Patent Application
20170158621
The present invention relates to mitigating, reducing or inhibiting fouling during the oxidation of alkenes, and more specifically relates to introducing an effective amount of an additive to mitigate, reduce, or inhibit fouling during the oxidation of alkenes.
Industrial methods for oxidizing alkenes to produce acrylates, including acrylonitrile, acrylic acid, vinylacetate, acrylates and acrolein, include separation and purification processes such as distillation to remove unwanted impurities or byproducts. Certain impurities, such as peroxides can undergo thermolysis and produce free radicals. These free radicals, in turn, catalyse unwanted polymerization of the alkenes, resulting in fouling caused by the buildup of polymer deposits. Substituted phenol derivatives are potentially useful compounds to mitigate, reduce, or inhibit fouling.
In one embodiment, the present invention provides a method, comprising: a. adding an effective amount of at least one compound selected from the group consisting of a substituted catechol, nitroxide free radicals, a compound of Formula 2, 4-hydroxy-2,2,6,6-tetramethylpiperidine-1-oxyl, phenol, hydroxylamine, and phenylene diamine to a solution of a monomer selected from the group consisting of acrylonitrile, acrylic acid, vinylacetate, acrylates and acrolein; b. placing the monomer solution containing the at least one compound in a pressure vessel, pressurizing the pressure vessel and removing oxygen from the pressure vessel; and c. heating the monomer solution containing the at least one compound, wherein the at least one compound inhibits fouling by preventing polymerization of the monomer.
In one embodiment, the substituted catechol is a compound of Formula 1:
wherein R1 and R2 may be or include an alkyl group, an aryl group, an alkyl group, an alkyl group having a heteroatom, an aryl group having a heteroatom, and combinations thereof.
In one embodiment, the compound of Formula 1 is selected from the group consisting of 4-tert-Butylcatechol, and 3,5-tert-Butylcatechol.
In one embodiment, the at least one compound is a compound of Formula 2:
wherein R may be or include an alkyl group, an aryl group, an alkyl group having a heteroatom, an aryl group having a heteroatom, and combinations thereof.
In one embodiment, the monomer solution containing the at least one compound is heated for a period of time from 0.5 to 48 hours.
In one embodiment, the monomer solution containing the at least one compound is heated to a temperature from 50° C. to 140° C.
In one embodiment, the pressure within the pressure vessel is from −14 psi to 1400 psi.
For clarity of disclosure, and not by way of limitation, the detailed description of the invention is divided into the following subsections that describe or illustrate certain features, embodiments or applications of the present invention.
In some embodiments, the present invention provides a method, comprising: a. adding an effective amount of at least one compound selected from the group consisting of a substituted catechol, nitroxide free radicals, a compound of Formula 2, 4-hydroxy-2,2,6,6-tetramethylpiperidine-1-oxyl, phenol, hydroxylamine, and phenylene diamine to a solution of a monomer selected from the group consisting of acrylonitrile, acrylic acid, vinylacetate, acrylates and acrolein; b. placing the monomer solution containing the at least one compound in a pressure vessel, pressurizing the pressure vessel and removing oxygen from the pressure vessel; and c. heating the monomer solution containing the at least one compound, wherein the at least one compound inhibits fouling by preventing polymerization of the monomer.
In some embodiments, the solution of acrylonitrile is formed via the ammoxidation of propylene. The method of ammoxidation is readily determined by one of ordinary skill in the art.
In some embodiments, the solution of acryloein is formed via the oxidation of propylene. The method of oxidation is readily determined by one of ordinary skill in the art.
In some embodiments, the solution of vinyl acetate is formed via the oxidation of ethylene. The method of oxindation is readily determined by one of ordinary skill in the art.
The term “mitigating fouling” or “preventing reducing fouling” or “inhibiting fouling” as used herein refers to the suppression or reduction of fouling, such as via the formation of polymer deposits.
