

Two-Stage Reverse Osmosis System
两级反渗透系统
- SKU RSY-0004
- RO Systems
- CE (to be confirmed)
- RoHS (to be confirmed)
- ISO 9001 manufacturing (to be confirmed)
Price on request — FOB / CIF quoted per order
Prices depend on configuration, quantity and destination port.
Key specifications
| Permeate flow | 20–200 L/h |
|---|---|
| Ion rejection | 98–99.5 % |
| Operating pressure | 10–20 bar |
| Stages | 2 |
| Permeate conductivity | 1–5 µS/cm |
| Recovery | 30–60 % |
By Lab Manufacturers China Technical TeamLast reviewed Standards: ISO 3696, CLSI GP40, IEC 61010-1
What is the Two-Stage Reverse Osmosis System?
A two-stage reverse osmosis system passes permeate through a second membrane to raise purity and improve recovery. It is used where feed is saline or where higher-quality Type III water is needed.
What is the Two-Stage Reverse Osmosis System?
A two-stage reverse osmosis system passes permeate through a second membrane to raise purity and improve recovery. It is used where feed is saline or where higher-quality Type III water is needed.
Overview
The two-stage system arranges membranes so that the concentrate of the first stage feeds a second stage, or so that permeate is re-processed by a second bank of membranes. In the first arrangement, recovery rises because more of the feed becomes product. In the second, purity rises because the permeate is polished again, reaching 98 to 99.5 percent rejection and a permeate of about 1 to 5 microsiemens per centimeter. Higher pressures, up to 15 to 20 bar, may be needed. Two-stage designs suit feed with moderate salinity, or laboratories that want better water before final deionization, since lower ionic load extends the life of ion exchange resins and reduces regeneration frequency. Monitoring covers inter-stage pressure, permeate conductivity and flow, and automatic flush protects both stages during standby.
How does it work?
Reverse osmosis applies pressure greater than the osmotic pressure of the feed water to force water through a semipermeable membrane. The membrane rejects most dissolved ions, large organic molecules, colloids, bacteria and particles, while water passes through. Feed is split into permeate, which is the purified product, and concentrate, which carries the rejected contaminants to drain. Recovery, the ratio of permeate to feed, typically ranges from 15 to 50 percent for laboratory units and higher for staged industrial designs. Prefilters remove sediment and chlorine because chlorine attacks polyamide membranes, and a pump supplies the required pressure of 4 to 15 bar depending on feed salinity and membrane type. Monitoring includes pressure, flow, conductivity of permeate and feed, and sometimes temperature correction, because permeate quality falls as temperature drops.
What are the key features?
- Two membrane stages in series or permeate-reprocessing
- Higher recovery or higher purity depending on layout
- Permeate of about 1–5 µS/cm
- Operating pressures up to 15–20 bar
- Inter-stage and permeate monitoring
- Extends downstream resin life
What are the technical specifications?
A typical two-stage reverse osmosis system configuration offers permeate flow of 20–200 L/h, ion rejection of 98–99.5 %, operating pressure of 10–20 bar, stages of 2, permeate conductivity of 1–5 µS/cm and recovery of 30–60 %. Values are indicative of the product class; the exact figures for each configuration are confirmed on the quotation and the calibration documents supplied with the instrument.
Which applications is it used for?
The Two-Stage Reverse Osmosis System is used in moderately saline feed water, high-purity Type III supply, feed for deionizers with long resin life, analytical laboratory water and pharmaceutical and food laboratory use. Across the wider RO Systems class, laboratories also deploy it for type III water for glassware rinsing, feed water for deionizers and ultrapure systems and reagent and buffer preparation.
Which standards and certifications apply?
Relevant standards and methods include ISO 3696, CLSI GP40, IEC 61010-1, IEC 61326-1 and ISO 9001. Certification candidates for this model are CE, RoHS and ISO 9001 manufacturing; each is to be confirmed for the specific configuration before shipment, and certificates are supplied only where they have been issued.
Protect the membrane by removing chlorine with carbon and softening hard feed to prevent scaling. Run the system regularly rather than leaving it idle, since stagnant water encourages biofilm, and use automatic flush cycles. Sanitize on the schedule recommended for your application, and replace prefilters before pressure drop becomes excessive. Measure permeate conductivity and flow to detect membrane fouling or degradation early. Keep feed water within the specified temperature range, because cold water reduces output and very warm water shortens membrane life. Follow IEC 61010-1 and local plumbing rules, and ensure the drain can carry the concentrate. Record conductivity, recovery and service dates so performance trends are visible.
How do I select the right Two-Stage Reverse Osmosis System?
Choose two stages when single-stage rejection is insufficient or when you want better feed for deionization to reduce resin regeneration. For soft, low-salinity feed a single stage is enough. In the RFQ, state feed analysis, target purity and volume.
How does it compare with other RO Systems variants?
Begin with the feed water analysis: hardness, chlorine, iron, silica, turbidity and conductivity determine the pretreatment and the membrane type. Then size the system by daily and peak permeate volume, remembering that temperature and feed quality affect output. Choose a benchtop or wall-mounted unit for a few liters per hour, and a larger or staged system for higher demand. Check whether you need a storage tank and a distribution pump, and whether the permeate will feed a deionizer or ultrapure unit. Confirm the recovery rate and concentrate handling, since water use and drain capacity matter. Look for conductivity monitoring and automatic flushing, and ask about membrane life, filter change intervals and consumable cost per liter, which usually dominates the total cost.
Full specifications
| Permeate flow | 20–200 L/h |
|---|---|
| Ion rejection | 98–99.5 % |
| Operating pressure | 10–20 bar |
| Stages | 2 |
| Permeate conductivity | 1–5 µS/cm |
| Recovery | 30–60 % |
| Membrane elements | 2–4 |
| Monitoring | Inter-stage and permeate |
| Pump power | 0.5–2.2 kW |
| Power supply | 220–380 V, 50/60 Hz |
Indicative values for this product class. Final specifications are confirmed on the quotation and in the calibration documents supplied with the instrument.
Applications
- Moderately saline feed water
- High-purity Type III supply
- Feed for deionizers with long resin life
- Analytical laboratory water
- Pharmaceutical and food laboratory use
Key features
- Two membrane stages in series or permeate-reprocessing
- Higher recovery or higher purity depending on layout
- Permeate of about 1–5 µS/cm
- Operating pressures up to 15–20 bar
- Inter-stage and permeate monitoring
- Extends downstream resin life
Frequently asked questions about Two-Stage Reverse Osmosis System
Not necessarily. If the second stage processes the concentrate, recovery increases while purity is similar. If it reprocesses permeate, purity increases. Confirm the layout you need.
Two-stage designs compress the same water more times, so feed pressure must rise to overcome the second membrane's osmotic pressure, especially with saline feed. Confirm the pump and membrane ratings.
Lower ionic load means the ion exchange resin is exhausted more slowly, so regeneration or replacement intervals lengthen and running costs fall. The resin also produces higher final resistivity.
Typically 90 to 99 percent rejection of dissolved ions, giving a permeate of about 1 to 15 microsiemens per centimeter from potable feed. This meets Type III water and is suitable as feed for deionization or ultrapure polishing.
It buffers peak demand, lets the system run efficiently at its design rate and provides water if the feed is interrupted. A tank should be vented, protected from light and periodically sanitized to prevent biofilm.
Typically every two to three years, or sooner with poor feed quality or high demand. Replace when permeate conductivity rises, flow falls or pressure drop increases despite cleaning.
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