image of a methane molecule

McElvaney
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bioconverter.com

5933 Russell Ln
Forestville, CA
95436

About Us

McElvaney Associates Corporation is a consulting and design firm working to commercialize our innovative conservation technology - the BioConverter! The present iteration of our continuing effort in this regard has evolved beyond our prior efforts with two companies initially intent upon commercialization of this unique process.

1993-97 - Sustainable Technologies, Inc., Kihei, HI

Sustainable Technologies began in 1993 to apply the original design of the BioConverter (vertical) to the production of biological hydrogen. A 2 ton/day production scale system was constructed in '94 and '95 with a concurrent shift to using the BioConverter to produce methane, as this was viewed as a vital precursor step in the company's plan. This system operated continuously from '95 through '97 on a feedstock of 10 - 12% total solids (50% Food waste, 25% Green waste, 25% Paper waste, dry wt. basis). Horticulture/aquaculture feed tests were performed on the outputs and units of Plant Tonic were sold in local hardware outlets beginning in June '97. Provisional and final patents were applied for in 1998 and 1999 resulting in the issuance of Patent No: US 6,254,775; Date of Patent: July 3, 2001 Anaerobic Digester System and Method to Inventor: James D. McElvaney.

1982-91 - UNISYN Biowaste, Waimanalo, HI

UNISYN Biowaste began in 1982 as Universal Synergetics in Tacoma, WA, with prototype development continuing through 1983. In 1984, construction of an $8M, 185 ton/day anaerobic digestion facility (1M gallon) was started in HI utilizing a design variation of the BioConverter (horizontal). The feedstock at this time was the flushed manure of 2,000 cows and of 250,000 poultry (layers), along with USDA fruit fly rearing waste from a nearby facility. The integrated system consisted of digesters, 1 MW cogeneration system, 2.5-acre Spirulina algae culture/freeze drying system, and 4-acre greenhouse producing 1,500 lbs. basil/day. The residue from the digestion system was spray-dryed as Single Cell Protein (SCP) for animal/aquaculture feed trials, which followed AAFCO guidelines and were approved by the HI Dept. of Agriculture. Good results were witnessed in feed trials for channel catfish and broilers, and growth factor response was achieved for Chinese catfish and tilapia. A patent was granted to the inventors in 1992 and it was assigned to what was by then UNISYN of Hawaii. In 1991, the inventor completed a Feasibility of Commercial Bioconversion Systems, including an Organic Waste Inventory, for the HI DBED, Energy Division. The result of the study was that the UNISYN facility was converted from processing manure to receiving $60/ton for processing 35 tons/day of Food Waste and Fats, Oils, and Grease (FOG). This activity continued until 1999.

2 ton/day production scale system

BioConverter system, 2-ton/dayreceiving waste
typical waste

  1. Input Processing
  2. BioConversion
  3. Output Processing
    1. Gas Processing
    2. Solids Removal
    3. Residual Liquid Treatment and Removal
  4. Power Generation and Heat Recovery


  1. Input Processing

    mix tank equipmentThe Mix Tank is the input point for solid material which is added to the BioConverters. It consists of a trough-like Tank, a Grinder, a Pump, and a Heat Exchange.

    loading the mix tankEffluent is loaded into the Tank by a Transfer Pump and raw waste material, i.e. food waste, paper waste, and/or green waste is dumped in at the mouth, where it is drawn through the Grinder with the Pump which discharges back to the Tank through a Heat Exchange. This action gradually grinds and heats the material. The resulting slurry is then loaded into the BioConverter(s).

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  2. BioConversion

    BioConvertersThe BioConverter is the heart of the BioConversion system. It provides an environment for the cultivation and maintenance of anaerobic bacteria, which biologically convert the organic waste added to the system into the output products of the system. A typical BioConverter consists of a cylindrical, translucent fiberglass vessel, which contains a heating coil for the temperature maintenance and sparging tubes for mixing/gas transfer. Pressure sensors are used to measure liquid level and gas pressure and a RTD measures the liquid temperature and acts upon the heating coil to maintain the temperature set point.

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    The following equipment provides support for the BioConverter:

    The Transfer Pump provides a means of moving slurry through and around the system. Valves provide for various flow paths for the transferring of liquid. The BioConverter may be operated in series or parallel fashion, in an up-flow mode for low solids or in a down-flow mode for high solids. Effluent can be removed from any vessel and pumped back to the Mix Tank, or over the Screen, or into a Surge Tank to allow maintenance of any Vessel or Tank.

    The Gas Blower provides pressure/flow to the Sparging Tubes in each Vessel. A Gas Cooler lowers the temperature of the pressurized gas below 100 F. Valves allow sparging to be accomplished in any or all Vessels simultaneously.

    The Air Compressor with Air Dryer provides dry instrument air for the actuation of valves throughout the system. It also provides drying air for the Gas Sample Analyzer.

