A Bio-Based Composite Hydrogel Substrate for Indoor Soilless Dandelion Cultivation: Growth Performance and Polysaccharide Accumulation
Abstract
1. Introduction
2. Results and Discussion
2.1. Preparation and Characterization of PKH and PKCH
2.2. Growth Evaluation of Dandelion
2.3. Long-Term Cultivation Experiment and Component Analysis
2.4. Technical Economic Analysis and Life Cycle Assessment
3. Conclusions
4. Materials and Methods
4.1. Materials
4.2. Preparation of Hydrogels
4.3. Characterization of Hydrogels
4.4. Swelling, Deswelling and Mechanical Properties
4.5. Growth and Metabolism of Dandelion
4.6. Statistical Analysis
Author Contributions
Funding
Data Availability Statement
Conflicts of Interest
Appendix A
| Material | Thermal Degradation Step | T onset (°C) | T endset (°C) | Weight Loss (%) |
|---|---|---|---|---|
| PKH-1 | I | 30 | 173 | 18.69 |
| II | 173 | 1000 | 55.55 | |
| PKH-2 | I | 30 | 173 | 13.31 |
| II | 173 | 1000 | 53.63 | |
| PKH-3 | I | 30 | 173 | 16.44 |
| II | 173 | 1000 | 53.22 | |
| PKH-4 | I | 30 | 173 | 14.35 |
| II | 173 | 1000 | 56.64 | |
| PKH-5 | I | 30 | 173 | 14.64 |
| II | 173 | 1000 | 55.23 |
| PKH | PKH-1 | PKH-2 | PKH-3 | PKH-4 | PKH-5 |
|---|---|---|---|---|---|
| BET surface area (m2/g) | 28.10 | 29.39 | 37.72 | 39.56 | 47.29 |
| Langmuir Surface Area (m2/g) | 26.86 | 36.98 | 39.07 | 46.87 | 59.77 |
| Total pore volume (cm3/g) at p/p0 = 0.019 | 0.054 | 0.057 | 0.076 | 0.076 | 0.093 |
| Adsorption pore Diameter (nm) | 5.001 | 4.139 | 3.789 | 3.389 | 3.018 |
| Time (d) | Temperature (°C) | Humidity (%) | Light |
|---|---|---|---|
| 1 | 22.5 ± 1.2 | 35 ± 5 | natural sunlight |
| 2 | 22.3 ± 1.2 | 36 ± 5 | natural sunlight |
| 3 | 22.0 ± 1.3 | 38 ± 5 | natural sunlight |
| 4 | 21.8 ± 1.3 | 37 ± 5 | natural sunlight |
| 5 | 21.5 ± 1.3 | 29 ± 5 | natural sunlight |
| 6 | 21.0 ± 1.5 | 30 ± 6 | natural sunlight |
| 7 | 20.8 ± 1.2 | 32 ± 6 | natural sunlight |
| 8 | 20.5 ± 1.5 | 31 ± 6 | natural sunlight |
| 9 | 21.0 ± 1.5 | 33 ± 6 | natural sunlight |
| 10 | 20.8 ± 1.5 | 34 ± 6 | natural sunlight |
| 11 | 20.5 ± 1.5 | 35 ± 7 | natural sunlight |
| 12 | 20.2 ± 1.5 | 36 ± 7 | natural sunlight |
| 13 | 20.0 ± 1.5 | 36 ± 7 | natural sunlight |
| 14 | 22.8 ± 1.5 | 34 ± 6 | natural sunlight |
| 15 | 21.5 ± 1.5 | 33 ± 5 | natural sunlight |
| 16 | 22.4 ± 1.5 | 32 ± 5 | natural sunlight |
| 17 | 21.8 ± 1.5 | 30 ± 6 | natural sunlight |
| 18 | 20.7 ± 1.5 | 33 ± 5 | natural sunlight |
| 19 | 20.5 ± 1.5 | 34 ± 5 | natural sunlight |
| 20 | 21.3 ± 1.5 | 36 ± 5 | natural sunlight |
| Name | Solution | Fresh Weight (g) | Dry Weight (g) |
|---|---|---|---|
| Water | Water | 5.58 ± 1.21 | 1.54 ± 0.09 |
| Kelcogel | Water | 4.75 ± 0.09 | 1.10 ± 0.06 |
| PKH | Water | 5.96 ± 0.34 | 1.69 ± 0.04 |
| PKCH | Water | 7.47 ± 0.46 | 1.84 ± 0.07 |
| Water | SL | 3.94 ± 0.68 | 1.02 ± 0.05 |
| Kelcogel | SL | 3.86 ± 0.77 | 0.78 ± 0.03 |
| PKH | SL | 5.19 ± 0.24 | 1.15 ± 0.10 |
| PKCH | SL | 7.45 ± 1.19 | 1.83 ± 0.08 |
| Water | MS | 10.63 ± 0.81 | 3.14 ± 0.47 |
| Kelcogel | MS | 7.56 ± 0.77 | 1.91 ± 0.14 |
| PKH | MS | 8.62 ± 0.85 | 2.70 ± 0.04 |
| PKCH | MS | 11.23 ± 0.85 | 3.43 ± 0.10 |
| pH | Electrical Conductivity µS·cm−1 | TOC g kg−1 | TN g kg−1 |
|---|---|---|---|
| 7.68 | 103.56 ± 2.33 | 12.32 ± 0.20 | 1.09 ± 0.27 |
| Name | Solution | Shoot Length (cm) | Root Length (cm) | Main Root Diameter (cm) |
|---|---|---|---|---|
| Water | Water | 11.59 ± 1.71 | 12.27 ± 1.63 | 0.45 ± 0.23 |
| Kelcogel | Water | 10.41 ± 2.16 | 5.42 ± 0.61 | 0.74 ± 0.19 |
| PKH | Water | 13.03 ± 2.13 | 7.01 ± 0.51 | 0.76 ± 0.17 |
| PKCH | Water | 14.48 ± 1.58 | 8.32 ± 1.52 | 0.83 ± 0.17 |
| Water | SL | 5.45 ± 0.95 | 4.33 ± 1.83 | 0.47 ± 0.11 |
| Kelcogel | SL | 7.98 ± 1.60 | 5.35 ± 0.45 | 0.55 ± 0.12 |
| PKH | SL | 7.76 ± 2.08 | 5.36 ± 1.56 | 0.61 ± 0.04 |
| PKCH | SL | 9.01 ± 1.81 | 6.13 ± 1.53 | 0.71 ± 0.08 |
| Water | MS | 12.21 ± 2.33 | 13.83 ± 2.16 | 0.59 ± 0.06 |
| Kelcogel | MS | 11.71 ± 1.93 | 7.71 ± 1.46 | 0.76 ± 0.12 |
| PKH | MS | 15.54 ± 2.19 | 7.76 ± 0.86 | 0.81 ± 0.10 |
| PKCH | MS | 16.32 ± 1.66 | 8.15 ± 1.45 | 0.92 ± 0.09 |
| Name | Solution | Shoot Length (cm) | Root Length (cm) | Main Root Diameter (cm) |
|---|---|---|---|---|
| Water | MS | 15.87 ± 0.25 | 16.10 ± 0.56 | 0.68 ± 0.07 |
| Kelcogel | MS | 14.41 ± 0.76 | 8.23 ± 0.09 | 0.85 ± 0.03 |
| PKH | MS | 17.23 ± 0.44 | 8.89 ± 0.18 | 0.88 ± 0.05 |
| PKCH | MS | 18.36 ± 0.30 | 9.28 ± 0.21 | 0.94 ± 0.02 |
| Name | Solution | Fresh Weight (g) | Dry Weight (g) |
|---|---|---|---|
| Water | MS | 14.46 ± 0.94 | 3.17 ± 0.38 |
| Kelcogel | MS | 9.39 ± 0.36 | 2.33 ± 0.28 |
| PKH | MS | 9.67 ± 0.37 | 3.63 ± 0.22 |
| PKCH | MS | 15.97 ± 0.58 | 3.58 ± 0.21 |
| Name | Oxalic Acid (mg/kg) | Acetic Acid (mg/kg) | Polysaccharides (%) |
|---|---|---|---|
| Water | 6.56 ± 0.23 | 3.41 ± 0.19 | 64.20 ± 1.06 |
| Kelcogel | 6.92 ± 0.21 | 3.75 ± 0.18 | 66.31 ± 0.91 |
| PKH | 8.72 ± 0.20 | 4.13 ± 0.34 | 68.15 ± 0.89 |
| PKCH | 10.66 ± 0.66 | 4.33 ± 0.28 | 69.40 ± 0.38 |
| Project | Parameter/Description | Value/USD | Remarks |
|---|---|---|---|
| CAPEX (Capital Expenditure) | 2.1 M | ||
| Reactor system | multi-stage continuous mixing tank (316L stainless steel) | 850,000 | Corrosion-resistant design, temperature control accuracy ± 1 °C |
| Purification module | Ultrafiltration + ion exchange integrated system | 620,000 | Membrane flux ≥ 50 L/(m2·h) The recovery rate (90%) |
| Drying and granulation equipment | Spray drying + fluidized bed granulation | 430,000 | The particle size (50–100 μm) |
| Automatic control system | DCS + online monitoring (pH/viscosity/selenium content) | 200,000 | Sensor calibration and redundancy design |
| OPEX (Operating Expenditure) | 1.35 M/yr | ||
| Material | pectin (Orange peel low degree, food grade) | 480,000/yr | Unit price 12 USD/kg, purity > 85% |
| Kelcogel | Kelcogel + Se/chitosan | 320,000/yr | Se load (0.8 wt%) |
| Energy consumption | Electricity + steam (0.8 MPa) | 290,000/yr | Dry energy consumption accounts for 65% |
| Catalyst and reagent | Enzyme catalyst (pectinase + transsulfase) | 150,000/yr | enzyme activity retention rate ≥ 80%/5 batches |
| Effluent disposal | COD removal (biological + membrane filtration) | 110,000/yr | Reuse rate ≥ 70% |
| Income | 3.8 M/yr | ||
| Sales revenue of PKCH products | Unit price: USD 3800/t | 3.8 M/yr | Based on the pricing of functional food additives market |
| Net proceeds (NPV) | Discount rate 10%, 10-year cycle | 6.2 M | IRR = 24.7%, investment payback period 3.8 years |
| Index | Value | Compared with Traditional Process (Baseline) |
|---|---|---|
| Greenhouse gas emission | 2.1 kg CO2-eq/kg PKCH | decrease 38% (baseline: 3.4 kg) |
