Direct factory-manufactured containerized SWRO units, produced water reuse skids, and ultrafiltration reverse osmosis assemblies tailored to international industrial specifications.
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Explore SpecificationsEvaluating the convergence of regulatory constraints, physical baseline water scarcity, and corporate Net-Positive Water targets across international heavy industries.
Coastal and maritime environmental regulations across the European Union, the GCC, and East Asia increasingly penalize direct hypersaline brine discharge. Thermal shock and heavy chemical coagulant carryover threaten benthic ecosystems. Industrial operators are procuring closed-loop seawater desalination systems where reject streams are recycled through second-stage high-pressure reverse osmosis or zero liquid discharge (ZLD) crystallizers.
Our OEM/ODM manufacturing facility integrates proprietary Disc Tube Reverse Osmosis (DTRO) modules operating up to 120–160 bar, turning standard 45% SWRO recovery rates into holistic 75%–85% water reclamation loops, minimizing ecological footprint.
Heavy chemical complexes, semiconductor fabrication parks, and coastal energy hubs face depleting local freshwater aquifers and surging municipal withdrawal tariffs. Global EPCs mandate decentralized, factory-assembled containerized seawater recycling equipment to secure continuous baseline water independence.
By engineering multi-pass SWRO-EDI systems directly within shipping container envelopes, we provide reliable utility-grade permeate (<10 µS/cm) and ultrapure boiler feedwater (<0.1 µS/cm) straight from raw marine intakes, removing operational exposure to regional drought risks.
Total Cost of Ownership (TCO) in modern seawater processing has shifted fundamentally from initial capital expenditure to lifetime specific energy consumption (SEC, kWh/m³) and membrane longevity. Tier-1 enterprise buyers evaluate energy recovery device (ERD) efficiencies, antiscalant dosing optimization, and smart automated flushing protocols.
Our ODM solutions utilize state-of-the-art isobaric pressure exchangers recovering up to 98% of brine hydraulic energy, compressing SWRO system energy requirements to below 2.8–3.2 kWh/m³ while enabling verifiable water-reuse accounting for ESG sustainability filings.
A granular look at the multistage chemical, mechanical, and membrane separation operations driving modern high-recovery seawater recycling equipment.
Raw seawater contains suspended solids, marine organics, algae, and colloidal silica that cause irreversible biological and colloidal fouling on polyamide membranes. Our engineering train employs Dissolved Air Flotation (DAF) paired with pressurized Dual Media Filters (DMF) or Ceramic Ultrafiltration (UF) hollow fiber barriers.
Automated dosing systems introduce sodium hypochlorite for biocide shock treatments, followed by sodium metabisulfite (SMBS) neutralization and specialized phosphonate-free antiscalants, maintaining a Silt Density Index (SDI₁₅) strictly under 2.5.
The pressurized feed is driven by positive displacement or multi-stage centrifugal pumps made of Super Duplex Stainless Steel (UNS S32750/2507) up to 65–85 bar. High-rejection thin-film composite (TFC) aromatic polyamide SWRO elements systematically reject monovalent and divalent ions (NaCl, SO₄²⁻, Ca²⁺, Mg²⁺) at >99.7% efficiency.
Isobaric Energy Recovery Devices (such as rotary ceramic pressure exchangers) transfer energy directly from the high-pressure concentrate stream into incoming feedwater at up to 98% hydraulic efficiency, slashing operating electrical demands.
To achieve true seawater recycling rather than standard single-pass desalination, the SWRO concentrate (typically 65,000–75,000 mg/L TDS) is routed to secondary Disc Tube RO (DTRO) or Special Tube RO (STRO) loops operating at pressures reaching 120–160 bar. This pushes brine TDS up to 120,000–140,000 mg/L.
The hyper-concentrated stream then enters Mechanical Vapor Recompression (MVR) evaporators and crystallizers, isolating solid commercial-grade sodium chloride and sodium sulfate while recovering virtually 100% of residual condensate for boiler makeup.
| Treatment Stage | Core Mechanism | Operating Pressure | Target Contaminants | Output Quality Metric |
|---|---|---|---|---|
| Pre-Treatment Clarification | DAF + Coagulation + Ceramic UF | 1.5 – 3.5 bar | TSS, Algae, Colloids, Oil & Grease | Turbidity < 0.1 NTU, SDI₁₅ < 2.5 |
| Primary SWRO Pass | TFC Polyamide SWRO Membranes | 55 – 82 bar | Dissolved Solids (TDS), Na⁺, Cl⁻, B | TDS < 350 mg/L, Boron < 0.5 mg/L |
| Secondary Brackish/BWRO | Low-Energy Polishing RO | 10 – 18 bar | Residual Boron, Conductivity, Silica | Conductivity < 10 µS/cm, Silica < 50 ppb |
| Hyper-Concentration (ZLD) | Open-Channel DTRO / STRO | 90 – 160 bar | SWRO Brine, Heavy Scaling Salts | Brine TDS up to 140,000 mg/L |
| Thermal MVR Crystallization | Vapor Recompression + Centrifuge | Vacuum / Atmospheric | Saturated Halite, Sulfates | Dry Salt Cake + Pure Distillate (<5 ppm) |
Tailoring membrane metallurgy, thermal endurance, and modular enclosures to extreme regional operating conditions across major global industrial corridors.
Engineering the next evolutionary leap in industrial water circularity through advanced nanomaterials, edge machine learning, and clean energy integration.
Traditional thin-film composite polyamide membranes face an inherent permeability-selectivity trade-off. R&D is rapidly commercializing Aquaporin-embedded biomimetic layers and aligned carbon-nanotube/graphene oxide sheets that allow ultra-fast hydraulic flux while rejecting 99.85%+ of sodium chloride.
