Patent Document

BACKGROUND OF THE INVENTION  
       [0001]     This invention relates generally to the problems associated with waste in animal confinements, and more specifically, to methods and systems for converting the resulting high concentrations of animal waste into useful energy.  
         [0002]     Animals have been raised for centuries for food. Previously animals grazed in fields or pens, and were at times confined to buildings for shelter. However, current state of the art animal production for swine, cattle, and other animals, includes housing large numbers of such animals in high concentration within confined buildings, and delivering food to the animals. This method of animal production has benefited consumers of meat by lowering food prices through increased efficiency. A drawback to the current methods of animal production includes the resulting high concentration of wastes that have to be removed from the buildings and disposed of in a safe manner.  
         [0003]     Typically, the waste is removed from animal confinement buildings and deposited into large lagoons. Once within these lagoons, which can be multi-acre in size, the waste decomposes. The solid and liquid wastes in the lagoons cause an odor problem for the surrounding area, both as it decomposes in the lagoon, and during field application as a fertilizer as further described.  
         [0004]     After partially decomposing, the waste from the lagoons is applied to land (e.g. fields where crop are grown) as a fertilizer. The potential for environmental contamination during field application of the waste is substantial and many fields in pork producing states have been over fertilized. In addition, some of the applied fertilizer can become windborne during application and is therefore a source of environmental contamination for adjacent areas.  
         [0005]     There are also additional weaknesses with waste lagoon technology, specifically, collapsed walls and ground leaching, both of which can contribute to waterway and well contamination. In a recent EPA report, 60% of the US streams identified as “impaired” were polluted by animal wastewater. Animal wastewater management has become a high priority for the EPA.  
         [0006]     Still another problem with current animal production methods is that air cycled through the confinement buildings to keep the animals cool is blown into the atmosphere through the fans at the end of these confinement buildings. This is another source of airborne waste in addition to the fertilizer application problems described above. Another problem caused in part by the airborne waste is an increased susceptibility to respiratory and other health problems in farm workers. Legislative pressures have forced at least one state to impose a moratorium on new swine confinements, and other states are predicted to follow.  
         [0007]     There have been numerous attempts to improve the current state of the art in animal production, but most of these attempts still include drawbacks. For example, some still require a waste lagoon. Another system uses an inclined belt to concentrate solids percentage of waste, but does not eliminate or gain beneficial results from the solid waste. Other systems are known in which the wastes are eliminated by burning, but the burning of such wastes is not utilized to provide a beneficial result. Other systems treat waste through chemicals, but the waste is returned to the environment as a dried sludge. Additionally, anaerobic digestion systems exist.  
         [0008]     There are additionally several energy conversion processes known but these systems do not describe any methods for getting the waste to the conversion system, nor the overall process of handling the animal waste.  
       BRIEF DESCRIPTION OF THE INVENTION  
       [0009]     In one aspect, a method for receiving animal waste from animal confinements or other concentrated animal waste sources and converting the waste into a usable form is provided. The waste contains liquids and solids and the method comprises separating the liquids and solids into separate waste streams and controlling an amount of moisture in the solids waste stream such that the amount of moisture in the solid waste stream is compatible with a selected energy conversion process. The method further comprises feeding the moisture controlled solid waste into the energy conversion process.  
         [0010]     In another aspect, a system for processing a waste stream from animal production confinements and other sources of concentrated wastes is provided. The system comprises a solids/liquids separator receiving the waste stream and configured to separate the waste stream into a solid waste stream and a liquid waste stream and a water treatment apparatus for treating the liquid waste stream. The system further comprises a control system for controlling an amount of moisture in the solid waste stream, an energy conversion processor receiving the moisture controlled solid waste stream and converting the solid waste stream into an energy source, and a power generator configured to utilize the energy source. 
     
    
     BRIEF DESCRIPTION OF THE DRAWINGS  
       [0011]      FIG. 1  is an overall conversion process diagram of a system for converting a waste stream into a fuel source, including a solids/liquids separator.  
         [0012]      FIG. 2  is a block diagram of a portion of the system of  FIG. 1 , including an embodiment of a solids/liquids separator for a waste stream including a high solids concentration.  
         [0013]      FIG. 3  is a block diagram of a portion of the system of  FIG. 1 , including an embodiment of a solids/liquids separator for a waste stream including a low solids concentration.  
         [0014]      FIG. 4  is a block diagram of a portion of the system of  FIG. 1 , illustrating an embodiment having multiple mechanical solids/liquids separators.  
         [0015]      FIG. 5  is a block diagram of a portion of the system of  FIG. 1 , illustrating an embodiment having multiple gravity solids/liquids separators.  
         [0016]      FIG. 6  is a block diagram of a portion of the system of  FIG. 1 , illustrating an embodiment of a heat and gas recovery sub-system.  
         [0017]      FIG. 7  is a block diagram of a portion of the system of  FIG. 1 , illustrating an embodiment having multiple gravity solids/liquids separators routed to a mechanical separator.  
         [0018]      FIG. 8  is a block diagram of one embodiment of an energy conversion processor. 
     
    
     DETAILED DESCRIPTION OF THE INVENTION  
       [0019]     The systems herein described provide methods for handling raw animal waste and converting the waste into fuel, which may then be used for heat, transportation, or preferably direct conversion to power through a generator driven by an engine or combustion turbine.  
         [0020]     Referring to  FIG. 1 , animal confinement  10  includes a manure collection area  12  for the collection of wastes and flushing water. The wastes and flushing water are transported to solid/liquid separator  14  utilizing a transporting mechanism  16 . In one embodiment, transporting mechanism  16  operates by gravity, but other embodiments of transporting mechanism  16  exist which may also use pumps and/or conveyors in addition to or instead of gravity to transport animal waste and other accompanying materials. As used herein, the term “transport” is utilized to describe methods for moving mass from one location to another, including, but not limited to, pumping, gravity, auger, conveyor, and the like.  
         [0021]     In a specific embodiment, a positive displacement pump designed for high solids contents is utilized for transporting animal waste from collection area  12  to solid/liquid separator  14 . One positive displacement pump is a grinding pump, one example of which is a Moyno L-Frame progressing cavity pump.  
         [0022]     Solid/liquid separator  14  may include one or more mechanical and gravity separators which are further described below. A gravity separator is sometimes referred to as a settling tank. In one embodiment, solid/liquid separator  14  is utilized to deliver volatile solids from the waste, which have a significant BTU content for use as fuel, to an energy conversion processor  20 . As further described below, the solid wastes are delivered to energy conversion processor  20  within a specified range of moisture content.  
         [0023]     The animal waste exiting manure collection area  12  is typically about 97% to about 99.5% liquid. This is a result of manure by nature being very wet. Additional moisture is added due to urine and the water used to flush the animal waste from confinement  10 . Small additional amounts of water are contributed to the animal waste by sloppy drinking and animal cleaning. Hog manure, for example, is typically about 80%-90% liquid by weight.  
         [0024]     Each embodiment of energy conversion processor  20  has a range for the moisture content of the solid waste being converted that enables proper conversion of the solid waste. For example, the well-known gasification process typically requires a relatively dry feedstock, for example, a fuel with about a 20% to about a 30% moisture level. By contrast, other conversion processes such as liquification or pyrolysis allow much wetter feedstock streams, up to about an 80% moisture level.  
         [0025]     As described above, the animal waste is transported into energy conversion processor, which may use pyrolysis, gasification, or one of a number of related conversion processes that utilize controlled temperature, pressure, and time to convert the waste into a one of a fuel gas, an oil, a solid, or a combination thereof. The converted animal waste is referred to herein as “fuel”.  
         [0026]     From energy conversion processor  20 , the fuel is filtered and processed by filter processor  22  as necessary for usage. In one embodiment, the system includes one or more optional fuel storage tanks  24 , or buffer tank(s). The fuel is then converted into electricity through a known device such as an engine or turbine-driven generator  26 .  
         [0027]     In the embodiment illustrated, a second power generator  28  is illustrated. In many locations, electrical power is more valuable during “peak demand” periods. One feature of the system illustrated is that power generator  26  is utilized to supply a certain quantity of power, while second power generator  28  supplies another quantity. Power generator  26  and second power generator  28  may provide equal power or may provide different power amounts (i.e., be differently sized). In a particular embodiment, power generator  26  supplies electricity and engine heat sufficient to keep the processes of the illustrated system continuously running except for maintenance. Second power generator  28  is turned on when power demand is at a peak. In a specific embodiment, power generator  26  is a Kohler 150REOZV and second power generator  28  is a Kohler 500REOZV.  
