JP2010150213A - Method for producing 1,4-bis(dichloromethyl)tetrafluorobenzene - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for quickly synthesizing 1,4-bis(dichloromethyl)tetrafluorobenzene (DCMTFB) in a high yield, suitable for mass production. <P>SOLUTION: The synthesis of 1,4-bis(dichloromethyl)tetrafluorobenzene by addition of formamide as a catalyst is achieved by reacting tetrafluoroterephthalaldehyde with SOCl<SB>2</SB>in an organic solvent and has remarkable advantages such as shortening of reaction time, simplification of synthesis process, improvement in yield of product, etc. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

  The present invention relates to a method for producing 1,4-bis (dichloromethyl) tetrafluorobenzene (DCMTFB), and more specifically, production of 1,4-bis (dichloromethyl) tetrafluorobenzene in high yield in mass production. Regarding the method.

  Parylene polymers have a number of advantages for manufacturing purposes. For example, the coating environment is at room temperature; there is no residual stress after coating; the thickness of the deposited film can be accurately controlled. In addition, the parylene polymer film has advantages such as uniformity, excellent acid and alkali resistance, high transparency and low dielectric constant. Thus, parylene polymer films are widely used in electrical insulation of printed circuit boards, moisture protection of sensors or medical devices, and corrosion protection of metal coatings. At present, fluoroparylene polymers are attracting attention because they have a low dielectric constant and a high melting point, and can be used in the electrical industry and the coating industry.

フルオロパリレンポリマーは、一般的に、室温での真空中の化学気相蒸着によって、製品上にコートされる。フルオロパリレンポリマーでコートした製品は、優れた防食、防湿および絶縁特性を有するだけではなく、格別に薄く、透明で、細孔が無いという利点をも有する。物体表面上の活性モノマーを重合することにより、フルオロパリレンポリマーコーティングを形成し得る。液体コーティング法の一般的工程とは異なり、初めにパリレンダイマーを気化し、熱分解条件でダイマー結合が開裂してモノマーフリーラジカルが生じるにつれて、モノマーフリーラジカルが重合してパリレンポリマーを形成するという、別のコーティング法がある。 One of the fluoroparylene polymers, for example, poly (tetrafluoro-p-xylene) has a structure represented by the following formula (1).

The fluoroparylene polymer is typically coated on the product by chemical vapor deposition in vacuum at room temperature. A product coated with a fluoroparylene polymer not only has excellent anti-corrosion, moisture-proof and insulating properties, but also has the advantage of being exceptionally thin, transparent and free of pores. By polymerizing active monomers on the surface of the object, a fluoroparylene polymer coating can be formed. Unlike the general process of the liquid coating method, the parylene dimer is first vaporized, and the monomer free radical is polymerized to form a parylene polymer as the dimer bond is cleaved and the monomer free radical is generated under thermal decomposition conditions. There is another coating method.

Currently, a dimer of fluoroparylene polymer frequently used in industry is octafluoro-2,2-paracyclophane represented by the following formula (2).

The dielectric constant of fluoroparylene polymers decreases as the number of fluorine atoms in the polymer increases. Accordingly, it can be expected that a parylene polymer represented by the following formula (3) and polymerized from a dimer of a fluoroparylene polymer not containing a hydrogen atom may have a lower dielectric constant.

It is important that 1,4-bis (bromodifluoromethyl) tetrafluorobenzene (BFTFB) represented by the following formula (4) is a monomer of the above dimer of the fluoroparylene polymer and does not contain any hydrogen atom. is there.

1,4-bis (dichloromethyl) tetrafluorobenzene (DCMTFB) represented by the following formula (5) is very important for the synthesis of 1,4-bis (bromodifluoromethyl) tetrafluorobenzene (BFTFB). Precursor.

しかし、この方法は時間がかかり、収率が低く、粗生成物の精製にシリカゲルカラムクロマトグラフィーを要する。従って、この方法は、大量生産には適さない。 Recently, 1,4-bis (dichloromethyl) tetrafluorobenzene (DCMTFB) reacts with 1,2,4,5-tetrafluorobenzene (TFB) with CHCl ₃ as shown in the following reaction (I). To be synthesized.

