

Benchtop Reverse Osmosis System
台式反渗透系统
- SKU RSY-0001
- 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 | 5–30 L/h |
|---|---|
| Ion rejection | 90–98 % |
| Feed pressure required | 2–4 bar |
| Operating pressure | 4–10 bar |
| Membrane type | Polyamide thin-film composite |
| Recovery | 15–30 % |
By Lab Manufacturers China Technical TeamLast reviewed Standards: ISO 3696, CLSI GP40, IEC 61010-1
What is the Benchtop Reverse Osmosis System?
A benchtop reverse osmosis system is a compact unit that produces a few liters per hour of Type III water from tap feed. It is used as a point-of-use purifier or as the first stage before deionization.
What is the Benchtop Reverse Osmosis System?
A benchtop reverse osmosis system is a compact unit that produces a few liters per hour of Type III water from tap feed. It is used as a point-of-use purifier or as the first stage before deionization.
Overview
The benchtop reverse osmosis system sits on the laboratory bench and connects to a tap or a small pressure tank. It typically produces 5 to 30 liters per hour of permeate with 90 to 98 percent ion rejection, using a low-pressure polyamide membrane and a booster pump rated 0.1 to 0.5 kilowatts. Pretreatment includes a sediment filter and an activated carbon block for chlorine removal, and often a small storage pressure vessel of 5 to 15 liters. Permeate conductivity is displayed or monitored, and an automatic flush valve protects the membrane during idle periods. The unit is easy to install, needs only a feed connection and a drain, and is used for glassware rinsing, reagent preparation and as feed to a deionizer. Consumables are the prefilters and the membrane, and recovery is usually 15 to 30 percent.
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?
- Compact benchtop form with tap feed and drain
- Output of 5–30 L/h of Type III water
- 90–98 % ion rejection with a polyamide membrane
- Sediment and carbon pretreatment filters
- 5–15 L pressure storage vessel
- Automatic flush to protect the membrane
What are the technical specifications?
A typical benchtop reverse osmosis system configuration offers permeate flow of 5–30 L/h, ion rejection of 90–98 %, feed pressure required of 2–4 bar, operating pressure of 4–10 bar, membrane type of Polyamide thin-film composite and recovery of 15–30 %. 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 Benchtop Reverse Osmosis System is used in glassware rinsing water, reagent preparation, feed to deionizer, general laboratory washing and autoclave feed. 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 Benchtop Reverse Osmosis System?
Choose a benchtop system for a small laboratory needing a few liters per hour at the point of use, and add a deionizer if higher purity is required. For larger volumes, use a wall-mounted or storage-tank system. In the RFQ, state feed quality, volume and purity target.
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 | 5–30 L/h |
|---|---|
| Ion rejection | 90–98 % |
| Feed pressure required | 2–4 bar |
| Operating pressure | 4–10 bar |
| Membrane type | Polyamide thin-film composite |
| Recovery | 15–30 % |
| Storage vessel | 5–15 L |
| Pretreatment | Sediment and carbon filters |
| Monitoring | Permeate conductivity display |
| Power supply | 220–240 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
- Glassware rinsing water
- Reagent preparation
- Feed to deionizer
- General laboratory washing
- Autoclave feed
Key features
- Compact benchtop form with tap feed and drain
- Output of 5–30 L/h of Type III water
- 90–98 % ion rejection with a polyamide membrane
- Sediment and carbon pretreatment filters
- 5–15 L pressure storage vessel
- Automatic flush to protect the membrane
Frequently asked questions about Benchtop Reverse Osmosis System
Yes, with a feed valve and a drain connection. Check that feed pressure is within range, because low pressure reduces output and high pressure may need a regulator.
Sediment and carbon filters are usually changed every three to six months, or when the pressure drop rises or chlorine breakthrough is detected. The membrane lasts two to three years typically.
Not directly. Reverse osmosis water is Type III and still contains ions and organics. Use it as feed to an ultrapure system that adds ion exchange, UV and ultrafiltration for Type I water.
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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