         [0028]     Operation of second power generator  28 , in one embodiment, is controlled by a controller  30 , which includes a timer (not shown), operating in conjunction with a level controller  32 , having a sensor input  34 . Controller  30  may also be controlled remotely by a remote signal  36  from a utility or an operator of the energy conversion system illustrated. This operation enables the energy conversion system to meet electrical load demand and also maximize economic benefit to the system&#39;s owner. Such operation provides benefits to the public and the electrical grid operators by reducing loading on transmission lines, by providing demand-based distributed generation. Additionally, fuel production will vary due to fluctuations in manure production and other factors. The twin power generator arrangement provides a solution for the fluctuations in fuel supply while allowing generators to run at peak efficiency.  
         [0029]     There is typically wastewater generated by the energy conversion system in the conversion process, either within energy conversion processor  20  or in filter/processor  22 . This wastewater is transported, by pump and/or gravity, to a water treatment apparatus  40 , which removes any remaining entrained solids, liquids and gases to levels approved by the applicable authorities. Water from water treatment apparatus  40  is either discharged to water bodies, or used for crop irrigation, or any number of other useful purposes that displace water currently taken from ground sources and/or water bodies.  
         [0030]     In a particular embodiment, the water is transported back to confinement  10  for a variety of purposes. As illustrated in  FIG. 1 , a holding tank  42  has a level control valve  44  that allows holding tank  42  to fill as needed. A control valve and/or pump  46  transmits the water through a flush line  48  into manure pit  12  as needed in order to provide the flushing water needed to clean manure out of confinement  10 .  
         [0031]     In one embodiment, water is also be pumped to devices which filter the air exiting confinement  10  via ventilation system  50 . An example of such a device is an air scrubber  52  as described in U.S. Pat. No. 6,059,865. Water washes down an inclined plate (not shown) of air scrubber  52 , as ventilation fans blow against the inclined plate. Odor containing particles and gases are captured within the water stream. This water is shown as being returned to holding tank  42 . The water can alternately be returned to water treatment apparatus  40  or utilized directly for flushing of manure pit  12 .  
         [0032]      FIG. 2  illustrates one embodiment of solid/liquid separator  14  (shown in  FIG. 1 ). Certain energy conversion processes utilize a low moisture level, for example, gasification. In such energy conversion processes, solid/liquid separator  14  may include one or more mechanical separators  60 . Individual mechanical separators  60  may be a type of press (e.g., a belt press), an auger, a conveyor, a centrifuge, a hydrocyclone, a screen separator, or another type of mechanical separator, alone, or in conjunction with one or more other mechanical separators that work in conjunction to remove substantially all of the useful volatile solids from the waste. At least some known mechanical separation equipment leaves much of the useful volatile solids in the wastewater.  
         [0033]     In the embodiment of solid/liquid separator  14  illustrated in  FIG. 2 , any solids retained in the waste are forwarded from mechanical separator  60  to settling tank  62 , either by gravity and/or by pumping. Some examples of mechanical separator  60  are the KCS&amp;C 48×30 Centrifuge, or Vincent KP-6L Screw Press. Settling tank  62  allows the retained solids to gravitate toward a bottom  64  of a fixed tank, while the liquid portion is forwarded for water treatment  66 . In additional embodiments, settling tank  62  may include more than one settling tank in series or parallel. The solids that gravitate toward bottom  64  of settling tank  62  are transported back to mechanical separator  60 , either directly, or to a buffer tank  68 , as illustrated in  FIG. 2 .  
         [0034]     The solids stream from mechanical separator  60  are forwarded, in one embodiment, to a shredder  70 . A shredder  70  may not be needed for some animal waste streams, and its function may be replaced by a standard pump or a grinding pump. The waste is then transported, either by pump or gravity, to a dryer  72 . In the embodiment shown in  FIG. 2 , dryer  72  is a helical auger in which heat and/or air is added to the unit, lowering the moisture content of the waste to meet the operating conditions of energy conversion processor  20 . In the embodiment shown, moisture content of the waste is controlled by a moisture sensor  74  that monitors the amount of heat and airflow entering dryer  72 . Moisture sensor  74  provides an analog or digital signal to the moisture controller (MIC)  76 . Moisture controller  76  is configured to vary a process variable to control the moisture level of the waste within pre-defined limitations for use by energy conversion processor  20 . A particular embodiment utilizes an Omega CDCE-90-1 moisture sensor, and an Omega CDCN-90 moisture controller. In this embodiment, moisture sensor  74  provides a proportional signal to moisture controller  76 . An output of moisture controller  76  is utilized to control devices affecting the moisture percentage of the waste.  
