Patent US4108798A successfully refreshed from Google Patents.
US4108798A
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Process for the production of petroleum coke
Assignee: Maruzen Petrochemical Co Ltd
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Filing: 1976-07-06
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Granted: 1978-08-22
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Expires: 1996-07-06
Abstract
Abstract A high crystalline coke can be prepared by heat-soaking a petroleum feedstock in the presence of added dissolved sulfur, heating to effect controlled thermal cracking thereof, separating non-crystalline substances as pitch, recovering a heavy cokable residue from the pitch free feed, and subjecting the residue to delayed coking.
Inventors
- 👤 Morgan C. Sze
- 👤 Thomas M. Bennett
- 👤 Andre A. Simone
- 👤 Kiyoshige Hayashi
- 👤 Mikio Nakaniwa
- 👤 Nobuyuki Kobayashi
- 👤 Yoshihiko Hase
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 18:47
CPC Classifications
C; C10; C10B; C10B55/00; C10G; C10G51/00; C10G51/02; C10G51/023
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
187 words
A process for producing high crystalline petroleum coke from a petroleum feedstock, comprising: heat soaking a petroleum feedstock at a temperature of at least 230° C for at least 5 minutes in the presence of 30 to 200 parts per million of added dissolved sulphur in the form of at least one member selected from the group consisting of elemental sulphur, mercaptan and carbon disulfide, said petroleum feedstock being a residual heavy oil having no greater than 1.5 wt.% sulphur which is selected from the group consisting of virgin crude oil, distillation residues, cracked residues and hydrodesulfurized distillation and cracked residues; heating the heat-soaked feedstock to effect controlled thermal cracking thereof at a pressure of no greater than 50 kg/cm 2 G and to a final temperature of from 450° C to 530° C; separating non-crystalline substances as pitch to produce a pitch free feed; recovering a heavy cokable residue from the pitch free feed; heating said heavy cokable residue to coking temperatures; and, subjecting the heated heavy cokable residue to delayed coking to produce high crystalline petroleum coke. Reconsideration and allowance of this application are requested.
Claim 2
Dependent Claim
187 words
A process for producing high crystalline petroleum coke from a petroleum feedstock, comprising: heat soaking a petroleum feedstock at a temperature of at least 230° C for at least 5 minutes in the presence of 30 to 200 parts per million of added dissolved sulphur in the form of at least one member selected from the group consisting of elemental sulphur, mercaptan and carbon disulfide, said petroleum feedstock being a residual heavy oil having no greater than 1.5 wt.% sulphur which is selected from the group consisting of virgin crude oil, distillation residues, cracked residues and hydrodesulfurized distillation and cracked residues; heating the heat-soaked feedstock to effect controlled thermal cracking thereof at a pressure of no greater than 50 kg/cm 2 G and to a final temperature of from 450° C to 530° C; separating non-crystalline substances as pitch to produce a pitch free feed; recovering a heavy cokable residue from the pitch free feed; heating said heavy cokable residue to coking temperatures; and, subjecting the heated heavy cokable residue to delayed coking to produce high crystalline petroleum coke. Reconsideration and allowance of this application are requested.
Claim 3
Dependent Claim
13 words
The process of claim 1 wherein the feedstock is a pyrolysis fuel oil.
Claim 4
Dependent Claim
24 words
The process of claim 1 wherein the heating of the heat-soaked residue is at a pressure of from 4 to 25 kg/cm 2 G.
Claim 5
Dependent Claim
18 words
The process of claim 3 wherein the residence time in the thermal cracking is less than 17 seconds.
Claim 6
Dependent Claim
20 words
The process of claim 3, wherein the residence time in the thermal cracking is from 30 seconds to 120 seconds.
Claim 7
Dependent Claim
29 words
The process of claim 3 wherein the heat soaking is effected at a temperature of from 230° to 315° C for a time of from 5 to 120 minutes.
Claim 8
Dependent Claim
31 words
The process of claim 1 wherein the delayed coking is effected at a temperature of from 430° to 460° C, at a pressure of from 4 to 20 kg/cm 2 G.
Claim 9
Dependent Claim
37 words
The process of claim 7 wherein non-crystalline substances are separated as a pitch bottoms by flash distillation at a temperature of from 380° to 510° C at a pressure of from 0 to 2 kg/cm 2 G.
Claim 10
Dependent Claim
58 words
The process of claim 8 wherein the feedstock is a pyrolysis fuel oil and the coke produced has a maximum transverse magnetoresistance (10 KGauss, 77° K) of at least 16.0% and a coefficient of thermal expansion (over 100°-400° C) of less than 1.0 × 10 -6 /° C, when measured in the form of a graphite artifact thereof.
Claim 11
Dependent Claim
12 words
A high crystalline petroleum coke produced by the process of claim 1.
Claim 12
Dependent Claim
17 words
A graphite electrode prepared from a high crystalline petroleum coke produced by the process of claim 1.
Claim 13
Dependent Claim
16 words
A calcined coke prepared from a high crystalline coke produced by the process of claim 1.
References Cited (Backward Citations)
US3472761A
Cited
US3547804A
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US3537976A
Cited
US3687840A
Cited
US3759822A
Cited
US3794579A
Cited
US3959115A
Cited
US4049538A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-08-21 | 1982-02-20 | 1982-08-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-08-21 | 1986-02-20 | 1986-08-22 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-08-21 | 1990-02-20 | 1990-08-22 | $7700.00 | Window Closed / Lapsed |