초록 ▼

The invention relates to a utility fluid, such as a fluid containing aromatic and non-aromatic ringed molecules, useful as a diluent when hydroprocessing pyrolysis tar, such as steam cracker tar. The specified utility fluid comprises ≧10.0 wt % aromatic and non-aromatic ring compounds and each of th

The invention relates to a utility fluid, such as a fluid containing aromatic and non-aromatic ringed molecules, useful as a diluent when hydroprocessing pyrolysis tar, such as steam cracker tar. The specified utility fluid comprises ≧10.0 wt % aromatic and non-aromatic ring compounds and each of the following: (a) ≧1.0 wt % of 1.0 ring class compounds; (b) ≧5.0 wt % of 1.5 ring class compounds; (c) ≧5.0 wt % of 2.0 ring class compounds; and (d) ≦0.1 wt % of 5.0 ring class compounds. The invention also relates to methods for producing such a utility fluid and to processes for hydroprocessing pyrolysis tar.

대표청구항 ▼

1. A pyrolysis tar hydroprocessing process comprising: (a) providing a first mixture comprising ≧10.0 wt % hydrocarbon;(b) pyrolysing the first mixture to produce a second mixture comprising ≧1.0 wt % of C2 unsaturates;(c) separating a tar stream from the second mixture, wherein the tar stream inclu

