Introduction To FOOD extrusion - K-Tron
Transcription
Introduction To FOOD extrusion - K-Tron
Introduction to FOOD extrusion Ed Beecher, Coperion Corp. , Ramsey, NJ Stefan Gebhardt, Coperion GmbH, Stuttgart Food Extrusion I 2013 I Page 2 Coperion company presentation From history to present From history to present 1879 Foundation of Werner & Pfleiderer. Core business: dough kneading machines UK 1881 Patent for continuous twin screw dough kneader 1957 Twin-screw ZSK 83 1960 ZSK 83 in use for chocolate extrusion 1961 ZPM twin-screw extruder for two stage continuous dough kneading 1972 Deep-cut flighted extruder CONTINUA for food extrusion 1996 Separation of WP bakery- technology 2001 ZSK MEGAvolume introduced 2007 ZSK MEGAvolume PLUS Hermann Werner at Leipziger Messe Exhibition end of 19th century. From history to present 1879 Foundation of Werner & Pfleiderer. Core business: dough kneading machines UK 1881 Patent for continuous twin screw dough kneader 1957 Twin-screw ZSK 83 1960 ZSK 83 in use for chocolate extrusion 1961 ZPM twin-screw extruder for two stage continuous dough kneading 1972 Deep-cut flighted extruder CONTINUA for food extrusion 1996 Separation of WP bakery- technology 2001 ZSK MEGAvolume introduced 2007 ZSK MEGAvolume PLUS From history to present 1879 Foundation of Werner & Pfleiderer. Core business: dough kneading machines UK 1881 Patent for continuous twin screw dough kneader 1957 Twin-screw ZSK 83 1960 ZSK 83 in use for chocolate extrusion 1961 ZPM twin-screw extruder for two stage continuous dough kneading 1972 Deep-cut flighted extruder CONTINUA for food extrusion 1996 Separation of WP bakery- technology 2001 ZSK MEGAvolume introduced 2007 ZSK MEGAvolume PLUS ZSK 83 for chocolate extrusion From history to present 1879 Foundation of Werner & Pfleiderer. Core business: dough kneading machines UK 1881 Patent for continuous twin screw dough kneader 1957 Twin-screw ZSK 83 1960 ZSK 83 in use for chocolate extrusion 1961 ZPM twin-screw extruder for two stage continuous dough kneading 1972 Deep-cut flighted extruder CONTINUA for food extrusion 1996 Separation of WP bakery- technology 2001 ZSK MEGAvolume introduced 2007 ZSK MEGAvolume PLUS ZPM 160 – 320/ 1280 From history to present 1879 Foundation of Werner & Pfleiderer. Core business: dough kneading machines UK 1881 Patent for continuous twin screw dough kneader 1957 Twin-screw ZSK 83 1960 ZSK 83 in use for chocolate extrusion 1961 ZPM twin-screw extruder for two stage continuous dough kneading 1972 Deep-cut flighted extruder CONTINUA for food extrusion 1996 Separation of WP bakery- technology 2001 ZSK MEGAvolume introduced 2007 ZSK MEGAvolume PLUS CONTINUA 37 lab extruder From history to present 1879 Foundation of Werner & Pfleiderer. Core business: dough kneading machines UK 1881 Patent for continuous twin screw dough kneader 1957 Twin-screw ZSK 83 1960 ZSK 83 in use for chocolate extrusion 1961 ZPM twin-screw extruder for two stage continuous dough kneading 1972 Deep-cut flighted extruder CONTINUA for food extrusion 1996 WP bakery – split into two (2) sep. companies 2001 ZSK MEGAvolume introduced 2007 ZSK MEGAvolume PLUS From history to present 1879 Foundation of Werner & Pfleiderer. Core business: dough kneading machines UK 1881 Patent for continuous twin screw dough kneader 1957 Twin-screw ZSK 83 1960 ZSK 83 in use for chocolate extrusion 1961 ZPM twin-screw extruder for two stage continuous dough kneading 1972 Deep-cut flighted extruder CONTINUA for food extrusion 1996 Separation of WP bakery- technology 2001 ZSK MEGAvolume introduced 2007 ZSK MEGAvolume PLUS with higher torque 2013 ZSK MEGAVolume, 27 mm lab machine Deep-cut flights – small crests – large free volume Company history Werner & Pfleiderer Waeschle 1879 1957 Foundation Werner & Pfleiderer First ZSK twin screw extruder 1900 1955 Foundation Waeschle Bulk materials processing in the plastics industry 2001 2007/2008 Merger to form the Coperion Group Realization of the world´s largest plants for polyolefin production 2002 Hartmann Acquisition and integration into the Coperion Group Acquisition and integration into the Coperion Group PELL-TEC (pelletizing equipment) Weicom (packaging 2007 2004 Keya Food Extrusion I 2013 I Page 11 2008 ZSK NT development machines) Brand consolidation / merger to form Coperion 2012 Hillenbrand, Inc. acquires Coperion 2010 Successful launch of ZSK Mc18 series Coperion part of the Process Equipment Group Production and assembly locations Coperion, Ramsey (USA) Coperion, Wytheville (USA) Food Extrusion I 2013 I Page 12 Coperion, Stuttgart (D) Coperion, Nanjing (CN) Facts and figures Compounding & Extrusion Over 130 years of experience with high shear mixing and kneading processes Pioneering work and continuous development of the closely intermeshing, co-rotating twin-screw extruder Comprehensive product portfolio: from laboratory extruder ZSK 18 MEGAlab to largest extruder ZSK 420 MEGAcompounder Turnkey compounding systems from raw material feeding to downstream pelletizing and handling equipment Throughput rates from 1 kg/h to 100 t/h Food Extrusion I 2013 I Page 13 Facts and figures Key figures of Coperion Extrusion systems installed worldwide, over 10,000 Bulk materials handling systems installed worldwide, over 8,000 Employees worldwide, over 1,900 Network of locations worldwide Food Extrusion I 2013 I Page 14 29 Coperion factories in Germany & USA Structure of production Inhouse manufacturing and assembly of: • • • • • all barrel types all screw element models / versions splined screw shafts discharge parts, die plates and knives control cabinet (assembly) & software design Overhaul of gear boxes, barrels, etc., global services Food Extrusion I 2013 I Page 15 Coperion GmbH Food & Pharma Team Stuttgart & Ramsey Process Edgar Strobel Ed Beecher, Ramsey Uta Kühnen Leona Krzyzanowski Fabian Specht Food Extrusion I 2013 I Page 16 Project Oldrich Lohr Martin Klein Sales Stefan Gebhardt Ed Beecher, Ramsey Viola Niederberger Andreas Weißenberger After Sales Carsten Benz ZSK – twin screw extruder Overview of ZSK series Food & Pharma machines Screw diameter [mm] ZSK Mc18 / compact version 18 ZSK 18 MEGAlab 26 ZSK 26 Mc 32 / 34 ZSK 32 Mc18 / ZSK 32 ZSK MEGAcompounder Mcc18 43 45 ZSK MEGAvolume PLUS / compact version Kombiplast with ZSK MEGAvolume PLUS ZSK 27 Mv KP 26 / 60 ZSK 34 Mv PLUS KP 34 / 100 ZSK 43 Mv PLUS / ZSK 43 Mvc PLUS KP 43 / 150 ZSK 54 Mv PLUS / ZSK 54 Mvc PLUS KP 54 / 150 ZSK 45 Mc18 / ZSK 45 Mcc18 54 58 / 62 ZSK 58 Mc18 / ZSK 58 Mcc18 ZSK 62 Mv PLUS / ZSK 62 Mvc PLUS KP 62 / 200 70 / 76 ZSK 70 Mc18 / ZSK 70 Mcc18 ZSK 76 Mv PLUS / ZSK 76 Mvc PLUS KP 76 / 250 82 ZSK 82 Mc18 / ZSK 82 Mcc18 92 / 98 ZSK 92 Mc18 ZSK 98 Mv PLUS KP 98 / 300 106 ZSK 106 Mc18 119 / 125 ZSK 119 Mc18 ZSK 125 Mv PLUS KP 125 / 350 133 ZSK 133 Mc PLUS 177 ZSK 177 Mc 250 ZSK 250 Mc 320 ZSK 320 Mc 350 ZSK 350 Mc 380 ZSK 380 Mc 420 ZSK 420 Mc Food I 24/04/2014 I Seite 18 ZSK 248 Mv compact version: with attached control cabinet ZSK – twin screw extruder Main components motor Food Extrusion I 2013 I Page 19 safety clutch gear box lantern processing section die plate and pelletizer Food grade Installation of ZSK Main components in full grade food version IP 65 / stainless steel HMI stainless steel gearbox lantern stainless steel barrels stainless steel clutch guard stainless steel junction boxes Food Extrusion I 2013 I Page 20 sealed machine bed in stainless steel or zinc coated Modular design of process section Barrels and screw elements Open Combi Barrel (Feed) vent Barrel Closed Barrel Side Feeder connection Open (Degassing) Barrel Closed Barrel Closed Barrel vacuum Screws in modular design with elements on a splined shaft Barrels coupled by flanges or tie-rods Each extruder is individually designed with its unique combination of component parts Food Extrusion I 2013 I Page 21 Metallurgical competence – Abrasion and corrosion resistant process section Liners in a barrel (various materials possible – cast iron; stainless steel, etc..) Powder metallurgical element with wear and corrosion resistant layer with softer core Screw elements Nitrided Crest welded Through-hardened Stainless Steel Powder metallurgical Food I 24/04/2014 I Seite 23 ZSK – evolution of torque and volume ZSK Standard Do / Di = 1,22 Md / a3 = 5,0 Nm/cm3 ZSK variable Do / Di = 1,44 Md / a3 = 5,0 Nm/cm3 ZSK Supercompounder Do / Di = 1,55 Md / a3 = 8,7 Nm/cm3 Increase of free volume (100%) and of specific torque Continua Do / Di = 1,71 Md / a3 = 2,6 Nm/cm3 Increase of free volume (additional 40%) ZSK MEGAcompounder Do / Di = 1,55 Md / a3 = 11,3 Nm/cm3 ZSK MEGAcompounder PLUS Do / Di = 1,55 Md / a3 = 13,5 Nm/cm3 Increase of torque ZSK Mc18 Do / Di = 1,55 Md / a3 = 18 Nm/cm3 Increase of torque Food Extrusion I 2013 I Page 24 ZSK MEGAvolume Do / Di = 1,80 Md / a3 = 8,7 Nm/cm3 ZSK MEGAvolume PLUS Do / Di = 1,80 Md / a3 = 11,3 Nm/cm3 Specific free volume and specific energy input 220 Q x 104 ns x a3 Capacity determining: specific volume L/h 1/ min x cm3 1.80 OD/ID 210 200 1.70 OD/ID 190 180 170 160 1.55 OD/ID 150 140 130 120 110 100 90 80 70 60 50 0 0,04 0,08 0,12 0,16 0,20 0,24 0,28 0,32 Quality determining: specific mechanical energy [ kWh / kg ] 2014 Specific Energy Input for 1.55 OD/ID and 1.80 OD/ID. Polyolefins ABS Thermoplastic Elastomers TPE Polymer Blends (PC/ABS. PC/PBT) Filling, Reenforcing of PA, PP, PBT Masterbatch Wood Plastic Profiles Direct Extrusion (PET, PLA, PP-Folien) Biologically degradable plastics (TPS) PP/Hollow glass PVC Cable, HFFR Rubber Polymerisation (PU, POM) Powder Coating Animal Feed Cereals, Starch Catalyst Carrier Adhesives Sealants 0 0.05 0.1 0.15 0.2 0.25 Specific Energy Input [kWh/kg] 2014 0.3 0.35 Food pelletizer ZGF 70 New hygienic design axial vernier adjustment for knives easy sampling simplified process startup and stop easy cleaning Food Extrusion I 2013 I Page 27 Food pelletizer / ZGF ZSK – twin screw extruder Coperion extrusion system: Da/Di ratio: With a Da/Di ratio of 1,8 it´s the industry‘s largest free volume available in a twin screw extruder; More free volume => more capacity => higher productivity Safer venting operation Higher output rates at lower stock temperatures Side degassing ZSEG: State of the art in other extrusion processes, the side degassing gives also the food industry advantages in production safety and operation security / e.g. pet food processes. Side feeding via side feeder: Capacity increases also with difficult raw materials are possible with using a side feeder in barrel one or two of the extruder; up to 30 % increase or more. Food Extrusion I 2013 I Page 29 ZSK – twin screw extruder Coperion extrusion system: FET: Feed EnhancementTechnology – for a significant increase of feeding capacity when processing powder materials (factor 2 x ) => increased capacity at same screw speed / reduces SEI => reducing screw speed at same capacity Direct steam injection: Due to the high free volume of the extruder we have possibilities to inject much more steam directly in the process and maybe leave out the preconditioning step, to save cleaning time, reduce danger of product contamination World wide service network With over 30 units worldwide Coperion and Coperion KTron are always there where the customer is – help and service nearby. Food Extrusion I 2013 I Page 30 ZSK – twin screw extruder Coperion extrusion system: Materials of construction: Various possibilities for wear and corrosion resistant materials Food grade material for barrels and screw elements – running in various machine sizes in food applications References in the food industry: More than 250 extruders running worldwide for food applications Cereals, pet food, snacks/sweets, starches, texturized protein, etc.. Food Extrusion I 2013 I Page 31 Advantages of Food Extrusion ZSK compared with single screw extruder conveying mixing dependency on die design dependency on particle size steady processing variability of residence time degassing self-wiping throughput range moisture of raw material (max.) fat content of raw material (max.) product quality investment operational costs Food Extrusion Seminar - Food processing with ZSK I 23.-24.04.2013 I Page 32 Single Screw ZSK drag flow bad high high low wide middle no small low low unsteady low high forced drag flow good low low high small good good wide high high steady high low Feed Section Design: Feed Enhancement Technology (FET): Solids conveying is improved by applying vacuum in the feed zone to a wall section which is porous and permeable to gas. Air FET insert vacuum Filter cake: densified powder Effects: • air is removed higher bulk density • friction is changed in the area of insert FET: Working Principle Friction and higher bulk density increase the conveying angle: Conveying angle FET not active low Angle of conveying approx. 20° FET active Angle of conveying approx. 40° high Q=F*H*n*e* h*g capacity Installation Options for FET In the feed section of the TSE upstream of the feeding point In the feed section of the TSE downstream of feeding point TSE FET can only be used for solids conveying! In the side feeder FET Configuration: Main Feed Additive Powders Bulk Preblend FET Experience with FET – ZSK wheat starch with 8% water added Extruder: •ZSK 50 Mc 700 600 + 140% * Md 69% Throughput [kg/h] 500 400 + 215% -90% of all particle between 30-40 µm -10% of all particle between 2-15 µm Md 79% 300 200 100 Md 38% Md 37% 0 300 Rpm without FET with FET - ZSK Wheat starch: • Bulk density: 0,55 g/cm3 • Particle size distribution: 600 Rpm * (no maximum) Experience: FET Configuration for Main Feed Production experience: Fine powder (wheat starch) 50 mm Twin screw Capacity increase From 214 kg/hr to 550 kg/hr Typical setup for FET: Downstream feeding Encapsulation Process Encapsulated Ingredient Minor Additives Food Resin FET Specific capacity [kg/h per revolution] Advantages of FET: higher capacity even with finer powders with FET torque or feed limit without FET feed limit Particle size d50 [µm] Advantages of FET: reduction of specific energy (SEI) SEI can be reduced by: • Increasing capacity at same screw speed • Reducing screw speed at same capacity Capacity [kg/h] SEI4 SEI4 < SEI1 SEI3 with FET SEI2 SEI1 without FET screw speed [min-1] FET Characteristics If necessary, filter membrane can be easily replaced Insert can be cooled to avoid melting of filter cake components Required vacuum depends on particle size and shape of the product Not suitable for melts or “wet“ products Food applications A wide range of extruded products Coperion GmbH Food & pharma applications Starch based Sugar based Protein based • Breakfast Cereals • Snacks • Modified Starches • Confectionary • Microencapsulation • Pet food / Pet treats • Feed / Aquatic feed • Texturized protein Food Extrusion I 2013 I Page 44 Others • Pharmaceuticals • Nutraceuticals • Flavours • Herbs / Spices Success stories Encapsulation of flavor (2011) Task • encapsulate fluid flavour within a carbohydrate matrix to improve shelf life and processability Process challenge • form small droplets • homogeneous distribution Solution • ZSK 76 MEGAvolume PLUS allows very good mixing and dispersing for homogeneous distribution no additional drying needed (advantage for sensitive ingredients) Food Extrusion I 2013 I Page 46 Presidential Initiative Banana Industrial Development (PIBID) Instant Matooke porridge (2012) Task • precooking of plantains to produce an instant porridge which offers a long shelf life and digestibility for ill and weak people Process challenge • produce a flour for an instant Matooke porridge which could even be prepared with cold water Solution • ZSK 54 MEGAvolume PLUS • modifying the flour by precooking and stopping the enzyme activity Food Extrusion I 2013 I Page 47 Cereal snack with fresh fruit / vegetable (2012) Task • healthy snacks containing grain flours and fresh fruits / vegetable Process Challenge • pleasant snack texture with high moisture ingredients Solution • ZSK 54 MEGAvolume PLUS • moisture reduction by vacuum degassing and product expansion at the die Food Extrusion I 2013 I Page 48 Food extrusion Process examples Cereals Process Upstream Equipment / Extrusion Dosing / Raw Material Intake Mixing / Kneading / Plastification Cooking (Maillard) Cutting Food Extrusion I 2013 I Page 50 Downstream Equipment Drying / Roasting / Cooling Coating Drying / Cooling Packaging Direct Expanded Breakfast Cereals flow chart flour / premix water homogeneous mixing kneading / plasticizing cooking forming / cutting shaped expanded extrudate cooling, drying, roasting, coating etc. Food Extrusion Seminar - Food processing with ZSK I 23.-24.04.2013 I Page 51 additives Cereals Applications and advantages Advantages • high free volume (Mv) - better intake and higher throughput • recipe flexibility • independent from particle size of the raw materials • high bran concentration • high fat concentration • direct steam injection • direct syrup injection • flexible in die design / product shape Applications • breakfast cereals • snacks … Food Extrusion I 2013 I Page 52 Encapsulation of flavours Process Upstream Equipment / Extrusion Basic material feeding / Raw Material Intake Mixing / Melting / Plastification Liquid flavour feeding / Dispersing / Cutting Food Extrusion I 2013 I Page 53 Downstream Equipment Drying / Cooling Packaging Encapsulation of flavours Applications and advantages Process • dispersion of small droplets of liquid flavours into a suitable matrix (e.g. sugar, food resin) Advantages • extend products’ shelf life due to the protection of oxygen sensitive flavours • improved handling • better solubility Applications • tea mixtures • confectionary • bakery products • soft drinks … Food Extrusion I 2013 I Page 54 Dry texturized protein Process Upstream Equipment / Extrusion Dosing / Raw Material Intake Mixing / Kneading / Texturizing Cutting Food Extrusion I 2013 I Page 55 Downstream Equipment Drying / Cooling Packaging Direct Expanded Low Moisture Protein flow chart protein powder water / steam homogeneous mixing kneading / plasticizing / cooking forming / pelletizing shaped extrudate drying Food Extrusion Seminar - Food processing with ZSK I 23.-24.04.2013 I Page 56 Dry texturized protein Applications & advantages Process • formation of aligned fibres – similar to the texture of muscle flesh (mouthfeel similar to meat) • adding colours and flavours leads to meat like appearance and taste Advantages • sterilized product • attractive for vegan, vegetarian and non-vegetarian people, pets • cost saving production compared to animal protein Applications: • instant gravies and soups • vegetarian spreads • meat extender • meat substitute Food Extrusion I 2013 I Page 57 Pet Treats flow chart flour / powder premix plasticizer acids meat slurry homogeneous mixing kneading / plasticizing / cooking vacuum degassing forming / pelletizing shaped strand cooling / drying cutting Food Extrusion Seminar - Food processing with ZSK I 23.-24.04.2013 I Page 58 steam Pet food / fish feed Applications & advantages Process • separate feeders for meat / fish waste, flour, fat and water • direct steam injection • die face pelletizing for dry pet food and fish feed Advantages • high fat contents possible • fresh meat / fish waste can be used • very good bioavailability of nutritive substances • sinking / floating properties exactly adjustable • very good mixing of all components Applications: • dry pet food • pet treats • fish feed Food Extrusion I 2013 I Page 59 Thank you very much for your attention. Food Extrusion I 2013 I Page 60
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