US4208268A
Expired / Lapsed
US
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Method of processing thermal cracked by-product oil
Assignee: Eneos Corp
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Filing: 1978-03-27
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Granted: 1980-06-17
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Expires: 1998-03-27
Abstract
Abstract This invention provides a method of processing thermal cracked by-product oil which comprises reacting a distillate from a thermal cracked by-product oil principally containing components of a boiling range between 75 DEG C. and 198 DEG C. said distillate being one of the distillates from the cracking of petroleum hydrocarbons at a cracking temperature of 700 DEG C. or higher, and containing a ratio of 5-100 molar percent aromatic olefins to non-olefinic aromatic hydrocarbons, in liquid phase in the presence of an acid catalyst under such conditions that the reaction temperature is 0 DEG C.-200 DEG C., the liquid residence time is 0.1 hour-5 hours and wherein the content of aromatic olefins in the reaction system are 5% by weight or less at the end of the reaction, to yield a processed distillate containing non-condensed di- and tricyclic aromatic compounds which are reaction products of aromatic olefins with other aromatic hydrocarbons but no substantial amount of unsaturated components.
Inventors
- 👤 Atsushi Sato
- 👤 Isoo Shimizu
- 👤 Eiichi Matsuzaka
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 10:25
CPC Classifications
C; C07; C07C; C07C7/00; C07C7/148; C10; C10G; C10G2400/00; C10G2400/30
Claims Analysis
Total Claims: 17
Claim 1
Independent Claim
182 words
Method of improving thermal cracked by-product oil to remove undesirable unsaturates and recover an improved processed distillate which comprises reacting a distillate from a thermal cracked by-product oil principally containing components of a boiling range between 75° C. and 198° C., said distillate being selected from one of the distillates from the thermal cracking of petroleum hydrocarbons at a temperature of 700° C. or higher, and containing a ratio of 5-100 molar percent undesirable aromatic olefins to non-olefinic aromatic hydrocarbons, in liquid phase in the presence of an acid catalyst under such conditions that the reaction temperature is 0° C.-200° C., the liquid residence time is 0.1 hour-5 hours and wherein the content of said aromatic olefins in the reaction system is maintained at 5% by weight or less, to yield a processed distillate containing non-condensed di- and tricyclic aromatic compounds which are reaction products of said aromatic olefins with a portion of said non-olefinic aromatic hydrocarbons and without substantial reaction with other unsaturated components and distilling said processed distillate to get said improved processed distillate and a heavy reaction product oil.
Claim 2
Dependent Claim
182 words
Method of improving thermal cracked by-product oil to remove undesirable unsaturates and recover an improved processed distillate which comprises reacting a distillate from a thermal cracked by-product oil principally containing components of a boiling range between 75° C. and 198° C., said distillate being selected from one of the distillates from the thermal cracking of petroleum hydrocarbons at a temperature of 700° C. or higher, and containing a ratio of 5-100 molar percent undesirable aromatic olefins to non-olefinic aromatic hydrocarbons, in liquid phase in the presence of an acid catalyst under such conditions that the reaction temperature is 0° C.-200° C., the liquid residence time is 0.1 hour-5 hours and wherein the content of said aromatic olefins in the reaction system is maintained at 5% by weight or less, to yield a processed distillate containing non-condensed di- and tricyclic aromatic compounds which are reaction products of said aromatic olefins with a portion of said non-olefinic aromatic hydrocarbons and without substantial reaction with other unsaturated components and distilling said processed distillate to get said improved processed distillate and a heavy reaction product oil.
Claim 3
Dependent Claim
40 words
Method or processing thermal cracked by-product oil according to claim 1 wherein a diluent is added to the reaction system so as to maintain the content of the aromatic olefins in the reaction system at 5% by weight or less.
Claim 4
Dependent Claim
77 words
Method of processing thermal cracked by-product oil according to claim 2 wherein the diluent is one or a mixture thereof selected from the group consisting of: (i) said processed distillate; (ii) one or more non-olefinic monocyclic aromatic hydrocarbons which are the same sort of non-olefinic aromatics present in the distillates from the thermal cracked by-product oil or said processed distillate; and, (iii) a light oil recovered from said processed distillate by separation of the heavy reaction product.
