A process for the recovery of hydrogen chloride and monomeric alkoxysilanes from mixtures of chlorine-containing silicon compounds

Abstract: Disclosed herein is a process of recovering hydrogen, hydrogen chloride and monomeric alkoxysilanes from mixtures of chlorine-containing silicon compounds whereby waste chlorine-containing silicon compounds are converted to useful, valuable silicon intermediates.

Description: This invention deals with a process of recovering hydrogen, hydrogen chloride and monomeric alkoxysilanes from mixtures of chlorine-containing silicon compounds whereby waste chlorine-containing silicon compounds are converted to useful, valuable silicon intermediates. European patent application no. 88103421.9 (EP-A-0 282 846) describes a process for preparing monomeric alkoxysilanes from chlorosilanes. Mixtures of chlorine-containing compounds, especially high boiling products, are invariably formed during the Direct Process syntheses of chlorosilanes. Such materials are often called Direct Process Residue Wastes. The Direct Process provides for the direct synthesis of monomeric chlorosilanes by the reaction of gaseous methyl chloride or hydrogen chloride with elemental silicon in a fluid bed reactor at an elevated temperature. This reaction is catalyzed and optimized to prepare dimethyldichlorosilane, by far the most important intermediate for the preparation of industrial "Silicones". The process can also be optimized to prepare trichlorosilane, a very important intermediate to prepare transistor grade silicon and many organotrichlorosilane intermediates. There is created in the Direct Process, a residue, which is obtained after separation of the dimethyldichlorosilane and other chlorosilanes. This residue consists of a large number of by-products such as, for example CH 3 Cl 2 SiSiCH 3 Cl 2 , CH 3 Cl 2 SiSi(CH 3 ) 2 Cl and other disilanes of the formula Si 2 (CH 3 ) x Cl 6-x wherein x equals 1, 2 or 3, as well as trisilanes of the formula Si 3 (CH 3 ) x Cl 8-x , wherein x equals 1, 2, 3 or 4 and minor amounts of disilylmethane structures such as CH 3 Cl 2 SiCH 2 SiCH 3 Cl 2 and lesser amounts of disilylethane structures such as CH 3 Cl 2 SiCH 2 CH 2 SiCH 3 Cl 2 and small amounts of numerous organochlorosilanes of unproven structures. A typical high boiling residue from the methyl chloride direct process usually contains more than fifty percent by weight of chloride. A typical high boiling residue from the reaction with hydrogen chloride usually consists mostly of compounds of the type Cl(HSiCl) x Cl wherein x = 1, 2, 3 or 4, as well as SiCl 4 . Many attempts have been made to utilize these residues as they are otherwise waste products and have to be subjected to various treatments to neutralize them and then they are landfilled which may create environmental problems. All attempts at utilizing certain of the distillable products from the residue have led to products which are expensive and are based on sources which are inconsistent at best and, therefore, are not desirable for large volumes of materials. The instant invention solves the problems set forth above and provides an economical process for obtaining valuable monomeric silane intermediates from Direct Process Residue Wastes, as well as the valuable recovery of hydrogen chloride and hydrogen for possible recycle. This invention deals with a process for the recovery of monomeric alkoxysilanes from Direct Process Residue mixtures of chlorine-containing silicon compounds formed during the Direct Process synthesis of monomeric chlorosilanes by the reaction of gaseous methyl chloride or hydrogen chloride with elemental silicon in a fluid bed reactor at an elevated temperature, the process comprising: (A) contacting the mixture of chlorine-containing silicon compounds with a stoichiometric excess of a lower alcohol at a temperature of at least 20°C. to form a liquid mixture and heating the mixture to remove by-produced gaseous hydrogen chloride; (B) contacting the products from (A) with a base at a temperature of at least 20°C. to form essentially monomeric alkoxysilanes while removing by-produced hydrogen gas for a period of time necessary to remove substantially all of such by-produced hydrogen gas, whereby a mixture of predominantly monomeric alkoxysilanes is obtained; and (C) subjecting the product of (B) to distillation to separate and collect monomeric alkoxysilanes. For purposes of this invention, "chlorine-containing silicon compounds" not only include those mixtures which contain chlorine and organic groups, but also include silanes having other groups substituted on silicon