CN1335291A - Preparation of 1,1,1,3,3-pentachloropropane - Google Patents
Preparation of 1,1,1,3,3-pentachloropropane Download PDFInfo
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- CN1335291A CN1335291A CN 00122013 CN00122013A CN1335291A CN 1335291 A CN1335291 A CN 1335291A CN 00122013 CN00122013 CN 00122013 CN 00122013 A CN00122013 A CN 00122013A CN 1335291 A CN1335291 A CN 1335291A
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Abstract
The preparation process of 1,1,1,3,3-pentachloropropane in high selectivity and high conversion rate is the reaction of carbon tetrachloride and chloroethylene inside one reactor in 85-130 deg.c for 2-10 hr and in the presence of cuprous chloride/alcohol amine composite catalyst. The molar ratio between cuprous chloride and alcohol amine is 0.2-10 and during reaction, one simple metal substance of Fe, Co, Ni, Ti, Zn and Cr in 0.30-1.0 wt% of the total reacted material may be added.
Description
The invention relates to a preparation method of saturated halogenated hydrocarbon, in particular to a preparation method of 1,1,1,3, 3-pentachloropropane.
1,1,1,3, 3-pentachloropropane is an intermediate in the preparation of 1,1,1,3, 3-pentafluoropropane. 1,1,1,3, 3-pentafluoropropane is known in the art as HFC245 fa. HFC245fa has very good special properties, so that it can be widely used in cleaning, foaming, refrigeration and other industries. The ODP value of HFC245fa is zero, and has no potential damage effect on the atmosphere, so that HFC245fa is considered as an ideal substitute for R141b, and is a novel environment-friendly product.
The literature reports that the methods for preparing the HFC245fa intermediate mainly comprise the following methods: firstly, 1,1,1,3,3, 3-hexachloropropane is synthesized by telomerization of 1, 1-dichloroethylene and carbon tetrachloride and then reduced to 1,1,1,3, 3-pentachloropropane as disclosed in WO 97/37956; 1, 1-dichloroethylene is a chemical substance which is easy to generate self-polymerization, is not beneficial to storage and transportation, is easy to generate high polymer in the reaction, so that the yield is reduced, and the telomerization reaction of the 1, 1-dichloroethylene and carbon tetrachloride has stronger corrosivity to equipment, so that the investment cost to the reaction equipment can be correspondingly improved; secondly, 1,1,1,3, 3-pentachloropropane is synthesized by telomerization of carbon tetrachloride and chloroethylene, CuCl is added as a catalyst, and amines are added as a cocatalyst, as disclosed in WO96/01797 patent application, but the conversion rate of raw materials in the process is not high; thirdly, starting from ethylene, 1,1,1, 3-tetrachloropropane is synthesized, and then 1,1,1,3, 3-pentachloropropane is synthesized by photochlorination of 1,1,1, 3-tetrachloropropane, as disclosed in U.S. Pat. No. 5,5705779; the conversion rate of 1,1,1,3, 3-pentachloropropane generated by the photochlorination reaction in the route is not high, the selectivity is poor, and the industrial amplification is difficult.
The 1,1,1,3, 3-pentachloropropane is used as an intermediate to prepare HFC245fa, the process is simple, the conversion rate of the raw materials is high, and reaction byproducts are few, so that the development of an economical and reasonable industrial production route of the 1,1,1,3, 3-pentachloropropane has high commercial value.
The invention aims to overcome the defects of the preparation method of 1,1,1,3, 3-pentachloropropane in the prior art, and provides the preparation method of 1,1,1,3, 3-pentachloropropane with high conversion rate and selectivity, which is economically feasible for large-scale production.
The technical scheme of the preparation method of the 1,1,1,3, 3-pentachloropropane is that a catalyst, carbon tetrachloride and chloroethylene are added into a reactor for reaction, and the preparation method is characterized in that the catalyst is a composite catalyst consisting of cuprous chloride and alcohol amine. The alcohol amine may be NH(3-n)[(CH2)2OH]n、 
One or a mixture thereof, wherein n is 1, 2 or 3.
In order to improve the selectivity of the reaction, a metal simple substance is added into a reactor in the reaction.
The mol ratio of the cuprous chloride to the alcohol amine of the composite catalyst used in the invention can be 1: 0.1-5, and the preferable mol ratio is 1: 0.5-2.
The reaction temperature of the invention can be 50-180 ℃, and the reaction time can be 2-10 hours.
The preferable reaction temperature of the invention is 85-130 ℃, and the reaction time is 3-6 hours.
The metal simple substance can be one of iron, cobalt, nickel, titanium, zinc and chromium.
The amount of the metal added into the reactor can be 0.30-1.0% of the total weight of the reaction materials, and preferably 0.40-0.80%.
