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CAS No. : | 10192-85-5 | MDL No. : | MFCD00067206 |
Formula : | C3H3KO2 | Boiling Point : | - |
Linear Structure Formula : | - | InChI Key : | ZUBIJGNKOJGGCI-UHFFFAOYSA-M |
M.W : | 110.15 | Pubchem ID : | 4429391 |
Synonyms : |
|
Signal Word: | Warning | Class: | N/A |
Precautionary Statements: | P261-P264-P271-P280-P302+P352-P304+P340-P305+P351+P338-P312-P321-P332+P313-P337+P313-P362-P403+P233-P405-P501 | UN#: | N/A |
Hazard Statements: | H315-H319-H335 | Packing Group: | N/A |
GHS Pictogram: |
* All experimental methods are cited from the reference, please refer to the original source for details. We do not guarantee the accuracy of the content in the reference.
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
7% | In N,N-dimethyl-formamide at 110 - 115℃; for 7h; |
Yield | Reaction Conditions | Operation in experiment |
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With hydrogen In water at 10 - 40℃; Ea; |
Yield | Reaction Conditions | Operation in experiment |
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76.2% |
Yield | Reaction Conditions | Operation in experiment |
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76% |
Yield | Reaction Conditions | Operation in experiment |
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76.1% |
Yield | Reaction Conditions | Operation in experiment |
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99% | With 4-methoxy-phenol; hydroquinone; In tert-butyl alcohol; at 180℃; for 6h;Conversion of starting material; | The catalyst was separated from the reaction liquid obtained in Example 5 by filtration, and the unreacted olefin was removed with an evaporator, giving 47.5 g of solid CF3(CF2)7CH2CH2I. A 200-ml SUS autoclave was charged with 47.5 g (0.082 mol) of the obtained solid CF3(CF2)7CH2CH2I, 9.9g (0.090 mol) of potassium acrylate, 25 g of t-butanol (solvent), 0.6 g of hydroquinone (polymerization inhibitor) and 0.01 g of hydroquinone monomethyl ether (polymerization inhibitor), and a reaction was then carried out with stirring at 180C for 6 hours.. As a result, CF3(CF2)7CH2CH2OCOCH=CH2 was obtained at a CF3(CF2)7CH2CH2I conversion rate of 99% and at a selectivity of 88%.. The results of NMR analysis revealed that polymerization of CF3(CF2)7CH2CH2OCOCH=CH2 was not detected. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
12% | With 4-methoxy-phenol; hydroquinone; In tert-butyl alcohol; at 180℃; for 6h; | The catalyst was separated from the reaction liquid obtained in Comparative Example 2 by filtration, and the unreacted olefin was removed with an evaporator, giving 0.9 g of liquid CF3(CF2)7CH2CH2Cl. This process was repeatedly conducted. Thereafter, a 200-ml SUS autoclave was charged with 39.5 g (0.082 mol) of the obtained liquid CF3(CF2)7CH2CH2Cl, 9.9 g (0.090 mol) of potassium acrylate, 25 g of t-butanol (solvent), 0.6 g of hydroquinone (polymerization inhibitor) and 0.01 g of hydroquinone monomethyl ether (polymerization inhibitor), and a reaction was then conducted with stirring at 180C for 6 hours. As a result, CF3(CF2)7CH2CH2OCOCH=CH2 was obtained at a CF3(CF2)7CH2CH2Cl conversion rate of 12% and at a selectivity of 80%. The results of NMR analysis revealed that a polymer generated by polymerization of CF3(CF2)7CH2CH2OCOCH=CH2 was produced at a selectivity of 5%. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
With 10H-phenothiazine; In tert-butyl alcohol; at 160℃; for 6h; | Into a pressure resistant autoclave (0.5 liter) equipped with stirring vanes (disk turbine), FI, potassium (meth)acrylate, PTZ and BuOH were charged in the amounts (unit: mol) as shown in Table 1, and an ester-forming reaction was carried out under the reaction conditions shown in Table 1 to obtain a reaction mixture. The conversion and selectivity of the reaction are shown in Table 1. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
