Patent Grant
10131620
The present disclosure relates to a method for producing dimethyl carbonate and dimethyl carbonate derivatives. The process is unique in that it produces a by-product that can be re-used in the process as a raw material for repeating the process.
Dimethyl carbonate (DMC) is an organic compound with the formula OC(OCH3)2. It is a colorless, flammable liquid. It is classified as a carbonate ester. It is useful as a methylating agent and as a solvent that is exempt from classification as a volatile organic compound (VOC) in the United States. Dimethyl carbonate is often considered to be a green reagent by minimizing the use and generation of hazardous substances. Dimethyl carbonate's main benefit over other methylating reagents such as iodomethane and dimethyl sulfate is its much lower toxicity and its biodegradability.
DMC has grown in popularity and applications as a replacement for methyl ethyl ketone, tert-butyl acetate, and parachlorobenzotrifluoride. It has an ester or alcohol like odor, which is more favorable to users than most hydrocarbon solvents it replaces. DMC has an evaporation rate of 3.22 (butyl acetate=1.0), which slightly slower than methyl ethyl ketone (MEK) (3.8) and ethyl acetate (4.1) and faster than toluene (2.0) and isopropanol (1.7). It has solubility profile similar to common glycol ethers, meaning DMC can solve most common coating resins. Hildebrand solubility parameter is 20.3 Mpa and Hansen solubility parameters are: dispersion=15.5, polar=3.9, H bonding=9.7. DMC is partially soluble in water up to 13%, however DMC has hydrolyzed in water based systems over time to methanol and CO2 unless properly buffered. DMC is a flammable liquid that has a flash point of 17° C. (63° F.) making it safer than acetone, methyl acetate and methyl ethyl ketone from a flammability point of view.
The present disclosure relates to a method for producing dimethyl carbonate (DMC) and dimethyl carbonate derivatives (compounds of Formula (VI)). The process is unique in that it produces a by-product that can be re-used in the process as a raw material for repeating the process. When the product of interest is dimethyl carbonate, for example, the by-product is 3-chloropropane-1,2-diol can be recycled back into the process as a starting material. The process is additionally unique in that it does not produce ethylene glycol or propylene glycol as by-products. Traditional processes for producing compounds such as dimethyl carbonate involve reacting an oxirane compound with carbon dioxide, which results in the formation of ethylene glycol and propylene glycol as by-products.
In general, the instant disclosure relates to a process for producing a compound of Formula (VI) comprising:
wherein, X is F, Cl, Br, or I; and R1 is a halide, hydrogen, hydroxyl, C1-C8 alkyl, C1-C8 alkenyl, C1-C8 alkoxy, C3-C8 cycloalkyl, C6-C10 aryl group or a 5-10 member heteroaryl group having 1-3 heteroatoms selected from the group consisting of N, O and S, wherein the alkyl, alkenyl, cycloalkyl, aryl group and heteroaryl group can optionally be substituted by one or more hydroxyl groups;
wherein, R1 is a halide, hydrogen, hydroxyl, C1-C8 alkyl, C1-C8 alkenyl, C1-C8 alkoxy, C3-C8 cycloalkyl, C6-C10 aryl group or a 5-10 member heteroaryl group having 1-3 heteroatoms selected from the group consisting of N, O and S, wherein the alkyl, alkenyl, cycloalkyl, aryl group and heteroaryl group can optionally be substituted by one or more hydroxyl groups; and
wherein, R is a C1-C8 alkyl, C1-C8 alkenyl, C1-C8 alkoxy, C3-C8 cycloalkyl, C6-C10 aryl group or a 5-10 member heteroaryl group having 1-3 heteroatoms selected from the group consisting of N, O and S, wherein the alkyl, alkenyl, cycloalkyl, aryl group and heteroaryl group can optionally be substituted by one or more hydroxyl groups.
The instant disclosure also relates to a method for producing dimethyl carbonate. The method typically comprises:
Implementations of the present technology will now be described, by way of example only, with reference to the attached figures, wherein:
It should be understood that the various aspects are not limited to the arrangements and instrumentality shown in the drawings.
