromethylpyridines, the latter is a kind of intermediate important in the fluoro nitrogen heterocycles agricultural chemicals, by its synthetic agricultural chemicals one class such as fluazifop, and the spirit of chlorine fluorine second standing grain, the weedicides such as haloxyfop, it is high that they have drug effect, and toxicity is low, pollutes the characteristics such as little; Another kind of such as process for preparation of benzoylurea compounds such as fluorine pyridine ureas, the mechanism of action is unique, has efficient, low toxicity, the distinguishing feature such as environmentally friendly; And the 2-chloro-5-trichloromethylpyridine is fluoridized the crucial mesosome that the 2-chloro-5-trifluoromethylpyridine that obtains is new herbicides agricultural chemicals fluazifop-p-butyl, the synthesis technique of two kinds of intermediates is similar, but traditional synthesis method is owing to using the difference of raw material and catalyzer, technological process also has difference, present invention focuses on by a covering device, one kettle way synthesizes these two kinds of products, only adjusts arbitrarily the ratio of two kinds of products in the process according to the ratio that adds two kinds of catalyzer.
Summary of the invention
The object of the invention provides a cover 2-chloro-5-trichloromethylpyridine and 2, the synthesis technique of two kinds of products of 3-two chloro-5-trichloromethylpyridines, and any adjustment that realizes two kinds of product proportions that is adjusted on the covering device by the catalyst combination ratio, the building-up reactions formula is as follows:
Possess and may further comprise the steps: take the raw material CMP as raw material, the compound that adds successively free radical reaction class of initiators catalyst A and another kind of catalyst B molybdenum or tungsten, carry out the chlorination building-up reactions, the gross weight that two kinds of catalyzer of described A, B add accounts for CMP 0.01%~2% of the weight that feeds intake; By adjusting the weight ratio of described catalyst A and catalyst B in the scope between 0:5~100:0, obtain the mixture of 2-chloro-5-trichloromethylpyridine and two kinds of product arbitrary proportions of 2,3-, two chloro-5-trichloromethylpyridines.
In the inventive method, the preferred Diisopropyl azodicarboxylate of described catalyst A or benzoyl peroxide free radical reaction initiator.
In the inventive method, muriate or the oxide compound of the preferred molybdenum of described catalyst B or tungsten.
In the solution of the present invention, the further preferred molybdenum pentachloride of described catalyst B or tungsten hexachloride.
In the preferred scheme of the present invention, the weight ratio of described catalyst A and B is preferably adjusted in the scope of 1:3.2~110:6; Further preferably in the scope of 1.05:3~100:7, adjust.
Among the present invention, because additional proportion and 2-chloro-5-trichloromethylpyridine and 2 of A, two kinds of catalyzer of B, there is corresponding relation in the proportion of composing of 3-two chloro-5-trichloromethylpyridines two products, therefore, by adjusting the ratio between catalyst A and the B, the mixture of 2-chloro-5-trichloromethylpyridine and 2,3-, two chloro-5-trichloromethylpyridines, two product arbitrary proportions can be accessed, any adjustment of two kinds of product proportions obtaining at a covering device can be realized thus.
Embodiment
In following examples, except special stipulation, described product proportion is mol ratio.
Embodiment 1:
Drop into CMP 100g, intensification 140-150 degree adds then logical chlorine reaction of catalyzer Diisopropyl azodicarboxylate 0.100g, and add catalyzer molybdenum pentachloride 0.030g after 10 hours and continued again 5 hours, middle control, the ratio of two kinds of products is 5:5 approximately.
Embodiment 2:
Drop into CMP 100g, intensification 140-150 degree, add then logical chlorine reaction of catalyzer Diisopropyl azodicarboxylate 1.0g, adding catalyzer molybdenum pentachloride 0.5g after 10 hours continued 5 hours again, middle control, the ratio of 2-chloro-5-trichloromethylpyridine and 2,3-, two chloro-5-trichloromethylpyridines is 4:6 approximately.
Embodiment 3:
Drop into CMP 100g, intensification 140-150 degree, add then logical chlorine reaction of catalyzer Diisopropyl azodicarboxylate 0.100g, adding catalyzer molybdenum pentachloride 0.130g after 10 hours continued 5 hours again, middle control, the ratio of 2-chloro-5-trichloromethylpyridine and 2,3-, two chloro-5-trichloromethylpyridines is 2:8 approximately.