With 10H-phenothiazine; In tert-butyl alcohol; at 150℃; for 6h; | Into a pressure resistant autoclave (10 liters) equipped with stirring vanes (Full Zone, manufactured by SHINKO PANTEC CO., LTD.), CqF2q+1(CH2)2I (wherein q is 4 or 6, hereinafter referred to as FI), potassium (meth)acrylate, phenothiazine (hereinafter referred to as PTZ) and tert-butanol (hereinafter referred to also as BuOH) were charged in the amounts (unit: mol) as shown in Table 1, and an ester-forming reaction was carried out under the reaction conditions shown in Table 1 to obtain a reaction mixture. The conversion and selectivity of the reaction are shown in Table 1. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
92.7% | In methanol | 2 EXAMPLE 2 EXAMPLE 2 110.2 g (1 mol) of potassium acrylate were admixed with 198.5 g (1 mol) of 3-chloropropyltrimethoxysilane, 2.8 g (0.01 mol) of 1-neopentyl-4-(4'-methylpiperidinyl)-pyridinium chloride and 0.3 g of N,N'-diphenyl-p-phenylenediamine, and the mixture was heated to 128° C. while stirring. After 2 hours at this temperature, the reaction mixture was cooled and the potassium chloride which had precipitated was filtered off. The potassium chloride was washed with 50 g of methanol. The methanol was evaporated from the combined filtrates, and the residue was distilled under reduced pressure, whereby 217 g of 3-acryloxypropyltrimethoxysilane with a boiling point of 80° C. (0.5 mbar) were obtained. The yield was 92.7% of theory, based on the amount of potassium acrylate which was used. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
With 4-methoxy-phenol; hydroquinone; In tert-butyl alcohol; at 180 - 190℃; for 6h;Product distribution / selectivity; | (Example 1) A mixture of ethylene adducts of fluoroalkyl iodides each of which adduct was represented by CF3(CF2)nCH2CH2I was obtained as a mixture containing the adducts of n≤6 in an amount of 5 mol%, the adduct of n=7 in an amount of 76 mol%, the adduct of n=8 in an amount of 0 mol%, the adduct of n=9 in an amount of 17 mol% and the adduct of n≥10 in an amount of 2 mol%. Next this mixture was reacted with an acrylic acid compound to give a mixture containing the fluorine-containing acrylic esters represented by the formula (1). Specifically, 1576g (2.67 mol) of the ethylene adducts of the fluoroalkyl iodides, 320g (2.90 mol) of potassium acrylate, 680mL of tert-butyl alcohol, and 1.8g of hydroquinone and 0.32g of hydroquinone monomethylether as inhibitors of polymerization were firstly charged into an autoclave with a volume of 3L and heated to 180C to 190C and reacted for 6 hours. After the reaction, a reaction mixture was cooled. Next, KI as a byproduct was removed by filtration. Thereafter, a filtrate was subjected to distillation to remove tert-butyl alcohol and then 1288g of a reaction mixture having a composition shown in Table 1 was obtained. 1000g of this reaction mixture was measured and charged into a still and then subjected to distillation for 2 hours at a pressure in a rectifier of 0.9kPa and a still temperature of 160C, introducing air into the still at a flow rate of 20 ml/min such that the oxygen concentration in the distillation column was 1 mol% relative to the total moles of gas-phase components in the distillation column. Further, the continuous distillation was carried out using an oldershaw-type distillation column with 20 plates which was made of glass as a whole (including the internal structure). As a result of the distillation, 886g of a mixture after distillation having a composition as shown in Table 1 was obtained as a distillate liquid (a recovery rate based on the fluorine-containing acrylic esters was 97%). In Table 1, the compositions of the reaction mixture and the mixture after distillation were determined by gas chromatography. Table 1 Component Reaction mixture (mol%) Mixture after distillation (mol%)C6F13CH=CH2 0.91 NDC8F17CH=CH2 13.65 NDC10F21CH=CH2 3.09 NDC12F25CH=CH2 0.34 0.01C6F13CH2CH2OH 0.11 NDC8F17CH2CH2OH 1.57 NDC10F21CH2CH2OH 0.35 0.04C12F25CH2CH2OH 0.04 0.05C6F13CH2CH2OCOCH=CH2 4.09 5.1C8F17CH2CH2OCOCH=CH2 60.73 75.93C10F21CH2CH2OCOCH=CH2 13.54 16.92C12F25CH2CH2OCOCH=CH2 1.58 1.96 As shown in Table 1, of the impurities contained in the reaction mixture, particularly C8F17CH=CH2, C10F21CH=CH2, C8F17CH2CH2OH and