         [0035]     In particular embodiments, if moisture sensor  74  indicates that the moisture percentage is too high to be processed properly by energy conversion processor  20 , then a hot air flow that is applied to the waste stream entering energy conversion processor  20  is increased. The hot air may be generated utilizing a variety of methods and one exemplary embodiment is illustrated in  FIG. 2 , where a coolant  80  from a power generator  82  is passed through a heat exchanger  84 , where heat is transferred to the incoming air in order to raise its temperature, which increases its capacity to remove moisture from the process stream. A variable speed blower  86  has a variable frequency drive or other modulating device such as a mechanical damper, that is controlled by the signal output by moisture controller  76 . In a specific embodiment, heat exchanger  84  is a pipe-in-pipe heat exchanger manufactured by a variety of other manufacturers and blower  86  is manufactured by the New York Blower Company.  
         [0036]     In other embodiments, drying methods include raising the temperature of the waste through electric or fuel fired heaters or heat exchanged from other higher temperature areas of the process via fluid, gas or steam heat exchange media. Alternately, gases from engine exhaust of power generator  82  or energy conversion processor  20  can be utilized directly, similarly to the hot air embodiment above described.  
         [0037]     In one embodiment, dryer  72  includes a perforated top screen (not shown) which allows the warmed moist air to escape. In other embodiments, the airflow is constant, but the amount of heat is varied, for example by a three-way valve modulating the amount of hot engine fluid (e.g., coolant  80 ) delivered to heat exchanger  84 . Alternately other process variables such as rotation speed of dryer  72  or temperature of heating media may be controlled to obtain the same effect. Other heat sources may be used, such as engine exhaust from power generator  82 , heat from energy conversion processor  20 , heat from the process stream  88  after energy conversion processor  20 , solar-heated thermal fluid, or heat from a separate combustion process, such as burning paraffins separated from the resultant fuel.  
         [0038]      FIG. 3  illustrates an alternate embodiment where energy conversion processor  20  is configured to utilize or allow higher moisture content feedstock (e.g., animal waste streams). In this embodiment, a portion of the solids stream from settling tank  62  is delivered to the line which contains the solid portion from mechanical separator  60 . The amount of this stream from settling tank  62  is controlled by moisture controller (MIC)  76 , based on an input from moisture sensor  74  or a similar instrumentation means. Alternately the amount of solids from settling tank  62  is controlled by simple experimental manual balancing. In the embodiment illustrated a three way control valve  100  and moisture sensor  74  are used to control the amount of solids from settling tank  62  into the waste stream. Alternatively one or more two-way control valves or solenoid operated valves may be utilized.  
         [0039]     The waste stream is exposed to heat from heat exchanger  84  before entry into energy conversion processor  20 . The heat for heat exchanger  74  may be provided from a variety of sources. In a specific embodiment, heat may be provided to heat exchanger  84  from a power generator (shown in  FIG. 1 ) from one or more of exhaust and engine cooling water. The waste stream in effect replaces the engine&#39;s radiator, in part or in whole. Additional heat sources may be used such as solar thermal, electric heat run by the unit&#39;s generator or other power source, or direct firing of a portion of the fuel, or waste fractions of the fuel. The heated waste is then transported to energy conversion processor  20  and processed as described with respect to  FIG. 1 .  
         [0040]      FIG. 4  illustrates an alternate embodiment of a solids/liquids separator  110  for energy conversion system which increases efficiency of separation between solids and liquids in the waste stream. In addition to mechanical separator  60 , a second mechanical separator  112  is included. Mechanical separator  60  and second mechanical separator  112  may be of the same type of construction, but in a specific embodiment, mechanical separator  60  is a highly energy efficient type separator, for example, a press, while second mechanical separator  100  is a more energy intensive separator, such as a centrifuge. In the embodiment, second mechanical separator  112  processes less mass flow than does mechanical separator  60  thereby raising overall efficiency of the energy conversion system. Specifically, mechanical separator  60  directs the high-solids fraction of the waste towards energy conversion processor  20 , while a high-liquids fraction of the waste is transported to second mechanical separator  112 . Second mechanical separator  112  also directs its high-solids fraction toward energy conversion processor  20 , while the high-liquids fraction is directed to settling tank  62 . From settling tank  62 , a high-solids fraction of the waste is directed back to buffer tank  68  or alternately to one or both of mechanical separators  60 ,  112  and another fraction is transported toward energy conversion processor  20 . Three-way valve  100 , which is controlled by moisture controller (MIC)  76 , based on the input from moisture sensor  74 . Three-way valve  100  varies the amount of high-solids waste fraction transported toward either energy conversion processor  20  and buffer tank  68 , or alternately between first and second mechanical separators  60 ,  112 .  
         [0041]      FIG. 5  illustrates another embodiment of a solids/liquids separator  120  for energy conversion system which also increases efficiency of separation between liquids and solids in a waste stream. Solids/liquids separator  120  includes a second settling tank  122 , which may be of the same type of construction as settling tank  62 , but typically will have a different geometry. Settling tank  122  directs the high-solids fraction of the waste towards energy conversion processor  20 , while the high-liquids fraction of the waste from second settling tank  122  is transported to settling tank  62 . Settling tank  62  transports its high-liquids fraction to waste water treatment (e.g., apparatus  40  shown in  FIG. 1 ). The prime advantages of gravity separation utilizing settling tanks are low energy consumption and high recovery of solids. Putting two gravity separators in series (i.e., settling tanks  62  and  122 ) downstream of mechanical separator  60  is thought to recover approximately 97% of the solids. The high-solids fractions of waste from both gravity separators  62 ,  122  are transported back to buffer tank  68  or combined with an output from mechanical separator  60  and directed to shredder  70  and onto energy conversion processor  20 . A three-way valve  124  operates in the same fashion as three way valve  100  described above, that is, controlled by moisture controller (MIC)  76 , based on an input from moisture sensor  74 . Three-way valves vary an amount of high-solids waste transported toward energy conversion processor  20 , buffer tank  68 , and mechanical separator  60 .  
         [0042]     For all of the above described embodiments, it should be easily understood that many variations can be made and still be within the spirit and scope herein described. For example, altering the arrangements and quantity of separators, such as three or more separators in a parallel or series-parallel arrangements are certainly contemplated.  
         [0043]      FIG. 6  displays one embodiment of a heat recovery system  140  which may be utilize to improve and/or optimize the processes performed by the energy conversion system. In the illustrated embodiment, the waste stream is heated via heat recovered from the cooling fluid of power generator  142 , typically a glycol/water mix, via heat exchanger  144 . The waste is further heated in a second heat exchanger  146 , using steam and/or exhaust gases available from energy conversion processor  20 . These may alternately be taken from a vessel within energy conversion processor  20  or a downstream apparatus such as a flash tank as utilized in the petroleum industry.  
         [0044]     Another source of heat recovery is shown which circulates a heat transfer medium through heat exchangers  148 ,  150 . The heat transfer medium transfers heat from the hot fuel from energy conversion processor to the incoming waste stream, preheating it, raising overall efficiency.  
         [0045]     Additional process control instrumentation is also illustrated in  FIG. 6  by way of example only. Recovery of constituents of exhaust gases is important with certain embodiments of energy conversion processor  20 . For example, one embodiment of energy conversion processors require carbon monoxide (CO) and/or carbon dioxide (CO2), which are readily available in significant quantities from the exhaust of an engine and/or combustion processes. In the embodiment shown, a portion of the exhaust gas is separated by gas separator  152  for delivery to energy conversion processor  20 . The exhaust gas may be filtered, or chemically converted (for example converting CO2 into CO and O2) to deliver the desired gas or gases to energy conversion processor  20 . In one embodiment, membrane technology is utilized within gas separator  152  to concentrate the amount of one gas, for example CO, for delivery into the process. Other more complex gas separation methods such as pressure-swing absorption, vacuum swing absorption, chemical separation, catalytic separation, and other gas separation methods may be utilized to accomplish the same goal of delivering a more desirable mix of gas to energy conversion processor  20 . The gas separation process typically utilizes a compressor for the feed gas (exhaust), or one or more vacuum pumps.  
         [0046]      FIG. 7  illustrates another embodiment for a solids/liquids separator  170  for an energy conversion system which controls a solids percentage, primarily for a low-solids energy conversion processor  20 . Solids/liquids separator  170  includes one or more gravity separators (settling tanks  62 ,  122  shown). The high-solids fraction of the waste from each settling tank  62 ,  122  is transported toward energy conversion processor  20 , except that a fraction of the high-solids fraction is directed through mechanical separator  60 , which raises the solids percentage of the waste to a desired level for input into energy conversion processor  20 . A three-way valve  172  is controlled by the moisture controller (MIC)  76 , based on an input from moisture sensor (MT)  74 . Three-way valve  172  could alternately be a combination of two-way valves and/or manual valves. The liquid fraction of the waste from mechanical separator  60  can alternately be transported to buffer tank  68  or directly to one of settling tanks  62 ,  122 .  
