Method for producing hydrogenated petroleum resin
US-2017096501-A1 · Apr 6, 2017 · US
US11485803B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11485803-B2 |
| Application number | US-201917041773-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 27, 2019 |
| Priority date | Mar 28, 2018 |
| Publication date | Nov 1, 2022 |
| Grant date | Nov 1, 2022 |
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Provided is a new method that effectively reduces odor components that are present in a hydrogenated petroleum resin, and adjusts a softening point to an appropriate range for exhibiting an adhesive performance.A method for deodorizing a hydrogenated petroleum resin, includes stripping a hydrogenated petroleum resin at a gas flow rate of 1 to 45 VVM.
Opening claim text (preview).
The invention claimed is: 1. A method for deodorizing a hydrogenated petroleum resin, the hydrogenated petroleum resin comprising a dicyclopentadiene/vinyl aromatic compound hydrogenated resin and volatile components, the method comprising: hydrogenating a dicyclopentadiene/vinyl aromatic compound polymer in a solvent; removing the solvent to obtain a dicyclopentadiene/vinyl aromatic compound hydrogenated resin comprising volatile compounds; blowing a stream of gas inert to the dicyclopentadiene/vinyl aromatic compound hydrogenated resin into the hydrogenated petroleum resin at a gas flow rate of 1 VVM to 45 VVM; and removing the gas stream with the volatile components from the hydrogenated petroleum resin; wherein the temperature of the hydrogenated petroleum resin is maintained at a temperature of from 150° C. to 250″ while the stream of gas is blown, and a softening point of the dicyclopentadiene/vinyl aromatic compound hydrogenated resin is from 90° C. to 105° C. 2. The method for deodorizing a hydrogenated petroleum resin according to claim 1 , wherein the temperature of the hydrogenated petroleum resin is maintained at a temperature of 160 to 240° C. while the stream of gas is blown. 3. The method for deodorizing a hydrogenated petroleum resin according to claim 1 , wherein the gas flow rate is from 5 VVM to 30 VVM.
Reduction, e.g. hydrogenation · CPC title
Copolymers of hydrocarbons and mineral oils, e.g. petroleum resins · CPC title
Removal of volatile materials, e.g. solvents {(C08F6/001, C08F6/003, C08F6/005, C08F6/006, C08F6/008, C08F6/02, C08F6/04 take precedence)} · CPC title
Styrene · CPC title
having one carbon-to-carbon double bond · CPC title
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