C10F21CH2CH2OH were able to be removed considerably by the distillation. As a result, the highly-pure mixture of the fluorine-containing acrylic esters was obtained, in which the contents of the fluorine-containing acrylic esters of n=7 and n=9 contained were large. Specifically, the mixture contained, as the impurities, C10F21CH2CH2OH (n=9) in an amount of 0.04 mol%, C12F25CH=CH2 (n=11) in an amount of 0.01 mol% and C12F25CH2CH2OH (n=11) in an amount of 0.05 mol%. (Comparative Example 1) The mixture of the fluorine-containing acrylic esters was obtained similarly to Example 1, and then the distillation was carried out similarly to Example 1. However, the distillation was carried out under the nitrogen atmosphere without using the inhibitor of polymerization and introducing oxygen into the distillation column. As a result, the esters were polymerized in the distillation column, and the intended mixture with a less impurity content was not able to be obtained well. It is considered that this was related also to the fact that the still temperature was made high in order that the ester with a large "n" value (n=7) was intended to be obtained by the distillation. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
With 4-methoxy-phenol; hydroquinone; In tert-butyl alcohol; at 180 - 190℃; for 6h;Product distribution / selectivity; | Example 2) The reaction mixture having a composition shown in Table 2 was obtained in the same manner as that in Example 1 except that a mixture of the ethylene adducts of fluoroalkyl iodides containing the adduct of n=7 in an amount of 80 mol% and the adduct of n=9 in an amount of 20 mol% was used. The mixture of the ethylene adducts containing ones of n=7 and n=9 was obtained by carrying out, before the ethylene addition, the rectification of the mixture of the fluoroalkyl iodides of n≥1 (which, however, does not substantially contain ones with "n" of an even number), in which distillation the initial distillate and the final distillate were cut in a large amount so that the fluoroalkyl iodides of n≤6 and n≥10 are not contained in the mixture that was then subjected to ethylene addition. 500g of this reaction mixture was measured and charged into the still with 22g of hydroquinone added, and then a continuous distillation was carried out at a pressure of the distillation column of 0.9kPa, a still temperature of 160C, introducing air into the still at a flow rate of 20ml/min such that the oxygen concentration in the distillation column was 1 mol% to the total moles of the gas-phase components in the distillation column. The continuous distillation was carried out for 10 hours providing the reaction mixture to the still at a rate of 80g/hr so that the total weight of the reaction mixture to be subjected to distillation was 1000g. Further, the distillation column was the same as that used in Example 1. As a result, 908g of the mixture after distillation having a composition as shown in Table 2 was obtained (a recovery rate based on the fluorine-containing acrylic esters was 98%) was obtained. In Table 2, the compositions of the reaction mixture and the mixture after distillation were determined by gas chromatography. Table 2 Component Reaction mixture (mol%) Mixture after distillation (mol%)C8F17CH=CH2 13.54 NDC10F21CH=CH2 3.41 NDC8F17CH2CH2OH 0.88 NDC10F21CH2CH2OH 0.18 0.03C8F17CH2CH2OCOCH=CH2 65.58 80.31C10F21CH2CH2OCOCH=CH2 16.41 19.66 As shown in Table 2, the highly-pure mixture of the fluorine-containing acrylic esters with less impurities was obtained in Example 2, similarly to Example 1. Specifically, only C10F21CH2CH2OH (n=9) was contained in an amount of 0.03 mol%. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
