SELECTIVE GRIND TECHNOLOGY and FIBER BY-PASS Fluid Quip Process Technologies, LLC 1940 South Yellow Springs Street Springfield, Ohio 45506 www.fqptech.com
Fluid Quip Process Technologies Leverage Years of Corn Wet Milling and Dry Grind Ethanol Experience to Bring Value Adding Technologies to the Ethanol Industry. Experienced staff of chemical and mechanical engineers Plant Management / Operation Expertise Experienced Construction and Project Managers Engineering Services Turn-Key Solutions Mass and Energy Balances Plant Expansions Energy Optimization Projects FQPT Headquarters, Springfield, Ohio
FQPT Technologies SGT MSC BOS Selective Grind Technology Secondary Milling Step to Increase Ethanol and Oil Yields *11 FQPT SGT Systems US Patent: 9,012,191 Maximized Stillage Co-Products High-Value Protein from Stillage *3 rd System Under Construction US Patent: 8,778,433 Brix Oil Separation System Oil Recovery from Liquefaction *4 th System Under Construction
FQPT DRY MILL TECHNOLOGIES Wet Fractionation System Patent Pending Cook Water Oil recovery system (BOS TM ) Corn Oil Low FFA Corn Flour Liquefaction Separation/Grind system (SGT TM ) Front- End Fiber Fermentation and Distillation Increased ethanol yield >2% Enhanced Back end oil recovery Evaps Protein recovery system MSC TM Protein dryer Protein 50% purity Backset Current decanters Current DDGS dryers DDGS Fluid Quip Process Technologies, LLC, 2015
FQPT FIBER TIMELINE First SGT Installation Milling Slurry Produced Clean Fiber Samples 5 Major Cellulose Companies Started MSC -Fiber -50% Purity Protein from Stillage Started CC Wash Liquefaction Enhancement First Fiber By-Pass Installation Full Scale FE Fiber 2009 2010 2011 2012 2013 2014 2015 Invented Filtration Centrifuge 2008 Developed MZSA High-Rate Washing Paddle Screen Fluid Quip Process Technologies, LLC, 2015
Selective Grind Technology (SGT) Why Mill? Kernel Hydration Enzyme Accessibility Release Starch from Fiber Open Grit Starch Release Starch from Germ Release Protein from Starch Release Protein from Germ
Starches Retrograded/Resistive RS1 Encapsulated Starch Starch is bound within protein or fiber matrix approximately 250-300 microns in size. Treated by effective milling (~500 microns) RS2 Crystallized (short-chain) Amylopectin Resistant due to high density and crystalline structure. The amylopectin strands form chain associations which are digested slowly but fully. Treated by effective cooking to open crystal structure and improve enzyme access RS3 Retrograded Amylose During heat processing in excess water, the amylose strands pack tightly to form a strong crystal structure. The presence of thermo-stable alpha-amylase can enhance this phenomena. The result is starch that is completely resistant to digestion. Not measureable using existing enzymatic test methods Treated by Effective cooking and avoidance of excessive alpha amylase during cooking
Starches Solution Reduce Grit and Germ Size by grinding later Target >500 micron particles Expose Starch and Oil Attack RS1 Enhance RS2 Eliminate RS3
SGT Slurry or Liq. Single Stage Particles To Mill Liquid and undersized particles Ground Particles Liq. Tank
SGT Multi Stage
SGT Performance Single Stage Performance +/-2% EtOH Yield Increase +/-18% Oil Yield Increase Multi Stage Performance +/-3-4% EtOH Yield Increase +/-20+% Oil Yield Increase Fluid Quip Double Disc Mill *Highest Performers: 2.83-2.9 gal/bu undenatured Fluid Quip 40 Mill
FIBER BY-PASS Separation and purification of fiber from existing liquefaction stream Separation of fiber pre-fermentation Multiple stages of solid/liquid separation and washing SGT Milling to Release Starch Counter-current washing to remove starches, proteins, and fats from fiber *Fiber By-Pass is Patent-Pending FQ-PS32- Paddle screen used in washing
FIBER BY-PASS SYSTEM 2 FQPT systems running full scale-2 more coming on line shortly 8-12% increase in plant throughput OR 8-12% fermentation increase Ethanol yield increase by removing non-fermentables Allows for further cellulosic conversion FQ-MZSA- Paddle screen Patent-Pending
FIBER BY-PASS BENEFITS Removal of non-fermentable material before fermentation 10% Increase in fermentation capacity/fermentation time Operational flexibility-option between increased yield or capacity increase FQ-PS32- Paddle screen used in washing
FIBER BY-PASS BENEFITS Reduced energy usage in distillation Improved heat transfer in evaporation Better beer/mash heat transfer Lower front end viscosity
FIBER BY-PASS-WET FRACTIONATION TM SGT SLURRY MILLING FIBER BYPASS FIBER Oil recovery system (BOSS TM ) CORN OIL FERMENTATION ETHANOL Protein recovery system MSC TM PROTEIN
FIBER BY-PASS: THE BIG PICTURE SLURRY SGT MILLING COOK SEPARATION FIBER BYPASS FIBER FERMENTATION
SGT TM MILLING SLURRY PADDLE SCREEN FQPT 52 GRIND MILL GRIND MILL LIQUEFACTION
COUNTER-CURRENT WASH STARCH PROTEIN SUGAR FAT Cook Water STAGE 1 STAGE 2 STAGE 3 STAGE 4 FIBER STARCH PROTEIN SUGAR FAT White Fiber
MZSA PADDLE SCREEN PURPOSE Separate solids and liquids based on incoming particle size Displace liquid in cake with water to wash cake OPERATION Internal screen determines particle size separation Paddles apply centrifugal forces to dewater and remove solids smaller than screen size Internal wash nozzles displace remaining liquids to improve separation
IMPROVING WASHING Manage current plant water input in more effective ways Number of wash stages Amount of water used in wash Effectiveness of water usage Displacement vs. Dilution washing
FIBER BY-PASS SOLIDS 1 st Pass Tank 2 nd Pass Tank 3 rd Pass Tank 4 th Pass Tank
FIBER BY-PASS LIQUIDS 1 st Pass Centrate 2 nd Pass Centrate 3 rd Pass Centrate 4 th Pass Centrate Decanter Centrate
FIBER BY-PASS-RESULTS Fiber yield can range from 3-10 lb/bu Composition ranges based on yield 60 MMGPY: 15,500 lb/hr out of fermentation 120 MMGPY: 31,000 lb/hr out of fermentation FQPT Clean Fiber Low High NDF 63% 68% Protein 10% 17% Fat 2% 7% Starch 1% 4% No net yield loss Combined with SGT technologies nets EtOH yield increase Fluid Quip White Fiber
FIBER BY-PASS-BENEFITS 8-12% fermentation capacity increase OR 8-12% fermentation time increase 7 o F increase in beer feed temperature 8% steam reduction to distillation Syrup total solids increase by 6-10% Reduced heat exchanger fouling Improved efficiency on pumps through distillation
Fiber By-Pass:Precursor to Protein Patent Pending Cook Water Oil recovery system (BOS TM ) Corn Oil Low FFA Corn Flour Liquefaction Separation/Grind system (SGT TM ) Front- End Fiber Fermentation and Distillation Increased ethanol yield >2% Enhanced Back end oil recovery Evaps Protein recovery system MSC TM Protein dryer Protein 50% purity Backset Current decanters Current DDGS dryers DDGS Fluid Quip Process Technologies, LLC, 2015
Maximized Stillage Co-Products 50%+ Protein From Stillage: Still Pro 50 In Operation for over 5 Years Patented Process and Equipment* Fluid-Quip Filtration Centrifuge: US Patent: 8,813,973
Maximized Stillage Co-Products PROTEIN Up to 4.5 lb/bu 50+% Protein Corn Gluten Meal + Brewer s Yeast Various Successful Feed Trials FIBER 27% Protein 7% Fat OIL ~0.4lb/Bu Oil Yield Improvement Yield Over 1.0lb/bu White Fiber
Still Pro 50 Protein Gluten Meal + Brewer s Yeast Brewer s Yeast: N. N. Growth Factors Gluten Meal: Excellent Palatability High Protein Concentration Still Pro 50 TM Protein Product Amino Acid Profile as % of Total Product (Dry Basis) StillPro TM Brewer's Yeast Corn Gluten Meal Soybean Meal Alanine (%) 3.93 3.31 5.04 2.07 Arginine (%) 2.62 2.15 1.91 3.48 Aspartic Acid (%) 3.74 4.39 3.98 5.36 Cystine (%) 1.53 0.22 1.11 0.74 Glutamic Acid (%) 7.72 6.79 13.52 8.70 Glycine (%) 1.89 1.76 1.51 1.98 Histidine (%) 1.55 1.08 1.34 1.28 Isoleucine (%) 2.01 2.19 2.51 2.16 Leucine (%) 5.32 4.60 10.51 3.66 Total Lysine (%) 2.48 2.32 1.00 3.02 Methionine (%) 1.07 0.82 1.29 0.67 Phenylalanine (%) 2.56 2.28 4.00 2.39 Proline (%) 3.75 2.28 4.86 2.32 Serine (%) 2.67 2.49 3.28 2.14 Threonine (%) 2.27 2.19 1.56 1.85 Tyrosine (%) 2.20 1.68 3.17 1.82 Tryptophan (%) 0.41 N/A 0.19 0.65 Valine (%) 2.83 2.49 2.92 2.27 Total 50.55% 43% 63.70% 46.56%
Maximized Stillage Co-Products Process Benefits Clarifies Evaporator Feed Reduces Evap fouling Syrup Viscosity Reduction, >50% DS 22% Increase in Evaporator Capacity 45% Reduction in DDGS Dryer Loading Increased Oil Yield No Additional Water Required Clarifies Backset Fluid-Quip Disc/Nozzle Centrifuge
FIBER BY-PASS-BIG PICTURE Multiple Systems running full scale TODAY Provides flexibility between throughput and yield Source of further cellulosic conversion Overall quality of life improvement for plant Ethanol yield benefits
For More Details THANK YOU Fluid Quip Process Technologies, LLC 1940 South Yellow Springs Street Springfield, Ohio 45506 mfranko@fqptech.com www.fqptech.com