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LECTURE 3�THEME: Grinding oilseeds and kernels. Preparing the roast (meal).

CREATED BY: BEKHZOD KURAMBOEV, ASSISTANT TEACHER, 2 YEAR PhD STUDENT OF THE FOOD TECHNOLOGY DEPARTMENT

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  • Lecture Objectives:
  • Understand the purpose and principles of crushing oilseeds and kernels.
  • Learn the different types of equipment used for crushing and their operational principles.
  • Grasp the science, purpose, and technology behind the roasting process.
  • Analyze the key parameters, formulas, and quality indicators for producing high-quality roasted meal.

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  • Part 1: Crushing of Oilseeds and Kernels
  • 1.1 Purpose of Crushing
  • The primary goal of crushing is to reduce the particle size of the oilseed or kernel to prepare it for subsequent processing, primarily flaking and cooking. The specific objectives are:
  • Size Reduction: To create smaller, more uniform pieces for efficient flaking.
  • Hull Liberation: For seeds with hulls (like sunflower, cottonseed), crushing helps to separate the brittle hull from the more pliable meat (kernel).
  • Increased Surface Area: Prepares the material for more effective heat and moisture transfer during subsequent cooking/roasting.

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  • 1.2 Equipment for Crushing
  • The choice of equipment depends on the type of seed and the desired final product.
  • A) Bar Crackers / Hammer Mills (for Husked Seeds)
  • Application: Primarily for seeds like sunflower, cottonseed, and palm kernels where the hull must be separated from the kernel.
  • Technical Scheme & Principle:
    • Principle: Impact and shear forces.
    • Scheme:
  • [Whole Seeds with Hulls] --> [Feed Hopper] --> [Rotating Rotor with Swing Hammers/Bars]
  • |
  • V
  • [Impact with Hammers & Liner] --> [Crushed Material & Hulls] --> [Screen/Grate]
  • |
  • V
  • [Hulls & Kernels separated by Aspiration & Screening]
  • Key Parameters:
    • Rotor Speed: 1,500 - 3,000 rpm.
    • Screen Size: 3-8 mm, depending on seed.
    • Objective: Achieve a clean break, liberating >90% of the kernels from the hulls without generating excessive fines.

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  • B) Corrugated Roller Mills (for Kernels & Dehulled Seeds)
  • Application: Ideal for soybeans, rapeseed, dehulled sunflower kernels, and peanuts. They offer a more controlled size reduction than hammer mills.
  • Technical Scheme & Principle:
    • Principle: Compression and shear forces between two counter-rotating rolls with corrugations.
    • Scheme:
  • text
  • [Whole Kernels/Seeds] --> [Feed Hopper] --> [Feeding Roller for even distribution]
  • |
  • V
  • [Nip Point/Gap between Two Corrugated Rolls]
  • (One fixed, one adjustable spring pressure)
  • |
  • V
  • [Crushed Product (Grits)]
  • Key Parameters & Formula:
    • Roll Speed Differential: The two rolls rotate at different speeds (e.g., a 1.5:1 ratio) to create a shearing action.
    • Corrugation: Number of corrugations per cm (e.g., 4-6 for coarse cracking, 8-10 for fine).
    • Gap Setting: The most critical parameter. It determines the particle size of the output (grits).
      • Typical Gap: 0.3 - 0.8 mm.

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  • 1.3 Statistics for Crushing
  • Throughput: A typical industrial hammer mill or roller mill can process 100 - 500 tons per day, depending on size and power.
  • Power Consumption: Hammer mills are generally more energy-intensive.
    • Hammer Mill: 8 - 15 kWh/ton of material.
    • Roller Mill: 4 - 8 kWh/ton of material.
  • Efficiency: A well-tuned dehulling/crushing system can achieve a hull removal efficiency of 92-97%.

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  • Part 2: Preparation of Roasted (Meal) Mass
  • The product from the crusher (grits) is now ready for thermal treatment, commonly known as cooking or roasting. In modern oil extraction, this is a multi-step process of conditioning, followed by roasting in a cooker.

