Highly aromatic base oil and method for producing highly aromatic base oil
A method for producing a highly aromatic base oil of the present invention includes a step of hydrorefining a clarified oil to obtain a highly aromatic base oil having an aromatic content of 50% by mass or more determined by a column chromatography analysis method. The step of hydrorefining a clarified oil is preferably performed under conditions of a hydrogen pressure of 5.0 to 20.0 MPa, a temperature of 280 to 400° C., a hydrogen oil ratio of 300 to 750 NL/L, and a space velocity of 0.3 to 2.0 h −1 . According to the present invention, a highly aromatic base oil used for rubber processing, asphalt reclamation and the like, and a novel method for producing a highly aromatic base oil can be provided.
1. A method for producing a mixed-base oil comprising:
hydrorefining a clarified oil to obtain a highly aromatic base oil having an aromatic content of 50% by mass or more determined by a column chromatography analysis method; and
mixing the highly aromatic base oil and one or more base oils selected from a mineral oil and a synthetic oil other than the highly aromatic base oil to obtain a mixed-base oil having an aromatic content of 50% by mass or more determined by a column chromatography analysis method, an aniline point of 100° C. or less, % C A of 20 to 80 according to ASTM D2140, a pour point of +10° C. or less, a glass-transition point of −30° C. to −60° C., and a rate of aromatic carbon of 0.1 to 0.5.
2. The method for producing a mixed-base oil according to claim 1 , wherein the mixed-base oil has a content of benzo(a)pyrene of 1 ppm by mass or less, and a total content of the following aromatic compounds 1) to 8):
1) benzo(a)pyrene,
2) benzo(e)pyrene,
3) benzo(a)anthracene,
4) chrysene,
5) benzo(b)fluoranthene,
6) benzo(j)fluoranthene,
7) benzo(k)fluoranthene, and
8) dibenzo(a,h)anthracene
of 10 ppm by mass or less.
3. A mixed-base oil comprising;
a highly aromatic base oil, obtained by a method comprising hydrorefining a clarified oil to obtain a highly aromatic base oil having an aromatic content of 50% by mass or more determined by a column chromatography analysis method,
and having an aromatic content of 50% by mass or more determined by a column chromatography analysis method, an aniline point of 60° C. or less, % C A of 30 to 80 according to ASTM D2140, a pour point of +10° C. or less, a kinematic viscosity at 40° C. of 100 mm 2 /s or more, a glass-transition point of −30° C. to −60° C., and a rate of aromatic carbon of 0.1 to 0.5;
and one or more base oils selected from a mineral oil and a synthetic oil other than the highly aromatic base oil, wherein
the mixed-base oil has an aromatic content of 50% by mass or more determined by a column chromatography analysis method, an aniline point of 100° C. or less, % C A of 20 to 80 according to ASTM D2140, a pour point of +10° C. or less, a glass-transition point of −30° C. to −60° C., and a rate of aromatic carbon of 0.1 to 0.5.
4. The mixed-base oil according to claim 3 , wherein the mixed-base oil has a content of benzo(a)pyrene of 1 ppm by mass or less, and a total content of the following aromatic compounds 1) to 8):
1) benzo(a)pyrene,
2) benzo(e)pyrene,
3) benzo(a)anthracene,
4) chrysene,
5) benzo(b)fluoranthene,
6) benzo(j)fluoranthene,
7) benzo(k)fluoranthene, and
8) dibenzo(a,h)anthracene
of 10 ppm by mass or less.
5. A method for producing a highly aromatic base oil comprising:
hydrorefining a clarified oil to obtain a highly aromatic base oil having an aromatic content of 50% by mass or more determined by a column chromatography analysis method, an aniline point of 60° C. or less, % C A of 30 to 80 according to ASTM D2140 a sour point of +10° C. or less, a kinematic viscosity at 40° C. of 100 mini/s or more, a glass-transition point of −30° C. to −60° C., a rate of aromatic carbon of 0.1 to 0.5, a content of benzo(a)pyrene of 1 ppm by mass or less, and a total content of the following aromatic compounds 1) to 8):
1) benzo(a)pyrene,
2) benzo(e)pyrene,
3) benzo(a)anthracene,
4) chrysene,
5) benzo(b)fluoranthene,
6) benzo(j)fluoranthene,
7) benzo(k)fluoranthene, and
8) dibenzo(a,h)anthracene
of 10 ppm by mass or less.
