Abstract:
A method for processing waste material into fuel or other useful substances without polluting the air comprising the steps of: a. Introducing waste material into a storage chamber which allows the liquid to drain into a tank, b. Moving the waste to a storage chamber where it is burned, c. Moving the emissions and dust to a cleaning and burning chamber where they are further condensed, Or a. Pasteurizing sludge and raw sewage and using the gases produced for heat energy, b. Forming a solid of the liquid substances by adding ground corn and/or millet to them and using the solid for fuel.

Description:
FIELD OF INVENTION  
       [0001]     The present invention relates to an apparatus and process for the incineration and/or condensing of municipal waste.  
       SUMMARY  
       [0002]     The condenser is an incinerator technology made up of three different units; while every unit performs different duties, they complement one another. Each unit has more than one chamber that it operates.  
         [0003]     The technology performs the following four duties: 
        1. Turns vapor substances (emissions), such as, nitrogen, sulfur oxide, carbon monoxide, carbon dioxide, sodium sulfite, dust and any other vaporous substance into a liquid state;     2. Turns liquid substances into a solid compound;     3. Turns these compounds into energy producing fuel; and     4. Turns municipal waste into ashes, which are subsequently converted into liquid waste.       
 
     
    
     DESCRIPTION OF THE DRAWINGS  
       [0008]     FIG. I shows the municipal waste processing unit.  
         [0009]     FIG. II shows the emission condenser unit.  
         [0010]     FIG. III shows the raw sewage and chemical waste-processing unit. 
     