In some embodiments, the effective amount of the at least one compound results in a 100% inhibition of fouling. In some embodiments, the effective amount of the at least one compound results in a 90% inhibition of fouling. In some embodiments, the effective amount of the at least one compound results in an 80% inhibition of fouling. In some embodiments, the effective amount of the at least one compound results in a 70% inhibition of fouling. In some embodiments, the effective amount of the at least one compound results in a 60% inhibition of fouling. In some embodiments, the effective amount of the at least one compound results in a 50% inhibition of fouling. In some embodiments, the effective amount of the at least one compound results in a 40% inhibition of fouling. In some embodiments, the effective amount of the at least one compound results in a 30% inhibition of fouling. In some embodiments, the effective amount of the at least one compound results in a 20% inhibition of fouling. In some embodiments, the effective amount of the at least one compound results in a 10% inhibition of fouling.
In some embodiments, the effective amount of the at least one compound results in a 10% reduction of fouling. In some embodiments, the effective amount of the at least one compound results in a 20% reduction of fouling. In some embodiments, the effective amount of the at least one compound results in a 30% reduction of fouling. In some embodiments, the effective amount of the at least one compound results in a 40% reduction of fouling. In some embodiments, the effective amount of the at least one compound results in a 50% reduction of fouling. In some embodiments, the effective amount of the at least one compound results in a 60% reduction of fouling. In some embodiments, the effective amount of the at least one compound results in a 70% reduction of fouling. In some embodiments, the effective amount of the at least one compound results in an 80% reduction of fouling. In some embodiments, the effective amount of the at least one compound results in a 90% reduction of fouling. In some embodiments, the effective amount of the at least one compound results in a 100% reduction of fouling.
In some embodiments, the at least one compound is a compound of Formula 1:
wherein R1 and R2 may be or include an alkyl group, an aryl group, an alkyl group, an alkyl group having a heteroatom, an aryl group having a heteroatom, and combinations thereof. The hetero atom may be or include, but is not limited to sulfur, nitrogen, oxygen, and combinations thereof. Non-limiting examples may be or include an ether group, a thiol group, and/or an ester group. R1 may be the same or different from R2.
In some embodiments, the compound of Formula 1 is selected from the group consisting of 4-tert-Butylcatechol, and 3,5-tert-Butylcatechol.
In some embodiments, the at least one compound is a compound of Formula 2:
wherein R may be or include an alkyl group, an aryl group, an alkyl group having a heteroatom, an aryl group having a heteroatom, and combinations thereof. The heteroatom may be or include, but is not limited to sulfur, nitrogen, oxygen, and combinations thereof.
In some embodiments, the at least one compound is 4-hydroxy-2,2,6,6-tetramethylpiperidine-1-oxyl.
In some embodiments, the at least one compound is hydroxylamine.
In some embodiments, the at least one compound is phenylene diamine.
In some embodiments, the at least one compound is added to the monomer solution by direct injection to pump suction or by quill during the distillation, purification, and/or fractionation process. Alternatively, the at least one compound may be added to the equipment used for distillation, purification, and/or fractionation of the monomer. In one non-limiting embodiment, the additive may be injected into the feed, the reflux, and/or the boiler loop on a continuous basis, or the additive may be injected about every 0.5 hour to about 1 hour in an alternative embodiment.
In some embodiments, the effective amount of the at least one compound is 0.01 ppm independently to 10,000 ppm. In some embodiments the effective amount of the at least one compound is 1 ppm to 5000 ppm. In some embodiments the effective amount of the at least one compound is 1 ppm to 1200 ppm. In some embodiments the effective amount of the at least one compound is 1 ppm to 500 ppm. In some embodiments the effective amount of the at least one compound is 1 ppm to 100 ppm. In some embodiments the effective amount of the at least one compound is 1 ppm to 50 ppm. In some embodiments the effective amount of the at least one compound is 1 ppm to 40 ppm. In some embodiments the effective amount of the at least one compound is 1 ppm to 30 ppm. In some embodiments the effective amount of the at least one compound is 1 ppm to 20 ppm. In some embodiments the effective amount of the at least one compound is 1 ppm to 10 ppm. In some embodiments the effective amount of the at least one compound is 40 ppm.
In some embodiments, the at least one compound may be dispersed in a suitable aqueous carrier, such as water. The amount of aqueous carrier may have a ratio based on weight ranging from a 100:1 ratio to a 2:1 ratio, alternatively from a 20:1 ratio to a 2:1 ratio.
In some embodiments, two compounds are added to the monomer solution. The ratio of the first and second compound may be 1:1 to 1:10, or, alternatively, 1:1 to 1:5.