Embodiment 4:
Drop into CMP 100g, intensification 140-150 degree, add then logical chlorine reaction of catalyzer Diisopropyl azodicarboxylate 0.100g, adding catalyzer molybdenum pentachloride 0.300g after 10 hours continued 5 hours again, middle control, the ratio of 2-chloro-5-trichloromethylpyridine and 2,3-, two chloro-5-trichloromethylpyridines is 1:9 approximately.
Embodiment 5:
Drop into CMP 100g, be warmed up to the 140-150 degree, add then logical chlorine reaction of catalyzer benzoyl peroxide 0.0105g, adding catalyzer tungsten hexachloride 0.0315g after 10 hours continued 5 hours again, middle control, the ratio of 2-chloro-5-trichloromethylpyridine and 2,3-, two chloro-5-trichloromethylpyridine products is 1:9 approximately.
Embodiment 6:
Drop into CMP 100g, be warmed up to the 140-150 degree, add then logical chlorine reaction of catalyzer benzoyl peroxide 0.105g, adding catalyzer tungsten hexachloride 0.140g after 10 hours continued 5 hours again, middle control, the ratio of 2-chloro-5-trichloromethylpyridine and 2,3-, two chloro-5-trichloromethylpyridine products is 2:8 approximately.
Embodiment 7:
Drop into CMP 100g, be warmed up to the 140-150 degree, add then logical chlorine reaction of catalyzer benzoyl peroxide 0.105g, adding catalyst oxidation tungsten 0.053g after 10 hours continued 5 hours again, middle control, the ratio of 2-chloro-5-trichloromethylpyridine and 2,3-, two chloro-5-trichloromethylpyridine products is 3:7 approximately.
The method of other embodiments of the invention and above-described embodiment 1-7 is basic identical, and wherein catalyzer add-on and the group of products corresponding relation between proportional is shown in Table 1.Wherein, A1 represents Diisopropyl azodicarboxylate, and A2 represents benzoyl peroxide; B1 represents molybdenum pentachloride, and B2 represents tungsten hexachloride; A represents the 2-chloro-5-trifluoromethylpyridine, and b represents 2,3-, two chloro-5-trifluoromethylpyridines.
Table 1
Embodiment |
A1(g) |
B1(g) |
A2(g) |
B2(g) |
a |
b |
8 |
0.1 |
0.08 |
? |
? |
30 |
70 |
9 |
0.1 |
0.024 |
? |
? |
60 |
40 |
10 |
0.1 |
0.018 |
? |
? |
70 |
30 |
11 |
0.1 |
0.012 |
? |
? |
80 |
20 |
12 |
0.1 |
0.006 |
? |
? |
90 |
10 |
13 |
? |
0.3 |
0.105 |
? |
10 |
90 |
14 |
? |
0.13 |
0.105 |
? |
20 |
80 |
15 |
? |
0.08 |
0.105 |
? |
30 |
70 |
16 |
? |
0.05 |
0.105 |
? |
40 |
60 |
17 |
? |
0.03 |
0.105 |
? |
50 |
50 |
18 |
? |
0.024 |
0.105 |
? |
60 |
40 |
19 |
? |
0.018 |
0.105 |
? |
70 |
30 |
20 |
? |
0.012 |
0.105 |
? |
80 |
20 |
21 |
? |
0.006 |
0.105 |
? |
90 |
10 |
22 |
0.1 |
? |
? |
0.31 |
10 |
90 |
23 |
0.1 |
? |
? |
0.134 |
20 |
80 |
[0029]?
24 |
0.1 |
? |
? |
0.083 |
30 |
70 |
25 |
0.1 |
? |
? |
0.052 |
40 |
60 |
26 |
0.1 |
? |
? |
0.034 |
50 |
50 |
27 |
0.1 |
? |
? |
0.027 |
60 |
40 |
28 |
0.1 |
? |
? |
0.02 |
70 |
30 |
29 |
0.1 |
? |
? |
0.014 |
80 |
20 |
30 |
0.1 |
? |
? |
0.007 |
90 |
10 |
31 |
? |
? |
0.105 |
0.084 |
30 |
70 |
32 |
? |
? |
0.105 |
0.035 |
50 |
50 |
33 |
? |
? |
0.105 |
0.028 |
60 |
40 |
34 |
? |
? |
0.105 |
0.021 |
70 |
30 |
35 |
? |
? |
0.105 |
0.014 |
80 |
20 |
36 |
? |
? |
0.105 |
0.007 |
90 |
10 |