Patent US2788798A successfully refreshed from Google Patents.
Patent US3953180A successfully refreshed from Google Patents.
US3953180A
Expired / Lapsed
US
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Production of low BTU sulfur-free gas from residual oil
Assignee: HRI Inc
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Filing: 1974-07-11
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Granted: 1976-04-27
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Expires: 1994-07-11
Abstract
Abstract An effective and economical supply of energy from residual oil for power generation can be obtained by a sequential process of partial combustion of a crude or residual oil such as Bunker C and other high sulfur stocks, in the presence of air and steam in a fluidized bed of inert particles followed by a fluidized bed heat exchange for the production of steam and control of solids build-up, the solids-free gas being desulfurized by commerical processes and thence being available for combustion for gas turbine operation to produce transportable electrical power or other types of mechanical power such as a compressor driver. Emission levels of contaminants are within forseeable requirements and turbine maintenance problems are reduced. Coal solids can be used as a supplement to the residual oil. Alternatively, the low BTU gas can be effectively added to pipeline gas as a supplementary source of energy when dilution of high-Btu gas is permitted or used directly as a low-Btu desulfurized industrial fuel.
Inventors
- 👤 Franklin D. Hoffert
- 👤 Harold H. Stotler
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 15:47
CPC Classifications
F; F02; F02C; F02C3/00; F02C3/20; C; C10; C10G; C10G47/00; C10G47/24; C10G47/30; F02C3/205; F05; F05D; F05D2200/00; F05D2200/20; F05D2200/26; F05D2200/262; Y; Y02; Y02T; Y02T50/00; Y02T50/60
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
207 words
The method of producing a low BTU heating value combustible gas of substantially sulfur free character at relatively high pressure and temperature from a sulfur containing low grade oil of the class of crude and residual oil which comprises: a. injecting said oil, steam, and air into a first bed of inert particulate matter under conditions to establish fluidization of the particulate matter and under a hydrogen partial pressure such that the oil is gasified and the bulk of the sulfur is converted to hydrogen sulfide with minimal amounts of carbonyl sulfide, the temperature in the bed being in the order of 1600°-2000°F., and the pressure being in the range of 200 to 400 psig; b. passing the resulting gases and vapors upwardly through a second bed of inert particulate matter in indirect heat exchanger with a cooling material to reduce the bed temperature to a range of 500° to 1000° F. to accomplish a concentration of ultra fine solid contaminants; c. removing said concentrated solid contaminants; d. cooling and desulfurizing the effluent gases from the second bed; and e. reheating said desulfurized gas, said reheated gas being product gas having a calorific value of under 350 BTU/SCF/(dry) and a sulfur content of less than 0.3 wt.%.
Claim 2
Independent Claim
207 words
The method of producing a low BTU heating value combustible gas of substantially sulfur free character at relatively high pressure and temperature from a sulfur containing low grade oil of the class of crude and residual oil which comprises: a. injecting said oil, steam, and air into a first bed of inert particulate matter under conditions to establish fluidization of the particulate matter and under a hydrogen partial pressure such that the oil is gasified and the bulk of the sulfur is converted to hydrogen sulfide with minimal amounts of carbonyl sulfide, the temperature in the bed being in the order of 1600°-2000°F., and the pressure being in the range of 200 to 400 psig; b. passing the resulting gases and vapors upwardly through a second bed of inert particulate matter in indirect heat exchanger with a cooling material to reduce the bed temperature to a range of 500° to 1000° F. to accomplish a concentration of ultra fine solid contaminants; c. removing said concentrated solid contaminants; d. cooling and desulfurizing the effluent gases from the second bed; and e. reheating said desulfurized gas, said reheated gas being product gas having a calorific value of under 350 BTU/SCF/(dry) and a sulfur content of less than 0.3 wt.%.
Claim 3
Dependent Claim
22 words
The method of claim 1 wherein the cooled gases are filtered of large particles and then scrubbed with water in countercurrent flow.
Claim 4
Dependent Claim
28 words
The method of claim 2 wherein the contaminated scrub water is depressurized and steam treated to remove sulfur compounds and the sulfur compounds are oxidized to recover sulfur.
Claim 5
Dependent Claim
28 words
The method of claim 1 wherein the heat exchange step in the second bed cools the bed to trap carbon particles therein and generate steam from feed water.
Claim 6
Dependent Claim
21 words
The method of claim 1 wherein the heat exchange step in the second bed reheats the desulfurized gas in step (e).
Claim 7
Dependent Claim
14 words
The method of claim 1 wherein the particulate matter in step (a) is sand.
Claim 8
Dependent Claim
15 words
The method of claim 1 wherein the particulate matter in step (a) is activated alumina.
Claim 9
Dependent Claim
20 words
The method of claim 1 wherein the oil is mixed with a solid fossil fuel from the class of coal.
Claim 10
Dependent Claim
26 words
The method of claim 8 wherein a stream of solid particles are continuously withdrawn from the upper bed and elutriated to separate carbon fines from ash.
Claim 11
Dependent Claim
17 words
The method of claim 8 wherein the coal to oil feed ratio is between 1.5:1 and 10:1.
Claim 12
Dependent Claim
38 words
The method of claim 1 wherein the desulfurized product gas is burned in the presence of air for the operation of a gas turbine to provide shaft power with an overall heat utilization of in excess of 83%.
Claim 13
Dependent Claim
37 words
The method of claim 11 wherein moderate pressure excess air not used for combustion is cooled by condensate injection then recompressed and injected into the first bed of particulate matter for supply of further compressed air thereto.
References Cited (Backward Citations)
GB665781A
Cited
US3177631A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-04-27 | 1979-10-27 | 1980-04-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-04-27 | 1983-10-27 | 1984-04-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-04-27 | 1987-10-27 | 1988-04-27 | $7700.00 | Window Closed / Lapsed |