In some embodiments, the monomer solution containing the at least one compound is heated for up to 48 hours. In some embodiments, the monomer solution containing the at least one compound is heated for up to 24 hours. In some embodiments, the monomer solution containing the at least one compound is heated for up to 12 hours. In some embodiments, the monomer solution containing the at least one compound is heated for up to 6 hours. In some embodiments, the monomer solution containing the at least one compound is heated for up to 5 hours. In some embodiments, the monomer solution containing the at least one compound is heated for up to 4 hours. In some embodiments, the monomer solution containing the at least one compound is heated for up to 3 hours. In some embodiments, the monomer solution containing the at least one compound is heated for up to 2 hours. In some embodiments, the monomer solution containing the at least one compound is heated for up to 1 hour. In some embodiments, the monomer solution containing the at least one compound is heated for up to 0.5 hour.
In some embodiments, the monomer solution containing the at least one compound is heated up to 50° C. In some embodiments, the monomer solution containing the at least one compound is heated up to 60° C. In some embodiments, the monomer solution containing the at least one compound is heated up to 70° C. In some embodiments, the monomer solution containing the at least one compound is heated up to 80° C. In some embodiments, the monomer solution containing the at least one compound is heated up to 90° C. In some embodiments, the monomer solution containing the at least one compound is heated up to 100° C. In some embodiments, the monomer solution containing the at least one compound is heated up to 110° C. In some embodiments, the monomer solution containing the at least one compound is heated up to 120° C. In some embodiments, the monomer solution containing the at least one compound is heated up to 130° C. In some embodiments, the monomer solution containing the at least one compound is heated up to 140° C.
In some embodiments, the pressure within the pressure vessel is from −14 psi to 1400 psi. In some embodiments, the pressure within the pressure vessel is −14 psi. In some embodiments, the pressure within the pressure vessel is −10 psi. In some embodiments, the pressure within the pressure vessel is 10 psi. In some embodiments, the pressure within the pressure vessel is 20 psi. In some embodiments, the pressure within the pressure vessel is 50 psi. In some embodiments, the pressure within the pressure vessel is 100 psi. In some embodiments, the pressure within the pressure vessel is 200 psi. In some embodiments, the pressure within the pressure vessel is 200 psi. In some embodiments, the pressure within the pressure vessel is 400 psi. In some embodiments, the pressure within the pressure vessel is 500 psi. In some embodiments, the pressure within the pressure vessel is 600 psi. In some embodiments, the pressure within the pressure vessel is 700 psi. In some embodiments, the pressure within the pressure vessel is 800 psi. In some embodiments, the pressure within the pressure vessel is 900 psi. In some embodiments, the pressure within the pressure vessel is 1000 psi. In some embodiments, the pressure within the pressure vessel is 1100 psi. In some embodiments, the pressure within the pressure vessel is 1200 psi. In some embodiments, the pressure within the pressure vessel is 1300 psi. In some embodiments, the pressure within the pressure vessel is 1400 psi.
In some embodiments, 100% of the oxygen is removed from the pressure vessel. In some embodiments, 90% of the oxygen is removed from the pressure vessel. In some embodiments, 80% of the oxygen is removed from the pressure vessel. In some embodiments, 70% of the oxygen is removed from the pressure vessel. In some embodiments, 60% of the oxygen is removed from the pressure vessel. In some embodiments, 50% of the oxygen is removed from the pressure vessel. In some embodiments, 40% of the oxygen is removed from the pressure vessel. In some embodiments, 30% of the oxygen is removed from the pressure vessel. In some embodiments, 20% of the oxygen is removed from the pressure vessel. In some embodiments, 10% of the oxygen is removed from the pressure vessel.
The present invention is further illustrated, but not limited by, the following examples.
Four pressure vessels, containing 50 ml freshly distilled acrylonitrile (40 ppm AIBN mole concentration) with 20 ppm (weight) of either HQ, TBC, 3,5-TBC, or 2,6-di-tertbutyl-secondary phenol (‘phenol”), was pressurized with air to 100 psi. A fresh acrylonitrile sample without any additive was also used as a control. All pressure vessels were heated at 90° C. for 4 hours. After the vessels were cooled down, the foulants were filtered, dried and weighed. The fouling reduction index was used to evaluate the effective of various additives. The fouling reduction index was calculated based on the following formula:
Fouling Reduction Index=100−(foulant formed without additives−foulant formed with additives)/foulant formed without additives×100. The results are shown in FIG. 1.