These breakthrough nanomaterials decrease feed pressure requirements by 20% to 30%, resisting biofouling and enabling wider pH tolerance during harsh Clean-in-Place (CIP) cycles.
Real-time edge microcontrollers continuously parse intake salinity, SDI fluctuations, temperature shifts, and trans-membrane pressure (TMP) variations. Neural-network-based Digital Twins predict incipient mineral scaling (calcium carbonate, silica, strontium sulfate) hours before flux decline begins.
Automated dosing dynamically modulates antiscalant stoichiometry and schedules micro-flush routines without human intervention, extending membrane operating life beyond 5 to 7 years.
Future industrial installations avoid the efficiency penalties of AC-DC-AC conversion by coupling containerized SWRO high-pressure pumps directly to coastal DC solar photovoltaic arrays and offshore wind turbines.
Smart variable-frequency drive (VFD) controllers adjust pump hydraulic ramping in response to solar irradiance curves without stopping the unit, maintaining steady membrane flux and eliminating cyclic pressure hammer damage.
How Shanghai Tongjie manages procurement security, rigorous Factory Acceptance Testing (FAT), pressure vessel stamping, and multinational engineering handover.
Every single containerized seawater desalination and ZLD recycling skid manufactured at our 25,000+ m² facility undergoes complete wet FAT before crating. We simulate target project water conditions—adjusting salinity, hardness, and temperature in our testing bays.
Full hydrostatic pressure testing up to 1.5× design rating, helium leak inspections, weld radiography, electrical dielectric testing, and PLC logic validation are carried out under accredited third-party witness protocols (SGS, TÜV, BV).
Seawater corrosion presents severe pitting and crevice risks (PREN > 42 required). We fabricate high-pressure manifolds using 2507 Super Duplex Stainless Steel, titanium Grade 2 for high-chlorine chemical injection zones, and FRP/GRP piping for low-pressure seawater headers.
Vessels adhere to ASME Boiler and Pressure Vessel Code (BPVC) Section X for fiber-reinforced plastic pressure vessels and CE-PED (Pressure Equipment Directive 2014/68/EU) for direct compliance within the European Economic Area.
Our localized delivery model pairs modular Chinese manufacturing cost advantages with regional field engineering dispatch. Skids arrive on-site pre-wired and pre-piped, requiring only intake, discharge, power, and chemical utility interconnections.
Standard commissioning completes within 10–15 business days. Cloud-based SCADA integration enables 24/7 remote performance auditing from our engineering headquarters, dispatching replacement membrane elements and consumables directly through regional bonded warehouses.
Authoritative answers on SWRO engineering parameters, boron rejection, high-pressure brine concentration, and containerized deployment logistics.
Standard SWRO membranes exhibit lower rejection rates for uncharged boric acid (B(OH)₃) at natural seawater pH (7.8–8.2). To achieve strict international guidelines (<0.5 mg/L Boron), our ODM systems implement a two-pass configuration with caustic (NaOH) dosing ahead of the second pass. Raising the pH to 9.5–10.0 converts boric acid into charged borate ions (B(OH)₄⁻), which are rejected by the second-pass brackish water membranes at rates exceeding 98.5%.
By pairing premium high-efficiency IE4 electric motors, multi-stage Super Duplex high-pressure pumps, and isobaric energy recovery devices (ERDs), our systems achieve a specific energy consumption of 2.8 to 3.4 kWh per cubic meter of produced permeate water (at 35,000 ppm TDS feed and 25°C). This represents an industry-leading benchmark compared to older hydraulic turbine designs which frequently consume 4.5 to 6.0 kWh/m³.
Spiral-wound membranes contain fine feed spacer meshes that trap suspended particles and promote biofouling under high recovery and high-salinity (>65,000 ppm TDS) conditions. DTRO utilizes an open-channel hydrodynamic architecture with disc carriers and octagonal membrane cushions. The flow path creates high fluid turbulence that actively scours the membrane surface, preventing concentration polarization, handling turbidity up to 5 NTU, and tolerating pressures up to 160 bar.
To deliver an engineered mass balance and P&ID schematic, please provide: (1) Comprehensive water analysis report including TDS, pH, temperature range, Ca²⁺, Mg²⁺, Ba²⁺, Sr²⁺, SiO₂, SO₄²⁻, and Free Chlorine; (2) Daily or hourly permeate volume targets (m³/day or GPD); (3) Target permeate specification (potable WHO standard, cooling tower makeup, or ultrapure boiler feed); (4) Local electrical grid supply (e.g., 380V/440V/480V, 50/60Hz); and (5) Footprint constraints (skid or containerized).
Yes. All our containerized enclosures are built using heavy-duty ISO standard Corten steel shipping containers finished with a marine-grade C5-M anti-corrosion coating system (minimum 320 µm dry film thickness). Internal piping exposed to raw seawater is constructed from 2507 Super Duplex or heavy-wall GRP/FRP, and the interior is fully insulated with rockwool panels and climate-controlled via heavy-duty corrosion-resistant HVAC systems.
Standard skid configurations (100 m³/day to 1,000 m³/day) feature pre-engineered building blocks with typical fabrication, assembly, and testing lead times of 6 to 8 weeks. Highly customized configurations requiring specialized metallurgy (Hastelloy C-276, Titanium), exotic hazardous-area explosion-proofing (ATEX/IECEx Class I Div 2), or dual-stage MVR crystallizers generally range from 12 to 16 weeks from approved engineering drawings.
Browse our factory-direct advanced membrane modules, brine concentration skids, and zero-discharge flowback fluid recycling systems built to international engineering codes.
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Explore SpecificationsConnect directly with our Shanghai membrane engineering center. Upload raw water data, target recovery goals, and local discharge standards to receive a customized P&ID, mass balance simulation, and equipment scope within 48 hours.