3, the preparation method of 4-ethene dioxythiophene
Technical field
The present invention relates to a kind of compound method of organic cpds, particularly a kind of method of preparation 3,4-ethene dioxythiophene.
Background technology
3,4-ethene dioxythiophene (EDOT), outward appearance are colourless or light yellow transparent liquid, Cas126213-50-1,10.5 ℃ of fusing points, 225 ℃ of boiling points (101.3kpa).It is to be used for preparing polyethylene dioxythiophene (PEDOT) as a kind of electron chemistry articles for use.Polyethylene dioxythiophene is a kind of novel organic conductive luminescent material; Having high conductivity, good environmental stability, film and be prone to advantages such as system and the transparency are good, is the ideal material of electronicss such as the demonstration of preparation organic electroluminescence, solar cell, ultracapacitor plastics antistatic coating, illumination film coating, transmitter, corrosion protection.Because its unique electricity and optical characteristics and wide application field, polyethylene dioxythiophene will cause the extensive concern of novel industry and related industries.
At present, domestic still do not have preparation 3, a 4-ethene dioxythiophene monomeric reported in literature.Foreign literature has been reported with 3; 4-dibromo thiophene is that raw material carries out Ullmann reaction and makes 3,4-ethene dioxythiophene, because the required raw material 3 of this method; 4-dibromo thiophene costs an arm and a leg; And severe reaction conditions, cost are high, product yield is low, cause this method can only be applied to the laboratory, and can not carry out suitability for industrialized production.
Summary of the invention
What the present invention solved is exactly the problem that the method raw materials cost is high, product yield is low of existing preparation 3,4-ethene dioxythiophene, and the preparation method of 3,4-ethene dioxythiophene that a kind of technology is simple, with low cost, yield is higher is provided.It is to be starting raw material with sulfo-two sweet acid, makes through esterification, condensation, etherificate, hydrolysis, decarboxylation five steps reaction, and reaction formula is:
The present invention is to realize through such technical scheme for reaching above purpose, is that starting raw material comprises the steps: with sulfo-two sweet acid
(a) esterification:
With sulfo-two sweet acid, methyl alcohol, catalyst mix; After reaction finishes, after neutralization, SX, drying,, promptly obtain carboxylate sulfo-two sweet dimethyl phthalates again through underpressure distillation;
(b) condensation reaction:
Above-mentioned carboxylate is added in the methanol solution of sodium methylate, add oxalic acid diethyl ester; After reaction finishes, after acidifying, filtration, drying, obtain condensation product 2,5-dioctyl phthalate dimethyl ester-3,4-dihydroxyl thiophene;
(c) Williamson reaction:
With above-mentioned condensation product, 1,2-dihalo-ethane, K
2CO
3, phase-transfer catalyst adds in the solvent; After reaction finishes, reclaim solvent, add water after the cooling, carry out successively obtaining etherificate product 2,5-dioctyl phthalate dimethyl ester-3,4-ethene dioxythiophene after suction filtration, washing, the drying;
(d) hydrolysis reaction:
With the aqueous solution of above-mentioned etherificate product, NaOH, after reaction finishes, carry out acidifying, after suction filtration, washing, drying, obtain hydrolysate 2,5-dioctyl phthalate-3,4-ethene dioxythiophene;
(e) decarboxylic reaction
With said hydrolyzed product, catalyzer, solvent, reaction under nitrogen protection; After reaction finished, through cooling, filtration, solution carried out underpressure distillation, collects the cut of 75~77 ℃ (1.33kpa), promptly gets 3,4-ethene dioxythiophene.
As improvement, step (a) is in the esterification, and the mass ratio of sulfo-two sweet acid, methyl alcohol, catalyzer is 1:2~10:0.1~0.5.Under reflux state, react, by the yield of the synthetic sulfo-two sweet dimethyl phthalates of sulfo-two sweet acid near 95%.
As improvement, step (b) is in the condensation reaction, and the mol ratio of sulfo-two sweet dimethyl phthalates, sodium methylate, oxalic acid diethyl ester is 1:2~5:1~3; This reaction must guarantee anhydrous state; Because of being exothermic process in the reaction process, therefore, must under lower temperature, carry out (0~40 ℃); Operating process is prone to slowly add oxalic acid diethyl ester.The condensation product yield is more than 90%.
As improvement, step (c) is in the etherification reaction, and the mol ratio of sulfo-two sweet dimethyl phthalates, sodium methylate, oxalic acid diethyl ester is 1:2~5:1~3.Solvent is benzene,toluene,xylene, chlorobenzene, ethanol, THF (THF), DMSO organic solvents such as (DMSO 99.8MIN.s).Phase-transfer catalyst is a quaternary ammonium salt-type phase transfer catalyst, like CETRIMIDE POWDER, tetrabutylammonium chloride, tetramethyl ammonium chloride, 4 bromide, Tetrabutyl amonium bromide, tetrabutylammonium iodide, benzyl tributyl brometo de amonio.The quality of phase-transfer catalyst is 2,5-dioctyl phthalate dimethyl ester-3,4-dihydroxyl thiophene, 1,2-dihalo-ethane and K
2CO
30.5~10% of three's quality sum.60~150 ℃ of temperature controls, the actual recovery of etherificate product can reach 65~70%.
As improvement, step (d) is in the hydrolysis reaction, and the mol ratio of 2,5-dioctyl phthalate dimethyl ester-3,4-ethene dioxythiophene, NaOH is 1:2~6, and the concentration of aqueous solution of NaOH is the best with 5%~30%.At 50~100 ℃ of reaction 3~8h, acidifying PH=1~2, the hydrolysate that after filtration, drying, obtains, its yield can reach more than 90%.
As improvement, step (e) is in the decarboxylic reaction, and solvent is meant toluene, YLENE, DMSO (DMSO 99.8MIN.), quinoline, Witcizer 300 etc.; The quality of solvent is 2~10 times of 2,5-dioctyl phthalate-3,4-ethene dioxythiophene quality.Catalyzer is verditer, verditer or their mixture, and catalyst levels is 1%~20% of 2,5-dioctyl phthalate-3,4-ethene dioxythiophene and a solvent quality sum.Hydrolysate is reaction 10~15h under 80~200 ℃, and the product yield after the purification can reach 65~70%.
The preparation method of 3,4-ethene dioxythiophene according to the invention has following characteristics:
(1) yield of product 3,4-ethene dioxythiophene is higher, and total recovery can reach more than 32%.
(2) adopt the high vacuum underpressure distillation, 3, the 4-ethene dioxythiophene product purity that obtains is high, color and luster is attractive in appearance.
(3) technology is simple in the reaction process, does not need HTHP in the reaction.
(4) used solvent can recycle and reuse in the reaction.
(5) required catalyst levels is few, price is low, easy preparation.
(6) synthesis technique of the present invention is simple, production cost is low, product yield is high, clean process is free from environmental pollution, is fit to commercialization production.
Embodiment
Below in conjunction with embodiment the present invention is described further.
The preparation of sulfo-two sweet dimethyl phthalates
Embodiment 1:
With the two sweet acid of 338g (2.25mol) sulfo-, 2560ml methyl alcohol, 135g sulfuric acid (catalyzer) mixes; Stir, be warming up to backflow, reaction times 6~8h, normal pressure steamed methyl alcohol after reaction finished; Cooling, the alkali lye of adding 5% is transferred PH=7~7.5, ether (3*300ml) extraction, anhydrous sodium sulfate drying.Normal pressure concentrates ether, underpressure distillation again, and collecting boiling point is the cut of 172~176 ℃/1.33kPa, promptly obtaining outward appearance is the carboxylate sulfo-two sweet dimethyl phthalate 382.8g of nearly colourless transparent liquid, content 99.3%, yield 94.8%.
Catalyst type and consumption are changed, and other is with embodiment 1, and its result sees table 1.
Table 1
Embodiment |
Catalyzer |
Catalyst levels (g) |
Sulfo-two sweet dimethyl phthalate amounts (g) |
Content (%) |
Yield (%) |
2 |
Sulfuric acid |
35 |
323.7 |
99.1 |
80.0 |
3 |
Sulfuric acid |
105 |
370.2 |
99.0 |
91.4 |
4 |
Phosphoric acid |
150 |
226.5 |
99.5 |
56.2 |
5 |
Tosic acid |
35 |
311.3 |
99.7 |
77.4 |
6 |
Tosic acid |
168 |
376 |
99.8 |
93.6 |
Methanol usage is changed, and other is with embodiment 1, and its result sees table 2.
Table 2
Embodiment |
Methanol usage (ml) |
Sulfo-two sweet dimethyl phthalate amounts (g) |
Content (%) |
Yield (%) |
7 |
855 |
324 |
99.5 |
80.4 |
8 |
1700 |
3.59 |
99.0 |
88.7 |
9 |
2130 |
372.4 |
99.6 |
92.5 |
10 |
3410 |
367.8 |
99.2 |
91.0 |
11 |
4250 |
357 |
99.3 |
88.4 |
Temperature of reaction is changed, and other is with embodiment 1, and its result sees table 3.
Table 3
Embodiment |
Temperature of reaction (℃) |
Sulfo-two sweet dimethyl phthalate amounts (g) |
Content (%) |
Yield (%) |
12 |
30 |
222 |
99.3 |
55 |
13 |
40 |
271.3 |
99.6 |
67.4 |
14 |
50 |
329.7 |
99.1 |
81.5 |
15 |
60 |
380 |
99.2 |
94.0 |
16 |
70 |
380.4 |
99.3 |
94.2 |
The preparation of 2,5-dioctyl phthalate dimethyl ester-3,4-dihydroxyl thiophene
Embodiment 17:
To add by the carboxylate 380g (2.13mol) that embodiment 1 makes in the 2475ml methanol solution of 460g (8.52mol) sodium methylate, drip 772g (5.33mol) oxalic acid diethyl ester, 0~10 ℃ of temperature control down in stirring; Be warming up to backflow after dropwising, reaction times 3~5h is after question response finishes; Reclaim methyl alcohol, add 1L water, use hcl acidifying; After filtration, drying, obtain condensation product 2,5-dioctyl phthalate dimethyl ester-3,4-dihydroxyl thiophene 455g of off-white color pressed powder; Content 99.4%, yield 92%.
The sodium methylate consumption is changed, and other is with embodiment 17, and its result sees table 4.
Table 4
Embodiment |
Sodium methylate consumption (g) |
2,5-dioctyl phthalate dimethyl ester-3,4-dihydroxyl thiophene amount (g) |
Content (%) |
Yield (%) |
18 |
230 |
436.6 |
99.0 |
87.4 |
19 |
345 |
449.3 |
99.3 |
90.2 |
20 |
518 |
457.8 |
99.5 |
92.1 |
21 |
575 |
460.3 |
99.4 |
92.5 |
The oxalic acid diethyl ester consumption is changed, and other is with embodiment 17, and its result sees table 5.
Table 5
Embodiment |
Oxalic acid diethyl ester consumption (g) |
2,5-dioctyl phthalate dimethyl ester-3,4-dihydroxyl thiophene amount (g) |
Content (%) |
Yield (%) |
22 |
308.9 |
418 |
99.4 |
80.4 |
23 |
463.3 |
423.4 |
99.4 |
85.1 |
24 |
617.7 |
450.9 |
99.6 |
90.8 |
25 |
926.6 |
459.3 |
99.5 |
92.4 |
The preparation of 2,5-dioctyl phthalate dimethyl ester-3,4-ethene dioxythiophene
Embodiment 26:
Condensation product 440g (1.9mol), 1198g (6.38mol) 1,2-ethylene dibromide, 503g (3.65mol) K that will make by embodiment 17
2CO
3, 105g CETRIMIDE POWDER (phase-transfer catalyst) adds in the 4500ml toluene (solvent), stir and heat up 90 ℃ of temperature controls; Reaction times 10~15h reclaims solvent and unreacted 1,2-ethylene dibromide with the material concentrating under reduced pressure after question response finishes; Cooling back adds 5L water, stirring at normal temperature 30min, carry out successively after suction filtration, washing, the drying the etherificate product 2 of off-white color to gray solid powder; 5-dioctyl phthalate methyl esters-3; 4-ethene dioxythiophene 319g, content 98.5%, yield 64%.
1,2-ethylene dibromide consumption is changed, and other is with embodiment 26, and its result sees table 6.
