ANIMAL-DERIVED AMINO ACID POWDER MANUFACTURING TECHNOLOGY ENCYCLOPEDIA
Animal-derived amino acid powder manufacturing involves the controlled processing of animal-based protein raw materials through hydrolysis, purification, concentration, drying and quality control stages. Animal-derived amino acid powder manufacturing technology encyclopedia explains the industrial production process, required equipment, operating conditions and key quality parameters for manufacturing animal-derived amino acid powder.
| CHAPTER / SECTION | TITLE | PAGE |
| CHAPTER 1 | PRODUCT IDENTITY, INDUSTRIAL DEFINITION AND COMMERCIAL MANUFACTURING OBJECTIVES | 1 |
| 1.1 | Definition of Animal-Derived Amino Acid Powder | 1 |
| 1.2 | Industrial Position of Hydrolyzed Animal Protein Products | 1 |
| 1.3 | Free Amino Acids, Peptides and Hydrolyzed Protein Fractions | 3 |
| 1.4 | Animal-Derived Amino Acid Powder versus Protein Meal | 3 |
| 1.5 | Animal-Derived Amino Acid Powder versus Protein Hydrolysate Liquid | 4 |
| 1.6 | Animal-Derived Amino Acid Powder versus Fish Amino Acid Products | 4 |
| 1.7 | Agricultural, Feed, Technical and Specialty Product Grades | 5 |
| 1.8 | Protein-Origin Claims and Raw-Material Traceability | 6 |
| 1.9 | Degree of Hydrolysis as a Product-Identity Parameter | 7 |
| 1.10 | Amino Nitrogen and Total Nitrogen in Commercial Positioning | 7 |
| 1.11 | Solubility and Powder-Performance Expectations | 7 |
| 1.12 | Ash, Salt and Mineral Content as Grade Differentiators | 8 |
| 1.13 | Color, Odor and Appearance Expectations | 8 |
| 1.14 | Industrial Manufacturing Objectives | 9 |
| 1.15 | From Animal Protein Feedstock to Finished Powder | 10 |
| CHAPTER 2 | ANIMAL PROTEIN FEEDSTOCK CLASSES, SOURCES AND RAW-MATERIAL SELECTION | 12 |
| 2.1 | Blood-Derived Protein Feedstocks | 12 |
| 2.2 | Feather and Keratin-Rich Feedstocks | 12 |
| 2.3 | Hide, Skin and Collagen-Rich Feedstocks | 14 |
| 2.4 | Gelatin and Gelatin-Production Side Streams | 15 |
| 2.5 | Meat-Trimming and Protein-Rich Tissue Streams | 15 |
| 2.6 | Poultry-Processing Protein Streams | 16 |
| 2.7 | Slaughterhouse Protein By-Products | 16 |
| 2.8 | Hydrolyzed Animal Protein Intermediates | 17 |
| 2.9 | Bone-Associated Protein Fractions | 18 |
| 2.10 | High-Fat versus Low-Fat Protein Feedstocks | 18 |
| 2.11 | Fresh versus Dried Feedstock Selection | 19 |
| 2.12 | Single-Source versus Blended Feedstocks | 20 |
| 2.13 | Protein Concentration and Process Yield | 20 |
| 2.14 | Contaminants Affecting Hydrolysis and Purification | 21 |
| 2.15 | Feedstock Selection According to Finished-Product Grade | 22 |
| CHAPTER 3 | RAW-MATERIAL RECEIVING, SAMPLING, STORAGE AND LOT-RELEASE CONTROL | 25 |
| 3.1 | Supplier Qualification | 25 |
| 3.2 | Raw-Material Specification Development | 26 |
| 3.3 | Receiving Inspection | 27 |
| 3.4 | Identification and Lot Coding | 28 |
| 3.5 | Representative Sampling | 28 |
| 3.6 | Moisture Determination | 29 |
