Techno-Economic Feasibility of Producing High-Protein Tofu from Chickpeas: Process Design and Nutrient Recovery
Abstract
1. Introduction
2. Background
2.1. Nutritional Composition and Allergenicity
2.2. Functional and Technological Properties of Chickpea Proteins
2.3. Conventional Tofu Production and Processing Constraints
2.4. Process Analogs and Applications of Chickpea-Based Tofu
2.5. Low-Cost Systems and Humanitarian Relevance
2.6. Motivation for Process Adaptation
3. Materials and Methods
3.1. Production of Chickpea Tofu
3.2. Physiochemical Properties
3.3. Calculated Attributes
3.3.1. Conversion of Chickpeas to Okara, Starch, and Tofu
- M0 is the wet mass of raw chickpeas (kg);
- Mi is the wet mass of product i (kg; okara i = 3, starch i = 4, or tofu i = 5) (Figure 1).
3.3.2. Operating Energy Needed
- QB_calculated is the sensible heat required for boiling (kJ);
- M is the mass of chickpea milk (kg);
- Cp is the specific heat capacity (3.8 kJ·kg−1·K−1) [46];
- ΔT is the temperature change (100 K).
- QD_calculated is the thermal energy needed for drying (kJ);
- Mv is the mass of water to be evaporated (kg);
- Hlatent is the latent heat of water (2260 kJ/kg).
- Tofu powder: derived from fresh tofu containing 70% moisture.
- Okara powder: derived from wet okara with 70% moisture, collected during the straining step.
- Starch powder: derived from wet starch sediment containing 55% moisture, following the 1.5 h sedimentation phase.
- Scotta powder: derived from liquid scotta with a soluble solids content of 3 °Bx.
3.4. Fresh Basis Mass Balance of Streams
4. Results
4.1. Raw Chickpea Nutritional Results
4.2. Okara, Starch, and Tofu Nutritional Results
4.3. Mass Balance of the Process
Component Recovery and Partitioning
4.4. Estimated Energy
5. Discussion
5.1. Nutritional Transformation
5.2. Yield Transformation
5.3. Techno-Economic Analysis
5.3.1. Fresh Tofu: Input Cost and Efficiency
5.3.2. Powdered Tofu: Shelf Stability and Cost Trade-Offs
5.3.3. Coproduct Costing and Assumptions
5.3.4. Summary Perspective
5.4. Valorization of Scotta: Drying Feasibility and Alternatives
- Lactic acid fermentation using existing pulse or dairy fermentation cultures, which can yield probiotic beverages or bio-acid solutions as mentioned by Peñas et al. (2006) [54].
- Direct culinary use as a base for soups, porridges, or fortified drinks, especially in institutional feeding settings.
- Microbial conversion for the production of bioactives or micronutrients such as vitamin B12, leveraging known capabilities of Propionibacterium species demonstrated by Yu et al. (2015) [55].
- Composting or animal feed blending, particularly in combination with okara to enhance nutrient recovery in agricultural or livestock systems.
5.5. Environmental Perspective (Conceptual)
5.6. Food Security Relevance (Perspective)
6. Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Conflicts of Interest
References
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Step | Name of Operation | Procedural Details * | Reference |
---|---|---|---|
1 | Raw material preparation | Chickpeas (Cicer arietinum L.) were purchased then rinsed with potable water. | |
2 | Soaking | Chickpeas were immersed in three parts water (1:3 w:w) at ambient temperature (~22 °C) for 10 h, to attain ~2:1 (soaked/dry) hydration. | [26] |
3 | Wet grinding/slurry preparation | A Braun Jug Blender JB3060WH (800 W, max speed 24,000 rpm; De’Longhi Braun Household GmbH, Neu-Isenburg, Germany) was used for homogenization in two phases. First phase: Soaked chickpeas were blended with water at a 1:2 (w/v) ratio until uniform. Second phase: Water was added to reach a final 1:4 (w/v) ratio, and blended until a homogeneous mixture was obtained (~5 min). | [26,36] |
4 | Filtration (okara removal) | The slurry was passed through a double-layer muslin cloth; retained fiber (okara) was removed. | [26] |