The instant disclosure relates to a process for producing a compound of Formula (VI) comprising:
wherein, X is F, Cl, Br, or I; and R1 is a halide, hydrogen, hydroxyl, C1-C8 alkyl, C1-C8 alkenyl, C1-C8 alkoxy, C3-C8 cycloalkyl, C6-C10 aryl group or a 5-10 member heteroaryl group having 1-3 heteroatoms selected from the group consisting of N, O and S, wherein the alkyl, alkenyl, cycloalkyl, aryl group and heteroaryl group can optionally be substituted by one or more hydroxyl groups;
wherein, R1 is a halide, hydrogen, hydroxyl, C1-C8 alkyl, C1-C8 alkenyl, C1-C8 alkoxy, C3-C8 cycloalkyl, C6-C10 aryl group or a 5-10 member heteroaryl group having 1-3 heteroatoms selected from the group consisting of N, O and S, wherein the alkyl, alkenyl, cycloalkyl, aryl group and heteroaryl group can optionally be substituted by one or more hydroxyl groups; and
wherein, R is a C1-C8 alkyl, C1-C8 alkenyl, C1-C8 alkoxy, C3-C8 cycloalkyl, C6-C10 aryl group or a 5-10 member heteroaryl group having 1-3 heteroatoms selected from the group consisting of N, O and S, wherein the alkyl, alkenyl, cycloalkyl, aryl group and heteroaryl group can optionally be substituted by one or more hydroxyl groups.
The halogenating agent in (a) may be hydrogen chloride or a mixture of gaseous hydrogen chloride and an aqueous solution of hydrogen chloride. Also, the reaction of the compound of Formula (I) with the halogenating agent in (a) can be carried out in the presence of a catalyst. The catalyst may be, for example, an organic acid catalyst, and inorganic acid catalyst, or a heterogeneous acid catalyst. In some cases, the catalyst is an organic acid catalyst selected from the group consisting of a carboxylic, a sulfonic, and a phosphoric acid. In other cases, the catalyst is an organic catalyst such as acetic acid.
The base in (b) can be a hydroxide, a carbonate and a bicarbonate of alkali metal or an alkaline earth metal. In some cases, for example the base in (b) is selected from the group consisting of LiOH, NaOH, KOH, CsOH, RbOH, Mg(OH)2, Ca(OH)2, Sr(OH)2, NH4OH, Ba(OH)2, Na2CO3, K2CO3, NaHCO3, KHCO3, and basic ion exchange resin. In other cases, the base is NaOH. Furthermore, the reaction of the compound of Formula (II) with a base to form a compound of Formula (III) in (b) may be carried out in a solvent. In some cases, the solvent is water.
Examples of basic ion exchange resins are provided in the table 1 below.
The reaction of the compound of Formula (III) with carbon dioxide in (c) is often carried out in the presence of a catalyst, such as an alkali metal halide salt or quaternary ammonium halide. Alkali metal halide salts include, for example, NaCl, NaBr, NaI, KCl, KBr and KI. Quaternary ammonium halides include, for example, tetraethylammonium bromide, tetrapropylammonium bromide, tetraethylammonium chloride and tetraethylammonium iodide.
The reaction of the compound of Formula (IV) with alcohol in (d) is also often carried out in the presence of a catalyst. Useful catalysts include, for example, a quadrivalent organotitanium compound having the formula Ti(OR)4, or a quadrivalent organozirconium compound having the formula Zr(OR)4, wherein, R is a C1-C8 alkyl, and C6-C10 aryl group. In other cases, the catalyst is tetrabutyl titanate.
The instant disclosure also relates specifically to a process for producing dimethyl carbonate, the process comprising:
The hydrogen halide in (a) may be, for example, HCl and the compound of Formula (II-a) may be, for example, 1,3-dichloro-2-propanol. Furthermore, the reaction of 3-chloropropane-1,2-diol with the hydrogen halide in (a) may be carried out in the presence of a catalyst. The catalyst may be an organic acid catalyst, an inorganic acid catalyst, or a heterogeneous acid catalyst. In some cases, the catalyst is an organic acid catalyst selected from the group consisting of a carboxylic, a sulfonic, and a phosphoric acid. In other cases, the organic acid catalyst is acetic acid.
The base in (b) may be, for example, a hydroxide, a carbonate and a bicarbonate of alkali metal and alkaline earth metal. In some cases, the base in (b) is selected from the group consisting of LiOH, NaOH, KOH, CsOH, RbOH, Mg(OH)2, Ca(OH)2, Sr(OH)2, NH4OH, Ba(OH)2, Na2CO3, and K2CO3, NaHCO3 KHCO3, and a basic ion exchange resin. In other cases, the base is NaOH. The reaction of the compound of Formula (II) with a base to form a compound of Formula (III) in (b) can be carried out in a solvent. In some cases, the solvent is water.
The reaction of epichlorohydrin with carbon dioxide in (c) can be carried out in the presence of a catalyst. For example, the catalyst may be an alkali metal halide salt, or quaternary ammonium halide. Examples of alkali metal halide salts include, but are not limited to, NaCl, NaBr, NaI, KCl, KBr , and KI. Quaternary ammonium halide include, but are not limited to, tetraethylammonium bromide, tetrapropylammonium bromide, tetraethylammonium chloride, and tetraethylammonium iodide.
The reaction of the compound of Formula (IV) with methanol in (d) can be carried out in the presence of a catalyst. The catalyst may be, for example, a quadrivalent organotitanium compound having the formula Ti(OR)4, or a quadrivalent organozirconium compound having the formula Zr(OR)4, wherein, R is a C1-C8 alkyl, and C6-C10 aryl group. In other cases, the catalyst is tetrabutyl titanate.
The instant disclosure further relates to a method for producing dimethyl carbonate comprising:
In some cases the reaction of the 3-chloropropane-1,2-diol with hydrochloric acid in (a) is carried out in the presence of a catalyst, such as, for example, an organic acid catalyst selected from the group consisting of carboxylic, sulfonic, and phosphoric acids. In other cases, the organic acid catalyst is acetic acid. Finally, the water and sodium chloride produced in (a) and/or (b) can be removed by decanter and distillation
A 3-chloropropane-1,2-diol (129.33 g), acetic acid (42.26 g), and 37% hydrogen chloride solution (461.36 g) was placed in a 1 liter glass reactor, and then stirred using an agitator. The solution was heating to 120° C. for 2 hours at 4.5 atm pressure. The product was analysed by GC, and the conversion of 3-chloropropane-1,2-diol was 93.6%, and the selectivity of 1,3-dichloro-2-propanol was 93.18%, and the selectivity of 2,3-dichloro-1-propanol was 2.26%.
1,3-dichloro-2-propanol (11.77 g), and 20% NaOH(18.24 g) were placed in a 50 ml sample bottle, and stirred with a teflon stir bar. The solution was cooling to 20° C. for 30 min at 1 atm pressure. The product was analysed by GC, and the conversion of 1,3-dichloro-2-propanol was 99.2%, and the selectivity of epichlorohydrin was 95%.
Tetrapropylammonium bromide was used to catalyze the reaction of epichlorohydrin to (chloromethyl)ethylene carbonate using carbon dioxide. Epichlorohydrin (320.32 g) and tetrapropylammonium bromide (9.2 g) were charged to the 400 mL stainless steel autoclave, and then the autoclave was filled with carbon dioxide. At room temperature the carbon dioxide was added to bring the initial pressure to 30 atm and the reaction was begun by heating to 100° C. Carbon dioxide was continually added to the autoclave to maintain this pressure. After a 4 hour reaction period, the reactor was cooled and vented, and the product was recovered. The results are presented in the table 2 below (Inventive Example 1) and contrasted with a comparative example from U.S. Pat. No. 4,931,571, which describes the formation of ethylene carbonate from ethylene oxide.