1. A pyrolysis tar hydroprocessing process comprising: (a) providing a first mixture comprising ≧10.0 wt % hydrocarbon;(b) pyrolysing the first mixture to produce a second mixture comprising ≧1.0 wt % of C2 unsaturates;(c) separating a tar stream from the second mixture, wherein the tar stream includes ≧90 wt % of the second mixture's molecules having an atmospheric boiling point of ≧290° C.;(d) providing a primer fluid, the primer fluid comprising (i) aromatic and non-aromatic ring compounds, (ii) vinyl aromatics, and having an ASTM D86 10% distillation point ≧60.0° C. and a 90% distillation point ≦350.0° C.;(d1) hydroprocessing the primer fluid to produce a hydroprocessed primer fluid by contacting the primer fluid with at least one hydroprocessing catalyst under catalytic hydroprocessing conditions in the presence of molecular hydrogen;(e) hydroprocessing the tar stream by contacting the tar stream with at least one hydroprocessing catalyst under catalytic hydroprocessing conditions in the presence of molecular hydrogen and in the presence of the hydroprocessed primer fluid to convert at least a portion of the tar stream to a hydroprocessed product; and(f) separating from the hydroprocessed product a mid-cut comprising from 20 to 70 wt % of the hydroprocessed product and having an ASTM D86 10% distillation point ≧60.0° C. and a 90% distillation point ≦350.0° C.; and(g) recycling at least a portion of the mid-cut and substituting the recycled mid-cut for at least a portion of the hydroprocessed primer fluid utilized in hydroprocessing the tar stream. 2. The process of claim 1, wherein the mid-cut comprises from 30 to 60 wt % of the hydroprocessed product. 3. The process of claim 1, wherein (i) the hydroprocessing is conducted continuously in a hydroprocessing zone from a first time t1 to a second time t2, t2 being ≧(t1+10 days) and (ii) hydroprocessing zone's pressure drop at the second time is increased ≦10.0% over the pressure drop at the first time. 4. The process of claim 3, wherein (i) t2 is ≧(t1+100 days) and (ii) hydroprocessing zone's pressure drop at the second time is increased ≦10.0% over the pressure drop at the first time. 5. The process of claim 1, wherein the first mixture's hydrocarbon comprises one or more of naphtha, gas oil, vacuum gas oil, waxy residues, atmospheric residues, residue admixtures, or crude oil. 6. The process of claim 1, wherein the second mixture's tar stream comprises (i) ≧10.0 wt % of molecules having an atmospheric boiling point ≧565° C. that are not asphaltenes, and (ii) ≦1.0×103 ppmw metals, the weight percents being based on the weight of the second mixture's tar. 7. The process of claim 1, wherein the mid-cut of step (f) comprises ≧10.0 wt % aromatic and non-aromatic ring compounds, wherein, the mid-cut includes: (a) ≧1.0 wt % of 1.0 ring class compounds comprising only one moiety selected from the group consisting of (i) one aromatic ring and(ii) two non-aromatic rings;(b) ≧5.0 wt % of 1.5 ring class compounds comprising only one moiety selected from the group consisting of (i) one aromatic ring and one non-aromatic ring, and(ii) three non-aromatic rings;(c) ≧5.0 wt % of 2.0 ring class compounds comprising only one moiety selected from the group consisting of (i) two aromatic rings,(ii) one aromatic ring and two non-aromatic rings, and(iii) four non-aromatic rings; and(d) ≦0.1 wt % of 5.0 ring class compounds comprising only one moiety selected from the group consisting of (i) five aromatic rings,(ii) four aromatic rings and two non-aromatic rings,(iii) three aromatic rings and four non-aromatic rings,(iv) two aromatic rings and six non-aromatic rings,(v) one aromatic ring and eight non-aromatic rings and(vi) ten non-aromatic rings, where the weight percents are based on the weight of the mid-cut. 8. A pyrolysis tar hydroprocessing process comprising: (a) providing a primer fluid, the primer fluid comprising (i) aromatic and non-aromatic ring compounds, (ii) vinyl aromatics, and having an ASTM D86 10% distillation point ≧60.0° C. and a 90% distillation point ≦350.0° C.;(b) hydroprocessing the primer fluid to produce a hydroprocessed primer fluid by contacting the primer fluid with at least one hydroprocessing catalyst under catalytic hydroprocessing conditions in the presence of molecular hydrogen;(c) providing a first mixture comprising ≧10.0 wt % hydrocarbon based on the weight of the first mixture;(d) pyrolysing the first mixture to produce a second mixture comprising ≧1.0 wt % of C2 unsaturates, based on the weight of the second mixture;(e) separating a tar stream from the second mixture, wherein the tar stream includes ≧90 wt % of the second mixture's molecules having an atmospheric boiling point of ≧290° C.; andhydroprocessing the tar stream by contacting the tar stream with the same hydroprocessing catalyst under catalytic hydroprocessing conditions in the presence of molecular hydrogen and the hydroprocessed primer fluid to convert at least a portion of the tar stream to a hydroprocessed product. 9. The process of claim 8, wherein the primer fluid comprises steam cracked gas oil. 10. The process of claim 8, wherein the hydroprocessed primer fluid comprises ≦10.0 wt % vinyl aromatics, based on the weight of the hydroprocessed primer fluid. 11. The process of claim 8, wherein the hydroprocessed primer fluid comprises ≦1.0 wt % vinyl aromatics, based on the weight of the hydroprocessed primer fluid. 12. The process of claim 8, wherein the hydroprocessed primer fluid of step (b) comprises ≧10.0 wt % aromatic and non-aromatic ring compounds, wherein, the hydroprocessed primer fluid includes: (a) ≧1.0 wt % of 1.0 ring class compounds comprising only one moiety selected from the group consisting of (i) one aromatic ring, and(ii) two non-aromatic rings;(b) ≧5.0 wt % of 1.5 ring class compounds comprising only one moiety selected from the group consisting of (i) one aromatic ring and one non-aromatic ring, and(ii) three non-aromatic rings;(c) ≧5.0 wt % of 2.0 ring class compounds comprising only one moiety selected from the group consisting of (i) two aromatic rings,(ii) one aromatic ring and two non-aromatic rings, and(iii) four non-aromatic rings; and(d) ≦0.1 wt % of 5.0 ring class compounds comprising only one moiety selected from the group consisting of (i) five aromatic rings,(ii) four aromatic rings and two non-aromatic rings,(iii) three aromatic rings and four non-aromatic rings,(iv) two aromatic rings and six non-aromatic rings,(v) one aromatic ring and eight non-aromatic rings, and(vi) ten non-aromatic rings, where the weight percents are based on the weight of the hydroprocessed primer fluid.