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US4042344A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the production of gaseous mixtures

Assignee: CALLCOTT THOMAS GEORGE 42 KERR STREET MAYFIELD NEW SOUTH WALES
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Filing: 1976-05-07
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Granted: 1977-08-16
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Expires: 1996-05-07
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Abstract

Abstract A process for the production of a gaseous mixture containing substantial amounts of carbon monoxide and hydrogen, which comprises: (1) blending an oxidizing gas and a primary fuel within a combustion chamber having a combustion zone, which is substantially free of baffles, to produce a compressible gas or gas-like mixture; (2) causing the mixture to assume a highly turbulent compact and self-contained configuration by subjecting it to swirl, the swirling mixture having a swirl number greater than 0.5 and no greater than 1.5, and igniting the mixture when in this configuration to achieve total combustion of the primary fuel to produce hot gaseous products; and (3) thereafter mixing and reacting the hot gaseous products with a gas-like secondary fuel in the combustion chamber, wherein the secondary fuel is introduced into the combustion chamber adjacent to the wall thereof and in physical contact with the self-contained configuration, to produce a gaseous mixture containing substantial amounts of carbon monoxide and hydrogen.

Inventors

  • 👤 Thomas George Callcott
  • 👤 Terrence Kevin Deague

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 17:39
CPC Classifications
F; F23; F23C; F23C1/00; C; C01; C01B; C01B3/00; C01B3/02; C01B3/22; C01B3/32; C01B3/34; C10; C10J; C10J3/00; C10J3/46; C10J3/48; C10J3/485; C10J3/487; C10J3/50; C10J3/506; C10J3/72; C10J3/74; C10J3/76; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/093; C10J2300/0946; C10J2300/0953; C10J2300/0956; C10J2300/0959; C10J2300/0973; C10J2300/0976

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 59 words
A process for the production of a gaseous mixture containing substantial amounts of carbon monoxide and hydrogen, comprising the steps of: 1. blending an oxidizing gas and a primary fuel within a combustion chamber having a combustion zone, said combustion chamber being substantially free of baffles in said combustion zone, to produce a compressible gas or gas-like mixture, 2.
Claim 2
Dependent Claim 59 words
A process for the production of a gaseous mixture containing substantial amounts of carbon monoxide and hydrogen, comprising the steps of: 1. blending an oxidizing gas and a primary fuel within a combustion chamber having a combustion zone, said combustion chamber being substantially free of baffles in said combustion zone, to produce a compressible gas or gas-like mixture, 2.
Claim 3
Dependent Claim 114 words
causing said mixture to assume a highly turbulent compact and self-contained configuration, provided that, however, when said self-contained configuration is achieved by causing the mixture to swirl, then the swirl number is greater than 0.5 and no greater than about 1.5, and igniting said mixture when in said configuration to achieve total combustion of said primary fuel to produce hot gaseous products, and 3. thereafter mixing and reacting the hot gaseous products of said combustion process with a gas-like secondary fuel in said combustion chamber, wherein the secondary fuel is introduced into said combustion chamber adjacent to the wall thereof and in physical contact with said self-contained configuration, to produce a gaeous mixture containing
Claim 4
Dependent Claim 114 words
causing said mixture to assume a highly turbulent compact and self-contained configuration, provided that, however, when said self-contained configuration is achieved by causing the mixture to swirl, then the swirl number is greater than 0.5 and no greater than about 1.5, and igniting said mixture when in said configuration to achieve total combustion of said primary fuel to produce hot gaseous products, and 3. thereafter mixing and reacting the hot gaseous products of said combustion process with a gas-like secondary fuel in said combustion chamber, wherein the secondary fuel is introduced into said combustion chamber adjacent to the wall thereof and in physical contact with said self-contained configuration, to produce a gaeous mixture containing
Claim 5
Dependent Claim 58 words
substantial amounts of CO and H 2 . 2. Process of claim 1, wherein steps 1 and 2 are conducted in a cylindrical combustion chamber and are achieved by causing said mixture to swirl, the swirl number of said mixture being not so great as to cause a wall jet to develop at the wall of the chamber.
Claim 6
Dependent Claim 29 words
Process of claim 1, wherein the secondary fuel forms a sheath around said combustion zone, which sheath is in direct physical contact with the products of the combustion process.
Claim 7
Dependent Claim 89 words
The process of claim 1, wherein said primary fuel is oil which is introduced into the combustion chamber in small axial jets, said oxidising gas being introduced with both axial and tangential components of motion to cause the oil to be atomised and the resultant mixture to swirl, said secondary fuel being gaseous and being introduced to the chamber adjacent to the wall thereof so that it forms a sheath around the total combustion zone, which sheath is in direct physical contact with the products of said combustion process.
Claim 8
Dependent Claim 51 words
The process of claim 4, wherein a major proportion of said oxidising gas is introduced into said chamber in a plurality of circumferentially spaced jets each at an angle of about 30° to the axis of the chamber, a minor proportion of said oxidising gas being introduced axially of the chamber.
Claim 9
Dependent Claim 100 words
The process of claim 1, wherein the primary and secondary fuels are gaseous, said primary fuel being introduced axially of said chamber, said oxidising gas is introduced with both axial and tangential components to cause the gaseous mixture to swirl and in quantities sufficient to cause stoichiometric burning of said primary fuel to CO 2 and H 2 O, said secondary fuel being gaseous and being introduced to the chamber adjacent to the wall thereof so that it forms a sheath around the total combustion zone, which sheath is in direct physical contact with the products of said combustion process.
Claim 10
Dependent Claim 51 words
The process of claim 6, wherein a major proportion of said oxidising gas is introduced into said chamber in a plurality of circumferentially spaced jets each at an angle of about 30° to the axis of the chamber, a minor proportion of said oxidising gas being introduced axially of the chamber.
Claim 11
Dependent Claim 123 words
The process of claim 1, wherein said primary fuel comprises a mixture of particulate solid fuel in a liquid carrier forming a slurry and a gaseous fuel, said primary fuel being introduced axially of said chamber, said oxidising gas being introduced with both axial and tangential components to cause the gas-like mixture of said primary fuel and oxidising gas to swirl and in quantities sufficient to cause stoichiometric burning of said solid and gaseous fuels to CO 2 and H 2 O, said secondary fuel being gaseous and being introduced to the chamber adjacent to the wall thereof so that it forms a sheath around the total combustion zone which sheath is in direct physical contact with the products of said combustion process.
Claim 12
Dependent Claim 23 words
The process of claim 8, wherein said mixture comprises 55% particulate coal and 45% water together with a small quantity of gaseous fuel.

References Cited (Backward Citations)

US2904417A Cited
US2398654A Cited
US2905544A Cited
US2898204A Cited
US3048476A Cited
US3669628A Cited
US3713588A Cited
US3955941A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-08-15 1981-02-14 1981-08-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-08-15 1985-02-14 1985-08-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-08-15 1989-02-14 1989-08-16 $7700.00 Window Closed / Lapsed

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