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Source high-capacity, skid-mounted, single and double pass industrial reverse osmosis (RO) plants from 500 LPH to 50,000+ LPH, pre-treatment filters, CIP skids, and plant components from ScientificEdge — India's trusted B2B water treatment sourcing partner.
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An industrial RO plant is a skid-mounted system that treats large volumes of borewell, surface or treated effluent water to a defined process, utility, boiler feed or cooling tower standard. Selecting one is not a single decision: feed water chemistry, required permeate flow, target conductivity, recovery and the degree of automation each move the design, and they move it in different directions.
Feed chemistry comes first, and TDS is only the headline. Hardness, silica, SDI and organic load each cap what the plant can do independently of the salinity — a feed at a comfortable 900 ppm with 40 ppm of silica constrains recovery more tightly than a 2,500 ppm feed with none. The plant is designed against the whole analysis, which is why a raw water report is the first thing asked for.
Capacity is then set by peak hourly demand rather than daily total. A facility drawing 40,000 litres a day across two shifts is not a 1,700 LPH plant if the draw arrives in a four-hour window; it is a larger plant, or a smaller one with storage sized to bridge the peak. Getting this wrong is the most common cause of a plant that meets its specification on paper and runs short in practice.
Architecture follows the purity target. A single pass reaches roughly 96 to 99 percent salt rejection and suits most process and utility duty. Where the specification asks for low-conductivity permeate — pharmaceutical purified water feed, or high-pressure boiler makeup — a second pass on the first pass permeate is the usual answer. Final selection should rest on the raw water analytical report, peak hour volumetric demand, footprint and electrical load limits, component brand preferences and the discharge disposal norms the site is bound by.

500 LPH – 50,000+ LPH
Plant capacity range
Roughly 0.5 to 50+ m³/hr. Compact 4040 skids at the low end, multi-stage 8040 vessel arrays at the high end.
65–85 %
Typical design recovery
Capped by concentrate saturation rather than by pump capability. Silica and calcium sulphate are usually the limiting salts.
< 2–5 µS/cm
Double pass permeate
Where a single pass typically lands in the tens of µS/cm. The second pass is what meets a pharmaceutical or HP boiler specification.
ScientificEdge supports sourcing and supply of suitable industrial RO plants, skid-mounted reverse osmosis systems, pre-treatment modules, high-pressure pump skids, and plant components based on raw feed water TDS, required permeate flow rate (LPH / m³/hr), target purity, brand preferences, technical documentation, and buyer specifications.
Six configurations across the range. Capacity sets the vessel size and count; the duty sets whether one pass is enough.
| Plant configuration | Capacity and typical application | Key technical features |
|---|---|---|
| Commercial & Small Industrial RO Plants | 500–2,000 LPH — hotels, hospitals, institutions, food processing and small manufacturing | Compact 4040 or single-vessel 8040 skid-mounted units, small footprint, single-phase or light three-phase load |
| Medium Industrial RO Plants | 3,000–10,000 LPH — factory utility supply, textile units, chemical mixing and boiler pre-treatment | Standard 8040 multi-vessel skids in a staged array, with media pre-treatment and dosing integrated on the frame |
| Large Industrial & Municipal RO Plants | 15,000–50,000+ LPH — heavy process industry, power stations, refineries and industrial water parks | Multi-stage 8040 vessel arrays, typically 2:1 or 3:2:1 staging, with instrumentation sized for normalised performance monitoring |
| Double Pass Industrial RO Plants | Pharmaceutical purified water feed and high-pressure boiler makeup | First pass permeate treated a second time for low-conductivity output, commonly below 2–5 µS/cm, often with interstage caustic dosing |
| Containerised / Mobile Industrial RO Systems | Remote project sites, temporary works and emergency utility supply | Insulated plug-and-play container housing pre-treatment, RO skid and CIP, commissioned on power and feed connection |
| High Recovery / ZLD Brine Concentrator RO Plants | Zero liquid discharge compliance in textile, dyeing and chemical plants | High-pressure configurations with energy recovery devices, reaching 80–85 % recovery where the concentrate chemistry permits |
Indicative configuration bands rather than fixed product models. Actual capacity, recovery, permeate conductivity, operating pressure and power draw depend on feed water chemistry, temperature and the components selected, and are confirmed against the technical datasheet and projection for the plant quoted.
