US2008178784A1PendingUtilityA1
Simultaneous Production of Electricity and Liquid Fuels from Municipal Solid Wastes
Individually held — no corporate assignee on recordPriority: Jan 29, 2007Filed: Jan 28, 2008Published: Jul 31, 2008
Est. expiryJan 29, 2027(~0.5 yrs left)· nominal 20-yr term from priority
Inventors:William A. Farone
F23G 2201/40C10J 3/00C10J 2300/0956C10J 2300/0903F23G 2206/203C10J 2300/1807C07C 29/1518C10J 2300/1671B01J 27/232C10J 2300/0946Y02E20/12F23G 2206/10C10J 2300/1884F23G 5/46F23G 5/027C10J 2300/165F23G 2201/303C10J 2300/1687Y02P20/52C10J 2300/0973Y02E50/30C10J 2300/1869C10J 2300/1665B01J 23/8872
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Claims
Abstract
An energy self sufficient process for treatment of municipal solid waste includes the production of mixed alcohols. The process also includes gasification of the solid waste producing a gas that can provide either or both electricity and heat to further power the process.
Claims
exact text as granted — not AI-modified1 . An energy self sufficient process for the production of mixed alcohols from components of municipal solid waste, which comprises:
gasifying combustible portions of municipal solid waste producing a synthesis gas having CO and hydrogen at temperature at around or above 700° C.; sending portion of said synthesis gas to a boiler or a turbine wherein excess electricity and heat produced operates process equipment; sending remainder of said synthesis gas to a gas conditioning system reducing temperature and increasing the pressure of said synthesis gas; sending the synthesis gas from said gas conditioning system to a catalytic conversion system producing said mixed alcohols; sending unconverted (excess/unused/unneeded) synthesis gas back to said boiler or said turbine; condensing product fluid from said catalytic conversion system; and separating said mixed alcohols from hydrocarbons and other combustible liquids wherein waste liquids from condensing step are regasified.
2 . The process of claim 1 further comprising maintaining supercritical pressure for the synthesis gas reaction mixture within the catalytic conversion system.
3 . The process of claim 1 further comprising maintaining supercritical temperature for the synthesis gas reaction mixture within the catalytic conversion system.
4 . The process of claim 2 further comprising:
monitoring the gas and liquid compositions from the catalytic reactor; and adjusting the pressure to maintain a supercritical state.
5 . The process of claim 3 comprising:
monitoring the gas and liquid compositions from the catalytic reactor; and adjusting the temperature to maintain a supercritical state.
6 . An energy self sufficient process for the production of mixed alcohols and pipeline quality natural gas from components of municipal solid waste, which comprises: gasifying combustible portions of municipal solid waste producing a synthesis gas having methane, lower hydrocarbons, CO and hydrogen at temperature at around or above 700° C.;
sending the synthesis gas from said gas conditioning system to a catalytic conversion system producing said mixed alcohols; sending residual from alcohol producing unit to a gas conditioning system to produce pipeline quality gas; and condensing product fluid from said catalytic conversion system.
7 . The process of claim 6 further comprising maintaining supercritical pressure for the synthesis gas reaction mixture within the catalytic conversion system.
8 . The process of claim 6 further comprising maintaining supercritical temperature for the synthesis gas reaction mixture within the catalytic conversion system.
9 . The process of claim 7 further comprising:
monitoring the gas and liquid compositions from the catalytic reactor; and adjusting the pressure to maintain a supercritical state.
10 . The process of claim 8 comprising:
monitoring the gas and liquid compositions from the catalytic reactor; and adjusting the temperature to maintain a supercritical state.Join the waitlist — get patent alerts
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