such as hydrogen of the type H y Si x Cl 2x+2-y where y = 0, 1, 2 or 3 and x = 2, 3 or 4, which are residues boiling above Cl 3 SiH (35°C.) and are obtained in the manufacture of Cl 3 SiH by reaction of hydrogen chloride with elemental silicon at elevated temperatures. The type of equipment is not critical in this process and any equipment which is reliable, efficient and normally used in such reactions is useful. Examples of such equipment are set forth in the examples below. The first step of the process, which is step (A), requires that the mixture of chlorine-containing silicon compounds be contacted with a lower alcohol. Such lower alcohols include those primary and secondary alcohols having from 1 to 6 carbon atoms and are exemplified by primary alcohols, such as methanol, ethanol and hexanol or secondary alcohols such as isopropanol. Preferred for this invention are the primary alcohols with methanol and ethanol being most preferred. By "contacting", it is meant that the alcohol is added to the chlorine-containing silicon compounds and mixed together in any given manner to produce intimate contact between the chlorine-containing silicon compounds and the alcohols. This mixing should be done at or above room temperature, preferably at the reflux temperature of the mixture of materials. When the mixing is performed, the chlorine-containing silicon compounds react very rapidly with the alcohol to form mixed alkoxy silicon compounds, and liberate hydrogen chloride essentially according to the following reaction: = SiCl + ROH → = SiOR + HCl ↑ To add to the economies of the process, the gaseous hydrogen chloride is collected and either re-used in related organosilicon processes or is sold for other purposes. Essentially all of the chloride can be liberated as hydrogen chloride, depending upon how the alcohol is added to the chlorosilane and the temperature at which the process is performed. The details of the ratios of alcohol to chloride, the temperatures and other significant factors regulating the evolution and collection of essentially all of the generated hydrogen chloride can be found in U.S. Patent No. 4,506,087 dated March 19, 1985. The mixture of materials is heated during this step in order to expel hydrogen chloride from the mixture as rapidly as it is formed and to convert the chlorine-containing silicon compounds to alkoxy-containing silicon compounds. Thus, this heating is carried out generally at the reflux temperature of the materials. The mixture of alkoxy-containing silicon compounds, after one equivalent of alcohol per equivalent of chloride has been added, are essentially the alkoxy equivalents of the chlorine-containing compounds of the starting material. In the second step of this process, the mixture of alkoxy-containing silicon compounds obtained by the previous step are further treated in solution with a base. Upon contact with the base, the alkoxy-containing silicon compounds are rapidly converted to monomeric alkoxysilanes. It should be understood that monomeric alkoxysilanes in the solution are not affected and they go through this step essentially without change. Examples of the reactions during this step are Also, any disilane or polysilane present is oxidized viz. Useful bases are alkali metal bases from the metals found in Group Ia of the periodic table. Preferred are the sodium, potassium and lithium metal bases. Especially preferred are the sodium and potassium bases because they are strong bases and are readily available. Thus, sodium ethoxide and potassium ethoxide as well as their methoxide equivalents are particularly useful for this process. This step of the process requires that the solution and the base be contacted at a temperature in the range of 20°C. to 100°C. for a period of time of 1-30 minutes. Since these reactions are nearly quantitative and go to completion in minutes near room temperature, it is preferred that the reaction be carried out in a range from at or near room temperature to 75°C. It should be recognized by those skilled in the art that when the reaction is exothermic, one must take precautions at the incipient stages to prevent the reaction from overheating. Control of the reaction will allow the materials of the reaction to be blended together without undue heating. One of the best means for controlling the exotherm and preventing undue heating is to add the base to the solution of silicon compounds at a slow rate. Hydrogen gas is by-produced by this reaction and such gas can be captured or it can be allowed to escape. One of the convenient ways to determine the endpoint of the reaction is to