5 | Starch sedimentation and milk decanting | The filtrate was held for 1.5 h; settled starch remained in the vessel while the clarified upper layer was decanted for curding. Starch sedimentation was achieved by manual decanting at a controlled ambient temperature (22–24 °C) without agitation | [7] |
6 | Thermal treatment | The decanted milk was heated to 98–100 °C for 3–5 min to denature proteins and inactivate enzymes. | [26] |
7 | Coagulation (CaCl2) | Hot milk (≈85 °C) treated with anhydrous CaCl2 at the rate of 2.5 g L−1; gentle stirring for 10 s, then standing 10 min formed curd. | [26] |
8 | Molding and passive drainage | Curd was ladled into a cloth-lined perforated mold and allowed to drain by gravity without pressing. | [26] |
9 | Refrigerated holding | Blocks were kept at 4 °C for 12 h for whey drainage and cooling prior to further testing. | [6] |
Stage | Stream | Mean ± SE |
---|---|---|
Input | Raw chickpeas | 1 |
Soak water * | 3 | |
Intermediate output ** | Soaked chickpeas | 1.98 ± 0.032 |
Intermediate streams | Okara (fresh) | 1.032 ± 0.055 |
Decanted milk (pre-coagulation) | 5.126 ± 0.335 | |
Starch sediment (fresh) | 2.272 ± 0.155 | |
Final output | Tofu (fresh) | 0.744 ± 0.021 |
Scotta (whey) | 4.384 ± 0.333 |
Component | Values (Mean ± SE) |
---|---|
Moisture | 13.45 ± 0.17 |
Protein (d.b.) | 20.52 ± 0.76 |
Fat (d.b.) | 6.03 ± 0.56 |
Ash (d.b.) | 5.71 ± 0.98 |
Fiber (d.b.) | 9.16 ± 0.14 |
Net Carbohydrates 1 (d.b.) | 58.59 ± 1.24 |
Total Carbohydrates 2 (d.b.) | 67.74 ± 1.18 |
Component | Okara (%) | Starch (%) | Tofu (%) |
---|---|---|---|
Moisture | 71.42 ± 1.86 | 53.30 ± 2.18 | 68.90 ± 4.94 |
Protein (d.b.) | 8.54 ± 0.40 | 3.77 ± 0.04 | 56.18 ± 1.38 |
Fat (d.b.) | 3.15 ± 0.22 | 0.95 ± 0.05 | 12.21 ± 0.59 |
Ash (d.b.) | 1.50 ± 0.05 | 0.18 ± 0.01 | 6.29 ± 1.43 |
Fiber (d.b.) | 10.27 ± 0.39 | 0.89 ± 0.03 | 1.55 ± 0.22 |
Net Carbohydrates 1 (d.b.) | 76.54 ± 0.31 | 94.22 ± 0.06 | 21.27 ± 2.38 |
Total Carbohydrates 2 (d.b.) | 86.81 ± 0.64 | 95.11 ± 0.06 | 22.82 ± 2.37 |
Product | Conversion Value (kg Raw Chickpeas/kg Product) |
---|---|
Soaked chickpeas | 0.523 ± 0.009 |
Okara powder | 3.26 ± 0.154 |
Wet okara (70% moisture equivalent) | 1.03 ± 0.515 |
Starch powder | 7.575 ± 0.518 |
Wet starch (50% moisture equivalent) | 2.273 ± 0.155 |
Tofu powder | 4.957 ± 0.152 |
Wet tofu (70% moisture equivalent) | 1.487 ± 0.507 |
Scotta (3 °Bx) | 0.289 ± 0.038 |
Scotta powder | 9.649 ± 1.277 |
Nutrient | Okara (%) | Starch (%) | Tofu (%) | Sum (%) |
---|---|---|---|---|
Protein | 13.45 ± 1.44 | 2.56 ± 0.20 | 59.09 ± 2.90 | 75.09 ± 3.13 |
Fat | 16.67 ± 1.92 | 2.20 ± 0.27 | 43.22 ± 3.22 | 90.37 ± 5.16 |
Fiber | 34.48 ± 0.75 | 1.30 ± 0.07 | 3.51 ± 0.49 | 39.29 ± 0.74 |
Net Carbohydrate 1 | 40.28 ± 2.58 | 21.59 ± 1.83 | 8.41 ± 0.54 | 77.53 ± 4.48 |
Product | Energy Required (kWh/kg Product) |
---|---|
Tofu (70% moisture) | 0.798 |
Tofu powder | 4.109 |
Okara powder | 1.465 |
Starch powder | 0.767 |
Scotta powder | 20.298 |
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Dimassi, O.; Jaber, L.; Toufeili, I.; Ouaijan, K.; Hamadeh, S. Techno-Economic Feasibility of Producing High-Protein Tofu from Chickpeas: Process Design and Nutrient Recovery. Foods 2025, 14, 3206. https://doi.org/10.3390/foods14183206
Dimassi O, Jaber L, Toufeili I, Ouaijan K, Hamadeh S. Techno-Economic Feasibility of Producing High-Protein Tofu from Chickpeas: Process Design and Nutrient Recovery. Foods. 2025; 14(18):3206. https://doi.org/10.3390/foods14183206
Chicago/Turabian StyleDimassi, Ossama, Lina Jaber, Imad Toufeili, Krystel Ouaijan, and Shady Hamadeh. 2025. "Techno-Economic Feasibility of Producing High-Protein Tofu from Chickpeas: Process Design and Nutrient Recovery" Foods 14, no. 18: 3206. https://doi.org/10.3390/foods14183206
APA StyleDimassi, O., Jaber, L., Toufeili, I., Ouaijan, K., & Hamadeh, S. (2025). Techno-Economic Feasibility of Producing High-Protein Tofu from Chickpeas: Process Design and Nutrient Recovery. Foods, 14(18), 3206. https://doi.org/10.3390/foods14183206