With 4-methoxy-phenol; hydroquinone; In tert-butyl alcohol; at 180 - 190℃; for 6h;Product distribution / selectivity; | (Example 3) A mixture containing the fluorine-containing acrylic esters represented by the formula (1) was obtained by obtaining a mixture of the ethylene adducts of the fluoroalkyl iodides, which adducts were represented by C8F17CH2CH2I (n=7) and then reacting this mixture with the acrylic acid compound. Specifically, 1533g (2.67 mol) of the ethylene adducts of fluoroiodides, 320g (2.90 mol) of potassium acrylate, 680mL of tert-butyl alcohol, and 1.8g of hydroquinone and 0.32g of hydroquinone monomethylether as inhibitors of polymerization were charged into an autoclave with a volume of 3L and heated to 180C to 190C and reacted for 6 hours. After the reaction, a reaction mixture was cooled. Next, KI as a byproduct was removed by filtration. Thereafter, a filtrate was subjected to distillation to remove tert-butyl alcohol and then 887g of a reaction mixture having a composition shown in Table 1 was obtained. 500g of this reaction mixture was measure and charged into a still and subjected to distillation for 6 hours at a pressure in a rectifier of 0.9kPa and a still temperature of 160C, introducing nitrogen into the still at a flow rate of 20 ml/min such that the oxygen concentration was 0 mol% relative to the total moles of gas-phase components in the distillation column. Further, the distillation column used in this example was the same as that used in Example 1. As a result of distillation, 272g of C8F17CH2CH2OCOCH=CH2 having a composition as shown in Table 1 was obtained as a distillate a distillate liquid (a recovery rate based on the fluorine-containing acrylic esters was 59%). In Table 1, the compositions of the reaction mixture and the mixture after distillation were determined by gas chromatography. Table 3 Component Reaction mixture (mol%) Mixture after distillation (mol%)C8F17CH=CH2 7.04 0C8F17CH2CH2OH 1.79 0.32C8F17CH2CH2OCOCH=CH2 88.79 97.18 As shown in Table 3, a highly-pure mixture of the fluorine-containing acrylic esters with less impurities was obtained also in Example 3, similarly to Examples 1 and 2. Specifically, the mixture contained, as the impurity, C8F17CH2CH2OH (n=7) in an amount of 0.32 mol%.(Comparative Example 2) The ethylene adducts of the fluoroalkyl iodides, which adduct was represented by C8F17CH2CH2I (n=7) was obtained and then this mixture was reacted with the acid ester compound to give a mixture containing the fluorine-containing acrylic esters represented by the formula (1). Specifically, 1533g (2.67 mol) of the ethylene adduct of the fluoroiodide and 320g (2.90 mol) of acrylate potassium, 680mL of tert-butyl alcohol, 1.8g of hydroquinone and 0.32g of hydroquinone monomethylether as the inhibitors of polymerization were firstly charged into an autoclave with a volume of 3L and heated to 180C to 190C and reacted for 6 hours. After the reaction, a reaction mixture was cooled. Next, KI as a byproduct was removed by filtration. Thereafter, a filtrate was subjected to distillation to remove tert-butyl alcohol and then 1360g of a reaction mixture having a composition shown in Table 1 was obtained. 500g of this reaction mixture was measured and charged into a still and subjected to distillation at a pressure in a distillation column of 0.9kPa and a still temperature of 160C, introducing air into the still at a flow rate of 20 ml/min such that the oxygen concentration in the distillation column was 1 mol% relative to the total moles of gas-phase components in the distillation column. Further, the continuous distillation was carried out using an oldershaw-type distillation column with 20 plates which is made of iron as a whole (including the internal structure). As a result of the distillation, 412g of C8F17CH2CH2OCOCH=CH2 having a composition as shown in Table 1 was obtained as a distillate liquid (a recovery rate based on the fluorine-containing acrylic esters was 89%). In Table 1, the compositions of the reaction mixture and the mixture after distillation were determined by gas chromatography. Table 4 Component Reaction mixture (mol%) Mixture after distillation (mol%)C8F17CH=CH2 7.04 NDC8F17CH2CH2OH 1.79 NDC8F17CH2CH2OCOCH=CH2 88.79 97.44 Comparative Example 2 is an example wherein the internal structure of the distillation column was made of iron having a low electrode potential. As shown in Table 4, a highly-pure mixture of the fluorine-containing acrylic esters with less impurities was obtained also in Comparative Example 2, similarly to Examples 1, 2 and 3. However, the recovery rate was low and the resultant distillate liquid was colored brownish yellow which could not be used as a product. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