Table 6
Embodiment |
1,2-ethylene dibromide consumption (g) |
2,5-dioctyl phthalate dimethyl ester-3,4-ethene dioxythiophene amount (g) |
Content (%) |
Yield (%) |
27 |
357 |
242.8 |
98.0 |
48.5 |
28 |
714 |
274.6 |
97.9 |
54.8 |
29 |
1428 |
322.2 |
98.2 |
64.5 |
30 |
1606.5 |
321.8 |
98.5 |
64.6 |
31 |
1785 |
324.1 |
98.1 |
64.8 |
With K
2CO
3Consumption changes, and other is with embodiment 26, and its result sees table 7.
Table 7
Embodiment |
K
2CO
3Consumption (g)
|
2,5-dioctyl phthalate dimethyl ester-3,4-ethene dioxythiophene amount (g) |
Content (%) |
Yield (%) |
32 |
262.2 |
238.1 |
98.5 |
47.8 |
33 |
393.3 |
284.6 |
98.6 |
57.2 |
34 |
786.6 |
321.9 |
98.3 |
64.5 |
35 |
1048.8 |
323.4 |
98.3 |
64.8 |
Phase-transfer catalyst kind and consumption are changed, and other is with embodiment 26, and its result sees table 8.
Table 8
Embodiment |
Phase-transfer catalyst |
Phase-transfer catalyst consumption (g) |
2,5-dioctyl phthalate dimethyl ester-3,4-ethene dioxythiophene amount (g) |
Content (%) |
Yield (%) |
36 |
Tetrabutylammonium chloride |
25 |
191.1 |
98.6 |
38.4 |
37 |
Tetrabutylammonium chloride |
250 |
247.8 |
98.2 |
49.6 |
38 |
Tetrabutyl amonium bromide |
25 |
213.6 |
98.3 |
42.8 |
39 |
Tetrabutyl amonium bromide |
250 |
266.7 |
98.4 |
53.5 |
40 |
Tetrabutylammonium iodide |
25 |
224.3 |
98.0 |
44.8 |
41 |
Tetrabutylammonium iodide |
250 |
274.8 |
98.0 |
54.9 |
42 |
CETRIMIDE POWDER |
25 |
248.6 |
97.9 |
49.6 |
43 |
CETRIMIDE POWDER |
50 |
281.6 |
98.6 |
56.6 |
44 |
CETRIMIDE POWDER |
150 |
319.1 |
98.7 |
64.2 |
45 |
CETRIMIDE POWDER |
250 |
322.1 |
98.7 |
64.8 |
Solvent species and consumption are changed, and other is with embodiment 26, and its result sees table 9.
Table 9
Embodiment |
Solvent |
Solvent load (ml) |
2,5-dioctyl phthalate dimethyl ester-3,4-ethene dioxythiophene amount (g) |
Content (%) |
Yield (%) |
46 |
THF |
2000 |
146 |
95.8 |
28.5 |
47 |
THF |
4000 |
167.8 |
96.2 |
32.9 |
48 |
Benzene |
2000 |
231.9 |
96.9 |
45.8 |
49 |
Benzene |
4000 |
259.4 |
97.4 |
51.5 |
50 |
Ethanol |
2000 |
196.3 |
97.2 |
38.9 |
51 |
Ethanol |
4000 |
212.1 |
96.0 |
41.5 |
52 |
Toluene |
2000 |
263.3 |
98.0 |
52.6 |
53 |
Toluene |
3500 |
291.4 |
98.0 |
58.2 |
54 |
Toluene |
5500 |
321.9 |
98.3 |
64.5 |
Temperature of reaction is changed, and other is with embodiment 26, and its result sees table 10.
Table 10
Embodiment |
Temperature of reaction (℃) |
2,5-dioctyl phthalate dimethyl ester-3,4-ethene dioxythiophene amount (g) |
Content (%) |
Yield (%) |
55 |
60 |
211.7 |
98.5 |
42.5 |
56 |
70 |
262.5 |
98.3 |
52.6 |
57 |
80 |
293.3 |
98.2 |
58.7 |
58 |
100 |
311.6 |
98.1 |
62.3 |
59 |
110 |
303.3 |
97.2 |
60.1 |
60 |
150 |
209.5 |
96.5 |
41.2 |
The preparation of 2,5-dioctyl phthalate-3,4-ethene dioxythiophene
Embodiment 61:
To stir, be warming up to backflow after mixing by etherificate product 310g (1.18mol), 198.5g (4.96mol) NaOH, the 2L water that embodiment 26 makes, reaction times 3~5h reduces to room temperature and carries out acidifying adjusting PH=1~2 with dilute sulphuric acid after question response finishes; Separate out gray precipitate; Obtain hydrolysate 2,5-dioctyl phthalate-3,4-ethene dioxythiophene 257g of gray solid powder after suction filtration, a small amount of washing, the drying; Content 99.4%, yield 94.6%.