| 3.7 | Protein Screening | 30 |
| 3.8 | Fat and Oil Determination | 30 |
| 3.9 | Ash and Mineral Screening | 31 |
| 3.10 | Foreign-Material Inspection | 32 |
| 3.11 | Microbiological Condition of Incoming Feedstock | 32 |
| 3.12 | Odor and Deterioration Indicators | 33 |
| 3.13 | Storage Temperature and Time Control | 33 |
| 3.14 | Raw-Material Blending before Processing | 34 |
| 3.15 | RELEASE, HOLD and REJECT Decisions | 35 |
| CHAPTER 4 | ANIMAL PROTEIN CHEMISTRY, AMINO ACID COMPOSITION AND HYDROLYSIS BEHAVIOR | 39 |
| 4.1 | Protein Structure Relevant to Industrial Hydrolysis | 39 |
| 4.2 | Peptide Bonds and Hydrolysis Reactions | 40 |
| 4.3 | Essential and Non-Essential Amino Acids | 41 |
| 4.4 | Collagen-Derived Amino Acid Profiles | 41 |
| 4.5 | Keratin-Derived Amino Acid Profiles | 42 |
| 4.6 | Blood-Protein Amino Acid Profiles | 43 |
| 4.7 | Protein Molecular Size and Hydrolysis Resistance | 44 |
| 4.8 | Disulfide Bonds in Keratin Materials | 44 |
| 4.9 | Denaturation before Hydrolysis | 45 |
| 4.10 | Peptides versus Free Amino Acids | 45 |
| 4.11 | Amino Nitrogen Development | 46 |
| 4.12 | Nitrogen Balance during Hydrolysis | 47 |
| 4.13 | Racemization and Amino Acid Degradation Risks | 48 |
| 4.14 | Heat-Sensitive Amino Acids | 49 |
| 4.15 | Chemistry-Based Process-Route Selection | 50 |
| CHAPTER 5 | PLANT LAYOUT, PROCESS FLOW, HYGIENIC ZONING AND EQUIPMENT ARCHITECTURE | 54 |
| 5.1 | Overall Manufacturing Flow | 54 |
| 5.2 | Raw-Material Receiving Zone | 55 |
| 5.3 | Pretreatment Zone | 55 |
| 5.4 | Hydrolysis Reactor Area | 57 |
| 5.5 | Chemical-Preparation Area | 58 |
| 5.6 | Solid–Liquid Separation Area | 58 |
| 5.7 | Purification Area | 59 |
| 5.8 | Concentration Area | 59 |
| 5.9 | Drying and Powder-Handling Area | 60 |
| 5.10 | Packaging Area | 61 |
| 5.11 | Finished-Goods Warehouse | 62 |
| 5.12 | Waste and By-Product Handling Area | 62 |
| 5.13 | Clean and Dirty Process-Line Segregation | 63 |
| 5.14 | Material-Flow and Personnel-Flow Design | 64 |
| 5.15 | Equipment Capacity Matching across the Plant | 66 |
| CHAPTER 6 | FEEDSTOCK CLEANING, SIZE REDUCTION, DEFATTING AND PRE-HYDROLYSIS PREPARATION | 70 |
| 6.1 | Removal of Foreign Materials | 70 |
| 6.2 | Washing of Fresh Protein Feedstocks | 71 |
| 6.3 | Draining and Dewatering | 71 |
| 6.4 | Cutting and Shredding | 73 |
| 6.5 | Crushing and Milling of Dry Materials | 73 |
| 6.6 | Particle-Size Selection | 75 |
| 6.7 | Feather Size Reduction | 75 |
| 6.8 | Skin and Hide Cutting | 76 |
| 6.9 | Blood-Derived Feed Preparation | 76 |
| 6.10 | Fat Separation and Defatting | 77 |
| 6.11 | Mechanical Pressing | 78 |
| 6.12 | Thermal Pretreatment | 78 |
| 6.13 | Feed Homogenization | 79 |
| 6.14 | Pretreatment Yield Determination | 80 |
| 6.15 | Prepared-Feed Release to Hydrolysis | 81 |
| CHAPTER 7 | HYDROLYSIS ROUTE SELECTION: ACID, ALKALINE, ENZYMATIC AND COMBINED PROCESSES | 85 |