Raising recovery from 75 to 85 percent sounds like a ten-point improvement and is often written into a tender as one. What it actually does is concentrate the feed from four times to nearly seven times at the tail of the array. Every sparingly soluble salt in the raw water is multiplied by that factor, and the plant runs against whichever one saturates first.
In Indian groundwater that is usually silica or calcium sulphate. Silica in particular has a hard practical ceiling — around 120 to 150 ppm in the concentrate depending on temperature, pH and the antiscalant used — and once it precipitates, the scale is not removed by ordinary acid cleaning. Calcium sulphate behaves similarly. Neither is a pump problem, so no amount of pressure buys past it.
The right sequence is to take the raw water analysis, calculate the saturation indices at the proposed recovery, and let that number set the recovery rather than the other way round. Where a higher recovery is genuinely needed, the honest routes are pre-treatment that removes the limiting ion, a different antiscalant with a verified threshold, or a two-stage arrangement with interstage adjustment — not simply a bigger pump.

A plant is a long BOQ before it is a skid. These are the lines quoted alongside it, so a new plant or a retrofit comes from one desk.
Pre-engineered skids across the range, specified from the feed analysis and the peak hourly draw.
The stage that decides how long the membranes last, sized on the worst-case raw water rather than the average.
The barrier that brings SDI reliably inside the element limit where media filtration alone cannot.
Vessels in the pressure class the pump shut-off head requires, not merely the class the elements fit.
Pumps matched to applied pressure and array flow, with mechanical seals and spares held against them.
Sized on the volume of one vessel bank and the flow the elements tolerate during cleaning.
Automation to the level the site will actually operate and maintain, which is not always the highest level available.
Dosing chemistry selected from concentrate saturation at the design recovery, not from a standing order.
The instrumentation without which normalised performance cannot be calculated or trended.
Wetted materials selected against chloride content and the cleaning chemistry the plant will see.
The duty decides the architecture. These are the plants most often specified in India, and what each one is actually solving for.
RO as the bulk removal stage ahead of DM or EDI, cutting the ionic load so regeneration frequency and chemical cost stay economic.
Double pass RO meeting the feed specification for the polishing stage, with documentation and qualification as much a requirement as performance.
Process water to a defined specification with wetted materials chosen for the site's chloride and cleaning chemistry.
High recovery configurations behind a UF or MBR barrier, where the discharge norm rather than the water demand drives the design.
Consistent product water with a controlled mineral profile, normally achieved through a blending line rather than by under-treating.
Bulk makeup water at high volume, with recovery set from concentrate saturation and the blowdown disposal route agreed at design stage.
RO as the front end of a high-purity train, sized so the downstream polishing stage is not carrying load it was never meant to.
Centralised plants sized on peak hourly draw with storage, where GST-compliant billing and tender-format documentation matter as much as the specification.
Ten details decide whether a plant can be configured on the first pass. Send what you have — the raw water analysis and the peak hourly demand alone are usually enough to begin.
Raw water source — borewell, surface or river water, STP/ETP outlet, or municipal supply
Raw water TDS (ppm), hardness and silica levels
Required permeate flow rate in LPH, GPD or m³/hr
Target permeate purity or conductivity limit in µS/cm
Single pass or double pass requirement
Framework and piping material preference — SS304, SS316 or UPVC
Degree of automation required — manual, semi-automatic or fully automatic PLC
Component brand preferences for membranes, pumps, vessels and PLC
Delivery location and target project schedule
GST, tender or corporate procurement requirement
As a trusted B2B distributor and supplier, ScientificEdge can coordinate technical datasheets, Process Flow Diagrams (PFD), Piping & Instrumentation Diagrams (P&ID), electrical single-line schematics, component performance test certificates, and ROSA/WAVE projection software calculations where available from the respective equipment manufacturer. Plant engineers are encouraged to share water analysis reports during enquiry to ensure precise plant design.
