Classifications

• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C319/00—Preparation of thiols, sulfides, hydropolysulfides or polysulfides
  • C07C319/02—Preparation of thiols, sulfides, hydropolysulfides or polysulfides of thiols
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C319/00—Preparation of thiols, sulfides, hydropolysulfides or polysulfides
  • C07C319/26—Separation; Purification; Stabilisation; Use of additives
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C323/00—Thiols, sulfides, hydropolysulfides or polysulfides substituted by halogen, oxygen or nitrogen atoms, or by sulfur atoms not being part of thio groups
  • C07C323/01—Thiols, sulfides, hydropolysulfides or polysulfides substituted by halogen, oxygen or nitrogen atoms, or by sulfur atoms not being part of thio groups containing thio groups and halogen atoms, or nitro or nitroso groups bound to the same carbon skeleton
  • C07C323/02—Thiols, sulfides, hydropolysulfides or polysulfides substituted by halogen, oxygen or nitrogen atoms, or by sulfur atoms not being part of thio groups containing thio groups and halogen atoms, or nitro or nitroso groups bound to the same carbon skeleton having sulfur atoms of thio groups bound to acyclic carbon atoms of the carbon skeleton
  • C07C323/03—Thiols, sulfides, hydropolysulfides or polysulfides substituted by halogen, oxygen or nitrogen atoms, or by sulfur atoms not being part of thio groups containing thio groups and halogen atoms, or nitro or nitroso groups bound to the same carbon skeleton having sulfur atoms of thio groups bound to acyclic carbon atoms of the carbon skeleton the carbon skeleton being acyclic and saturated

Definitions

• the invention relates to methods for synthesizing 2,2,2-trifluoroethanethiol (CF 3 CH 2 SH), which is a useful etchant for electronics applications.
• the fluorothiol compound 2,2,2-trifluoroethanethiol which has the chemical structure CF 3 CH 2 SH, has utility as an etchant in the manufacture of various electronic products and as an intermediate in the synthesis of various organic compounds. It is also useful in creating self-assembled monolayers on electrode surfaces and the like.
• a commercially viable process for synthesizing 2,2,2-trifluoroethanethiol using readily available starting materials has not been described or developed.
• One aspect of the present invention provides a method of making CF 3 CH 2 SH, comprising a step of reacting CF 3 CH 2 X, wherein X is a leaving group selected from the group consisting of halide and tosylate, with MSH, wherein M is an alkali metal.
• X may be Cl and/or M may be Na.
• the reaction may be carried out in at least one organic solvent, in particular in at least one polar organic solvent such as dimethylsulfoxide, dimethylacetamide, N-methylpyrrolidone, dimethylformamide and/or ethylene glycol.
• the reaction may be carried out in the presence of at least one phase transfer catalyst, in particular a tetra alkyl ammonium salts such as tetra-n-butylammonium bromide, methyltrioctylammonium chloride (Aliquat®) and mixtures thereof.
• the reactant MSH may be reacted in molar excess with the CF 3 CH 2 X.
• at least two moles of MSH per mole of CF 3 CH 2 X may be reacted.
• the reaction may be conducted at a temperature within a range of about 70° C. to about 110° C.
• the CF 3 CH 2 X and MSH may be reacted for a period of time of from about 1 hour to about 5 hours, for example.
• the reaction may be carried out at a pressure above atmospheric pressure, for example in a pressurized vessel.
• Hydrogen sulfide (H 2 S) may be additionally present during the reacting of the CF 3 CH 2 X and MSH.
• Reacting CF 3 CH 2 SH and MSH may yield a reaction product mixture comprised of CF 3 CH 2 SH and at least one by-product selected from the group consisting of (CF 3 CH 2 ) 2 S 2 and (CF 3 CH 2 ) 2 S.
• the method may additionally comprise a further step of separating CF 3 CH 2 X from the reaction product mixture and/or additionally comprise a further step of separating the at least one by-product from the reaction product mixture.