| 7.1 | Purpose of Protein Hydrolysis | 85 |
| 7.2 | Acid Hydrolysis Route | 86 |
| 7.3 | Alkaline Hydrolysis Route | 86 |
| 7.4 | Enzymatic Hydrolysis Route | 87 |
| 7.5 | Combined Chemical–Enzymatic Hydrolysis | 88 |
| 7.6 | Feedstock Compatibility with Each Route | 89 |
| 7.7 | Free Amino Acid Yield versus Peptide Retention | 91 |
| 7.8 | Processing Time Comparison | 91 |
| 7.9 | Reagent Consumption | 92 |
| 7.10 | Salt Generation | 92 |
| 7.11 | Amino Acid Degradation Risks | 93 |
| 7.12 | Color and Odor Consequences | 94 |
| 7.13 | Downstream Purification Burden | 95 |
| 7.14 | Production Cost Comparison | 95 |
| 7.15 | Route Selection according to Final Product Grade | 96 |
| CHAPTER 8 | ACID HYDROLYSIS: REACTOR CHARGING, ACID ADDITION AND PROTEIN CONVERSION | 101 |
| 8.1 | Acid-Hydrolysis Process Architecture | 101 |
| 8.2 | Feedstock-to-Water Ratio | 103 |
| 8.3 | Reactor Charging Sequence | 104 |
| 8.4 | Acid Selection | 105 |
| 8.5 | Acid Concentration Preparation | 106 |
| 8.6 | Controlled Acid Addition | 107 |
| 8.7 | Mixing during Acidification | 108 |
| 8.8 | Temperature Increase | 109 |
| 8.9 | Hydrolysis Reaction Development | 109 |
| 8.10 | Time Control | 110 |
| 8.11 | Sampling during Hydrolysis | 110 |
| 8.12 | Protein Conversion Monitoring | 111 |
| 8.13 | Avoiding Local Acid Overexposure | 112 |
| 8.14 | Amino Acid Degradation Control | 113 |
| 8.15 | Acid-Hydrolysate Release Criteria | 114 |
| CHAPTER 9 | ALKALINE HYDROLYSIS OF COLLAGEN, KERATIN AND DIFFICULT ANIMAL PROTEINS | 121 |
| 9.1 | Alkali-Hydrolysis Process Principle | 121 |
| 9.2 | Alkali Selection | 122 |
| 9.3 | Caustic-Solution Preparation | 123 |
| 9.4 | Feed Wetting before Alkali Addition | 125 |
| 9.5 | Controlled Alkali Charging | 126 |
| 9.6 | pH Development | 127 |
| 9.7 | Heat-Up and Reaction Control | 128 |
| 9.8 | Keratin Bond Disruption | 128 |
| 9.9 | Collagen and Connective-Tissue Hydrolysis | 130 |
| 9.10 | Mixing Requirements | 131 |
| 9.11 | Solids Disintegration | 132 |
| 9.12 | Reaction Endpoint Monitoring | 132 |
| 9.13 | Excess Alkali and Salt Burden | 134 |
| 9.14 | Amino Acid Damage under Severe Conditions | 135 |
| 9.15 | Alkaline-Hydrolysate Transfer Criteria | 137 |
| CHAPTER 10 | ENZYMATIC HYDROLYSIS AND CONTROLLED PEPTIDE PRODUCTION | 142 |
| 10.1 | Industrial Protease Hydrolysis Principle | 142 |
| 10.2 | Protease Selection | 143 |
| 10.3 | Endoprotease and Exoprotease Functions | 144 |
| 10.4 | Feedstock Preparation for Enzymatic Treatment | 145 |
| 10.5 | Enzyme-Dose Calculation | 146 |
| 10.6 | pH Preparation | 147 |
| 10.7 | Temperature Preparation | 148 |
| 10.8 | Enzyme Addition Sequence | 148 |
| 10.9 | Hydrolysis-Time Control | 149 |
| 10.10 | Degree-of-Hydrolysis Monitoring | 150 |
| 10.11 | Peptide-Size Control | 151 |
| 10.12 | Enzyme Inactivation | 152 |
| 10.13 | Recovery of Enzymatic Hydrolysate | 152 |
| 10.14 | Enzyme Cost versus Product Value | 153 |
| 10.15 | Enzymatic-Route Release Criteria | 154 |
| CHAPTER 11 | SEQUENTIAL AND COMBINED HYDROLYSIS FOR HIGH-CONVERSION PRODUCTS | 163 |
| 11.1 | Why Sequential Hydrolysis Is Used | 163 |
| 11.2 | Thermal Pretreatment followed by Enzymatic Hydrolysis | 164 |
| 11.3 | Alkali Pretreatment followed by Enzymatic Hydrolysis | 165 |
| 11.4 | Acid Treatment followed by Enzyme Finishing | 165 |
| 11.5 | Multi-Enzyme Hydrolysis | 167 |
| 11.6 | First-Stage Endpoint | 167 |
| 11.7 | Intermediate pH Adjustment | 168 |
| 11.8 | Second-Stage Charging | 169 |
| 11.9 | Intermediate Solids Removal | 169 |
| 11.10 | Peptide-to-Free-Amino-Acid Balance | 170 |
| 11.11 | Reagent Carryover | 170 |
| 11.12 | Yield Improvement versus Added Complexity | 172 |
| 11.13 | Product Damage Risk | 172 |
| 11.14 | Combined-Route Economics | 173 |
| 11.15 | Selection of the Commercial Optimum | 174 |
| CHAPTER 12 | HYDROLYSIS REACTORS, MIXING, HEAT TRANSFER AND BATCH OPERATION | 181 |
| 12.1 | Reactor Vessel Selection | 181 |
| 12.2 | Working Volume and Freeboard | 183 |
| 12.3 | Reactor Construction Materials | 184 |
| 12.4 | Agitator Selection | 185 |
| 12.5 | Impeller Configuration | 185 |
| 12.6 | Solids Suspension | 187 |
| 12.7 | Torque and Motor Load | 187 |
| 12.8 | Heating Systems | 188 |
| 12.9 | Cooling Systems | 189 |
| 12.10 | Temperature-Sensor Positioning | 189 |
| 12.11 | pH-Sensor Positioning | 190 |
| 12.12 | Chemical-Injection Points | 191 |
| 12.13 | Foam and Headspace Management | 191 |
| 12.14 | Batch-Record Requirements | 193 |
| 12.15 | Reactor-Cycle Capacity Calculation | 194 |
| CHAPTER 13 | HYDROLYSIS ENDPOINT, DEGREE OF HYDROLYSIS, AMINO NITROGEN AND IN-PROCESS SAMPLING | 203 |
| 13.1 | Definition of Hydrolysis Endpoint | 203 |
| 13.2 | Time-Based Endpoint Limitations | 204 |
| 13.3 | Visual Reaction Indicators | 204 |
| 13.4 | Soluble-Solids Development | 205 |
| 13.5 | Soluble-Nitrogen Development | 206 |
| 13.6 | Amino-Nitrogen Monitoring | 207 |
| 13.7 | Degree-of-Hydrolysis Concept | 207 |
| 13.8 | Peptide-Size Changes | 208 |
| 13.9 | Residual Insoluble Protein Testing | 209 |
| 13.10 | Standardized Sample Clarification | 210 |
| 13.11 | pH and Temperature Recording | 210 |
| 13.12 | Marginal-Yield Evaluation | 211 |
| 13.13 | Over-Hydrolysis Risk | 212 |
| 13.14 | HOLD, CONTINUE and RELEASE Decisions | 212 |
| 13.15 | Hydrolysis-Campaign Performance Review | 214 |
| CHAPTER 14 | PRIMARY SOLID–LIQUID SEPARATION AND UNHYDROLYZED RESIDUE REMOVAL | 221 |
| 14.1 | Hydrolysate Transfer to Separation | 221 |
| 14.2 | Settling Behavior | 222 |
| 14.3 | Coarse Screening | 223 |
| 14.4 | Decanter Centrifuge Operation | 223 |
| 14.5 | Filter Press Operation | 224 |
| 14.6 | Screw Press Applications | 225 |
| 14.7 | Wet-Cake Formation | 226 |
| 14.8 | Mother-Liquor Entrapment | 227 |
| 14.9 | Cake-Washing Strategy | 227 |
| 14.10 | Product Loss in Wet Residue | 228 |
| 14.11 | Insoluble-Protein Recovery | 229 |