The NaOH consumption is changed, and other is with embodiment 61, and its result sees table 11.
Table 11
Embodiment |
NaOH consumption (g) |
2,5-dioctyl phthalate-3,4-ethene dioxythiophene amount (g) |
Content (%) |
Yield (%) |
62 |
94.4 |
242.3 |
99.1 |
88.4 |
63 |
141.6 |
250.5 |
99.2 |
91.5 |
64 |
236 |
258.2 |
99.6 |
94.7 |
65 |
283.2 |
259 |
99.4 |
94.8 |
The water yield that adds in the reaction is changed, and other is with embodiment 61, and its result sees table 12.
Table 12
Embodiment |
Water consumption (L) |
2,5-dioctyl phthalate-3,4-ethene dioxythiophene amount (g) |
Content (%) |
Yield (%) |
66 |
0.48 |
188.5 |
99.0 |
68.7 |
67 |
1.1 |
226.9 |
99.1 |
82.8 |
68 |
2.5 |
254.1 |
99.2 |
92.8 |
69 |
3.7 |
237.9 |
99.2 |
86.9 |
Temperature of reaction is changed, and other is with embodiment 61, and its result sees table 13.
Table 13
Embodiment |
Temperature of reaction (℃) |
2,5-dioctyl phthalate-3,4-ethene dioxythiophene amount (g) |
Content (%) |
Yield (%) |
70 |
50 |
203.3 |
99.0 |
74.1 |
71 |
70 |
225.3 |
99.2 |
82.3 |
72 |
80 |
237.7 |
99.3 |
86.9 |
73 |
90 |
247.2 |
99.0 |
90.1 |
The preparation of 3,4-ethene dioxythiophene
Embodiment 74:
To under nitrogen protection, stir intensification, 160 ℃ of temperature controls, reaction times 10~12h by hydrolysate 255g (1.1mol), 100g verditer (catalyzer), the 1250ml quinoline (solvent) that embodiment 61 makes.React the postcooling that finishes, leach catalyzer, solution carries out underpressure distillation, and the cut of collecting 75~77 ℃/1.33kpa promptly gets decarboxylate 3,4-ethene dioxythiophene 103g of nearly colourless transparent liquid, yield 65.9%, content 99.5%.
Catalyst type and consumption are changed, and other is with embodiment 74, and its result sees table 14.
Table 14
Solvent species and consumption are changed, and other is with embodiment 74, and its result sees table 15.
Table 15
Embodiment |
Solvent |
Solvent load (ml) |
3,4-ethene dioxythiophene amount (g) |
Content (%) |
Yield (%) |
89 |
YLENE |
1250 |
53 |
98.5 |
33.4 |
90 |
YLENE |
2250 |
60.6 |
98.3 |
38.1 |
91 |
Quinoline |
550 |
82.7 |
99.1 |
52.4 |
92 |
Quinoline |
900 |
92.3 |
99.0 |
58.4 |
93 |
Quinoline |
2000 |
103.7 |
99.2 |
65.8 |
94 |
Witcizer 300 |
550 |
65.8 |
98.6 |
41.5 |
95 |
Witcizer 300 |
900 |
79.6 |
98.4 |
50.1 |
96 |
Witcizer 300 |
1800 |
85.1 |
98.1 |
53.4 |
Temperature of reaction is changed, and other is with embodiment 74, and its result sees table 16.
Table 16
Embodiment |
Temperature of reaction (℃) |
3,4-ethene dioxythiophene amount (g) |
Content (%) |
Yield (%) |
97 |
80 |
64.9 |
99.1 |
41.1 |
98 |
100 |
85.0 |
99.7 |
54.2 |
99 |
150 |
96.2 |
99.2 |
61.5 |
100 |
180 |
98.8 |
99.4 |
62.8 |
101 |
200 |
84.3 |
99.5 |
53.6 |