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Technical Design for Water Quality Compliance Using Reverse Osmosis Membrane Treatment for Comprehensive Wastewater in the Papermaking Industry

by endalton 09 Mar 2026

Technical Design for Water Quality Compliance Using Reverse Osmosis Membrane Treatment for Comprehensive Wastewater in the Papermaking Industry

I. Design Basis and Objectives

1.1 Wastewater Characteristics and Treatment Challenges

To achieve deep reuse of papermaking composite wastewater or meet stringent discharge standards after primary physicochemical (coagulation-sedimentation/flotation) and secondary biological treatment (e.g., anaerobic + aerobic), reverse osmosis (RO) membrane treatment is a key technology. Its influent water quality characteristics and treatment challenges are as follows:

  • High Residual Organics: Contains lignin, hemicellulose degradation products, organic acids, residual dyes, etc., with poor biodegradability, easily causing organic and biological fouling of RO membranes.

  • High Hardness and High Silica Content: High concentrations of Ca²⁺, Mg²⁺, and SiO₂, which are prone to cause inorganic scaling under the high concentration factor of RO systems, leading to irreversible flux decline.

  • High Salinity: Contains ions like Na⁺, Cl⁻, SO₄²⁻ from raw materials and chemicals, resulting in high conductivity, posing challenges to RO membrane salt rejection load and concentration factor.

  • Residual Suspended Solids and Colloids: Biological effluent still contains colloids, bacteria, microbial fragments, etc., which are major factors causing membrane fouling.

  • Water Quality Fluctuations: Influenced by production raw materials, processes, and product changes, the biological effluent quality (especially COD, hardness, conductivity) exhibits certain fluctuations.

1.2 Design Influent and Product Water Quality Targets

Parameter

RO System Design Influent Quality (Post-Biological Treatment)

RO Product Water Quality Target

Design Basis

CODCr(mg/L)

≤ 80 - 150

≤ 10 - 30

For reuse in pulping, rinsing, etc., or high-standard discharge.

Conductivity (µS/cm)

1500 - 4000

≤ 100 - 500

Total Hardness (as CaCO₃, mg/L)

≤ 150 - 300

Significantly Reduced

SiO₂ (mg/L)

≤ 20 - 50

≤ 1 - 5

Turbidity (NTU)

≤ 1 - 3

≤ 0.1

SDI₁₅

≤ 3 - 5

-

Key influent index for RO membranes

pH

6.5 - 8.5

6.5 - 7.5

Temperature (°C)

20 - 35

Ambient

1.3 Design Objectives and Principles

  • Core Objective: Ensure long-term stable operation of the RO system, with product water quality consistently and stably meeting the above targets, and a system recovery rate ≥ 70%.

  • Design Principles:

    1. Pretreatment Priority: Design enhanced, diverse, and reliable pretreatment processes targeting the three major challenges of "scaling, fouling, and fluctuation" as the foundation for RO system success.

    2. Anti-fouling and Anti-scaling Design: Select specialized anti-fouling membrane elements, optimize system hydraulic design, and coordinate with efficient antiscalant/dispersant dosing.

    3. System Adaptability and Flexibility: Design considers water quality/quantity fluctuations, includes reasonable conditioning and buffering units, and allows adjustable operational parameters (e.g., recovery rate).

    4. Intelligent Monitoring: Implement online monitoring and automatic control of key water quality and operational parameters for early warning and refined management.

II. Full-Process Technical Design for Water Quality Compliance

Addressing the characteristics of papermaking wastewater, this plan proposes a tripartite technical route of "Pretreatment Safeguard → Membrane Purification → Concentrate Management". The core lies in ensuring the safety of water quality entering the RO membranes through multiple barriers and optimizing the entire process.

2.1 Full-Process Flow Diagram

2.2 Key Points for Technical Design of Critical Units

(1) Pretreatment Safeguard Unit (Prerequisite for Water Quality Compliance)

  • Chemical Softening/Coagulation-Sedimentation: Dose NaOH and Na₂CO₃, combined with coagulant (PAC) and flocculant (PAM), into the wastewater. Precipitation reactions remove most Ca²⁺, Mg²⁺ and partial SiO₂, significantly reducing scaling tendency. This unit is key for handling high-hardness, high-silica wastewater.

  • Multi-Stage Filtration:

    • Multi-Media Filter: Further removes chemical sludge and suspended solids, ensuring effluent turbidity <1 NTU.

    • Self-Cleaning Filter + Ultrafiltration System: Forms the ultimate barrier for the RO system. Ultrafiltration can almost completely remove colloids, bacteria, and macromolecular organics, ensuring RO influent SDI₁₅ stable <3 and turbidity <0.2 NTU. This is the core measure to prevent colloidal and biological fouling of RO membranes.

(2) Core Membrane Purification Unit (Core of Water Quality Compliance)

  • Primary Reverse Osmosis System:

    • Membrane Selection: Use brackish water desalination RO membrane elements with wide feed spacers, anti-fouling properties, and high salt rejection. Array configuration often uses a 2-stage primary setup to increase recovery.

    • Operational Parameters: Design recovery rate 70-75%, operating pressure 1.0-1.6 MPa. Strictly control the Langelier Saturation Index (LSI) and silica concentration product within design limits.

    • Chemical Protection: Before UF product water enters the RO, continuous dosing of: ① Specialized antiscalant/dispersant to inhibit inorganic salt and silica scaling; ② Reducing agent to eliminate oxidants like residual chlorine in the feed; ③ Non-oxidizing biocide for periodic dosing to inhibit biofouling.

  • Secondary Reverse Osmosis System: Further concentrates the primary RO concentrate, increasing total system recovery to over 85%. Secondary RO permeate merges with the main product water tank; secondary concentrate goes to the ultimate treatment unit.

(3) Concentrate Management and Intelligent Monitoring Unit

  • Concentrate Treatment: Secondary RO concentrate has extremely high COD and salinity. The route of "Advanced Oxidation Pretreatment + Evaporation Crystallization" is recommended. Advanced oxidation effectively degrades organics, reducing scaling and corrosion risks for subsequent evaporators.

  • Intelligent Monitoring:

    • Online Instruments: Install key instruments at UF inlet/outlet and RO stages to monitor SDI, turbidity, pH, conductivity, hardness, pressure, etc., in real time.

    • Automated Control: The PLC system automatically adjusts chemical dosing and recovery rate based on water quality and pressure data, and triggers warnings or automatic flushing procedures upon abnormal parameters.

III. Main Technical Parameters and Design Safeguards

Safeguard Aspect

Key Technical Measures

Design Target/Parameter

Scaling Prevention

1. Chemical softening for hardness/silica removal;
2. Efficient antiscalant dosing;
3. Control recovery rate and concentrate saturation.

Concentrate LSI < 0, SiO₂ concentration < 80% of its saturation solubility.

Fouling Prevention

1. UF system ensures SDI<3;
2. Use anti-fouling membrane elements;
3. Periodic non-oxidizing biocides.

Membrane flux annual decline rate < 7-10%, chemical cleaning cycle > 3 months.

Product Water Quality

1. High-rejection membrane elements;
2. Reasonable inter-stage flux ratio;
3. Stable operating pressure and recovery.

Product water conductivity consistently below design value, water quality compliance rate > 99%.

System Stability

1. Backup for key equipment (high-pressure pumps, instruments);
2. Automated control and interlock protection;
3. Comprehensive CIP cleaning system.

System annual availability > 95%.

IV. Economic Analysis (Example: 1000 m³/d Product Water Capacity)

  • Total Investment Estimate: Approximately 6 - 10 million RMB. Pretreatment unit (softening, UF) accounts for ~30-40%, RO membrane system ~30-35%, concentrate treatment and automation system ~25-35%.

  • Operating Cost: 2.0 - 3.5 RMB per cubic meter of product water.

    • Power Consumption: 0.8-1.5 RMB/m³ (mainly high-pressure pumps, UF feed pumps).

    • Chemical Costs: 0.5-1.0 RMB/m³ (antiscalant, acids/alkalis, cleaning agents, etc.).

    • Membrane Replacement: 0.4-0.7 RMB/m³ (based on 3-5 year membrane life).

    • Concentrate Treatment: 0.3-0.5 RMB/m³ (allocated to evaporation or external treatment costs).

  • Benefits: Product water value (saving freshwater costs, reducing discharge fees) is significant. In regions with strict environmental requirements, the environmental and social benefits of RO water reuse are substantial.

V. Conclusion and Operational Recommendations

This technical design, through the systematic strategy of "Enhanced Pretreatment for Hardness/Silica Removal, UF for Influent Quality Assurance, Optimized Anti-fouling RO Operation, Effective Ultimate Concentrate Disposal", provides a reliable technical path for achieving stable water quality compliance in reverse osmosis treatment of papermaking composite wastewater.

Key Operational Recommendations:

  1. Strengthen Pretreatment Operation Management: The effectiveness of the chemical softening unit is the source; regular monitoring and optimization of dosing are essential to ensure efficient hardness and silica removal.

  2. Establish Comprehensive Membrane System O&M Procedures: Include daily logging, standardized flushing, predictive chemical cleaning based on monitoring data, and strict membrane element replacement criteria.

  3. Conduct Specialized Pilot Testing: Before engineering design, long-term pilot testing with actual wastewater is mandatory to verify pretreatment process parameters, antiscalant suitability, membrane fouling rate, and cleaning protocols, providing precise design basis for scale-up.

  4. Focus on Professional Team Development: RO membrane systems are technically demanding; it is necessary to train or equip an O&M team with professional knowledge and fault diagnosis capabilities.

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