| 14.12 | Mineral and Bone Residue Removal | 230 |
| 14.13 | Separation Throughput | 230 |
| 14.14 | Dry-Solids Recovery Calculation | 232 |
| 14.15 | Clarified Hydrolysate Release | 232 |
| CHAPTER 15 | FINE CLARIFICATION, FAT REMOVAL, OIL SEPARATION AND SUSPENDED-SOLIDS CONTROL | 239 |
| 15.1 | Secondary Clarification Objective | 239 |
| 15.2 | Residual Protein Fines | 240 |
| 15.3 | Fat and Oil Carryover | 240 |
| 15.4 | Gravity Fat Separation | 241 |
| 15.5 | Disc-Stack Centrifugation | 242 |
| 15.6 | Fine Decanting | 243 |
| 15.7 | Guard Filtration | 243 |
| 15.8 | Depth Filtration | 244 |
| 15.9 | Filter-Aid Considerations | 245 |
| 15.10 | Turbidity Measurement | 245 |
| 15.11 | Total Suspended Solids | 246 |
| 15.12 | Filter Differential Pressure | 247 |
| 15.13 | Product Loss during Polishing | 247 |
| 15.14 | Clarification Endpoint | 249 |
| 15.15 | Low-Turbidity Hydrolysate Release | 249 |
| CHAPTER 16 | DEODORIZATION, COLOR CONTROL, ACTIVATED CARBON AND ORGANIC-IMPURITY REDUCTION | 257 |
| 16.1 | Origin of Animal-Protein Odor | 257 |
| 16.2 | Origin of Dark Color | 258 |
| 16.3 | Thermal Color Formation | 259 |
| 16.4 | Activated-Carbon Treatment | 260 |
| 16.5 | Carbon Dose Selection | 261 |
| 16.6 | Contact Time | 262 |
| 16.7 | Temperature during Adsorption | 262 |
| 16.8 | Mixing Control | 263 |
| 16.9 | Removal of Activated Carbon | 264 |
| 16.10 | Product Adsorption Loss | 265 |
| 16.11 | Alternative Adsorbent Technologies | 266 |
| 16.12 | Oxidation Risks | 267 |
| 16.13 | Odor Reduction without Product Damage | 267 |
| 16.14 | Color Specification Development | 268 |
| 16.15 | Purified-Liquor Sensory Release | 269 |
| CHAPTER 17 | ASH, SALT, CHLORIDE, SODIUM, POTASSIUM AND MINERAL-IMPURITY CONTROL | 278 |
| 17.1 | Total Ash versus Insoluble Minerals | 278 |
| 17.2 | Naturally Occurring Mineral Burden | 279 |
| 17.3 | Acid-Derived Salt Formation | 280 |
| 17.4 | Alkali-Derived Salt Formation | 281 |
| 17.5 | Sodium Balance | 282 |
| 17.6 | Potassium Balance | 283 |
| 17.7 | Chloride Balance | 283 |
| 17.8 | Sulfate Balance | 284 |
| 17.9 | Calcium and Magnesium | 284 |
| 17.10 | Iron and Trace Metals | 285 |
| 17.11 | Conductivity as a Process Fingerprint | 286 |
| 17.12 | Ash Prediction before Drying | 287 |
| 17.13 | Technical versus Low-Ash Grades | 288 |
| 17.14 | Required Salt-Removal Calculation | 289 |
| 17.15 | Release to Desalting/Purification | 291 |
| CHAPTER 18 | AMINO ACID LIQUOR PURIFICATION, DESALTING AND SELECTIVE MEMBRANE PROCESSING | 297 |
| 18.1 | Purification Objectives | 297 |
| 18.2 | Adsorbent-Resin Applications | 298 |
| 18.3 | Ion-Exchange Applications | 299 |
| 18.4 | Cation Exchange | 300 |
| 18.5 | Anion Exchange | 300 |
| 18.6 | Membrane Pretreatment | 302 |
| 18.7 | Ultrafiltration | 302 |
| 18.8 | Nanofiltration | 303 |
| 18.9 | Diafiltration | 304 |
| 18.10 | Electrodialysis | 305 |
