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Application of Decanter Centrifuge in Separation of Soybean Peptides

Soybean Peptides separation
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Application of Decanter Centrifuge in Separation of Soybean Peptides

1. Process Application in Three Stages of Soybean Peptide Production

1.1 Raw Material Leaching: Coarse Crude Fiber Separation after Defatted Soybean Meal Slurrying (Primary Separation)

Raw material: Low-temperature defatted soybean meal mixed with warm water to prepare feed slurry (solid content: 6%~12%, pH 7.5~8.5 for alkaline extraction of soluble protein).
  • Function: Separate coarse soybean dregs containing crude fiber and soybean hull impurities; overflow clear liquid is crude soybean protein solution as feedstock for subsequent enzymolysis. Discharged cake moisture content ranges from 68% to 72%, available for secondary water extraction to recover residual peptides for higher product yield.
  • Advantage: Continuous feeding, free of filter cloth clogging and adaptable to fluctuating feed concentration.
Application of Decanter Centrifuge in Separation of Soybean Peptides 1Application of Decanter Centrifuge in Separation of Soybean Peptides 2

1.2 Post-enzymolysis Primary Separation: Removal of Undigested Macromolecular Protein & Fine Residues (Core Working Section)

After enzymolysis at 50~60℃ for 2~4 h with neutral/alkaline protease followed by enzyme deactivation, the hydrolysate is fed into decanter centrifuge for key purification of soybean peptides:
  • Liquid overflow: Rich in target small-molecule soybean peptides (300~3000 Da), directly delivered to activated carbon decolorization, concentration and spray drying to produce finished soybean peptide powder.
  • Solid cake discharged via spiral conveyor: Denatured undigested macromolecular protein and fine soybean residues, which can be recycled for secondary enzymolysis or processed into feed-grade protein powder as by-product.

1.3 Isoelectric Precipitation & Acid Precipitation for Deep Purification

The clarified enzymolysis liquid is pH-adjusted to 4.2~4.5 (isoelectric point of soybean protein), inducing flocculation and precipitation of macromolecular impurity protein, then further separated by decanter:
  • Overflow clear liquid: High-purity aqueous soybean peptide solution with low ash content and reduced bitter taste, improving finished peptide purity by 8%~12%.
  • Discharged solid: Acid-precipitated crude protein residue for by-product recovery.
Defects of traditional process: Plate-and-frame filtration requires filter aids such as diatomite, intermittent manual cake discharge, resulting in over 10% peptide loss. Decanter centrifuge needs no filter aid, runs under fully sealed continuous condition and increases peptide recovery rate by 5%~9%.

2. Food-grade Decanter Selection & Standard Operating Parameters

2.1 Model Selection (All contact parts in SUS304/SUS316L food-grade stainless steel, spiral blades with tungsten carbide overlay for abrasion resistance)

Capacity Recommended Model Throughput
Small scale: 500~1500 L/h LW350 / LW430 food-specialized type 0.5~1.5 m³/h
Medium scale: 2~5 m³/h LW450 / LW530 2~5 m³/h
Large scale: 5~12 m³/h LW650 / LW720 5~12 m³/h

2.2 Operating Process Parameters for Soybean Peptide Working Condition

  1. Separation factor G: 2200~3000 G (Medium-high G-force balances clarification efficiency and cake dewatering against relatively high viscosity of peptide solution)
  2. Bowl rotating speed: 2200~2900 rpm; differential speed: 5~12 rpm (Lower differential speed improves solid dewatering with slightly turbid overflow; medium differential speed is preferred for peptide production)
  3. Feed solid content: 3%~15%, feed temperature: 45~60℃ (inherent temperature of raw enzymolysis liquid)
  4. Discharge index: Overflow turbidity ≤15 NTU; discharged cake moisture: 65%~72%

3. Exclusive Advantages for Soybean Peptide Production

  1. Fully sealed continuous production: Prevent oxidation and browning of soybean peptides by avoiding air exposure, optimizing finished product color and flavor while mitigating bitter taste.
  2. Excellent adaptability to feed fluctuation: Tolerant to variable particle size ranging from 0.005 mm fine protein flocs to 0.5 mm coarse soybean residues and fluctuating solid content; disc separator is prone to clogging and filter equipment suffers frequent filter cloth blinding.
  3. Compatible with CIP (Clean-in-place) sanitization: Sanitary structural design for in-situ cleaning, compliant with GMP food regulation and eliminating hidden risks of residual protein spoilage.
  4. Value-added by-product utilization: Separated crude protein residues are collected and processed into feed-grade soybean protein powder to maximize overall economic benefit.

4. Downstream Matching Process Flow

Decanter clarified liquid → Activated carbon decolorization & debittering → Flash deodorization → Vacuum concentration → High-pressure homogenization → Spray drying → Finished low-molecular-weight soybean peptide powder with superior water solubility and high bioavailability.

5. Troubleshooting & Process Optimization

  1. Turbid overflow with residual fine solids entrained: Slightly raise bowl rotating speed, reduce differential speed and cut down feed flow rate.
  2. Excessively wet cake (moisture>75%): Lower differential speed, adjust to shallow pond depth to extend dewatering residence time in conical bowl section.
  3. High-viscosity hydrolysate: Preheat feed liquid to 55~60℃ to reduce viscosity and enhance separation performance.

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