• the at least one by-product separated from the reaction product mixture may be reacted with a hydrogenating agent to form CF 3 CH 2 SH.
• One particular embodiment of the invention provides a method of making CF 3 CH 2 SH, comprising a step of reacting CF 3 CH 2 Cl with a molar excess of NaSH in a reaction medium comprised of one or more polar organic solvents at a temperature of from about 70° C. to about 110° C. for a time of from about 1 to about 5 hours.
• One particular embodiment of the invention provides a method of making CF 3 CH 2 SH, comprising a step of reacting CF 3 CH 2 Cl with a molar excess of NaSH in a in the presence of a phase transfer catalyst at a temperature of from about 70° C. to about 110° C. for a time of from about 1 to about 5 hours.
• a compound or mixture of compounds corresponding to the chemical formula CF 3 CH 2 X, wherein X is a halide or tosylate, is utilized as one of the starting materials in the process of the present invention.
• X is Br (bromine) or Cl (chlorine).
• HCFC-133a Such compounds are well known in the art and may be synthesized using conventional methods or obtained from commercial sources.
• the compound CF 3 CH 2 Cl is sold under the designation HCFC-133a.
• the MSH starting material functions as a source of the nucleophile HS ⁇ , which reacts with CF 3 CH 2 X to displace the halide or tosylate X thereby substituting a thiol functional group (—SH) for the halide or tosylate.
• MSH is suitably an alkali metal hydrosulfide, wherein M is an alkali metal.
• M is K (potassium) or, even more preferably, Na (sodium).
• Any suitable source of the MSH may be utilized as the starting material.
• sodium hydrogen sulfide hydrate which is readily available from multiple commercial sources at low cost, may be used. If so desired, the MSH may be generated in situ in the initial reaction mixture.
• reaction of the CF 3 CH 2 X and MSH starting materials may be carried out in the presence of one or more solvents, in particular one or more organic solvents.
• the solvent(s) may function as a reaction medium in which one or both of the starting materials is dissolved.
• the amount of solvent relative to the starting materials is not believed to be critical and may be optimized in accordance with standard experimental procedures.
• the solvent is a polar organic solvent or combination of polar organic solvents.
• the solvent may be non-protic, but in other embodiments of the invention a protic solvent may be utilized.
• suitable solvents include, but are not limited to, sulfoxides such as dimethylsulfoxide, amides such as dimethylacetamide, N-methylpyrrolidone and dimethylformamide, and glycols such as ethylene glycol and combinations thereof.
• the solvent(s) may be recovered from the reaction product mixture by distillation or other suitable methods and recycled for use in the reaction to make the desired 2,2,2-trifluoroethanethiol.
• the recovered solvent may be subjected to any known or conventional purification method prior to such re-use.
• the reaction of the CF 3 CH 2 X and MSH starting materials may be carried out in the presence of one or more transfer catalysts, in particular tetra alkyl ammonium salts such as tetra-n-butylammonium bromide and methyltrioctylammonium chloride (Aliquat®) and mixtures thereof.
• transfer catalysts in particular tetra alkyl ammonium salts such as tetra-n-butylammonium bromide and methyltrioctylammonium chloride (Aliquat®) and mixtures thereof.
• hydrogen sulfide (H 2 S) is additionally present during reaction of the MSH and CF 3 CH 2 X.
• the presence of hydrogen sulfide has been found to help favor the production of 2,2,2-trifluoroethanethiol, relative to bis-sulfide by-product. Formation of the desired product CF 3 CH 2 SH occurs according to Equation (1) below:
• H 2 S present helps to prevent the formation of by-products by shifting to the left the equilibrium depicted in (a).
• sufficient H 2 S is present in the sealed reactor such that the partial pressure of H 2 S above the liquid reaction medium is greater than the saturation partial pressure.
