(meth)acrylic acid production method, and, hydrophilic resin production method
US-9522867-B2 · Dec 20, 2016 · US
US9314784B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9314784-B2 |
| Application number | US-201013257838-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 21, 2010 |
| Priority date | Mar 26, 2009 |
| Publication date | Apr 19, 2016 |
| Grant date | Apr 19, 2016 |
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The process for producing an olefin dimer of the present invention includes a first step of carrying out a dimerization reaction of an olefin in the presence of a solid phosphoric acid catalyst in which phosphoric acid is supported on inorganic support particles at a reaction temperature of 55 to 300° C. by introducing into a reactor an olefin-containing raw material containing water in an amount of 10 ppm by mass or more and less than the saturated water content at the reaction temperature, thereby preparing a reaction product containing an olefin dimer, a second step of washing the reaction product prepared in the first step at a temperature of 50° C. or higher using an alkaline substance-containing water adjusted to pH 8 to 13 and a third step of washing the reaction product after the alkaline washing in the second step with water at a temperature of 0 to 110° C., thereby preparing an olefin dimer.
Opening claim text (preview).
The invention claimed is: 1. A process for producing an olefin dimer comprising: carrying out a dimerization reaction of an olefin in the presence of a solid phosphoric acid catalyst in which phosphoric acid is supported on inorganic support particles at a reaction temperature of 55 to 300° C. by introducing into a reactor an olefin-containing raw material containing water in an amount of 10 ppm by mass or more and less than the saturated water content at the reaction temperature, thereby preparing a reaction product containing an olefin dimer, washing the reaction product at a temperature of 80° C. or higher using an alkaline substance-containing water adjusted to pH 8 to 13, and washing the reaction product after the alkaline washing with water at a temperature of 0 to 110° C. to remove oxygen-containing compounds selected from an alcohol, a ketone, an ether, and an ester having 3 to 7 carbon atoms, thereby preparing an olefin dimer. 2. The process according to claim 1 , wherein the solid phosphoric acid catalyst has a ratio of orthophosphoric acid to the phosphoric acid of 60% by mole or more in terms of phosphorus atoms. 3. The process according to claim 1 , wherein the inorganic support particles have an average particle size of 3.0 mm or less. 4. The process according to claim 1 , wherein the olefin-containing raw material has a water content of 100 ppm by mass or more and less than the saturated water content at a reaction temperature. 5. The process according to claim 1 , wherein the dimerization reaction is carried out in liquid phase. 6. The process according to claim 1 , wherein the reaction product is washed with water at a temperature of 0 to 50° C. to remove the oxygen-containing compounds selected from an alcohol, a ketone, an ether, and an ester having 3 to 7 carbon atoms. 7. The process according to claim 1 , wherein the olefin is a monoolefin having 3 to 7 carbon atoms.
with silicon · CPC title
characterised by dimensions, e.g. grain size (in a colloidal state B01J35/23; crystallite size B01J35/77) · CPC title
using catalysts, e.g. selective catalysts · CPC title
Impregnation · CPC title
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