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GEORGIA ALTERNATIVE FUELS, LLC
          MULTI-FEEDSTOCK PROCESS
       “ELECTRO-CATALYSIS FOR ALL OILS
     INCLUDING HIGH FREE FATTY ACID OILS


 WHY BIODIESEL AND WHY NOW?
 WHAT TECHNOLOGIES ARE USED?
WHAT COST SAVINGS ARE AVAILABLE?
 WHAT IS THE BEST TECHNOLOGY?
    HOW CAN I LEARN MORE?




                                   NO2 DIESEL FUEL   BIODIESEL
HIGH FFA OIL TYPE PROCESS REACTIONS
                 USING
          “ELECTRO-CATALYSIS”




1ST REACTION – ESTERIFICATION FOLLOWED IMMEDIATELY BY
2ND REACTION - TRANSESTERIFICATION
MULTI-FEED STOCK BIODIESEL
REACTION PROCESS OUTLINE
“ELECTRO-CATALYSIS” VERSES
    CONVENTIONAL BIODIESEL PROCESSES
•   Most Biodiesel processors use a single step Transesterification
    reaction, because it is low cost, and easily understood. It does
    lower yield, degrade quality significantly, increase costs, and
    limit the oil type used in the process to low Free Fat Oils, with
    ever increasing costs
•   “Electro-Catalysis begin with an Esterificiation Reaction to
    convert Free Fatty Acids to Esters, speeding reaction times and
    increasing yield. The process also lowers chemical costs and has
    no upper limit on Free Fatty Acids.
•   “Electro-Catalysis” also expand available oil types that can be
    efficiently processed, improves overall margin on all oils used.
•   “Electro-Catalysis” are not restricted for use on just low FFA oils,
    but can be used on any oil type.
“ELECTRO-CATALYSIS” REACTOR 17 GPM
            FLOW RATE




  ANY REACTOR FLOW RATE CAN BE CONFIGURED
  TO MEET THE LARGEST BIODIESEL PLANT FLOW
  REQUIREMENTS, CONTACT A SPECIALIST TODAY
GENERAL PROCESS TRENDS OF “ELECTRO-
  CATALYSIS” VERSES CONVENTIONAL
      BIODIESEL TECHNOLOGIES
 The general trends for conventional Biodiesel, as FFA content
 increases, chemical costs increase proportionally, reaction
 times can increase, and yield drops. This trend is not the
 same with “Electro-Catalysis” reactions. See Tables 1 and 2
“ELECTRO-CATALYSIS”
                     REACTOR
•   Please note: reaction times can vary depending on oil type and
    contamination quantities. Consult your oil supplier for any
    detailed analysis of the oils used in the process.
•   Oil types can vary significantly and therefore require alterations
    in process conditions and reaction times.
•   Sometimes, feed oil analysis is required to measure
    contamination levels for adequate process set-up conditions.
•   Alternative plant plans should be considered for worst case oil
    contamination.
•   Expect changes, plan for changes in oil feed stock contamination.
•   Also note, these procedures are well understood by the industry
    and is very common for lower cost oil types.
•   If your not sure, ask questions
ESTIMATED ANNUAL SAVINGS “ELECTRO-CATALYSIS”
         REACTOR VERSES CONVENTIONAL
   TRANSESTERIFICATION REACTION TECHNOLOGIES

             Table 1; Estimatedsavings are basedon 5,000,000 gallons
                                processed per year

$4,000,000
$3,500,000
$3,000,000
$2,500,000
                                                                Annua Chem
                                                                     l
$2,000,000
                                                                Annua Yield
                                                                     l
$1,500,000
$1,000,000
 $500,000
       $0

                5%FFA           10%FFA         +15%FFA
“ELECTRO-CATALYSIS”
  ESTIMATED ANNUAL SAVINGS USING HIGH FFA OIL
TYPES VERSES CONVENTIONAL TRANSESTERIFICATION
                   REATIONS

             Table 2: Savings are basedon 5,000,000 gallons processed per
                                         year

$6,000,000

                                                                   INCLUDES
$5,000,000
                                                                   SAVINGS DATA
                                                                   FROM TABLE 1
$4,000,000

                                                                     Oil Savings
$3,000,000
                                                                     Table1




                                                       TABLE 1
                                      TABLE 1
$2,000,000


$1,000,000


       $0

                 5%FFA            10%FFA            15%FFA
COST SAVINGS ANALYSIS USING “ELECTRO-
                CATALYSIS”
   ESTERIFICATION/TRANSESTERIFICATION
           REACTION PATHWAYS

• Test data shows benefits of using the reactor system for
  savings:
      • General savings trends

          – 5% FFA Oil annual estimated annual savings
             » $1,600,000

          – 10% FFA Oil annual estimated annual savings
              » $3,600,000

          – 15% FFA Oil annual estimated annual savings
              » $5,400,000
COST SAVINGS ANALYSIS USING “ELECTRO-
                  CATALYSIS”
     ESTERIFICATION/TRANSESTERIFICATION
             REACTION PATHWAYS

•    A general statement, technology benefits, as the FFA content
    increases, cost savings increase proportionally
•   Users have a wide option on oil type selection, higher FFA oils are
    generally lower in cost and improves Biodiesel plant operating
    margins
•   Use less chemicals with high FFA oils, improves quality
•   Fast reaction times keeps plant production at maximum capacity
    even when processing high FFA oils
•   Reaction times and savings can vary depending on oil
    contamination, oil type, and other factors
•   In some cases, tests of oils with unknown origin and contaminate
    level is required to determine best process setup parameters, and
    can affect costs and Biodiesel plant production
PRODUCE HIGH QUALITY BIODIESEL
         FROM CHICKEN FAT
USE LOW COST OILS
IMPROVE MARGIN
Additional details