< 0.5%Chromat.; < 0.5%Chromat. | at 100℃; for 4h;Product distribution / selectivity; | The process of Example 1 was repeated except that potassium acrylate was used in place of silver oxide and the following conditions applied. Using a potassium acrylate/8-2-I molar ratio of 1.1 and an acrylic acid/8-2-I weight ratio of 4, for 4 hours at 100 C. provided less than 5% conversion of 8-2-I; less than <0.5% yield of the fluorinated alkyl acrylate, CF3(CF2)7CH2CH2O2CCHCH2; less than 0.5% yield of the alcohol, F(CF2CF2)nCH2CH2OH; and less than 0.5% yield of the olefin, CF3(CF2)7CHCH2. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
A mixture of fluoroalkyl alcohols represented by C2F5(CF2CF2)nI was produced as follows. 100g of CF3CF2I as a telogen was charged into a reactor together with 10g of a copper catalyst. These are stirred to give a slurry in which the copper catalyst was suspended and the slurry was heated to 80C. Tetrafluoroethylene as a taxogen was charged into the reactor with the temperature inside the reactor kept at 80C and the reaction pressure was maintained at 0.8MPa. At the time when 10g of tetrafluoroethylene was charged, it was confirmed by gas chromatography that the telomerization reaction proceeded. The resultant mixture of the fluoroalkyl iodides was subjected to distillation selecting the theoretical number of ten(10), the bottom temperature of from 60C to 140C and the pressure in the column of from 100 to 10kPa. The telomers with smaller "n" values were withdrawn from the column top sequentially and then a mixture containing the fluoroalkyl iodides of n=3 and n=4 in an amount of 91 mol% in total was drawn from the column top and this mixture was used in the next ethylene addition step. More specifically, this mixture contained the fluoroalkyl iodides with n≤2 in an amount of 5 mol%, one with n=3 in an amount of 76 mol%, one with n=4 in an amount of 17 mol% and one with n≥5 in an amount of 2 mol%. The mixture obtained in this manner was subjected to ethylene addition to give ethylene adducts. The ethylene addition step was carried out as follows. 100g of the fluoroalkyl iodide mixture and 5g of copper catalyst as a catalyst were charged into an autoclave and then heated to 100C. Next, an ethylene gas was charged into a gas phase so that the reaction pressure was kept at 0.3MPa, and the reaction was made for three hours. As a result, a mixture of the ethylene adducts was obtained. An yield of the ethylene adducts was 99 mass%. Next, an esterification step was carried out according to the following procedures. 1576g (2.67 mol) of the mixture of the ethylene adducts obtained by carrying out the ethylene addition step according to the above procedures, 320g (2.90 mol) of potassium acrylate, 680mL of tert-butyl alcohol, and 1.8g of hydroquinone and 0.32g of hydroquinone monomethylether were firstly charged into an autoclave with a volume of 3L and heated to 180C-190C and reacted for 6 hours. After the reaction, a reaction mixture was cooled. Next, KI as a byproduct was removed by filtration. Thereafter, a filtrate was subjected to distillation to remove tert-butyl alcohol and then a reaction mixture having a composition shown in Table 1 was obtained. 1000g of this reaction mixture was measured and charged into a still and then subjected to distillation using a rectifier with theoretical plate number of ten(10) and selecting the pressure inside the rectifier of 0.9kPa and the still temperature of 160C. As a result, a mixture after distillation having a composition as shown in Table 1 was obtained as a distillate liquid In Table 1, the compositions of the reaction mixture and the mixture after distillation were determined by gas chromatography; As shown in Table 1, the impurities contained in the reaction mixture, specifically, C8F17CH=CH2, C10F21CH=CH2, C8F17CH2CH2OH and C10F21CH2CH2OH were able to be removed considerably by the distillation. As a result, the highly-pure mixture of the fluorine-containing acrylic esters was obtained, in which the contents of the fluorine-containing acrylic esters of n=3 and n=4 contained were large. Specifically, the mixture contained, as the impurities, C10F21CH2CH2OH (n=4) in an amount of 0.04 mol%, C12F25CH=CH2 (n=5) in an amount of 0.01 mol% and C12F25CH2CH2OH (n=5) in an amount of 0.05 mol% |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
The reaction mixture having a composition as shown in Table 3 was obtained in the same manner as that in Example 1 except that the rectification conditions of the fluoroalkyl iodide mixture were changed and the rectification after the telomerization reaction was carried out so that a mixture wherein only the fluoroalkyl iodides of n≤2 were removed (that is, a mixture of the fluoroalkyl iodides of n≥3) was obtained by carrying out the rectification, and then the mixture was used in the ethylene addition step. 1000g of this reaction mixture was measured, charged into a still and subjected to distillation using a rectifier with the theoretical plate number of ten(10) and selecting the pressure inside the rectifier of 0.9kPa and the still temperature of 160C. As a result, a mixture after distillation having a composition as shown in Table 3 was obtained as a still residue. In Table 3, the compositions of the reaction mixture and the mixture after distillation were determined by gas chromatography; The impurities derived from CnF2nI of n≥5 is contained in addition to the impurities derived from CnF2nI of n=3 and n=4 in the mixture of the fluorine-containing acrylic esters obtained in this comparative example. Of these impurities, the alcohols and the olefins with smaller "n" values were able to be removed considerably, but the alcohols and the olefins with larger "n" values remained in the mixture after distillation. Specifically, the proportion of the sum of the impurities (the alcohols and the olefins) was 0.95 mol% and the proportion of C10F21CH2CH2OH (n=5) was 0.37 mol%. As described above, the mixture of the fluorine-containing (meth)acrylic esters can be obtained wherein the proportion of the impurities is reduced to a ppm level according to the production method of the present invention. The monomer mixture with less impurities is useful for producing a polymer of high quality. Further, the method of the present invention makes it possible to give the mixture which contains the fluorine-containing (meth) acrylic esters with "n" values of 3 and 4 at a high ratio and the fluorine-containing (meth)acrylic esters with n≤2 or n≥5 at a low ratio. As described above, the fluorine-containing (meth)acrylic esters with n=3 and 4 are monomers which produce the polymer useful as the water- and oil-repellent, and therefore the production method of the present invention contributes to improvement in the quality of the polymer in this point. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
The reaction mixture having a composition shown in Table 2 was obtained in the same manner as that in Example 1 except that the rectification was carried out so that more initial distillate and more final distillate were cut and the fluoroalkyl iodides of n=2 and n=5 were not contained in the mixture, to give a mixture which contains the fluoroalkyl iodide of n=3 in an amount of 80 mol% and the fluoroalkyl iodide of n=4 in an amount of 20 mol%. 1000g of this reaction mixture was measured, charged into a still and subjected to continuous distillation using a rectifier with the theoretical plate number of ten(10) and selecting the pressure in the rectifier of 0.9kPa and the still temperature of 160C. As a result, a mixture after distillation having a composition as shown in Table 2 was obtained as a distillate liquid In Table 2, the compositions of the reaction mixture and the mixture after distillation were determined by gas chromatography; As shown in Table 2, the highly-pure mixture of the fluorine-containing acrylic esters with less impurities was obtained also in Example 2 similarly to Example 1. Specifically, only C10F21CH2CH2OH (n=4) was contained in an amount of 0.03 mol% as the impurity |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
