← Back to Patent Explorer
US5055724A Expired / Lapsed US ⏱️ 0.0 years remaining

Open-cycle magnetohydrodynamic power plant with CO2 recycling

Assignee: ENERGY United States, Department of
•
Filing: 1989-10-30
•
Granted: 1991-10-08
•
Expires: 2009-10-30
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A method of converting the chemical energy of fossil fuel to electrical and mechanical energy with a MHD generator. The fossil fuel is mixed with preheated oxygen and carbon dioxide and a conducting seed of potassium carbonate to form a combustive and electrically conductive mixture which is burned in a combustion chamber. The burned combustion mixture is passed through a MHD generator to generate electrical energy. The burned combustion mixture is passed through a diffuser to restore the mixture approximately to atmospheric pressure, leaving a spent combustion mixture which is used to heat oxygen from an air separation plant and recycled carbon dioxide for combustion in a high temperature oxygen preheater and for heating water/steam for producing superheated steam. Relatively pure carbon dioxide is separated from the spent combustion mixture for further purification or for exhaust, while the remainder of the carbon dioxide is recycled from the spent combustion mixture to a carbon dioxide purification plant for removal of water and any nitrous oxides present, leaving a greater than 98% pure carbon dioxide. A portion of the greater then 98% pure carbon dioxide stream is recovered and the remainder is recycled to combine with the oxygen for preheating and combination with the fossil fuel to form a combustion mixture.

Inventors

  • 👤 Gregory F. Berry

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 12:09
CPC Classifications
H; H02; H02K; H02K44/00; H02K44/08

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 209 words
A method of converting the chemical energy of fossil fuel to electrical and mechanical energy comprising: mixing the fossil fuel with preheated oxygen and carbon dioxide and a conducting seed of potassium carbonate to form a combustive and electrically conductive mixture, burning the combustive and electrically conducting mixture in a combustion chamber; passing the burned combustion mixture through a MHD generator to generate electrical energy; passing the burned combustion mixture through a diffuser to restore the mixture approximately to atmospheric pressure, leaving a spent combustion mixture; exchanging heat from the spent combustion mixture with oxygen from an air separation plant and recycled carbon dioxide for combustion in a high temperature oxygen preheater; removing relatively pure carbon dioxide from the spent combustion mixture for further purification or for exhaust; recycling the remainder of the carbon dioxide from the spent combustion mixture to a carbon dioxide purification plant for removal of water and any nitrous oxides present, leaving a greater than 98% pure carbon dioxide; recovering a portion of the greater than 98% pure carbon dioxide stream and recycling the remainder to combine with the oxygen for preheating and combination with the fossil fuel, recycling the preheated oxygen and the carbon dioxide and the fossil fuel to form a combustion mixture.
Claim 2
Independent Claim 209 words
A method of converting the chemical energy of fossil fuel to electrical and mechanical energy comprising: mixing the fossil fuel with preheated oxygen and carbon dioxide and a conducting seed of potassium carbonate to form a combustive and electrically conductive mixture, burning the combustive and electrically conducting mixture in a combustion chamber; passing the burned combustion mixture through a MHD generator to generate electrical energy; passing the burned combustion mixture through a diffuser to restore the mixture approximately to atmospheric pressure, leaving a spent combustion mixture; exchanging heat from the spent combustion mixture with oxygen from an air separation plant and recycled carbon dioxide for combustion in a high temperature oxygen preheater; removing relatively pure carbon dioxide from the spent combustion mixture for further purification or for exhaust; recycling the remainder of the carbon dioxide from the spent combustion mixture to a carbon dioxide purification plant for removal of water and any nitrous oxides present, leaving a greater than 98% pure carbon dioxide; recovering a portion of the greater than 98% pure carbon dioxide stream and recycling the remainder to combine with the oxygen for preheating and combination with the fossil fuel, recycling the preheated oxygen and the carbon dioxide and the fossil fuel to form a combustion mixture.
Claim 3
Dependent Claim 25 words
The method of claim 1, wherein the heat from the spent combustion mixture leaving the MHD diffuser is used to produce steam to produce power.
Claim 4
Dependent Claim 25 words
The method of claim 1, wherein substantially all of the CO 2 is recovered for resale to prevent exhausting the CO 2 to the atmosphere.
Claim 5
Dependent Claim 53 words
The method of claim 1, and further comprising removing potassium sulfate and ash from the spent combustion gases to a seed reprocess plant producing potassium carbonate, leaving ash and sulfur, and recycling potassium carbonate to combine with the preheated oxygen and the carbon dioxide and the fossil fuel to form a combustion mixture.
Claim 6
Dependent Claim 21 words
The method of claim 1, wherein the associated steam cycle equipment is small due to reduced lower volumetric flue gas rate.
Claim 7
Dependent Claim 18 words
The method of claim 1, wherein the off gas to the atmosphere is substantially free of nitrogen oxides.

References Cited (Backward Citations)

US3895243A Cited
US4107557A Cited
US4345173A Cited
US4718361A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1994-10-07 1995-04-08 1995-10-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1998-10-07 1999-04-08 1999-10-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2002-10-07 2003-04-08 2003-10-08 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag