Patent US4692270A successfully refreshed from Google Patents.
US4692270A
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Surface active agent
Assignee: Eneos Corp
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Filing: 1985-02-14
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Granted: 1987-09-08
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Expires: 2005-02-14
Abstract
Abstract PCT No. PCT/JP85/00059 Sec. 371 Date Sep. 23, 1985 Sec. 102(e) Date Sep. 23, 1985 PCT Filed Feb. 14, 1985 PCT Pub. No. WO85/03647 PCT Pub. Date Aug. 29, 1985.A surfactant is obtained by treating a mixture of 20 to 95 wt. % of a thermal cracking oil fraction obtained by thermally cracking a petroleum heavy residual oil at 400 DEG to 700 DEG C., for example, by delayed coking and 80 to 5 wt. % of other aromatic source, for example, an aromatic fraction having a comparatively high boiling point with an acid catalyst, and sulfonating and neutralizing the product. This surfactant is used as a dispersing agent for a coal-oil mixture (COM).
Inventors
- 👤 Atsushi Sato
- 👤 Yoshikazu Murai
- 👤 Tatsuo Yamaguchi
- 👤 Kanji Mochizuki
- 👤 Kunio Sugisawa
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 19:16
CPC Classifications
C; C10; C10L; C10L1/00; C10L1/32; C10L1/322; C09; C09K; C09K23/00; C09K23/12
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
257 words
A water soluble surface active agent obtained by sulfonating a reaction product boiling higher than hydrocarbons contained in a mixture and not lower than 260° C., under sulfonating conditions, followed by neutralization, which reaction product is obtained by treating said mixture in liquid phase in the presence of an acid catalyst at a reaction temperature of 0° to 330° C. to alkylate aromatics with aliphatic olefins followed by distillation, said mixture consisting of: (A) 20-95 weight percent of a thermal-cracked oil distillate obtained from a delayed coking process for coking a petrolic heavy residual oil at a temperature not lower than 400° C. and not exceeding 700° C., said distillate containing aliphatic olefins; and, either (B) 80-5 weight percent of one or more members boiling in the range of 150° to 250° C. and selected from the following (a) through (c): (a) a thermal-cracked by-product oil distillate obtained by thermal cracking of a petrolic light oil at a temperature of 750° to 850° C. followed by treatment for reducing the content of unsaturated compounds; (b) an reformate distillate obtained by catalytic reforming of a petrolic light oil boiling in the range of 50° to 250° C., followed by treatment for reducing the content of unsaturated compounds if necessary; and (c) an aromatic distillate consisting mainly of aromatic hydrocarbons and obtained by separation from said thermal-cracked by-product oil distillate (a) and/or said reformate distillate (b); or (C) 80-5 weight percent of aromatic hydrocarbons having a boiling range lower than 150° C. and not having an aliphatic double bond.
Claim 2
Dependent Claim
257 words
A water soluble surface active agent obtained by sulfonating a reaction product boiling higher than hydrocarbons contained in a mixture and not lower than 260° C., under sulfonating conditions, followed by neutralization, which reaction product is obtained by treating said mixture in liquid phase in the presence of an acid catalyst at a reaction temperature of 0° to 330° C. to alkylate aromatics with aliphatic olefins followed by distillation, said mixture consisting of: (A) 20-95 weight percent of a thermal-cracked oil distillate obtained from a delayed coking process for coking a petrolic heavy residual oil at a temperature not lower than 400° C. and not exceeding 700° C., said distillate containing aliphatic olefins; and, either (B) 80-5 weight percent of one or more members boiling in the range of 150° to 250° C. and selected from the following (a) through (c): (a) a thermal-cracked by-product oil distillate obtained by thermal cracking of a petrolic light oil at a temperature of 750° to 850° C. followed by treatment for reducing the content of unsaturated compounds; (b) an reformate distillate obtained by catalytic reforming of a petrolic light oil boiling in the range of 50° to 250° C., followed by treatment for reducing the content of unsaturated compounds if necessary; and (c) an aromatic distillate consisting mainly of aromatic hydrocarbons and obtained by separation from said thermal-cracked by-product oil distillate (a) and/or said reformate distillate (b); or (C) 80-5 weight percent of aromatic hydrocarbons having a boiling range lower than 150° C. and not having an aliphatic double bond.
Claim 3
Dependent Claim
23 words
A surface active agent as set forth in claim 1, wherein said acid catalyst is hydrogen fluoride, aluminum chloride, or a complex thereof.
Claim 4
Dependent Claim
28 words
A surface active agent as set forth in claim 1, wherein said treatment for reducing the content of unsaturated compounds is a selective catalytic hydrogenation treatment for olefins.
Claim 5
Dependent Claim
37 words
A surface active agent as set forth in claim 1, wherein said aromatic distillate (c) is obtained by a solvent extraction or an extractive distillation from said thermal-cracked by-product oil distillate (a) and/or said reformate distillate (b).
Claim 6
Dependent Claim
23 words
A surface active agent as set forth in claim 1, wherein said sulfonation is performed at a temperature of 0° to 100° C.
Claim 7
Dependent Claim
25 words
A surface active agent as set forth in claim 1, wherein said sulfonation is performed using concentrated sulfuric acid, fuming sulfuric acid or sulfuric anhydride.
Claim 8
Dependent Claim
24 words
A surface active agent as set forth in claim 1, wherein said neutralization is performed using an alkali metal or an alkali metal hydroxide.
References Cited (Backward Citations)
US2673207A
Cited
JPS291486B1
Cited
US2915517A
Cited
US3030410A
Cited
JPS421536B1
Cited
US3798261A
Cited
US4148821A
Cited
US4252192A
Cited
US4547201A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1990-09-07 | 1991-03-09 | 1991-09-08 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-09-07 | 1995-03-09 | 1995-09-08 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-09-07 | 1999-03-09 | 1999-09-08 | $7700.00 | Window Closed / Lapsed |