Method for carrying out a chemical reaction in an upflow reactor
US-2024042406-A1 · Feb 8, 2024 · US
US10138325B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10138325-B2 |
| Application number | US-201715581171-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 28, 2017 |
| Priority date | May 12, 2016 |
| Publication date | Nov 27, 2018 |
| Grant date | Nov 27, 2018 |
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Polyphenolic condensates and epoxidized products prepared from said condensates are prepared by a reaction utilizing multi catalysts to control the weight average molecular weight (Mw) and the number average molecular weight (Mn). Improved color and ultraviolet absorbance are possessed by the condensates described herein.
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The invention claimed is: 1. Polyphenolic condensates from aldehydes and phenolic compounds which comprise: an aldehyde-phenolic condensate having a range of weight average molecular weight (Mw), calculated as polystyrene and phenol, satisfying the expression, 1.3×[1×(Molecular weight of aldehydes)+2×(Molecular weight of phenolic compounds)−2×(Molecular weight of water)] to 1.5×[3×(Molecular weight of aldehydes)+3×(Molecular weight of phenolic compounds)−2×(Molecular weight of water)]; the Mw range takes about 35% to about 50% of overall Gel-Permeation Chromatography (GPC) integrated area at a detection wavelength of 254 nm; and a Gardner Index is not more than 13. 2. The condensates of claim 1 , wherein the phenolic compound is selected from the group consisting of phenol, o-methylphenol, m-methylphenol, p-methylphenol, para-tert-butyl-phenol, p-octylphenol, p-phenylphenol, p-cumylphenol, p-isopropylphenol, p-nonylphenol, 2,3-dimethylphenol, 2,4-dimethylphenol, 2,5-dimethylphenol, 2,6-dimethylphenol, 3,4-dimethylphenol, 3,5-dimethylphenol, o-ethylphenol, m-ethylphenol, p-ethylphenol and mixtures thereof. 3. The condensates of claim 1 , wherein the aldehyde is selected from the group consisting of glyoxal, fumaraldehyde, hexa-2, 4-dienedial, octa-2, 4, 6-trienedial, phenylglyoxal, terephthalaldehyde, phthalaldehyde, isophthaldehyde, napthalene dicarbaldehyde and mixtures thereof. 4. An epoxy compound which is epoxidized from the condensates of claim 1 and comprise: having a range of weight average molecular weight (Mw), calculated as polystyrene and phenol, satisfying the expression, 1.3×[1×(Molecular weight of aldehydes)+2×(Molecular weight of phenolic compounds)−2×(Molecular weight of water)] to 1.5×[3×(Molecular weight of aldehydes)+3×(Molecular weight of phenolic compounds)−2×(Molecular weight of water)+168]; the Mw range takes about 60% to about 70% of overall Gel-Permeation Chromatography (GPC) integrated area at a detection wavelength of 254 nm; and a Gardner Index is not more than 13. 5. The epoxy compound of claim 4 , wherein the epoxy compound has an ultraviolet (UV) absorbance of at least 0.240 at 365 nm or at least 0.430 at 350 nm. 6. A process of preparing polyphenolic condensates from aldehydes and phenolic compounds which comprise: (a) condensing a mixture of condensates, from a molar ratio of aldehydes to phenolic compounds being about 0.11 to 0.17; (b) adding at least one acid catalyst to the mixture in the presence of about 0.05% to 16% of aldehyde charged for condensation reactions; (c) obtaining polyphenolic condensates having a range of weight average molecular weight (Mw), calculated as polystyrene and phenol, wherein the range satisfying the expression, 1.3×[1×(Molecular weight of aldehydes)+2×(Molecular weight of phenolic compounds)−2(Molecular weight of water)] to 1.5×[3×(Molecular weight of aldehydes)+3×(Molecular weight of phenolic compounds)−2×(Molecular weight of water)]; the Mw range takes about 35% to about 50% of overall Gel-Permeation Chromatography (GPC) integrated area at a detection wavelength of 254 nm; and a Gardner Index is not more than 13. 7. The process of claim 6 , wherein the phenolic compound is selected from the group consisting of phenol, o-methylphenol, m-methylphenol, p-methylphenol, para-tert-butyl-phenol, p-octylphenol, p-phenylphenol, p-cumylphenol, p-isopropylphenol, p-nonylphenol, 2,3-dimethylphenol, 2,4-dimethylphenol, 2,5-dimethylphenol, 2,6-dimethylphenol, 3,4-dimethylphenol, 3,5-dimethylphenol, o-ethylphenol, m-ethylphenol, p-ethylphenol, 2,3,4-trimethylphenol, 2,3,5-trimethylphenol, 3,4,5-trimethylphenol and mixtures thereof. 