However, this method is time consuming, yields low, and requires silica gel column chromatography to purify the crude product. Therefore, this method is not suitable for mass production.

  Accordingly, it is desirable to provide a method for the rapid and high yield synthesis of 1,4-bis (dichloromethyl) tetrafluorobenzene (DCMTFB) that is suitable for mass production.

The present invention provides a method for producing 1,4-bis (dichloromethyl) tetrafluorobenzene. This method can shorten the reaction time, simplify the process, and improve the yield of 1,4-bis (dichloromethyl) tetrafluorobenzene production. The reaction of this method is shown in the following reaction (II).

The present invention is a method for producing 1,4-bis (dichloromethyl) tetrafluorobenzene,
(a) mixing tetrafluoroterephthalaldehyde, catalyst and SOCl ₂ with or without an organic solvent to form a mixture, wherein the catalyst belongs to formamide;
(b) heating the mixture;
(c) cooling the mixture, slowly adding the mixture into water and allowing the mixture to separate into two layers;
(d) obtaining an organic layer from a layer of the mixture; and
(e) A method comprising purifying an organic layer, removing an organic solvent and a catalyst in the organic layer, and providing 1,4-bis (dichloromethyl) tetrafluorobenzene.

In the process of the invention, the molar ratio of tetrafluoroterephthalaldehyde to SOCl ₂ is at least greater than 2. The molar ratio of tetrafluoroterephthalaldehyde to SOCl ₂ is preferably in the range of 2-20, more preferably in the range of 5-8.

  In the process of the invention, the weight ratio of catalyst to tetrafluoroterephthalaldehyde is in the range of 0.1 to 1.0, preferably in the range of 0.2 to 0.4.

  In the method of the present invention, the weight ratio of the organic solvent to tetrafluoroterephthalaldehyde is in the range of 0 to 3, preferably in the range of 1 to 2.

  In the method of the present invention, in step (b), the mixture is heated until its temperature rises to a range of 60-130 ° C, preferably 85-100 ° C.

  In the method of the present invention, the reaction time of step (b) is in the range of 2 to 30 hours, preferably in the range of 4 to 6 hours.

  In the method of the present invention, in order to avoid an excessive reaction of hydrolysis, in step (c), the mixture is cooled in the range of 0 to 60 ° C, preferably in the range of 25 to 40 ° C.

  In the method of the present invention, in step (c), the mixture is slowly added to water at 0-25 ° C., preferably ice water, to avoid hydrolysis overreaction.

The process of the invention can be carried out with or without an organic solvent that does not react with SOCl ₂ . The organic solvent is preferably at least one selected from the group consisting of toluene, chloroform, p-xylene, benzene, dioxane, 1,2-dichloroethane, tetrachloromethane, tetrahydrofuran, nitrobenzene, and o-dichlorobenzene. More preferably, it is toluene or benzene.

In the method of the present invention, the catalyst is N, N- dialkylformamide, alkyl groups are C ₁ -C ₇ alkyl group. Preferably, the catalyst is N, N-dimethylformamide (DMF) or N, N-diethylformamide (DEF).

In the method of the present invention, the purification in step (e) is preferably
(e1) adding an organic solvent and water (H ₂ O) to the organic layer with stirring;
(e2) neutralizing the mixture;
(e3) isolating the organic layer and then concentrating the organic layer; and
(e4) A step of cooling the organic layer to obtain a solid product.

  In the step (e), the volume ratio of the organic solvent to the water in the step (e1) is in the range of 1 to 10, preferably 1. The organic solvent can be any organic solvent that can dissolve 1,4-bis (dichloromethyl) tetrafluorobenzene but is immiscible with water, and is preferably dichloromethane in step (e1). The mixture can be neutralized with any basic solution, but is preferably neutralized with concentrated ammonia in step (e2).

  Other objects, advantages and novel features of the invention will become more apparent from the following detailed description when taken in conjunction with the accompanying drawings.