CONTACT INFORMATION:
Georgia Alternative Fuels, LLC
244 John B. Brooks Road
P.O. Box 167
Pendergrass, GA 30567

Alan Lawson
CEO/President
404 735-5866

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Biodiesel Reaction Presentation 1[1]

  • 1. GEORGIA ALTERNATIVE FUELS, LLC MULTI-FEEDSTOCK PROCESS “ELECTRO-CATALYSIS FOR ALL OILS INCLUDING HIGH FREE FATTY ACID OILS WHY BIODIESEL AND WHY NOW? WHAT TECHNOLOGIES ARE USED? WHAT COST SAVINGS ARE AVAILABLE? WHAT IS THE BEST TECHNOLOGY? HOW CAN I LEARN MORE? NO2 DIESEL FUEL BIODIESEL
  • 2. HIGH FFA OIL TYPE PROCESS REACTIONS USING “ELECTRO-CATALYSIS” 1ST REACTION – ESTERIFICATION FOLLOWED IMMEDIATELY BY 2ND REACTION - TRANSESTERIFICATION
  • 4. “ELECTRO-CATALYSIS” VERSES CONVENTIONAL BIODIESEL PROCESSES • Most Biodiesel processors use a single step Transesterification reaction, because it is low cost, and easily understood. It does lower yield, degrade quality significantly, increase costs, and limit the oil type used in the process to low Free Fat Oils, with ever increasing costs • “Electro-Catalysis begin with an Esterificiation Reaction to convert Free Fatty Acids to Esters, speeding reaction times and increasing yield. The process also lowers chemical costs and has no upper limit on Free Fatty Acids. • “Electro-Catalysis” also expand available oil types that can be efficiently processed, improves overall margin on all oils used. • “Electro-Catalysis” are not restricted for use on just low FFA oils, but can be used on any oil type.
  • 5. “ELECTRO-CATALYSIS” REACTOR 17 GPM FLOW RATE ANY REACTOR FLOW RATE CAN BE CONFIGURED TO MEET THE LARGEST BIODIESEL PLANT FLOW REQUIREMENTS, CONTACT A SPECIALIST TODAY
  • 6. GENERAL PROCESS TRENDS OF “ELECTRO- CATALYSIS” VERSES CONVENTIONAL BIODIESEL TECHNOLOGIES The general trends for conventional Biodiesel, as FFA content increases, chemical costs increase proportionally, reaction times can increase, and yield drops. This trend is not the same with “Electro-Catalysis” reactions. See Tables 1 and 2
  • 7. “ELECTRO-CATALYSIS” REACTOR • Please note: reaction times can vary depending on oil type and contamination quantities. Consult your oil supplier for any detailed analysis of the oils used in the process. • Oil types can vary significantly and therefore require alterations in process conditions and reaction times. • Sometimes, feed oil analysis is required to measure contamination levels for adequate process set-up conditions. • Alternative plant plans should be considered for worst case oil contamination. • Expect changes, plan for changes in oil feed stock contamination. • Also note, these procedures are well understood by the industry and is very common for lower cost oil types. • If your not sure, ask questions
  • 8. ESTIMATED ANNUAL SAVINGS “ELECTRO-CATALYSIS” REACTOR VERSES CONVENTIONAL TRANSESTERIFICATION REACTION TECHNOLOGIES Table 1; Estimatedsavings are basedon 5,000,000 gallons processed per year $4,000,000 $3,500,000 $3,000,000 $2,500,000 Annua Chem l $2,000,000 Annua Yield l $1,500,000 $1,000,000 $500,000 $0 5%FFA 10%FFA +15%FFA
  • 9. “ELECTRO-CATALYSIS” ESTIMATED ANNUAL SAVINGS USING HIGH FFA OIL TYPES VERSES CONVENTIONAL TRANSESTERIFICATION REATIONS Table 2: Savings are basedon 5,000,000 gallons processed per year $6,000,000 INCLUDES $5,000,000 SAVINGS DATA FROM TABLE 1 $4,000,000 Oil Savings $3,000,000 Table1 TABLE 1 TABLE 1 $2,000,000 $1,000,000 $0 5%FFA 10%FFA 15%FFA
  • 10. COST SAVINGS ANALYSIS USING “ELECTRO- CATALYSIS” ESTERIFICATION/TRANSESTERIFICATION REACTION PATHWAYS • Test data shows benefits of using the reactor system for savings: • General savings trends – 5% FFA Oil annual estimated annual savings » $1,600,000 – 10% FFA Oil annual estimated annual savings » $3,600,000 – 15% FFA Oil annual estimated annual savings » $5,400,000
  • 11. COST SAVINGS ANALYSIS USING “ELECTRO- CATALYSIS” ESTERIFICATION/TRANSESTERIFICATION REACTION PATHWAYS • A general statement, technology benefits, as the FFA content increases, cost savings increase proportionally • Users have a wide option on oil type selection, higher FFA oils are generally lower in cost and improves Biodiesel plant operating margins • Use less chemicals with high FFA oils, improves quality • Fast reaction times keeps plant production at maximum capacity even when processing high FFA oils • Reaction times and savings can vary depending on oil contamination, oil type, and other factors • In some cases, tests of oils with unknown origin and contaminate level is required to determine best process setup parameters, and can affect costs and Biodiesel plant production
  • 12. PRODUCE HIGH QUALITY BIODIESEL FROM CHICKEN FAT USE LOW COST OILS IMPROVE MARGIN Additional details CONTACT INFORMATION: Georgia Alternative Fuels, LLC 244 John B. Brooks Road P.O. Box 167 Pendergrass, GA 30567 Alan Lawson CEO/President 404 735-5866