Claim 5
Dependent Claim
68 words
Method of processing thermal cracked by-product oil according to claim 1 wherein said distillate from the cracked by-product oil is a xylene distillate within a boiling range between 130° C. and 150° C. and reduction of the m-xylene and styrene contents in said xylene distillate is achieved by aralkylation reaction by which noncondenced di- and tricyclic aromatic hydrocarbons are produced between xylenes and styrene in said xylene distillate.
Claim 6
Dependent Claim
43 words
Method of processing thermal cracked by-product oil according to claim 1 wherein said cracked oil contains 5-15% by weight of saturated aliphatic hydrocarbons, 55-85% by weight of aromatic hydrocarbons, 2-10% by weight of unsaturated aliphatic hydrocarbons and 2-15% by weight of aromatic olefins.
Claim 7
Dependent Claim
29 words
Method of processing thermal cracked by-product oil according to claim 1 wherein said acid catalyst is selected from the group comprising solid acid catalysts, mineral acids and Friedel-Crafts catalysts.
Claim 8
Dependent Claim
27 words
Method of processing thermal cracked by-product oil according to claim 4 wherein said acid catalyst is selected from the group comprising solid acid catalysts and mineral acids.
Claim 9
Dependent Claim
28 words
Method of processing thermal cracked by-product oil according to claim 6 wherein said solid acid catalyst is selected from the group comprising acid clay, active clay and silica-alumina.
Claim 10
Dependent Claim
28 words
Method of processing thermal cracked by-product oil according to claim 6 wherein said mineral acid is selected from the group comprising hydrogen fluoride, sulfuric acid and phosphoric acid.
Claim 11
Dependent Claim
44 words
Method of processing thermal cracked by-product oil according to claim 6 wherein said Friedel-Crafts catalyst is selected from the group comprising aluminum chloride, aluminum bromide, boron fluoride, boron chloride, ferric chloride, titanium bromide, titanium chloride, tin chloride, zinc chloride and their etherate or phenolate.
Claim 12
Dependent Claim
28 words
Method of processing thermal cracked by-product oil according to claim 7 wherein said solid acid catalyst is selected from the group comprising acid clay, active clay and silica-alumina.
Claim 13
Dependent Claim
28 words
Method of processing thermal cracked by-product oil according to claim 7 wherein said mineral acid is selected from the group comprising hydrogen fluoride, sulfuric acid and phosphoric acid.
Claim 14
Dependent Claim
26 words
Method of processing thermal cracked by-product oil according to claim 1 wherein said non-condensed di- and tricyclic aromatic compounds are separated from the said processed distillate.
Claim 15
Dependent Claim
34 words
Method of processing thermal cracked by-product oil according to claim 4 wherein said non-condensed di- and tricyclic aromatic compounds which are reaction product with xylenes and styrene are separated from the said processed distillate.
Claim 16
Dependent Claim
43 words
Method of processing thermal cracked by-product oil according to claim 1 wherein said non-condensed dicyclic aromatic hydrocarbons are non-condensed diphenyl hydrocarbons, C n H 2n-14 ; n=14-20 and said non-condensed tricylic aromatic hydrocarbons are non-condensed triphenyl hydrocarbons, C n H 2n-22 ; n=22-30.
Claim 17
Dependent Claim
34 words
Method of processing thermal cracked by-product oil according to claim 4 wherein said non-condensed dicyclic aromatic hydrocarbons are xylylphenylethane--C 16 H 18 and non-condensed tricyclic aromatic hydrocarbons are triphenyl hydrocarbons--C 24 H 26 .
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1983-06-17 | 1983-12-17 | 1984-06-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-06-17 | 1987-12-17 | 1988-06-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-06-17 | 1991-12-17 | 1992-06-17 | $7700.00 | Window Closed / Lapsed |