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US4067700A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for gasifying coal

Assignee: Gilbert Associates Inc
•
Filing: 1976-05-24
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Granted: 1978-01-10
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Expires: 1996-05-24
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Abstract

Abstract Apparatus and a method of comminuting coal to about 1 to 10 microns size comprising introducing the coal particles into a plurality of vessels, each of which is subjected to high pressure, superheated steam which infuses into the pores of said particles equalizing the pressure therein with that surrounding the particles in the vessel. By opening a discharge valve of each vessel connected to a nozzle leading into a housing, in which a paddle wheel is located, the particles will burst in each vessel to smaller size because of the reduction of the pressure therein surrounding the particles. Opening of said valve will effect acceleration, turbulence and collision of the particles to cause further breakage particularly as the particles are further expanded through the nozzle and against the blades of the paddle wheel driven in a direction opposite that of the nozzle jets. The vessel may be operated under partial vacuum by connection to a steam condenser through which cooling water flows. The communited coal is heated to produce gases and submicron char.

Inventors

  • 👤 George W. Switzer

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 03:16
CPC Classifications
C; C21; C21B; C21B5/00; C21B5/001; C21B5/003; B; B02; B02C; B02C19/00; B02C19/0012; C10; C10J; C10J3/00; C10J3/46; C10J3/466; C10J3/48; C10J3/50; C10J3/506; C10J3/72; C10J3/78; C10J2300/00; C10J2300/09; C10J2300/0903; C10J2300/0906; C10J2300/0913; C10J2300/093; C10J2300/0953; C10J2300/0973; C10J2300/0979; C10J2300/18; C10J2300/1861; C10J2300/1884; C10J2300/1892; Y; Y10; Y10S; Y10S48/00; Y10S48/04

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 257 words
The method of gasifying porous particles of coal of ultra-fine size of the order of about 1 to 10 microns, comprising introducing said particles into a vessel, subjecting the interior of the vessel to high pressure superheated steam which infuses into the pores of said particles and equalizes the pressure in the pores with that surrounding the particles within said vessel, suddenly reducing the pressure surrounding said particles in said vessel so as to effect higher pressure in the pores than in the vessel space surrounding said particles, resulting in bursting of the particles, and expanding said steam by opening a discharge outlet of said vessel to effect acceleration, turbulence and collision of said particles causing further breakage of said particles and further expanding broken particles in said discharge outlet through nozzle means leading to the interior of a housing against the blades of a paddle wheel driven therein but in a direction opposite to that in which said wheel is driven so as to effect further breakage of said particles from expansion and collision through said nozzle means as well as further breakage from collision with the blades of said paddle wheel to provide particles of ultra fine size which are discharged from said housing into a separator from which the broken particles are discharged and cooling said particles, after said further breakage, and introducing them through a nozzle into a heated reactor so as to burst to submicron size, and filtering the resulting gaseous products to produce separate sources of hydrocarbon gas and submicron char.
Claim 2
Independent Claim 257 words
The method of gasifying porous particles of coal of ultra-fine size of the order of about 1 to 10 microns, comprising introducing said particles into a vessel, subjecting the interior of the vessel to high pressure superheated steam which infuses into the pores of said particles and equalizes the pressure in the pores with that surrounding the particles within said vessel, suddenly reducing the pressure surrounding said particles in said vessel so as to effect higher pressure in the pores than in the vessel space surrounding said particles, resulting in bursting of the particles, and expanding said steam by opening a discharge outlet of said vessel to effect acceleration, turbulence and collision of said particles causing further breakage of said particles and further expanding broken particles in said discharge outlet through nozzle means leading to the interior of a housing against the blades of a paddle wheel driven therein but in a direction opposite to that in which said wheel is driven so as to effect further breakage of said particles from expansion and collision through said nozzle means as well as further breakage from collision with the blades of said paddle wheel to provide particles of ultra fine size which are discharged from said housing into a separator from which the broken particles are discharged and cooling said particles, after said further breakage, and introducing them through a nozzle into a heated reactor so as to burst to submicron size, and filtering the resulting gaseous products to produce separate sources of hydrocarbon gas and submicron char.
Claim 3
Dependent Claim 30 words
The method recited in claim 1 wherein said filtered hydrocarbon gas and submicron char are passed through a mixer to form a fuel suspension suitable as a source of fuel.

References Cited (Backward Citations)

US1781614A Cited
CH216476A Cited
US2515542A Cited
US3688991A Cited
US3852048A Cited
US3854896A Cited
US3973733A Cited
US3989477A Cited
US3991557A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-01-09 1981-07-11 1982-01-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-01-09 1985-07-11 1986-01-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-01-09 1989-07-11 1990-01-10 $7700.00 Window Closed / Lapsed

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