The invention adopts cuprous chloride and alcohol amine as composite catalyst, uses carbon tetrachloride and chloroethylene to regulate and polymerize to synthesize 1,1,1,3, 3-pentachloropropane, and the reaction formula is as follows: 。
in order to dissolve the catalyst, a solvent inert to the reactants and the final product may be used in the telomerization, for example dimethyl sulfoxide, dimethylformamide, acetonitrile, tert-butanol.
In order to improve the conversion rate of vinyl chloride, a method of excess carbon tetrachloride is adopted for reaction, and the molar ratio of the carbon tetrachloride to the vinyl chloride can be 1: 0.2-1, and preferably 1: 0.5-0.9.
The dosage of the composite catalyst is 1-5%, preferably 2-3% of the mole number of the raw material chloroethylene.
The experimental research shows that compared with the prior art, the invention adopts the composite catalyst consisting of cuprous chloride and alcohol amine, the selectivity and the product yield of the reaction are greatly improved, the selectivity can be improved from about 90 percent (the prior art) to about 96 percent (the invention), the product yield can be improved from about 45 percent (the prior art) to about 87 percent (the invention), the reaction time can also be reduced, and can be reduced from 11 hours (the prior art) to 4 hours (the invention), and the reaction can be carried out under a milder condition, so that the byproducts of the reaction, especially high polymers, can be reduced, the generation of acidic substances can be reduced, and the corrosivity to equipment can be reduced; the invention of adding metal simple substance during reaction can further improve the yield of the product, which can be improved from about 87% to about 95%.
The following describes embodiments of the present invention.
EXAMPLE 1 absence of Complex catalyst
320 g CCl were placed in a Teflon lined autoclave4100ml acetonitrile, 4 g CuCl, autoclave closed and purged with N2Replacing air in the kettle, stirring and heating to 110 ℃, continuously adding 80 g of chloroethylene, controlling the kettle pressure not to exceed 1Mpa, keeping the temperature at 120 ℃ after the kettle pressure is completely added, reacting for 11 hours, cooling to normal temperature, taking out the content, carrying out reduced pressure distillation to recover acetonitrile serving as a solvent and unreacted carbon tetrachloride, filtering to obtain 136 g of product, and carrying out GC (gas chromatography) separationThe purity was 94.52% and the yield was 46.3% based on vinyl chloride.
EXAMPLE 2 addition of composite catalyst
2 g of CuCl and 1 g of NH were added to the reactor2(CH2)2The composite catalyst consisting of OH was reacted at 120 ℃ for 4 hours under the same conditions as in example 1, to obtain 249 g of a product having a purity of 96.13% and a yield of 86.5% based on vinyl chloride.
EXAMPLE 3 addition of composite catalyst
2 g of CuCl and 1 g of NH [ (CH) are introduced into the reactor2)2OH]2The composite catalyst of composition, other conditions and procedure were the same as in example 2, yielding 246 grams of product with a purity of 95.76% and a product yield of 85.2% based on vinyl chloride.
Example 4 addition of composite catalyst
1.5 g of CuCl and 1.5 g of N were charged into a reactor[(CH2)2OH]3The composite catalyst composition, other conditions and procedures were the same as in example 2, to provide 252 grams of product having a purity of 96.35% and a product yield of 87.7% based on vinyl chloride.
EXAMPLE 5 addition of composite catalyst to a reactor, 1.5 g of CuCl and 1.5 g were addedThe composite catalyst of composition, other conditions and procedure were the same as in example 2, giving 249 grams of product having a purity of 96.32% and a product yield of 86.1% based on vinyl chloride.
EXAMPLE 6-addition of composite catalyst 1.5 g of CuCl and 1.5 g of catalyst were charged to a reactorThe composite catalyst composition, other conditions and procedures were the same as in example 2, to give 250 g of product having a purity of 96.12% and a product yield of 86.8% based on vinyl chloride.EXAMPLE 7 addition of composite catalyst to a reactor, 1.5 g of CuCl and 1.5 g were added
NH2CH2CH2CH2OH、N[(CH2)2OH]30.5 g of each composite catalyst, the other conditions and procedure being identical to those of example 2, gave 248 g of product having a purity of 96.53% and a product yield of 86.4% based on vinyl chloride.
Example 8 addition of composite catalyst and elemental titanium
The reactor was charged with 2 g of titanium and the procedure was otherwise the same as in example 4 to give 266 g of product having a purity of 99.70% and a product yield of 95.7% based on vinyl chloride.
Example 9 addition of composite catalyst and elemental iron
2 g of iron were charged to the reactor and the procedure was otherwise the same as in example 4, to give 263 g of a liquid product having a purity of 99.12% and a product yield of 94.1% based on vinyl chloride.
Example 10 addition of composite catalyst and elemental Metal Nickel
The reactor was charged with 2 grams of nickel and the procedure was otherwise the same as in example 4 to provide 266 grams of product having a purity of 99.55% and a product yield of 95.5% based on vinyl chloride.