[Example 1]
Production of 1,4-bis (dichloromethyl) tetrafluorobenzene (solvent: toluene, catalyst: N, N-dimethylformamide)
Tetrafluoroterephthalaldehyde (TFTPA, 15.45 g), N, N-dimethylformamide (DMF, 3.01 g), and toluene (15.01 g) are added to a 250 mL three-necked reactor equipped with a temperature probe, condenser and aeration tube. added. Under a nitrogen atmosphere, SOCl ₂ (63.37 g) was slowly added into the flask from the flow path for the temperature probe by a feed hopper. After removing the feed hopper, the flask was again fitted with a temperature probe. The reaction mixture was heated with stirring in an oil bath with nitrogen aeration closed and refluxed at 85-95 ° C. for 2 hours until the reaction was complete by gas chromatography (GC) analysis. After the reaction mixture was cooled to room temperature, ice water was slowly introduced thereto to hydrolyze the remaining SOCl ₂ . The reaction mixture was allowed to stand for a while and the aqueous layer was removed. Subsequently, appropriate amounts of dichloromethane (DCM) and H ₂ O (volume ratio DCM / H ₂ O = 1/1) were added to the remaining organic layer. The pH value of the mixture was adjusted to 7.0 with concentrated ammonia (concentrated NH ₃ water). The organic phase was then isolated, washed with water, dried over anhydrous magnesium sulfate and concentrated to remove DCM, toluene and DMF. Finally, the resulting product was cooled to room temperature to obtain a crude product (22.23 g, crude yield: 93.8%). The crude product was recrystallized with n-heptane to give 13.33 g of crystalline product. The remaining n-heptane solution was distilled off and then recrystallized again to obtain 6.28 g of crystalline product. The total amount of the two recrystallizations was 19.61 g of crystalline product (yield: 82.75%).

Chemical analysis data:
(a). Mass spectrum: M ⁺ = 316.
(b). ¹ H NMR (CDCl ₃ ; external standard: TMS) chemical shift (δ): 6.90 ppm (s, 2H).
(c). ¹⁹ F NMR (CDCl ₃ ; external standard: CFCl ₃ ) chemical shift (δ): −139.37 ppm (s, 4F).
(d). ¹³ C NMR (CDCl ₃ ; external standard: TMS) Chemical shift (δ): 143.45 ppm (d, J _CF = 257 Hz, 4 aromatic C), 120.72 ppm (s, 2 aromatic C), 58.26 ppm (s, 2 aliphatic C).

[Example 2-16]
Production of 1,4-bis (dichloromethyl) tetrafluorobenzene Examples 2 to 16 were carried out in the same manner as in Example 1. However, the amounts of reagents and solvents, reaction conditions, and product yields are listed in Table 1.

  In Examples 1-16, the solvent can be toluene, chloroform, p-xylene, benzene, dioxane, 1,2-dichloroethane, tetrachloromethane, tetrahydrofuran, nitrobenzene, or o-dichlorobenzene, and the catalyst is most preferably formamide Indicates that

Comparative example

Conventional production of 1,4-bis (dichloromethyl) tetrafluorobenzene The comparative example is a conventional production method of 1,4-bis (dichloromethyl) tetrafluorobenzene, which is 1,2,4,5-tetrafluorobenzene. Benzene (TFB) is reacted with CHCl ₃ to give 1,4-bis (dichloromethyl) tetrafluorobenzene. This method is described in detail below.

1,2,4,5-Tetrafluorobenzene (TFB, 3.77 g), anhydrous AlCl ₃ (20.34 g), and CHCl ₃ dehydrated with NaH as solvent were placed in a 100 mL reactor. The mixture was heated in an oil bath with stirring and refluxed for 24 hours. Subsequently, the mixture was slowly added into ice water to hydrolyze the remaining AlCl ₃ . After the mixture was extracted with chloroform, the organic phase was washed with water, dried over anhydrous magnesium sulfate, and concentrated to obtain a crude product. The crude product was purified by silica gel column chromatography using n-hexane as an eluent and recrystallized from n-hexane to obtain 1,4-bis (dichloromethyl) tetrafluorobenzene (yield: 59.33%).