• a “head pressure” of H 2 S is preferably maintained that ensures that the reaction liquid is, at the very least, completely saturated with H 2 S and such that the maximum concentration of H 2 S possible is in solution. In that way, the greatest (positive) influence on equilibrium (a) will be realized.
• the MSH is initially combined with the solvent(s) or phase transfer catalyst(s) to form a reaction mixture, with the CF 3 CH 2 X then being introduced into the reaction mixture by any suitable method (e.g., bubbling the CF 3 CH 2 X into the reaction mixture sub-surface as a gas).
• a solvent or phase transfer catalyst is introduced into a vessel or other apparatus and cooled to below room temperature, with the CF 3 CH 2 X and then the MSH then being sequentially introduced before heating the reaction mixture up to the temperature effective to initiate reaction between the MSH and the CF 3 CH 2 X.
• reaction temperatures above room temperature are used in order to achieve a satisfactory rate of reaction.
• the reaction mixture may be heated at a temperature of from about 70° C. to about 110° C., although lower or higher temperatures may also be used depending upon the selection of reactants, solvent, phase transfer catalyst, pressure and other reaction parameters.
• Reaction (heating) times of from about 1 to 5 hours are typically sufficient to obtain a useful yield of CF 3 CH 2 SH, but the selection of other reaction parameters may influence the optimum reaction time.
• reaction temperatures above room temperature are employed, it will generally be advantageous to carry out the reaction in a vessel or other apparatus capable of being pressurized, in view of the relative volatility of the CF 3 CH 2 X reactant (when X is a halide) and the optional H 2 S component.
• the maximum pressure within the vessel or other apparatus may range from about 1 to about 400 psig.
• the method of the present invention may be carried out in a batch, semi-continuous or continuous manner.
• a first portion of MSH is reacted with CF 3 CH 2 X in a first stage, followed by the addition of a second portion of MSH and further reaction in a second stage (i.e., the MSH may be combined with the CF 3 CH 2 X portion-wise or step-wise).
• the reaction mixture may be stirred or otherwise agitated while contacting the MSH and CF 3 CH 2 X.
• the reaction product mixture obtained as a result of the above-described reaction between the MSH and the CF 3 CH 2 X may be subjected to any desired purification, neutralization, separation, fractionation and/or recovery step(s) to isolate in purified form the CF 3 CH 2 SH product.
• the other components of the reaction product mixture may be recycled, disposed of, or further reacted as may be desired.
• the solvent(s) may be separated and reused, as may any unreacted CF 3 CH 2 X.
• sulfide-containing by-products such as (CF 3 CH 2 ) 2 S 2 and/or (CF 3 CH 2 ) 2 S may be generated in combination with the desired CF 3 CH 2 SH.
• the present invention comprisies:
• This example shows that the amount of desired thiol relative to other products can be increased by increasing the ratio of NaSH relative to HCFC-133a.
• This example demonstrates the reaction of HCFC-133a added as a gas with NaSH in solvent with added H 2 S over-pressure.
• Hastelloy “C” stirred pressure reactor (Parr Instrument Company) was used for the reaction of HCFC-133a with NaSH in solvent and using an over-pressure of H 2 S.
• the added H 2 S is intended to reduce the formation of bis-sulfide and bis-disulfide by-products.
• the reactor was heated to 90° C. and held at that temperature for six hours during which time the pressure increased to 65 psig. After the specified time, the heat was shut off and the reactor contents were stirred overnight as the reactor cooled to ambient temperature. The next day, the reactor was vented and sampled for 19 F NMR analysis. The 19 F NMR results showed 42% (I) product yield and 23% (II) by-product. There was also 11% unreacted HCFC133a.
• This example illustrates the reaction of HCFC-133a added as a liquid with NaSH in solvent with added H 2 S over-pressure.