         [0047]      FIG. 8  illustrates one example of an energy conversion processor  200 . In the example illustrated, pump  202  raises pressure of the waste within energy conversion processor  200 . As described above, the waste has been controlled to a specified moisture level. The waste is pumped through a length of tubing  204 . A example includes 1000′ of 1.5 inch NPS Schedule 80 304ss with an inside diameter of about 1.5″, which coiled in about a 12 foot diameter, with 27 turns. A flowrate of approximately 4.6 gpm is pumped into energy conversion processor  200 . A step down transformer  206  converts 480 volt, single phase power from power  208  generator to a low voltage, for example 30 VAC. Temperature sensor  210  provides a signal to temperature controller  212 . The amount of power from power generator  208  delivered to energy conversion processor  200  is controlled by power controller  214 . Power controller  214 , in one embodiment, is the phase angle SCR (Silicon Controlled Rectifier) type or another similar type. A specific SCR type power controller is supplied by EuroTherm. Power controller  214  delivers an amount of power to step down transformer  206  proportional to the signal received from temperature controller  212 . Power controller  214  regulates the voltage applied to the primary of transformer  206 , which regulates the voltage applied to energy conversion processor  200  by the same ratio. Such an arrangement maintains the temperature of the waste at the outlet  216  of energy conversion processor  200 . Another embodiment, not shown, utilizes multiple zones, for example, two transformers  206 , two power controllers  214 , two temperature sensors  210 , and two temperature controllers  212 , where each zone may have differing temperature setpoints or the same temperature setpoint to have a zone of temperature rise rather then a zone of maintaining temperature.  
         [0048]     In one embodiment, tubing  204  of energy conversion processor  200  includes a jacketed pipe wherein heat from a power generator is applied as one of heated fluid or heated gas to the jacketed pipe to maintain desired temperature setpoints. In this and other embodiments, heat from a power generator is therefore applied indirectly to the waste stream within energy conversion processor ( 20 ,  200 ) by induction.  
         [0049]     The above described embodiments are utilized to control an amount of moisture within a waste stream to attempt to provide an optimum waste for the particular energy conversion processor  20 . When energy conversion processor  20  is a gasification processor, a moisture percentage entering mechanical separator  60 , for example, an inclined screw press, is about 95%. The moisture percentage in the high-solids stream exiting mechanical separator  60  is about 65%. The mass fraction of solids forwarded to shredder  70  is then about 30%. The remaining 70% mass fraction of waste is forwarded to a gravity separator (e.g., settling tank  62 ). The solid fractions in the gravity separator are continually recycled to buffer tank  68 , where it is mixed with fresh slurry and reintroduced into mechanical separator  60 . For the waste stream exiting shredder  70 , hot air is introduced into dryer  72  (shown in  FIG. 2 , and is regulated as described above to reduce the moisture percentage in the waste stream being fed to energy conversion processor  20  to about 25%.  
         [0050]     When energy conversion processor  20  is a pyrolysis or liquification processor, a moisture percentage entering mechanical separator  60 , for example, a solid bowl basket centrifuge, is about 97%. The moisture percentage in the high-solids stream exiting mechanical separator  60  is about 72%. The mass fraction of solids forwarded to shredder  70  is then about 65%. The remaining 35% mass fraction is forwarded to a gravity separator (e.g., settling tank  62 ). The moisture percentage of the solid fraction in the gravity separator is about 90%. The flow from gravity separator is divided at a three-way valve, with nominally 50% of the flow directed to the pipe connecting mechanical separator  60  and shredder  70 . This results in a desired mixture moisture percentage of about 80% in this case. The three-way valve position is regulated as previously described, to maintain this moisture percentage setpoint. The remaining high-solids stream from the gravity separator is continually recycled to buffer tank  68 , where it is mixed with fresh slurry and reintroduced into the mechanical separator.  
         [0051]     The above described embodiments and examples serve to illustrate how control of moisture content from a waste stream is utilized by a number of different energy conversion processor types in order to provide a method for disposing of and gaining beneficial use from animal production waste streams. The above described embodiments also do not involve methods that contribute to odor released into the atmosphere, providing a more desirable approach to the problem of animal production waste than known solutions which include lagoons and field spreading.  
         [0052]     While the invention has been described in terms of various specific embodiments, those skilled in the art will recognize that the invention can be practiced with modification within the spirit and scope of the claims.

Technology Category: y