| 18.11 | Amino Acid Retention versus Salt Removal | 306 |
| 18.12 | Conductivity Reduction | 307 |
| 18.13 | Membrane Fouling | 308 |
| 18.14 | Purification Yield | 309 |
| 18.15 | Grade-Specific Purification Endpoint | 310 |
| CHAPTER 19 | AMINO ACID LIQUOR STANDARDIZATION, pH, SOLIDS, AMINO NITROGEN AND COMPOSITION CONTROL | 319 |
| 19.1 | Standardization-Tank Operation | 319 |
| 19.2 | Compatible Batch Blending | 320 |
| 19.3 | Total Solids | 321 |
| 19.4 | Organic Solids | 321 |
| 19.5 | Total Nitrogen | 322 |
| 19.6 | Amino Nitrogen | 322 |
| 19.7 | Protein/Peptide Fraction | 323 |
| 19.8 | Free Amino Acid Content | 323 |
| 19.9 | Ash | 324 |
| 19.10 | Conductivity | 324 |
| 19.11 | pH | 325 |
| 19.12 | Dry-Basis Calculations | 326 |
| 19.13 | Water Adjustment | 327 |
| 19.14 | Predicted Powder Composition | 328 |
| 19.15 | Release to Concentration | 329 |
| CHAPTER 20 | VACUUM CONCENTRATION AND HIGH-SOLIDS AMINO ACID LIQUOR PRODUCTION | 336 |
| 20.1 | Why Pre-Concentration Is Required | 336 |
| 20.2 | Evaporator Selection | 337 |
| 20.3 | Falling-Film Evaporation | 338 |
| 20.4 | Forced-Circulation Evaporation | 339 |
| 20.5 | Multiple-Effect Evaporation | 339 |
| 20.6 | Vacuum Generation | 340 |
| 20.7 | Feed Preheating | 340 |
| 20.8 | Boiling-Temperature Control | 341 |
| 20.9 | Water-Removal Calculation | 341 |
| 20.10 | Solids Build-Up | 342 |
| 20.11 | Viscosity Development | 343 |
| 20.12 | Foam Control | 344 |
| 20.13 | Entrainment and Condensate Loss | 344 |
| 20.14 | Concentration Endpoint | 346 |
| 20.15 | Concentrate Release to Drying | 346 |
| CHAPTER 21 | DRYING-ROUTE SELECTION AND DRYER-FEED CONDITIONING | 353 |
| 21.1 | Spray Drying versus Alternative Drying Routes | 353 |
| 21.2 | Drum Drying Considerations | 355 |
| 21.3 | Vacuum Drying Considerations | 355 |
| 21.4 | Freeze-Drying Reference Applications | 356 |
| 21.5 | Industrial Spray-Dryer Selection | 356 |
| 21.6 | Dryer-Feed Tank | 357 |
| 21.7 | Feed Homogenization | 357 |
| 21.8 | Feed-Solids Adjustment | 358 |
| 21.9 | Feed Temperature | 358 |
| 21.10 | Viscosity Control | 359 |
| 21.11 | Deaeration | 360 |
| 21.12 | Foam Control | 361 |
| 21.13 | Final Guard Filtration | 361 |
| 21.14 | Feed-Pump Compatibility | 361 |
| 21.15 | Dryer-Feed Release | 362 |
| CHAPTER 22 | SPRAY DRYING: ATOMIZATION, THERMAL CONTROL AND POWDER FORMATION | 370 |
| 22.1 | Spray-Drying Process Architecture | 370 |
| 22.2 | Pressure-Nozzle Atomization | 371 |
| 22.3 | Rotary Atomization | 372 |
| 22.4 | Two-Fluid Atomization | 372 |
| 22.5 | Droplet-Size Development | 373 |
| 22.6 | Drying-Air Preparation | 374 |
| 22.7 | Inlet Temperature | 374 |
| 22.8 | Outlet Temperature | 375 |
| 22.9 | Feed-Rate Control | 376 |
| 22.10 | Water-Evaporation Capacity | 377 |
| 22.11 | Particle Formation | 377 |
| 22.12 | Powder Moisture Control | 378 |
| 22.13 | Wall Deposition and Stickiness | 378 |
| 22.14 | Cyclone and Bag-Filter Recovery | 380 |
