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
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-modified
1 . 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.

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