EXAMPLE 11 addition of composite catalyst and reaction at lower temperatures
80 g of vinyl chloride was continuously added to the reactor heated to 105 ℃ and the reaction was carried out at 115 ℃ for 4 hours under the same conditions as in example 2, to obtain 245 g of a product having a purity of 96.78% and a yield of 85.2% based on vinyl chloride.
Claims (10)
1. The preparation method of 1,1,1,3, 3-pentachloropropane is characterized in that a catalyst is a composite catalyst consisting of cuprous chloride and alcohol amine, and the catalyst is prepared by adding the catalyst, carbon tetrachloride and chloroethylene into a reactor for reaction.
2. The process for preparing 1,1,1,3, 3-pentachloropropane according to claim 1, characterized in that the alcohol amine is NH(3-n)[(CH2)2OH]n、 One or a mixture thereof, wherein n is 1, 2 or 3.
3. The process for preparing 1,1,1,3, 3-pentachloropropane according to claim 1 or 2, characterized in that the reaction is carried out by adding the metal element into the reactor.
4. The method for preparing 1,1,1,3, 3-pentachloropropane according to claim 3, wherein the molar ratio of cuprous chloride to alcohol amine is 1: 0.1-5.
5. The method for preparing 1,1,1,3, 3-pentachloropropane according to claim 4, wherein the reaction temperature is 50-180 ℃ and the reaction time is 2-10 hours.
6. The method for preparing 1,1,1,3, 3-pentachloropropane according to claim 5, wherein the reaction temperature is 85-130 ℃.
7. The method for preparing 1,1,1,3, 3-pentachloropropane according to claim 5, wherein the reaction time is 3 to 6 hours.
8. The method for preparing 1,1,1,3, 3-pentachloropropane according to claim 5, wherein the metal is one of iron, cobalt, nickel, titanium, zinc, and chromium.
9. The method for preparing 1,1,1,3, 3-pentachloropropane according to claim 8, wherein the metal added is 0.30-1.0% of the total amount of the reaction materials.
10. The method for preparing 1,1,1,3, 3-pentachloropropane according to claim 9, wherein the metal added is 0.40-0.80% of the total amount of the reaction materials.
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| CN 00122013 CN1213005C (en) | 2000-07-20 | 2000-07-20 | Preparation of 1,1,1,3,3-pentachloropropane |
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| CN 00122013 CN1213005C (en) | 2000-07-20 | 2000-07-20 | Preparation of 1,1,1,3,3-pentachloropropane |
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| CN1335291A true CN1335291A (en) | 2002-02-13 |
| CN1213005C CN1213005C (en) | 2005-08-03 |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101913980A (en) * | 2010-09-07 | 2010-12-15 | 西安近代化学研究所 | Production method of 1,1,1,3,3-pentachloropropane |
| CN101544535B (en) * | 2009-05-01 | 2012-07-18 | 浙江三美化工股份有限公司 | Method for preparing synthetic 1,1,1,3,3-pentachloro propane |
| CN104230648A (en) * | 2013-06-18 | 2014-12-24 | 徐家乐 | Preparation method for synthesizing 1,1,1,3,3-pentachloropropane by carbon tetrachloride |
| CN104226367A (en) * | 2013-06-18 | 2014-12-24 | 林卫荃 | Composite catalyst |
| CN104230649A (en) * | 2013-06-18 | 2014-12-24 | 林卫荃 | Method for preparing pentachloropropane |
| CN114634396A (en) * | 2021-12-29 | 2022-06-17 | 山东东岳化工有限公司 | Pentachloropropane and preparation method thereof |
-
2000
- 2000-07-20 CN CN 00122013 patent/CN1213005C/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101544535B (en) * | 2009-05-01 | 2012-07-18 | 浙江三美化工股份有限公司 | Method for preparing synthetic 1,1,1,3,3-pentachloro propane |
| CN101913980A (en) * | 2010-09-07 | 2010-12-15 | 西安近代化学研究所 | Production method of 1,1,1,3,3-pentachloropropane |
| CN104230648A (en) * | 2013-06-18 | 2014-12-24 | 徐家乐 | Preparation method for synthesizing 1,1,1,3,3-pentachloropropane by carbon tetrachloride |
| CN104226367A (en) * | 2013-06-18 | 2014-12-24 | 林卫荃 | Composite catalyst |
| CN104230649A (en) * | 2013-06-18 | 2014-12-24 | 林卫荃 | Method for preparing pentachloropropane |
| CN114634396A (en) * | 2021-12-29 | 2022-06-17 | 山东东岳化工有限公司 | Pentachloropropane and preparation method thereof |
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| CN1213005C (en) | 2005-08-03 |
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Granted publication date: 20050803 |