observe the absence of hydrogen gas evolution. The products that are obtained by this process are monomeric alkoxysilanes. The term "monomeric" refers to molecules having only one silicon atom. In this case, the silanes can be a mixture as regards how many alkoxy groups are on silicon and also, depending on the base that is used, the silanes can be mixtures of the types of alkoxy groups on silicon as well. Once the reaction with the base is finished, the solution is distilled to recover the individual monomeric alkoxysilanes. Now, so so that those skilled in the art can further appreciate this invention, the the following examples are presented. Example 1 Absolute ethanol (329 g) was pumped at a rate of 2 ml/min below the surface of Cl 3 SiH/Direct Process Residue (390 g) which was situated in a I-liter, round-bottomed, three-necked, glass flask. The residue contained 52 weight percent Cl. The addition was made at room temperature (25°C.). After addition of the alcohol, the temperature of the liquid was slowly raised to reflux. Hydrogen chloride (192.3 g) was expelled from the mixture, which accounted for 95% of the original chloride in the residue. Next, sodium ethoxide (21 weight percent dissolved in ethanol) was slowly added into the refluxing liquid until the evolution of hydrogen ceased. The mixture was then distilled. Recovered were 281 g of ethanol (b.p. 78°C.) followed by 302 g of tetraethoxysilane (b.p. 155°C.), leaving only a small amount of dry solid residue in the flask. Methanol (330 g) was pumped at a rate of 10 ml/min below the surface of 563 g of the same Direct Process Residue as was used in example 1, using the same type of apparatus. After the addition of the methanol at room temperature, 261 g of hydrogen chloride had been expelled from the system without further heating, 86% of the original chloride. Thereafter, sodium methoxide (25% in methanol)(175 g) was added and the mixture was distilled. Methanol, (b.p. 64°C., 164 g) was recovered followed by tetramethoxysilane, (b.p. 104°C., 270 g) leaving only a dry solid residue in the flask. No other silicon compounds could be detected in the distillate by gas liquid chromatography. Example 3 Methanol (425 g) was pumped beneath the surface of stirred dimethyl-Direct Process Residue (804.5 g) (46 weight percent chloride) at about 60°C. in a three-necked, two liter round bottomed glass flask and hydrogen chloride was permitted to escape through a distillation head until 338 g (91%) of the original chloride was expelled from the reaction mass. Then sodium methoxide (25 weight % in methanol, 606 g) was added to the mixture at 60°C., causing rapid evolution of hydrogen and the mixture was then distilled to a temperature of 250°C. The distillate was methanol (588 g, b.p. 64°); dimethyldimethoxy-silane (56 g; b.p. 82°); methyltrimethoxysilane (259 g; b.p. 104°); and higher boiling liquid (75 g). The higher boiling liquid is believed to be a mixture of disilylmethylene compounds of the formula (CH 3 ) x (CH 3 O) 3-x SiCH 2 Si(CH 3 ) x (CH 3 O) 3-x wherein x = 1 or 2.

Claims: A process for the recovery of monomeric alkoxysilanes from Direct Process Residue mixtures of chlorine-containing silicon compounds formed during the Direct Process synthesis of monomeric chlorosilanes by the reaction of gaseous methyl chloride or hydrogen chloride with elemental silicon in a fluid bed reactor at an elevated temperature, the process comprising: (A) contacting the mixture of chlorine-containing silicon compounds with a stoichiometric excess of a lower alcohol at a temperature of at least 20°C. to form a liquid mixture and heating the mixture to remove by-produced gaseous hydrogen chloride; (B) contacting the products from (A) with a base at a temperature of at least 20°C. to form essentially monomeric alkoxysilanes while removing by-produced hydrogen gas for a period of time necessary to remove substantially all of such by-produced hydrogen gas, whereby a mixture of predominantly monomeric alkoxysilanes is obtained; and (C) subjecting the product of (B) to distillation to separate and collect monomeric alkoxysilanes. The process of claim 1 wherein in step (A), mixtures of Cl(SiCl 2-x H x ) y Cl where x equals 0 or 1 and y equals 1 to 4, are contacted with ethanol or methanol. The process of claim 1 wherein,in step (A), mixtures of Cl{Si(CH 3 ) x Cl (2-x) } y Cl where x equals 1 or 2 and y equals 1 to 4, are contacted with methanol or ethanol.

Inventors: SPEIER JOHN LEOPOLD, SPEIER, JOHN LEOPOLD
Applicants: DOW CORNING, DOW CORNING CORPORATION
Application year: 1993
Main classification: C07F7
IPC codes: C01B7, C07F7