  Table 2 shows the disadvantages and advantages of this comparative example compared to Example 1.

  According to Table 2, the cost of Example 1 is 1.5 times that of the comparative example. However, the method of Example 1 can shorten the reaction time, simplify the process, increase the reactor capacity, and improve the production yield of 1,4-bis (dichloromethyl) tetrafluorobenzene. These aspects of Example 1 are superior to the comparative example.

  Although described with respect to preferred embodiments of the present invention, it should be understood that numerous other possible modifications or changes may be made without departing from the scope of the present invention as claimed below.

DMF: N,N-ジメチルホルムアミド
DMAC: ジメチルアセトアミド
NMP: N-メチルピロリドン
DEF: N,N-ジエチルホルムアミド
*1: 溶液が黒くなった。
*2: TFTPAは純度が低かった。
*3: 溶液は黒くなり、生成物は殆ど得られなかった。
*4: 溶液は黒くなり、生成物は殆ど得られなかった。

DMF: N, N-dimethylformamide
DMAC: Dimethylacetamide
NMP: N-methylpyrrolidone
DEF: N, N-diethylformamide
* 1: The solution turned black.
* 2: TFTPA has low purity.
* 3: The solution turned black and almost no product was obtained.
* 4: The solution turned black and almost no product was obtained.

Claims (16)

A process for producing 1,4-bis (dichloromethyl) tetrafluorobenzene, comprising:
(a) mixing tetrafluoroterephthalaldehyde, catalyst and SOCl ₂ with or without an organic solvent to form a mixture, wherein the catalyst belongs to formamide;
(b) heating the mixture;
(c) cooling the mixture, slowly adding the mixture into water and allowing the mixture to separate into two layers;
(d) obtaining an organic layer from a layer of the mixture; and
(e) A method comprising purifying an organic layer, removing an organic solvent and a catalyst in the organic layer, and providing 1,4-bis (dichloromethyl) tetrafluorobenzene. The method of claim 1, the molar ratio of SOCl ₂ tetrafluoroterephthalic aldehyde is in the range of 2 to 20, the method. The method of claim 1 wherein the weight ratio of catalyst to tetrafluoroterephthalaldehyde is in the range of 0.1 to 1.0. The method of claim 1, wherein the weight ratio of organic solvent to tetrafluoroterephthalaldehyde is in the range of 0-3. The method according to claim 1, wherein in step (b), the mixture is refluxed by heating. The method according to claim 1, wherein in step (b) the mixture is heated until its temperature rises to the range of 60-130 ° C. The method according to claim 1, wherein the reaction time of step (b) is in the range of 2 to 30 hours. The method according to claim 1, wherein in step (c), the mixture is cooled to within the range of 0-60 ° C. The method of claim 1, wherein in step (c), the mixture is slowly added to ice water. The method according to claim 1, wherein the organic solvent is selected from the group consisting of toluene, chloroform, p-xylene, benzene, dioxane, 1,2-dichloroethane, tetrachloromethane, tetrahydrofuran, nitrobenzene, and o-dichlorobenzene. A method that is at least one selected. The method of claim 1, the catalyst is N, N- dialkylformamide, the alkyl group is a C ₁ -C ₇ alkyl group, the process. The method according to claim 1, wherein the catalyst is N, N-dimethylformamide (DMF) or N, N-diethylformamide (DEF). The method of claim 1, wherein step (e) comprises:
(e1) adding an organic solvent and water (H ₂ O) to the organic layer with stirring;
(e2) neutralizing the mixture;
(e3) isolating the organic layer and then concentrating the organic layer; and
(e4) A method comprising cooling the organic layer to obtain a solid product. 14. The method according to claim 13, wherein in step (e1), the volume ratio of the organic solvent to water is in the range of 1-10. 14. The method according to claim 13, wherein in step (e1) the organic solvent is dichloromethane. 14. The method according to claim 13, wherein in step (e2), the mixture is neutralized with concentrated ammonia.