6. The method for producing a highly aromatic base oil according to claim 5 , wherein hydrorefining a clarified oil is performed under conditions of a hydrogen pressure of 10.0 to 20.0 MPa, a temperature of 280 to 400° C., a hydrogen oil ratio of 300 to 750 NL/L, and a space velocity of 0.3 to 2.0 h −1 .
7. A method for producing a mixed-base oil comprising:
hydrorefining a clarified oil to obtain a highly aromatic base oil having an aromatic content of 50% by mass or more determined by a column chromatography analysis method, an aniline point of 60° C. or less, a content of benzo(a)pyrene of 1 ppm by mass or less, and a total content of the following aromatic compounds 1) to 8):
1) benzo(a)pyrene,
2) benzo(e)pyrene,
3) benzo(a)anthracene,
4) chrysene,
5) benzo(b)fluoranthene,
6) benzo(j)fluoranthene,
7) benzo(k)fluoranthene, and
8) dibenzo(a,h)anthracene
of 10 ppm by mass or less; and
mixing the highly aromatic base oil and one or more base oils selected from a mineral oil and a synthetic oil other than the highly aromatic base oil to obtain a mixed-base oil having an aromatic content of 50% by mass or more determined by a column chromatography analysis method, an aniline point of 100° C. or less, % C A of 20 to 80 according to ASTM D2140, a pour point of +10° C. or less, a glass-transition point of −30° C. to −60° C., a rate of aromatic carbon of 0.1 to 0.5, a content of benzo(a)pyrene of 1 ppm by mass or less, and a total content of the following aromatic compounds 1) to 8):
1) benzo(a)pyrene,
2) benzo(e)pyrene,
3) benzo(a)anthracene,
4) chrysene,
5) benzo(b)fluoranthene,
6) benzo(j)fluoranthene,
7) benzo(k)fluoranthene, and
8) dibenzo(a,h)anthracene
of 10 ppm by mass or less.
8. A highly aromatic base oil, wherein
the highly aromatic base oil has an aromatic content of 50% by mass or more determined by a column chromatography analysis method, an aniline point of 60° C. or less, % C A of 30 to 80 according to ASTM D2140, a pour point of +10° C. or less, a kinematic viscosity at 40° C. of 100 mm 2 /s or more, a glass-transition point of −30° C. to −60° C., a rate of aromatic carbon of 0.1 to 0.5, a content of benzo(a)pyrene of 1 ppm by mass or less, and a total content of the following aromatic compounds 1) to 8):
1) benzo(a)pyrene,
2) benzo(e)pyrene,
3) benzo(a)anthracene,
4) chrysene,
5) benzo(b)fluoranthene,
6) benzo(j)fluoranthene,
7) benzo(k)fluoranthene, and
8) dibenzo(a,h)anthracene
of 10 ppm by mass or less.
9. A mixed-base oil comprising the highly aromatic base oil according to claim 8 and one or more base oils selected from a mineral oil and a synthetic oil other than the highly aromatic base oil, wherein
the mixed-base oil has an aromatic content of 50% by mass or more determined by a column chromatography analysis method, an aniline point of 100° C. or less, % C A of 20 to 80 according to ASTM D2140, a pour point of +10° C. or less, a glass-transition point of −30° C. to −60° C., a rate of aromatic carbon of 0.1 to 0.5, a content of benzo(a)pyrene of 1 ppm by mass or less, and a total content of the following aromatic compounds 1) to 8):
1) benzo(a)pyrene,
2) benzo(e)pyrene,
3) benzo(a)anthracene,
4) chrysene,
5) benzo(b)fluoranthene,
6) benzo(j)fluoranthene,
7) benzo(k)fluoranthene, and
8) dibenzo(a,h)anthracene
of 10 ppm by mass or less.