(Chloromethyl)ethylene carbonate (20.17 g), methanol (46.90 g), and tetrabutyl titanate (1.0 g) were placed in a 150 mL stainless steel autoclave, and then the autoclave was filled with nitrogen to 10 kg/cm2 G at room temperature. The reaction was begun by heating to 150° C., and this temperature was maintained for 1 hours. The reaction pressure was 15 kg/cm2 (increased with temperature, 30° C.→150° C., 10 kg/cm2→24 kg/cm2). The product was analyzed by GC. The conversion of (chloromethyl) ethylene carbonate was 74.8%, and the selectivity of dimethyl carbonate was 84.1%, and the selectivity of 3-chloropropane-1,2-diol was 84.6%.
Tetrapropylammonium bromide was used to catalyze the reaction of epichlorohydrin to (chloromethyl)ethylene carbonate using carbon dioxide. Epichlorohydrin (40.06 g) and tetrapropylammonium bromide (0.12 g) were charged to the 400 mL stainless steel autoclave, and then the autoclave was filled with carbon dioxide. At room temperature the carbon dioxide was added to bring the initial pressure to 30 atm and the reaction was begun by heating 100° C. Carbon dioxide was continually added to the autoclave to maintain this pressure. After a 19.5 hour reaction period, the reactor was cooled and vented, and the product was recovered. The product was analysed by GC, and the conversion of epichlorohydrin was 97.11%, and the selectivity of (chloromethyl) ethylene carbonate was 99.82%.
Tetrapropylammonium bromide was used to catalyze the reaction of epichlorohydrin to (chloromethyl)ethylene carbonate using carbon dioxide. Epichlorohydrin (80.15 g) and tetrapropylammonium bromide (2.3 g) were charged to the 400 mL stainless steel autoclave, and then the autoclave was filled with carbon dioxide. At room temperature the carbon dioxide was added to bring the initial pressure to 30 atm and the reaction was begun by heating to 100° C. Carbon dioxide was continually added to the autoclave to maintain this pressure. After an 8 hour reaction period, the reactor was cooled and vented, and the product was recovered. The product was analyzed by GC, and the conversion of epichlorohydrin was 99.46%, and the selectivity of (chloromethyl) ethylene carbonate was 99.81%.
(Chloromethyl)ethylene carbonate (20.11 g), methanol (47.03 g), and tetrabutyl titanate (0.1 g) were placed in a 150 mL stainless steel autoclave, and then the autoclave was filled with nitrogen to 10 kg/cm2 G at room temperature. The reaction was begun by heating to 150° C., and this temperature was maintained for 1 hour. The reaction pressure was 15 kg/cm2 (increased with temperature, 30° C.→150° C., 10 kg/cm2→24 kg/cm2). The product was analyzed by GC. The conversion of (chloromethyl) ethylene carbonate was 52.5%, and the selectivity of dimethyl carbonate was 76.5%, and the selectivity of 3-chloropropane-1,2-diol was 78.6%.
(Chloromethyl)ethylene carbonate (26.03 g), methanol (36.59 g), and tetrabutyl titanate (1.0 g) were placed in a 150 mL stainless steel autoclave, and then the autoclave was filled with nitrogen to 10 kg/cm2 G at room temperature. The reaction was begun by heating to 150° C., and this temperature was maintained for 1 hours. The reaction pressure was 15 kg/cm2 (increased with temperature, 30° C.→150° C., 10 kg/cm2→24 kg/cm2). The product was analyzed by GC. The conversion of (chloromethyl) ethylene carbonate was 65.3%, and the selectivity of dimethyl carbonate was 80.9%, and the selectivity of 3-chloropropane-1,2-diol was 83.3%.
This application is a Continuation-in-Part of U.S. application Ser. No. 14/918,015, filed Oct. 20, 2015, the entire content of which is fully incorporated herein by reference.
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| Number | Date | Country | |
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| Number | Date | Country | |
|---|---|---|---|
| Parent | 14918015 | Oct 2015 | US |
| Child | 15285024 | US |
