US4339422A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Carbon black manufacture
Assignee: Phillips Petroleum Co
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Filing: 1980-10-16
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Granted: 1982-07-13
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Expires: 2000-10-16
Abstract
Abstract High tint residual carbon black is produced in a vortex flow, venturi oil furnace carbon black reactor by charging the liquid feed or make hydrocarbon axially as a solid jet into a swirling mass of hot combustion gases upstream from the venturi and passing the hydrocarbon feed and hot combustion gases under carbon black forming conditions through the venturi section of the carbon black reactor.
Inventors
- 👤 Paul J. Cheng
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 09:52
CPC Classifications
C; C09; C09C; C09C1/00; C09C1/44; C09C1/48; C09C1/50; C01; C01P; C01P2006/00; C01P2006/12; C01P2006/19
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
160 words
A process for producing high tint residual carbon black which comprises: (a) introducing a hydrocarbon feed into a generally cylindrical vortex zone having a diameter at least about equal to its length, said feed being introduced as a solid jet stream at essentially zero degree exit spray angle along the axis of said vortex zone; (b) establishing a mass of hot combustion gases surrounding the jet stream of said hydrocarbon feed in said vortex zone by continuously injecting tangentially thereinto combustion supporting oxygen-containing gas and a combustible fuel; (c) passing the jet stream of hydrocarbon feed surrounded by hot combustion gases under carbon black forming conditions axially through a venturi-shaped furnace reaction chamber having an inlet diameter which is equal to or less than that of said vortex zone; and (d) forming carbon black having a high tint residual from said hydrocarbon feed by pyrochemical action due to the heat of the surrounding hot combustion gases in said reaction chamber.
Claim 2
Dependent Claim
160 words
A process for producing high tint residual carbon black which comprises: (a) introducing a hydrocarbon feed into a generally cylindrical vortex zone having a diameter at least about equal to its length, said feed being introduced as a solid jet stream at essentially zero degree exit spray angle along the axis of said vortex zone; (b) establishing a mass of hot combustion gases surrounding the jet stream of said hydrocarbon feed in said vortex zone by continuously injecting tangentially thereinto combustion supporting oxygen-containing gas and a combustible fuel; (c) passing the jet stream of hydrocarbon feed surrounded by hot combustion gases under carbon black forming conditions axially through a venturi-shaped furnace reaction chamber having an inlet diameter which is equal to or less than that of said vortex zone; and (d) forming carbon black having a high tint residual from said hydrocarbon feed by pyrochemical action due to the heat of the surrounding hot combustion gases in said reaction chamber.
Claim 3
Dependent Claim
30 words
A process according to claim 1 wherein the point of introduction of hydrocarbon feed into said vortex zone is in close proximity to the upstream wall of said vortex zone.
Claim 4
Dependent Claim
18 words
A process according to claim 1 wherein said hydrocarbon feed is a highly aromatic, high molecular weight hydrocarbon.
Claim 5
Dependent Claim
36 words
A process according to claim 1 wherein the jet of hydrocarbon feed is introduced into the vortex section at a point between the face of the upstream wall and the entrance to the venturi diverging section.
Claim 6
Dependent Claim
34 words
A process according to claim 1 wherein the point of hydrocarbon feed introduced into the vortex section is within 1 to 28 inches of the face of the upstream wall of the vortex zone.
Claim 7
Independent Claim
98 words
The method of producing high tint residual carbon black in a furnace reactor which comprises the steps of (a) directing a solid stream of a hydrocarbon feedstock axially in said reactor in such a manner that said stream does not diverge substantially in any direction from the axis of introduction (b) surrounding said stream with a swirling mass of hot gases which are at an elevated temperature sufficient to pyrolyze said hydrocarbon feedstock, and (c) passing said mass of hot gases and said stream through a venturi reaction section under conditions which produce high tint residual carbon black.
Claim 8
Independent Claim
98 words
The method of producing high tint residual carbon black in a furnace reactor which comprises the steps of (a) directing a solid stream of a hydrocarbon feedstock axially in said reactor in such a manner that said stream does not diverge substantially in any direction from the axis of introduction (b) surrounding said stream with a swirling mass of hot gases which are at an elevated temperature sufficient to pyrolyze said hydrocarbon feedstock, and (c) passing said mass of hot gases and said stream through a venturi reaction section under conditions which produce high tint residual carbon black.
Claim 9
Dependent Claim
37 words
A process according to claim 6 wherein the gaseous reaction mass existing in the venturi section is quenched to reduce the temperature below carbon black forming temperature and carbon black product is recovered from the gaseous effluent.
Claim 10
Dependent Claim
18 words
A process according to claim 6 wherein said hydrocarbon feed is a highly aromatic, high molecular weight hydrocarbon.
Claim 11
Dependent Claim
34 words
A process according to claim 6 wherein said hydrocarbon feed is introduced into the vortex section at a point between the face of the upstream wall and the entrance to the venturi diverging section.
Claim 12
Dependent Claim
34 words
A process according to claim 7 wherein the point of hydrocarbon feed introduction into the vortex section is within 1 to 28 inches of the face of the upstream wall of the vortex zone.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1985-07-12 | 1986-01-11 | 1986-07-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-07-12 | 1990-01-11 | 1990-07-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-07-12 | 1994-01-11 | 1994-07-13 | $7700.00 | Window Closed / Lapsed |