← Back to Patent Explorer
US4047489A Expired / Lapsed US ⏱️ 0.0 years remaining

Integrated process for preparing and firing bagasse and the like for steam power generation

Assignee: John Zink Co LLC
•
Filing: 1976-01-07
•
Granted: 1977-09-13
•
Expires: 1996-01-07
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract An integrated method is disclosed for preparing and suspension firing of bagasse and the like as the primary fuel for steam power generation in a cane sugar refinery. The method comprises mixing wet bagasse with de-ashed hot flue gases of a steam boiler, thereby drying it; separating bagasse dried thereby from the drying flue gases, capturing substantially all suspended dust; sizing the dried bagasse; directing bagasse fines to temporary storage while grinding and resizing any oversize bagasse; metering out and pneumatically suspending the fines, providing a smooth-flowing fuel responsive to a burner fuel feed control means; combusting the suspended fuel in a scroll feed type burner firing the steam boiler; de-ashing the combustion effluent, and utilizing the resultant flue gases for drying wet bagasse. Alternatively, the wet bagasse may be dried partially by de-ashed hot flue gases and partially by a bagasse fired supplementary hot air dryer, thereby further improving boiler operation efficiency.

Inventors

  • 👤 Temple S. Voorheis
  • 👤 James H. White

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-24 23:14
CPC Classifications
F; F23; F23G; F23G7/00; F23G7/02; Y; Y02; Y02E; Y02E20/00; Y02E20/12

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 222 words
An integrated method for preparing and suspension firing bagasse and bagassillo as a primary fuel for heating and steam power generation in a sugar cane refinery which produces bagasse and bagassillo as a wet by-product which comprises the repetitive substantially continuous sequential steps of: mixing the wet by-product with de-ashed hot flue gases of a bagasse fired suspension burner, thereby driving it and reducing the temperature of the drying flue gases; separating the by-product dried thereby from the drying flue gases in a primary cyclone collector and directing the flue gases emitted from said primary cyclone collector through a secondary cyclone collector to capture substantially all suspended particulate material preventing its exhaustion into the atmosphere; thereafter sizing the dried by-product, directing by-product fines up to a maximum pre-selected size to temporary substantially enclosed storage while regrinding and resizing oversized by-product; thereafter metering out, spacing and pneumatically suspending the by-product fines, for providing a smooth-flowing suspended fuel-air mixture; thereafter controllably firing the suspended mixture in a suspension type furnace burner to produce a relatively high temperature heat output and a combustion effluent characterized by substantially complete combustion; thereafter directing the combustion effluent through a cyclone collector to extract substantially all ash from the hot flue gases of the burner; and thereafter utilizing the resultant flue gases for subsequent drying of further wet by-product.
Claim 2
Dependent Claim 222 words
An integrated method for preparing and suspension firing bagasse and bagassillo as a primary fuel for heating and steam power generation in a sugar cane refinery which produces bagasse and bagassillo as a wet by-product which comprises the repetitive substantially continuous sequential steps of: mixing the wet by-product with de-ashed hot flue gases of a bagasse fired suspension burner, thereby driving it and reducing the temperature of the drying flue gases; separating the by-product dried thereby from the drying flue gases in a primary cyclone collector and directing the flue gases emitted from said primary cyclone collector through a secondary cyclone collector to capture substantially all suspended particulate material preventing its exhaustion into the atmosphere; thereafter sizing the dried by-product, directing by-product fines up to a maximum pre-selected size to temporary substantially enclosed storage while regrinding and resizing oversized by-product; thereafter metering out, spacing and pneumatically suspending the by-product fines, for providing a smooth-flowing suspended fuel-air mixture; thereafter controllably firing the suspended mixture in a suspension type furnace burner to produce a relatively high temperature heat output and a combustion effluent characterized by substantially complete combustion; thereafter directing the combustion effluent through a cyclone collector to extract substantially all ash from the hot flue gases of the burner; and thereafter utilizing the resultant flue gases for subsequent drying of further wet by-product.
Claim 3
Dependent Claim 35 words
A method according to claim 1 wherein said de-ashed hot flue gases in excess of a temperature of approximately 610° F. dry said wet by-product to a moisture content of between approximately 15% and 25%.
Claim 4
Dependent Claim 20 words
A method according to claim 2 wherein the dried by-product is sized to a maximum of approximately 12 mesh (ASTM).
Claim 5
Dependent Claim 26 words
A method according to claim 1 further including the step of suspension firing said dried by-product in a scroll feed type burner firing a steam boiler.
Claim 6
Dependent Claim 20 words
A method according to claim 4 wherein said wet by-product is partially dried by a dried by-product fired air heater.
Claim 7
Dependent Claim 30 words
A method according to claim 4 wherein the stored fines are metered out through an arch breaking means, is spaced by a shaker table and pneumatically suspended by a fan.
Claim 8
Dependent Claim 26 words
A method according to claim 6 wherein said suspended fines are provided in a smooth flowing fuel mixture responsive to a burner fuel feed control signal.

References Cited (Backward Citations)

US1817228A Cited
US2148981A Cited
US3387574A Cited
US3734036A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-09-12 1981-03-14 1981-09-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-09-12 1985-03-14 1985-09-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-09-12 1989-03-14 1989-09-13 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag