Method for refining dicyclopentadiene
View Patent ↗A first method for refining dicyclopentadiene of the present invention is characterized in that the method separates and recovers dicyclopentadiene by distilling the crude dicyclopentadiene that contains dicyclopentadiene and is obtained by removing a C5 fraction and a BTX fraction from the reaction product obtained by dimerization reaction of the cracked gasoline by-produced in an ethylene plant that uses as feed stock a C2 fraction, a C3 fraction and a C4 fraction. A second method for refining dicyclopentadiene of the present invention is characterized in that the dicyclopentadiene-containing fraction refined by distillation is brought into contact with an inert gas or a hydrocarbon gas having 1 to 3 carbon atoms.
1. A method for distilling dicyclopentadiene consisting essentially of:
distilling a crude dicyclopentadiene, which comprises 10 to 40% by mass methyl dicyclopentadiene, once to obtain at least a first fraction comprising a separated and recovered dicyclopentadiene, which comprises less than 1.0% by mass methyl dicyclopentadiene, and a second fraction that is heavier than the first fraction
wherein the crude dicyclopentadiene is obtained by removing a C5 fraction and a BTX fraction from a reaction product obtained by performing a dimerization reaction on a cracked gasoline by-produced in an ethylene plant that uses as a feedstock a C2 fraction, a C3 fraction and a C4 fraction.
2. The method for distilling dicyclopentadiene according to claim 1 , wherein:
the content of dicyclopentadiene in the crude dicyclopentadiene is 40 to 90% by mass; and
the crude dicyclopentadiene is distilled in such a way that the purity of the separated and recovered dicyclopentadiene is 93% by mass or more.
3. The method for distilling dicyclopentadiene according to claim 1 , wherein the crude dicyclopentadiene is distilled at 130° C. or lower.
4. The method for distilling dicyclopentadiene according to claim 1 , wherein the crude dicyclopentadiene is distilled over 30 to 60 stages of the theoretical number of stages.
5. The method for distilling dicyclopentadiene according to claim 2 , wherein the crude dicyclopentadiene is distilled at 130° C. or lower.
6. The method for distilling dicyclopentadiene according to claim 2 , wherein the crude dicyclopentadiene is distilled over 30 to 60 stages of the theoretical number of stages.
7. The method for distilling dicyclopentadiene according to claim 3 , wherein the crude dicyclopentadiene is distilled over 30 to 60 stages of the theoretical number of stages.
8. The method for distilling dicyclopentadiene according to claim 2 , wherein the crude dicyclopentadiene is distilled at 130° C. or lower and over 30 to 60 stages of the theoretical number of stages.
9. The method for distilling dicyclopentadiene according to claim 1 , wherein the cracked gasoline by-product by-produced in an ethylene plant that uses as a feedstock a C2 fraction, a C3 fraction and a C4 fraction comprises isoprene and piperylene and the sum of these two components is half or less than half of an amount of cyclopentadiene contained in the by-product.
10. The method for distilling dicyclopentadiene according to claim 1 , wherein the reaction product is obtained by performing the dimerization reaction under liquid-phase reaction conditions at a temperature of from 75° C. to 200° C.
11. The method for distilling dicyclopentadiene according to claim 1 , wherein the sum content of isopropenylnorbornene and propenylnorborene in the crude dicyclopentadiene is less than 4% by mass in relation to dicyclopentadiene content.