Stage sequence, instrumentation points and control philosophy, so the plant can be reviewed by your engineers before it is ordered.
Membrane, pump, vessel and instrument documentation for the items quoted, coordinated where the manufacturer issues them.
Connected load, starter arrangement and control supply, so the site electrical capacity is confirmed rather than assumed.
Array performance modelled against your feed chemistry, temperature range and staging, using the brand's own projection tool where it is available.
A projection is a model, not a performance guarantee — its output is only as good as the feed water analysis and temperature range it is run against, which is why both are asked for. Document availability depends on the manufacturer, the product and the supplied batch, and is confirmed once stock and specifications are established. ScientificEdge does not itself certify plant performance.
On the projection tools by name: ROSA is DuPont's legacy software, now superseded by WAVE; IMSDesign is Hydranautics'. Buyers still ask for all of them by name, so the projection is produced with whichever tool matches the membrane being quoted. Run it at the coldest month the plant will operate in — a design that only works at 25 °C is the most common avoidable fault in Indian industrial RO.
ScientificEdge supports sourcing and distribution enquiries for industrial RO plants, skids, and high-performance components from reputed global and domestic brands, including Grundfos, CNP, Pentair, Wave Cyber, DuPont Filmtec, Hydranautics, Toray, Vontron, Schneider, Siemens, and equivalent options, subject to stock availability, buyer specification, technical compatibility, and documentation.
Brand names indicate the sourcing enquiries ScientificEdge can support. They do not indicate authorised distribution, official dealership or an exclusive partnership, and no brand logos are displayed. All brand and product names are the trademarks of their respective owners and are referenced only because buyers and tender documents specify by them; where your BOQ names a component we quote against it, and where it does not we usually offer more than one option so the comparison stays with you.
On a plant order the skid is one line among dozens. Splitting the rest across separate vendors is where lead times, compatibility gaps and commissioning delays come from.
A supply partner in India for industrial WTP OEMs, EPC contractors, O&M teams and plant utility heads.
Technical assistance matching raw feed water chemistry, recovery targets and peak flow demand to the correct plant configuration.
Pre-engineered skids, replacement membrane sets, pressure vessels, high-pressure pumps and CIP skids quoted together, so interfaces match at quotation stage.
Unbiased evaluation of single pass against double pass against containerised, including what each costs to run rather than only to buy.
GST-compliant billing and procurement alignment for private factories and government tenders alike.
Dispatch coordination across Delhi NCR, Gujarat, Maharashtra, Tamil Nadu, Telangana, Karnataka, West Bengal and other industrial corridors.
Fields marked with an asterisk are required. Capacity, feed TDS and configuration are what size the plant; everything else refines the quotation.
ScientificEdge is a B2B distributor and sourcing partner covering the whole plant BOQ from one desk — skid, pre-treatment, vessels, membranes, high-pressure pumps, CIP, dosing, instrumentation and piping — so interfaces are settled at quotation stage rather than discovered during commissioning.
The practical value is in sizing and paperwork: matching feed chemistry, recovery targets and peak demand to the right configuration, coordinating P&ID schematics, datasheets and projections where the manufacturer issues them, and invoicing in the form your procurement or tender process requires.
From roughly 500 LPH to 50,000+ LPH, which is about 0.5 to 50+ cubic metres per hour. Below about 2,000 LPH the plants are compact 4040 or single-vessel 8040 skids; from 3,000 to 10,000 LPH they are standard multi-vessel 8040 skids; above 15,000 LPH they are multi-stage 8040 arrays.
Size the plant on peak hourly demand rather than on daily total. A facility using 40,000 litres a day is not a 1,700 LPH plant if the draw arrives in a four-hour window — it is a larger plant, or a smaller one with storage sized to bridge the peak.