HQ showed the best performance in the presence of the air. However TBC and 3,5-TBC can be used to reduce foulant formation. Due to the lower toxicity, TBC can be effectively used as HQ replacement to mitigate the fouling, which was caused by the free radical polymerizations.
Four pressure vessels, containing 50 ml freshly distilled acrylonitrile (40 ppm AIBN mole concentration) with 10 ppm (weight) of either TBC, HTEMPO or hydroxylamine, was pressurized with nitrogen to 100 psi. A fresh acrylonitrile sample without any additive was also used as a control. All pressure vessels were heated at 90° C. for 4 hours.
After the vessels were cooled down, the foulants were filtered, dried and weighed. The fouling reduction index was used to evaluate the effective of various additives. The fouling reduction index was calculated based on the following formula:
Fouling Reduction Index=100−(foulant formed without additives−foulant formed with additives)/foulant formed without additives×100. The results are shown in FIG. 2.
The test data indicated that removal of oxygen from the pressure vessel greatly enhanced the ability of TBC, 3,5-TBC, or 2,6-di-tertbutyl-secondary phenol (“phenol”) to reduce fouling.
Three pressure vessels, containing 50 ml freshly distilled acrylonitrile (40 ppm AIBN mole concentration) with 10 ppm (weight) of either 10 ppm (weight) TBC and 10 ppm (weight) HTEMPO, or 10 ppm (weight) TBC plus 10 ppm (weight) DEHA, was pressurized with air to 100 psi. A fresh acrylonitrile sample without any additive was also used as a control. All pressure vessels were heated at 90° C. for 4 hours. After the vessels were cooled down, the foulants were filtered, dried and weighed. The fouling reduction index was used to evaluate the effective of various additives. The fouling reduction index was calculated based on the following formula:
Fouling Reduction Index=100−(foulant formed without additives−foulant formed with additives)/foulant formed without additives×100. The results are shown in FIG. 3.
The combination of TBC and DEHA showed the best performance in the presence of the air. The TBC/HTEMPO significantly reduced the formation of foulant. Therefore the synergetic effect of additives with TBC derivatives could significantly increase the performance of single components of phenol to mitigate the fouling.
Three pressure vessels, containing 50 ml freshly distilled acrylonitrile (40 ppm AIBN mole concentration) with 10 ppm (weight) of either 10 ppm (weight) TBC and 10 ppm (weight) HTEMPO, or 10 ppm (weight) TBC plus 10 ppm (weight) DEHA, was pressurized with nitrogen to 100 psi. A fresh acrylonitrile sample without any additive was also used as a control. All pressure vessels were heated at 90° C. for 4 hours. After the vessels were cooled down, the foulants were filtered, dried and weighed. The fouling reduction index was used to evaluate the effective of various additives. The fouling reduction index was calculated based on the following formula:
Fouling Reduction Index=100−(foulant formed without additives−foulant formed with additives)/foulant formed without additives×100. The results are shown in FIG. 4.
The combination of TBC and DEHA showed the best performance in the presence of the air. The TBC/HTEMPO significantly reduced the formation of foulant. Therefore the synergetic effect of additives with TBC derivatives could significantly increase the performance of single components of phenol to mitigate the fouling.
The test data indicated that the synergistic effect of substituted catechol+HTEMPO and substituted catechol+DEHA could greatly reduce polymer formation. Therefore the combination of these additives can improve the reliability of alkene oxidation process by mitigating the fouling in the process.
Publications cited throughout this document are hereby incorporated by reference in their entirety. Although the various aspects of the invention have been illustrated above by reference to examples and preferred embodiments, it will be appreciated that the scope of the invention is defined not by the foregoing description but by the following claims properly construed under principles of patent law.
This application claims the benefit, and priority benefit, of U.S. Provisional Patent Application Ser. No. 62/263,419, filed Dec. 4, 2015, the disclosure and contents of which are incorporated by reference herein in their entirety.
| Number | Date | Country | |
|---|---|---|---|
| 62263419 | Dec 2015 | US |