| 22.15 | Spray-Dryer Shutdown and Batch Release | 381 |
| CHAPTER 23 | POWDER COOLING, MILLING, SIEVING, PARTICLE-SIZE AND FINAL BLENDING | 387 |
| 23.1 | Powder Discharge from the Dryer | 387 |
| 23.2 | Main-Chamber Powder Fraction | 388 |
| 23.3 | Cyclone Powder Fraction | 388 |
| 23.4 | Bag-Filter Fines | 389 |
| 23.5 | Powder Cooling | 390 |
| 23.6 | Moisture Equilibration | 390 |
| 23.7 | Agglomerate Inspection | 391 |
| 23.8 | Milling of Oversize Only | 391 |
| 23.9 | Low-Heat Milling | 392 |
| 23.10 | Final Sieving | 392 |
| 23.11 | d10, d50 and d90 Control | 393 |
| 23.12 | Fine-Fraction Control | 394 |
| 23.13 | Bulk-Density Control | 394 |
| 23.14 | Final Powder Blending | 395 |
| 23.15 | Finished Blend Release | 396 |
| CHAPTER 24 | FINISHED-PRODUCT SPECIFICATIONS AND ANALYTICAL METHODS | 404 |
| 24.1 | Finished-Product Sampling | 404 |
| 24.2 | Appearance | 405 |
| 24.3 | Moisture | 405 |
| 24.4 | Total Nitrogen | 406 |
| 24.5 | Amino Nitrogen | 407 |
| 24.6 | Free Amino Acid Content | 408 |
| 24.7 | Degree of Hydrolysis Indicator | 409 |
| 24.8 | Total Peptides | 410 |
| 24.9 | Ash | 412 |
| 24.10 | Sodium and Potassium | 412 |
| 24.11 | Chloride and Sulfate | 413 |
| 24.12 | Water-Insoluble Matter | 413 |
| 24.13 | pH | 414 |
| 24.14 | Particle Size and Bulk Density | 414 |
| 24.15 | RELEASE, HOLD, REWORK and REJECT | 415 |
| CHAPTER 25 | MICROBIOLOGICAL CONTROL, FACTORY HYGIENE AND CONTAMINATION PREVENTION | 427 |
| 25.1 | Microbiological Risks of Animal Feedstocks | 427 |
| 25.2 | Raw-Material Microbial Load | 428 |
| 25.3 | Thermal Kill Steps | 428 |
| 25.4 | Post-Hydrolysis Recontamination Risk | 430 |
| 25.5 | Hygienic Zoning | 430 |
| 25.6 | Process-Water Hygiene | 431 |
| 25.7 | Tank Hygiene | 431 |
| 25.8 | Pipeline Hygiene | 432 |
| 25.9 | Drying as a Microbial-Control Step | 432 |
| 25.10 | Powder-Handling Hygiene | 433 |
| 25.11 | Environmental Monitoring | 434 |
| 25.12 | Personnel Hygiene | 435 |
| 25.13 | Pest Control | 435 |
| 25.14 | Cleaning Verification | 436 |
| 25.15 | Microbiological Release Program | 437 |
| CHAPTER 26 | PACKAGING, MOISTURE PROTECTION, STORAGE STABILITY AND SHELF-LIFE CONTROL | 447 |
| 26.1 | Packaging Objectives | 447 |
| 26.2 | Hygroscopicity of Amino Acid Powder | 448 |
| 26.3 | Moisture-Barrier Liners | 448 |
| 26.4 | Multiwall Bags | 449 |
| 26.5 | Laminated Barrier Packaging | 449 |
| 26.6 | Drums and Bulk Packaging | 451 |
| 26.7 | Net-Weight Control | 451 |
| 26.8 | Heat-Sealing | 451 |
| 26.9 | Seal-Integrity Testing | 452 |
| 26.10 | Lot Coding | 453 |
| 26.11 | Palletization | 453 |
| 26.12 | Warehouse Conditions | 454 |
| 26.13 | Caking Control | 454 |
| 26.14 | Real-Time Stability Testing | 456 |
| 26.15 | Shelf-Life Establishment | 456 |
| CHAPTER 27 | PROCESS WATER, STEAM, ELECTRICITY, COMPRESSED AIR, CIP AND PLANT UTILITIES | 464 |
| 27.1 | Process-Water Demand | 464 |
| 27.2 | Water-Quality Zones | 465 |