A single pass sends the feed through one RO stage and typically achieves 96 to 99 percent salt rejection, landing permeate in the tens of microsiemens per centimetre. That suits most process, utility and boiler pre-treatment duty.
A double pass treats the first pass permeate a second time, commonly reaching below 2 to 5 µS/cm. It is specified where the requirement genuinely demands it — pharmaceutical purified water feed, high-pressure boiler makeup, high-purity manufacturing — because it costs more to buy and to run. Where the specification does not demand it, a single pass with correct pre-treatment is the better plant.
The usual train is a multi-media or sand filter for suspended solids, activated carbon or metabisulphite dosing for free chlorine, a softener or antiscalant dosing for hardness and scaling salts, and 5 micron cartridge filtration immediately before the high-pressure pump.
What the plant actually needs comes from the raw water analysis. High SDI calls for ultrafiltration rather than media filtration alone; iron and manganese need oxidation and a solids barrier; high organic load calls for a UF or MBR barrier. Free chlorine in particular must be removed — it damages polyamide membranes irreversibly, and no cleaning recovers them.
Recovery is permeate flow divided by feed flow, expressed as a percentage. A plant taking 100 m³/hr of feed and producing 75 m³/hr of permeate is running at 75 percent recovery, with 25 m³/hr going to concentrate.
The achievable figure is set by the concentrate chemistry rather than by the pump. At 75 percent recovery the feed is concentrated four times at the tail of the array; at 85 percent, nearly seven times. Whichever sparingly soluble salt saturates first — usually silica or calcium sulphate in Indian groundwater — caps the recovery, and no amount of pressure buys past it.
Where the site has no suitable building, where the plant must move between locations, where the requirement is temporary, or where commissioning time matters more than capital cost. A container arrives with pre-treatment, RO skid and CIP already installed and interconnected, and needs only power, feed and drain connections.
A conventional skid inside an existing plant room is usually less expensive for the same capacity and easier to expand later. The container is bought for mobility, speed and site independence, not for treatment performance — the process inside is the same.
P&ID and process flow schematics, electrical single-line diagrams and membrane projection calculations can be coordinated where the respective manufacturer makes them available. ROSA is DuPont's legacy projection software, now superseded by WAVE; IMSDesign is Hydranautics'. The projection is produced with whichever tool matches the membrane being quoted.
A projection is a model rather than a performance guarantee, and its output is only as good as the inputs. Send the raw water analysis, the temperature range and the required permeate flow with the enquiry, and ask for the projection at the coldest month the plant will operate in rather than at 25 °C.
Yes, and replacement is a large part of the enquiry volume on this category. Membranes, pressure vessels, high-pressure and booster pumps, mechanical seals, CIP skids, dosing pumps, cartridge filters, instrumentation and control panel components are all supplied for plants already in service.
Send the existing plant capacity, the element model and vessel configuration currently installed, and the pump make and model if it is being replaced. Where the original component is discontinued, an equivalent can usually be offered — but the interface dimensions and pressure class need confirming rather than assuming, so include a photograph of the existing installation where you can.
Sourcing and distribution enquiries are supported for reputed global and domestic brands including Grundfos, CNP, Pentair, Wave Cyber, DuPont Filmtec, Hydranautics, Toray, Vontron, Schneider and Siemens, along with equivalent options.
This is subject to stock availability, buyer specification, technical compatibility and documentation, and does not indicate authorised distribution, official dealership or an exclusive partnership with any brand.
Yes. Dispatch is coordinated across Delhi NCR, Gujarat, Maharashtra, Tamil Nadu, Telangana, Karnataka, West Bengal and other industrial corridors, covering factory, project, municipal and institutional sites.
Lead time is confirmed per line item at quotation stage, because a stocked pump and a made-to-order skid differ substantially. Complete plants also need site readiness — foundation, power and drainage — confirmed against the delivery date, so tell us the site location and the target project schedule with the enquiry.
Specified alongside an industrial RO plant, and the component pages that carry the detail.
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