    The Hot Water Pump circulates a heat transfer fluid through the Engine Exhaust Heat Exchange and Engine Jacket Water Heat Exchange where it is heated. The fluid then passes through the Mix Tank Heat Exchange and BioConverter Heating Coils where it is cooled and transfers active heat. It then returns to the Hot Water Pump through the Radiator Fan for final temperature adjustment.

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  3. Output Processing

    1. Gas Processing

      gas processingThe equipment in the gas processing area functions to clean, measure, separate and store the gas produced by the system. A solid media hydrogen sulfide scrubber removes hydrogen sulfide from the BioGas. A Membrane Separation System separates the BioGas into two streams. The reject stream returns to the BioConverter vessels through the sparging tubes. The product stream of approximately 99% methane is compressed using two Gas Compressors and stored in four High Pressure Storage Bottles.

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      gas compressorgas storage bottlesVarious instruments comprise the Gas Measurement System. Two Annubars with Differential Pressure Sensors provide for gas flow measurement. Respective Sensors correct both for the Temperature and Pressure. A Gas Analyzer System provides for 0-100% measurement of Methane, Carbon dioxide, and Hydrogen. And a selectable 0-25,0-10 or 0-1% measurement of Oxygen is also performed. This information combined with flow data allows for the calculation of the mass of the BioGas being produced. System performance is thereby determined.

      safety flare burning BioGasA Safety Flare provides for the burning of gas or gas components relieved from the system. Safety relief valves on all vessels connect to a header leading to the Safety Flare.

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    2. Solids Removal

      vibrating screenThe Vibrating Screen is the primary device for removing solids from the system. BioConverter effluent is passed over the screen with the Effluent Pump. The portion of the effluent which is smaller than the Screen mesh size, e.g., the liquid containing dissolved solids and bacterial solids, passes through the Screen and is held in a Surge Tank for further processing by the Ultrafilter. The coarse, non-converted solids "shake" off the vibrating screen, fall on to the Dryer Input conveyor and are loaded into the Dryer.

      filterThe Filter is the secondary device for removing or classifying solids from the system. It consists of a Batch Tank, Pump, Filter Module and Heat Exchange. The screened effluent is added to the Filter Batch Tank. The Pump circulates this liquid through the Filter Module, Heat Exchange and back to the Batch Tank. This action separates the effluent into two streams, Permeate or Filtrate and Retentate or Solids Concentrate. Filtrate is removed into appropriate containers for use as dilute nutrient fertilizer. What does not pass the filter (due to its molecular size) is gradually concentrated in the Batch Tank. This concentrate is a bacterial solids emulsion, a portion of which is periodically discharged to the Mix Tank to inoculate the input solids. The remainder is harvested as a soil inoculant, slow release liquid fertilizer or BioFeed additive.

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      dryerThe Dryer provides blending and moisture adjustment for the non-converted and bacterial solids which are removed from the system. It consists of a Blender/ Dryer, Evacuation Blower and Input and Output Conveyors for loading and unloading the unit. The Input Conveyor loads coarse solids from the Vibrating Screen. The Evacuation Blower draws hot exhaust gas from the Engine Generator through the unit. The Heat Exchange providing temperature control for the bioconversion process has cooled this hot exhaust from 1200 degrees F. down to 400 degrees F. This cooled exhaust pasteurizes and removes moisture from the solids.

      bagg23bagger.jpgBioSoilUpon completion of the drying cycle, the resulting Biosoil is removed from the Dryer by the Output Conveyor which discharges into the Bagging System Surge Hopper for input to a bulk bag or smaller units.

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    3. Residual Liquid Treatment and Removal

      BioFilter w/ BioConvertersIn the course of daily operation a wet Sump receives washdown water from the waste receiving and liquid handling stations. The sump is equipped with a Pump, which can transfer this volume to the Mix Tank or Storage Tanks for admixing to the daily waste received. If sufficient wastewater is available for that purpose, the Sump Pump charges the BioFilter with the wastewater volume collected.

      pondsThe BioFilter is a small constructed wetland of emergent plants growing in a cinder /gravel base with an overflow weir at the opposite end leading to a second Sump/Pump which can transfer the stripped overflow liquid to storage, to irrigation, or to a membrane-lined pond for storage.

      humbnails/35storage.jpg"The retention time in the BioFilter will vary with the volume of cleanup water charged to it. It serves as a useful nutrient removal device of the soluble solids in the wastewater, capable of stripping in a ten day period concentrations of COD ten times the concentration of dilute sewage wastewater.

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  4. Power Generation and Heat Recovery

    bi-fuel generatorElectrical energy and heat for operating the system is made available from a bi-fuel engine generator capable of utilizing the Biogas produced on a daily basis.

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UNISYN of Hawaii

overhead view of UNISYN system


Spirulina pondsdigesters

before they were broilersgreenhouse

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