8. The process of claim 6 , wherein the aldehyde is selected from the group consisting of glyoxal, fumaraldehyde, hexa-2,4-dienedial, octa-2,4,6-trienedial, phenylglyoxal, terephthalaldehyde, phthalaldehyde, isophthalaldehyde, naphthalene dicarbaldehyde and mixtures thereof. 9. The process of claim 6 , wherein the acid catalyst is selected from the group consisting of p-Toluenesulfonic acid, oxalic acid, hydrochloric acid, sulfuric acid, phosphoric acid, trichloroacetic acid, acid-functional cationic exchange catalyst and their mixtures. 10. An epoxy compound which is epoxidized from the polyphenolic condensates of claim 6 . 11. A glyoxal-phenolic condensate from glyoxal and phenolic compounds which comprises: an glyoxal-phenolic condensate having a range of weight average molecular weight (Mw), calculated as polystyrene and phenol, satisfies the expression, 1.3×[1×(Molecular weight of aldehydes)+2×(Molecular weight of phenolic compounds)−2×(Molecular weight of water)] to 1.5×[3×(Molecular weight of aldehydes)+3×(Molecular weight of phenolic compounds)−2×(Molecular weight of water)]; the Mw range takes about 35% to about 50% of overall Gel-Permeation Chromatography (GPC) integrated area at a detection wavelength of 254 nm; and a Gardner Index is not more than 13. 12. The condensates of claim 11 , wherein the phenolic compound is selected from the group consisting of phenol, o-methylphenol, m-methylphenol, p-methylphenol, para-tert-butyl-phenol, p-octylphenol, p-phenylphenol, p-cumylphenol, p-isopropylphenol, p-nonylphenol, 2,3-dimethylphenol, 2,4-dimethylphenol, 2,5-dimethylphenol, 2,6-dimethylphenol, 3,4-dimethylphenol, 3,5-dimethylphenol, o-ethylphenol, m-ethylphenol, p-ethylphenol, 2,3,4-trimethylphenol, 2,3,5-trimethylphenol, 3,4,5-trimethylphenol and mixtures thereof. 13. An epoxy compound which is epoxidized from the glyoxal-phenolic condensates of claim 11 comprise: a range of weight average molecular weight (Mw), calculated as polystyrene and phenol, satisfying the expression, 1.3×[1×(Molecular weight of aldehydes)+2×(Molecular weight of phenolic compounds)−2×(Molecular weight of water)] to 1.5×[3×(Molecular weight of aldehydes)+3×(Molecular weight of phenolic compounds)−2×(Molecular weight of water)+168]; the Mw range takes about 60% to about 70% of overall Gel-Permeation Chromatography (GPC) integrated area at a detection wavelength of 254 nm; an ultraviolet (UV) absorbance at least 0.240 at 365 nm or at least 0.430 at 350 nm; and a Gardner Index is not more than 13. 14. The epoxy compound of claim 13 , wherein the phenolic compound is selected from the group consisting of phenol, o-methylphenol, m-methylphenol, p-methylphenol, para-tert-butyl-phenol, p-octylphenol, p-phenylphenol, p-cumylphenol, p-isopropylphenol, p-nonylphenol, 2,3-dimethylphenol, 2,4-dimethylphenol, 2,5-dimethylphenol, 2,6-dimethylphenol, 3,4-dimethylphenol, 3,5-dimethylphenol, o-ethylphenol, m-ethylphenol, p-ethylphenol, 2,3,4-trimethylphenol, 2,3,5-trimethylphenol, 3,4,5-trimethylphenol and mixtures thereof. 15. The glyoxal-phenolic condensate from glyoxal and phenolic compounds according to claim 11 , wherein the glyoxal-phenolic condensate has an UV absorbance at 365 nm is at least 0.320 with a Mw range takes about 35% to about 50% of overall Gel-Permeation Chromatography (GPC) integrated area of Mw=274 to 630 at a detection wavelength of 254 nm or the UV absorbance at 350 nm is at least 0.550 with the Mw range takes about 35% to about 50% of GPC integrated area of Mw=274 to 630 at a detection wavelength of 254 nm. 16. A process of preparing glyoxal-phenolic condensates from glyoxal and phenol which comprise: (a) condensing a mixture of condensates, from a molar ratio of glyoxal to phenol being about 0.11 to 0.15; (b) adding at least one acid catalyst to the mixture in the presence of about 0.05% to 16% of glyoxal charged for condensation reactions and the a pKa value of at least one acid catalyst is not more than 1.0; (c) obtaining glyoxal-ph
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