With triethylamine at -8 - -6℃; for 3h; |
Yield | Reaction Conditions | Operation in experiment |
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40% | With hydroquinone In N,N-dimethyl-formamide for 6h; boiling; | 1 Reference example 1Preparation of l,3-bis(acryIoyloxymethyl)-l,l53,3-tetramethyldisiloxane (SDA)Compound of the general formula (Ila), wherein X = H, m = 0, n = 1A 500-ml four-necked flask equipped with a thermometer, a reflux condenser closed with a CaCl2 tube, a stirrer and a dropping funnel is charged with 90.0 g (0.7965 mol) of potassium acrylate (which was previously prepared from acrylic acid and potassium carbonate), 2.0 g of hydroquinone and 200 ml of dimethylformamide. The reaction mixture is heated until dissolution and then 77.0 g (0.3333 mol) of (ClCH2SiMe2)20, i.e. 1.3-bis(chloromethyl)-l,l,3,3,-tetramethyldisiloxane is slowly added thereto. The reaction mixture is boiled for 6 hours and then the KCl salt formed is filtered over a G3 glass filter. 80% of the solvent is distilled off, the residue is dissolved in 300 ml of diethyl ether, washed four times with distilled water and then dried overnight over CaCl2. The mixture is filtered, the solvent is distilled off and the residue is distilled under vacuum.Deinhibiting (hereinafter similarly): the crude product obtained is extracted using diethyl ether, washed with In aqueous NaOH solution and then washed neutral with water. It is dried over CaCl2i filtered, finally the solvent is distilled off.m=39.9 g of desired compound is obtained. Yield: 40.0%nd20= 1.4400. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
85.6% | With tetrabutylammomium bromide at 125 - 130℃; for 5h; Large scale; | 3 example 3 In with mechanical stirring device, a thermometer, a reflux condenser 1000 litres of enamel in the reactor, are sequentially added 397.2 kg (2kmol) 3-chloro-propyl trimethoxy silane, 220.4 kg (2kmol) acrylic acid potassium, 2.0 kg antipolymerizer ZJ-705,6.0 kg of tetrabutyl ammonium bromide, stirring and mixing. Through steam heating, the temperature control of reaction is in the 125 °C -130 °C, is carried out under the atmospheric pressure the stirring, the stirring time is 5 hours, cooling, rufous turbid mixture obtained; the centrifuge rufous turbidity of the mixed solution is filtered, and the filter residue rufous transparent filtrate obtained; with 200 kg of methanol wash the filter residue, collecting the washing liquid, washing filtrate is combined and. And the filtrate into the washing liquid in a tank, first rectification under the atmospheric pressure, removing methanol. Then at the temperature 96 °C -98 °C, vacuum -0.098 MPa lower rectifying, get 340.1 kg 3-acryloxy propyl trimethoxy silane, it is a colorless transparent liquid. The 3-acryloxypropyltrimethoxysilane product obtained by the above-mentioned production method had a purity of 99.6%, and the mass yield was 85.6% based on the 3-chloropropyltrimethoxysilane used. |
Yield | Reaction Conditions | Operation in experiment |
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86% | With 2,6-di-tert-butyl-4-methyl-phenol In toluene at 45 - 50℃; for 6h; Inert atmosphere; | 1 Example 1 In a three-necked flask with 1000 ml of stirring, nitrogen and condensing tubes in a three-necked flask, under the protection of nitrogen, according to the ratio of triisopropylsilyl chloride: potassium acrylate:toluene=1πο 1:1.1 mol:300 ml The apparatus was charged with 193 g of triisopropylsilyl chloride, 121 g of potassium acrylate and 300 ml of toluene while adding 3.71 g of the 8 crown 6 catalyst, 4.23 g of the polymerization inhibitor 2,6-di-tert-butyl-4-methylphenol, and then a three-neck flask apparatus. While stirring, the temperature was raised to (45-50) °C, and reacted at this reaction temperature for 6 hours to obtain a reaction solution containing triisopropylsilyl acrylate;(2) Next, the reaction solution obtained in step (1) is filtered at room temperature to obtain filtrate residue 120g, and a filtrate containing triisopropylsilyl acrylate 403g;(3) Next, 4.03 g of polymerization inhibitor 2,6-di-tert-butyl-4-methylphenol is added to the filtrate obtained by filtration in step (2), and then the filtrate containing the polymerization inhibitor is subjected to vacuum distillation to obtain Triisopropylsilyl acrylate 197g.The triisopropylsilyl acrylate obtained in this example has a purity of 99.1% and a yield of 86%. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
82.7% | With 2,2-diphenyl-1-picrylhydrazine at 150℃; for 1h; | 3.2 (2) Add 0.34mol of potassium acrylate to the trimethylsilyl methanesulfonate system prepared in (1) above to inhibit polymerization agent 1,1-diphenyl-2-bitter hydrazine 1.1g, warm to 150°C, react for 1 hour, cool to room temperature, filter with suction, filter cake with 100ml dimethylbenzene washing. The filtrate was rectified to obtain trimethylsilyl acrylate, GC: 99.3%, yield 82.7%. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
93.3% | With 10H-phenothiazine; methanesulfonyl chloride; 4-methoxy-phenol In acetone for 0.5h; Cooling with ice; | 1-4 <Synthesis of acrylate anhydride; potassium acrylate, MsCl type> Acetone 151.5 mL, potassium acrylate 50.5 g (0.46 mol), 4-methoxyphenol 50.5 mg, and phenothiazine 50.5 mg under an ice bath while passing pure air through a 300 ml four-necked flask equipped with a stirrer and a thermometer. Was charged, stirred and dispersed. 25.0 g (0.22 mol) of MsCl was added dropwise thereto over 30 minutes. Then, the mixture was stirred under an ice bath, and when it was confirmed that the exotherm had subsided, the outside temperature was set to 25 ° C., and the reaction was followed by GC while aging for 1 hour. As a result, it was confirmed that MsCl had disappeared. The conversion rate of the crude body was 99.1%. After completion of the reaction, the mixture was filtered using a filter paper, washed with 100 mL of acetone three times, and then acetone was distilled off under reduced pressure to obtain 28.5 g of crude acrylic anhydride (crude yield 103.5% with respect to MsCl, GC). Purity 95.3%) was obtained. The crude product was distilled under reduced pressure under pure air to obtain 25.7 g of acrylic anhydride (b.p. 40 ° C. (O.4 kPa), yield 93.3% with respect to MsCl, GC purity 99.3%). |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
With potassium hydroxide In water at 60℃; Electrochemical reaction; |
Tags: 10192-85-5 synthesis path| 10192-85-5 SDS| 10192-85-5 COA| 10192-85-5 purity| 10192-85-5 application| 10192-85-5 NMR| 10192-85-5 COA| 10192-85-5 structure
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Code | Phrase |
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Response | |
Code | Phrase |
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Code | Phrase |
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Health hazards | |
Code | Phrase |
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H311 | Toxic in contact with skin |
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H318 | Causes serious eye damage |
H319 | Causes serious eye irritation |
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H362 | May cause harm to breast-fed children |
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H371 | May cause damage to organs |
H372 | Causes damage to organs through prolonged or repeated exposure |
H373 | May cause damage to organs through prolonged or repeated exposure |
Environmental hazards | |
Code | Phrase |
H400 | Very toxic to aquatic life |
H401 | Toxic to aquatic life |
H402 | Harmful to aquatic life |
H410 | Very toxic to aquatic life with long-lasting effects |
H411 | Toxic to aquatic life with long-lasting effects |
H412 | Harmful to aquatic life with long-lasting effects |
H413 | May cause long-lasting harmful effects to aquatic life |
H420 | Harms public health and the environment by destroying ozone in the upper atmosphere |
Sorry,this product has been discontinued.
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