• Example 4 Similar methodology as that described in Example 4 was used for this Example. Thus, sodium hydrogen sulfide hydrate, NaSH 2 O, 11.28 g (152.3 mmol) was dissolved in N-methylpyrrolidone (NMP) solvent (136.3 g) and trifluorotoluene (TFT), 2.54 g (17.4 mmol) was added to the mixture as an internal standard. The reactor was sealed and H 2 S, 13.36 g (392.0 mmol) was then added over 7 minutes during which time the pressure increased to 25 psig. The reactor was then heated to 90° C. while the pressure increased to 120 psig.
• NMP N-methylpyrrolidone
• TFT trifluorotoluene
• HCFC-133a 15.0 g (126.6 mmol) was added over the course of 15 minutes as a liquid by way of a high pressure liquid delivery pump. Following the addition of HCFC-133a, the pressure was 120 psig @ 90° C. The reaction mixture was stirred at 90° C. for an additional 2 hours and then permitted to cool with stirring overnight. The following day the reactor was vented and sampled to permit 19 F NMR analysis of the reaction mixture. F-19 NMR results showed 31% product (I) yield and 5% by-product (II) yield.
• This example illustrates the reaction of HCFC-133a added as a liquid with NaSH in solvent with added H 2 S over-pressure.
• This example illustrates the reaction of CF 3 CH 2 OTs with NaSH in a Phase Transfer Catalyzed (PTC) System.
• a 150 ml Chemglass pressure reactor was charged with 8.53 g CF 3 CH 2 OTs (33.6 mmol), 46.29 g toluene (0.503 mmol), and 0.8525 g trifluorotoluene (5.8 mmol). Trifluorotoluene is used as internal standard for 19 F NMR analysis. The reactor was then charged with: 0.97 g tetra-n-butylammonium bromide, (n-Bu) 4 NBr (3.0 mmol); and 1.19 g Aliquat® ®336, methyltrioctylammonium chloride (2.9 mol) phase transfer catalysts.
• Example 7A the mol ratio of NaSH:CF 3 CH 2 OTs was 3:1 and the phase transfer catalysts were used at approximately 9 mol % each.
• a 600-cc 316-SS Parr reactor was charged with CF 3 CH 2 OTs (40.33 g/158.6 mmol), toluene (228.56 g/2.48 mol) and Aliquat® 336 (1.33 g/3.3 mmol). Separately, NaHS.H 2 O (35.36 g/477.5 mmol) and (n-Bu) 4 NBr (1.01 g/3.1 mmol) were dissolved with water (40.33 g/2.2406 mol) and this aqueous mixture was subsequently added to the Parr reactor. Trifluorotoluene (2.42 g/16.6 mmol) was added to serve as an internal standard.
• the reactor Prior to sampling for analysis by 9 F NMR, the reactor was placed in dry ice, cooled to ⁇ 20° C., and vented to a scrubber. The conversion was 32.7% and the product (I) yield was 25.6 mol %.
• the reactor was charged with additional nBu 4 NBr (1.50 g/4.6 mmol) dissolved in 1.5 g water and then heated for an additional 16 hours. Following the heating time period the mixture was cooled in dry ice to ⁇ 20° C., vented to scrubber, and sampled for analysis by 19 F NMR spectroscopy. The conversion was 49.5% and the product (I) yield was 41.8 mol %.
• the reactor was subsequently charged with additional nBu 4 NBr (5.11 g/15.8 mmol) dissolved in 5.0 g water and Aliquat® 336 (4.74 g/1.17 mmol) dissolved in 5.0 g toluene with a syringe inserted through a septum.
• the reaction mixture was re-heated to 90° C. for an additional 16 hours and then permitted to cool overnight with stirring to ambient temperature.
• the reactor Prior to sampling for analysis by 9 F NMR, the reactor was placed in dry ice, cooled to ⁇ 20° C., and vented to a scrubber. The conversion was 94.6% and the final product (I) yield was 71.5 mol %.
• the amounts of reagents used are summarized in Table 6. The results are summarized in Table 7.

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• 2015
  • 2015-07-31 KR KR1020177003454A patent/KR102417295B1/ko active IP Right Grant
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