| Water consumption | 4.8 m3/t PKCH | reduce 52% (baseline: 10 m3) |
| Energy intensity | 18.7 MJ/kg PKCH | decrease 29% to (baseline: 26.3 MJ) |
| Project | Parameter/Description | Value/USD | Remarks |
|---|---|---|---|
| CAPEX (Capital Expenditure) | 1.8 M | ||
| PKCH hydroponic substrate module | Customized porous gel scaffold (containing selenium-controlled release) | 750,000 | Life span of 5 years, support root air permeability and nutrient release |
| Environment control system | Light + temperature and humidity + CO2 regulation integration | 520,000 | Optimized LED spectrum, energy efficiency > 85% |
| Nutrient solution circulation purification system | Membrane filtration + UV sterilization + ion balance | 380,000 | Water recycling rate ≥ 95% |
| Automatic monitoring platform | Sensor network +AI growth model | 150,000 | Real-time monitoring of pH, EC and selenium content |
| OPEX (Capital Expenditure) | 680,000/yr | ||
| PKCH supplement cost | Annual consumption 12 t (unit price 25,000 USD/t) | 300,000/yr | The gel degradation rate (8%/year) |
| Energy cost | Power rate (0.15 USD/kWh) | 180,000/yr | Lighting (55%), environmental control (30%) |
| Labor and maintenance | Technicians (3) + equipment maintenance | 120,000/yr | Includes sensor calibration and membrane component replacement |
| Seeds and consumables | Dandelion seedlings + nutrient solution additives | 80,000/yr | Medicinal varieties, germination rate ≥ 90% |
| Income | 2.5 M/yr | ||
| Dandelion product sales revenue | Unit price USD 50,000/t (pharmaceutical grade) | 2.5 M/yr | The market demand is stable and used for anti-inflammatory preparation production |
| Net proceeds (NPV) | Discount rate 8%, 10-year cycle | 4.1 M | IRR = 28.3%, investment payback period 3.1 years |
| Index | Value | Compared with Traditional Process (Baseline) |
|---|---|---|
| Greenhouse gas emission | 1.2 kg CO2-eq/kg Dandelion | decrease 60% (baseline: 3.0 kg) |
| Water consumption | 0.5 m3/t Dandelion | reduce 90% (baseline: 5 m3) |
| Soil occupancy | 0 (soilless cultivation) | decrease 100% (baseline: 10 m2/t) |
| Utilization of selenium resources | 92% | The utilization rate of traditional fertilization method < 40% |
Appendix B





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Guo, Y.; Ma, J.; Zheng, Y.; Wang, G.; Zhang, H.; Yu, Y.; Zhang, J. A Bio-Based Composite Hydrogel Substrate for Indoor Soilless Dandelion Cultivation: Growth Performance and Polysaccharide Accumulation. Gels 2026, 12, 235. https://doi.org/10.3390/gels12030235
Guo Y, Ma J, Zheng Y, Wang G, Zhang H, Yu Y, Zhang J. A Bio-Based Composite Hydrogel Substrate for Indoor Soilless Dandelion Cultivation: Growth Performance and Polysaccharide Accumulation. Gels. 2026; 12(3):235. https://doi.org/10.3390/gels12030235
Chicago/Turabian StyleGuo, Yongxin, Jianxun Ma, Yuhan Zheng, Gang Wang, Hongda Zhang, Yong Yu, and Jinpeng Zhang. 2026. "A Bio-Based Composite Hydrogel Substrate for Indoor Soilless Dandelion Cultivation: Growth Performance and Polysaccharide Accumulation" Gels 12, no. 3: 235. https://doi.org/10.3390/gels12030235
APA StyleGuo, Y., Ma, J., Zheng, Y., Wang, G., Zhang, H., Yu, Y., & Zhang, J. (2026). A Bio-Based Composite Hydrogel Substrate for Indoor Soilless Dandelion Cultivation: Growth Performance and Polysaccharide Accumulation. Gels, 12(3), 235. https://doi.org/10.3390/gels12030235