    
     DETAILED DESCRIPTION OF THE INVENTION  
       [heading-0011]     Description of FIG. I  
         [0012]     FIG. I shows the municipal waste-processing unit made up of six (6) primary chambers and sixteen (16) secondary chambers. All secondary chambers are designed to complement the six primary chambers. The storage chamber  10  is for the collection of municipal waste. The leachate water tank  11  is for the municipal waste drain off. The legs  12  are the chamber stands.  13  is the automatically controlled electronic door and  14  is the waste transit escalator. The hydraulic chamber automatic door lock is shown as  15 .  16  denotes the municipal waste condenser (burner) chamber. The chamber cleaner and waste level gage  17  is connected to the gas entrance line.  19 A is the air pressure in-let used to ignite fire while  19 B is the air-cooling entrance. (Its functions may not be necessary.) The hydraulic door lock  20  prevents ashes, air pressure, gases and dust that is in chamber  16  from entering chamber  26  and chamber  25  during condensation initiation. The floor of chamber  16  is labeled  21  and it is made of heat conductors.  22  is the residue and air pressure passage way with an automatically, electronically controlled door lock at the end of it. The lock prevents air pressure, ashes and dust from entering chamber  26  and forcing them into chamber  25 . The air vacuum pipe is  23 A and  23 C and  23 D are leachate water pump lines. The water-cooling tank for chamber  16  is  24 . The ash and dust residing chamber is  25 . The filtration chamber  26  filters the air and emissions before they enter the unit of  FIG. 1I . The vacuum machine is  30  and the air filter is number  31 . The air compressor tank is  33 , while the gas line is  34 .  
         [heading-0013]     Description of FIG. II  
         [0014]     FIG. II units are the gas and dust control chambers. Their functions are to clean all emissions that enter the unit and condense them into a solid form, rather releasing them into the environment.  27 A is the emissions cleansing chamber operating at approximately 1,500 degrees Celsius. The emission in-let pumping machine is  27 B and AC is the pressure hold and release outlet.  28 A are the water boiler units and  28 B are the water cooler units. The air vacuums are labeled  23 B and  29 A are the filters.  32  is the escaped air tank.  33 ACB is the water sprinkler. The leachate water vacuum line is  23 C and the leachate water tank is  23 D.  
         [heading-0015]     Description of FIG. III  
         [0016]     The deposit, treatment and mixing chamber for raw sewage and chemical waste is Z 1 . Z 2  is the mixer. Z 3  are the chamber stands. The raw sewage-pumping machine is Z 4 , while the raw sewage deposit pipeline is Z 5 . Z 6  is the formation tank; Z 7  is the grease tank; and Z 8  is the droop mouth. The spray pipe is Z 9 . The raw sewage transport escalator wall is Z 10  and Z 11  is the raw sewage transport escalator. The raw sewage drying and burning chamber is Z 12  and it spins at 25 mph. Z 13  is a storage chamber.  
         [heading-0017]     Processing Description of FIG. I  
         [0018]     Chamber  10  is a storage chamber for municipal waste. During the condensation process, waste is moved from chamber  10  to chamber  16  by the escalator carrier. As the escalator moves, the hydraulic door opens automatically to allow waste to enter chamber  16 . When the waste in chamber  16  reaches the gage level, the escalator automatically turns off, allowing the control door to close seal off gases, dust, odor and air from escaping. Then gas is introduced into chamber  16  through the gas line and the ignition switch is turned on to ignite a fire spark. At the same time hot air pressure is introduced into chamber  16  through pipe holes  19 A. The hot air pressure helps the condensation in chamber  16 . It flushes ashes, emissions, and dust out of chamber  16  into the passageway  22  and finally, to chamber  25  where they reside before they are moved to a landfill or used for other purposes.  
         [0019]     Chamber  26  filters the emissions and dust before they enter the FIG. II unit. The emissions enter chamber  27 A, which is an emission gases, dust and leachate water cleansing and burning chamber; the substances are turned into a mixture of vapors before they are released to chamber  28 A for cleansing. The cleaned vapor is then released to chamber  28 B where it is condensed into a solid.  
         [heading-0020]     Processing Description of FIG. II  
         [0021]     FIG. II is the emissions, dust and leachate water cleansing and condensing unit. Its purpose is to collect emissions, dust and leachate water from FIG. I and FIG. III units. The substances are cleansed at a temperature of approximately 1500 degrees Celsius in chamber  27 A and released into chamber  28 A as vapor for further cleansing.  
         [0022]     Turning these substances into vapor and the final stage of cleaning is done by forcing the vapor to loop out of the boiling tank  27 A through the AC pressure holder into chamber  28 A. The water temperature in  28 A is 150 degrees Celsius and above. Chambers  28 B collect the vapor and freezes it into a solid form at a temperature of −150 degrees Celsius. Subsequently the solid is returned to a liquid state, filtered and the residue is pumped into FIG. III unit for condensation.  
         [heading-0023]     Processing Description of FIG. III  
         [0024]     FIG. III unit processes liquid substances that include that include water, ammonia, gasoline, alcohol, other solvents, thinners, methyl ethyl ketone, oil, and chemicals, such as, nitrogen oxide, anhydrous hydrogen chloride, sodium chlorate, hydrogen peroxide, sodium sulphite, and acid.  
         [0025]     In Z 1  chamber, sludge sewage and raw sewage are turned into a solid compound by the addition of ground corn and/or millet, which absorb the liquid. The reason for using two at the same time is because they complement each other and become more absorbent. There is no standard of measurement for use in this process and the measurement used can be based on the choice of how solid an individual wants the compound to be. The purpose for mixing the three substances into one solid compound is to avoid heavy dripping. The reason for grinding corn and millet before using them is because they absorb liquid substances faster. The compound from Z 1  is pumped into Z 6  chamber to go through the final condensation treatment, which involved adding more ground corn and/or millet and oil. The purpose of the oil is to prevent the compound from sticking to the chamber walls. Cooking oil is preferred.  
         [0026]     Energy is cultimated from energy producing substances in two different formats: 
        1. When raw sewage, sludge sewage, or animal manor are moved into chamber Z 1 , the chamber is heated and kept at a temperature of 380 deg. Celsius to 420 deg. Celsius to pasteurize the substances in the chamber, as a result, the substances produce gases. The gases are extracted through a pipeline to a gas storage tank to produce heat energy.     2. The second energy producing substance is the solid compound made from the liquid substances mixed with ground corn and millet; they become fuel to power electric generators. During the process of drying the substances one and a half tons of solid substances are produced for every two tons of wet substance. 10 tons of dried solid substances will produce one MW/hour of electricity, when used to produce electricity energy due to its calorific values.     3. The dried substances could be burned if not needed for energy producing fuel. One ton of ashes are produced for every twenty tons of the solid substance burned.