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  • 2.1 The Purpose of Roasting/Cooking
  • This is a critical step that dramatically impacts both oil yield and meal quality.
  • Coagulation of Proteins: Heat denatures proteins, destroying the cell wall structure that encapsulates the oil. This makes the oil more fluid and easier to extract.
  • Moisture Adjustment: Optimal moisture is crucial for flaking and extraction. Cooking dries the meal to the perfect moisture level for pressing or solvent extraction.
  • Enzyme Inactivation: Destroys harmful enzymes like lipase (which causes free fatty acid increase) and urease (in soybeans, important for animal feed).
  • Sterilization: Kills molds, bacteria, and other microorganisms.
  • Texture Modification: Makes the material more plastic and suitable for forming flakes in the next step.

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  • 2.2 The Science: Moisture and Temperature
  • The roasting process is a delicate balance of Time (t), Temperature (T), and Moisture Content (MC).
  • Typical Temperature Range: 90°C - 110°C for cooking; up to 130°C for toasting post-solvent extraction.
  • Moisture Content (In/Out):
    • Initial Moisture (after conditioning): ~10-12%
    • Final Moisture (after cooking/roasting): 3-5% for direct screw pressing; 5-7% for flaking prior to solvent extraction.

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  • 2.3 Key Formulas and Calculations
  • A) Moisture Content ( Wet Basis %)�This is the standard measurement in the industry.�MC_wb (%) = (Mass of Water / Total Mass of Sample) * 100
  • B) Dry Matter (DM)�DM (%) = 100 - MC_wb
  • C) Evaporation Rate in the Cooker�To calculate the amount of water that needs to be evaporated.�Water Removed (kg/h) = Feed Rate (kg/h) * [(MC_in - MC_out) / (100 - MC_out)]

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  • 2.4 Equipment: The Stack Cooker
  • The most common industrial equipment is the vertical stack cooker, often a 5- or 6-high stack.
  • Technical Scheme & Process Flow:
  • text
  • [Cracked Grits from Crusher] --> [Conditioning Bin: Adjusted to ~10-12% MC, 60-70°C]
  • |
  • V
  • [Top Tray of Stack Cooker]
  • |
  • V
  • [Steam-Heated Trays with Sweeping Agitators] --> [Progressive Heating & Drying]
  • (Tray 1: ~75°C) -> (Tray 2: ~85°C) -> (Tray 3: ~95°C) -> (Tray 4: ~105°C)
  • |
  • V
  • [Bottom Tray: Discharge at 3-7% MC, 105-110°C]
  • |
  • V
  • [To Flaking Mills or Presses]

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  • Operation Principle:
    • The material enters the top tray.
    • As it moves horizontally across each steam-heated tray, it is agitated by sweep arms.
    • The temperature increases progressively from top to bottom.
    • Live steam can be sparged directly into the meal on certain trays to provide both heat and moisture control.
    • The total residence time in the cooker is typically 30-60 minutes.

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  • 2.5 Quality Control of Roasted Meal
  • The quality of the roasted mass is determined by several lab tests:
  • Urease Activity Index (for Soybeans): Measures the degree of protein denaturation.
    • Target: A pH rise of 0.05 to 0.20 units. (<0.05 is undercooked, >0.20 is overcooked).
  • Protein Dispersibility Index (PDI): A more precise measure of protein quality.
    • Target for Solvent Extraction: 20-40% PDI.
  • Moisture Content: As calculated above (3-7%).
  • Color: A visual and instrumental check. Over-roasting leads to dark-colored meal and oil.

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  • 2.6 Impact of Roasting: Statistics
  • Oil Yield: Proper roasting can increase oil yield during pressing by 1-3%.
  • Energy Consumption: The cooking/roasting process is energy-intensive, accounting for ~15-25% of the thermal energy in an oil mill.
  • Throughput: A single large stack cooker can handle 200 - 1,000 tons of material per day.
  • Summary and Conclusion
  • The preparatory steps of Crushing and Roasting are not merely mechanical and thermal operations; they are the foundation of efficient and profitable oil extraction.
  • Crushing creates the optimal particle size, liberates valuable components, and prepares the seed for uniform heat penetration.
  • Roasting is a scientifically controlled process where time, temperature, and moisture are meticulously managed to:
    • Maximize Oil Yield by breaking cell walls.
    • Ensure Meal Quality for the feed market.
    • Stabilize the Product for safe storage.

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THANKS A LOT GIRLS FOR YOUR ATTENTION @@@