| 27.3 | Boiler and Steam System | 467 |
| 27.4 | Reactor Heating Load | 468 |
| 27.5 | Evaporator Steam Demand | 468 |
| 27.6 | Spray-Dryer Thermal Demand | 469 |
| 27.7 | Cooling-Water System | 469 |
| 27.8 | Electrical Load Distribution | 470 |
| 27.9 | Compressed-Air Uses | 470 |
| 27.10 | Vacuum Systems | 470 |
| 27.11 | Cleaning-in-Place Architecture | 471 |
| 27.12 | Chemical Cleaning | 472 |
| 27.13 | Rinse Endpoint | 473 |
| 27.14 | Utility Metering | 473 |
| 27.15 | Utility Consumption per Tonne Product | 475 |
| CHAPTER 28 | SOLID RESIDUES, LIQUID EFFLUENTS, BY-PRODUCTS AND ENVIRONMENTAL MANAGEMENT | 484 |
| 28.1 | Unhydrolyzed Protein Residue | 484 |
| 28.2 | Bone and Mineral Residues | 485 |
| 28.3 | Fat and Oil By-Products | 486 |
| 28.4 | Clarification Sludge | 487 |
| 28.5 | Activated-Carbon Waste | 488 |
| 28.6 | High-Salt Wastewater | 488 |
| 28.7 | Ion-Exchange Regenerant Waste | 489 |
| 28.8 | Membrane Reject Streams | 489 |
| 28.9 | Evaporator Condensate | 491 |
| 28.10 | Spray-Dryer Dust | 491 |
| 28.11 | Recoverable Protein Co-Products | 492 |
| 28.12 | Wastewater Organic Load | 492 |
| 28.13 | Nitrogen Load | 493 |
| 28.14 | Source-Reduction Strategy | 494 |
| 28.15 | Waste per Tonne Finished Product | 496 |
| CHAPTER 29 | PRODUCTION YIELD, MASS BALANCE, SCALE-UP, TROUBLESHOOTING AND PROCESS OPTIMIZATION | 505 |
| 29.1 | Plant-Wide Mass Balance | 505 |
| 29.2 | Dry-Solids Balance | 507 |
| 29.3 | Total Nitrogen Balance | 507 |
| 29.4 | Amino-Nitrogen Balance | 508 |
| 29.5 | Free-Amino-Acid Recovery | 509 |
| 29.6 | Product Yield per Tonne Feedstock | 510 |
| 29.7 | Hydrolysis Yield Losses | 511 |
| 29.8 | Separation Yield Losses | 511 |
| 29.9 | Purification Yield Losses | 512 |
| 29.10 | Dryer Yield Losses | 512 |
| 29.11 | Scale-Up of Hydrolysis Reactors | 514 |
| 29.12 | Scale-Up of Separation Equipment | 514 |
| 29.13 | Scale-Up of Membrane/Purification Systems | 515 |
| 29.14 | Scale-Up of Evaporation and Spray Drying | 516 |
| 29.15 | Plant-Wide Root-Cause Troubleshooting | 517 |
| CHAPTER 30 | INTEGRATED PROFESSIONAL FACTORY MANAGEMENT, PRODUCTION COST AND COMMERCIAL GRADE CONTROL | 526 |
| 30.1 | Integrated Production Route | 526 |
| 30.2 | Daily Production Planning | 527 |
| 30.3 | Raw-Material Requirement per Tonne Powder | 528 |
| 30.4 | Chemical Consumption per Tonne Powder | 529 |
| 30.5 | Water Consumption per Tonne Powder | 529 |
| 30.6 | Energy Consumption per Tonne Powder | 530 |
| 30.7 | Resin and Membrane Consumption | 531 |
| 30.8 | Labor Requirement | 532 |
| 30.9 | Maintenance Cost | 532 |
| 30.10 | Packaging Cost | 533 |
| 30.11 | Waste-Treatment Cost | 533 |
| 30.12 | Total Manufacturing Cost per Kilogram | 534 |
| 30.13 | Technical versus Premium Grade Economics | 535 |
| 30.14 | Bottleneck and Capacity Management | 536 |
| 30.15 | Continuous Improvement and Factory KPI System | 537 |




Reviews
There are no reviews yet.