Seawater desalination plant 1,000 L/h – SWRO

A 1,000 L/h SWRO seawater desalination plant quoted to order. Flocea studies the intake, pre-treatment, energy, discharge and operation.

Technical assessment
Requirements checked before quotation

Tailored response
Configuration matched to your site

Tracked delivery
Arranged to suit the project

Flocea support
A named point of contact

SKU: FLO-SWRO-1000
Category:

Description

A 1,000 litre-per-hour SWRO desalination plant for coastal sites with a substantial daily requirement: hotels, work camps, farms, construction sites or small infrastructure. The solution is designed at quotation from the raw water and the consumption profile.

1,000 L/hnominal output
Seawatertarget raw water
Mains supply to be confirmedsupply to be provided
Subject to studypre-treatment and configuration

Nominal capacity: actual output depends above all on salinity, temperature, pressure, membrane fouling and the quality of the pre-treatment. Flocea validates these parameters before proposing anything.

What projects is it for?

  • Hotel and residential development on the coast
  • Construction site or remote work camp
  • Farm and small community infrastructure

This capacity represents up to 24 m³ a day in continuous nominal operation. Sizing cannot stop at the flow rate, though: redundancy, buffer storage, pre-treatment, clean-in-place, brine discharge and continuity of service shape the project.

Choosing between a marine watermaker, seawater SWRO and brackish water BWRO

A complete study, not just a membrane

Water analysisTDS or salinity, pH, hardness, iron, turbidity and temperature.
Treatment trainIntake, pre-filtration, dosing, reverse osmosis, flushing and post-treatment.
Site conditionsEnergy, space, ventilation, corrosion, maintenance and concentrate discharge.

Specification of the proposed configuration

Nominal output 1,000 litres per hour, i.e. up to 24 m³/day over 24 hours
Raw water Seawater; analysis and seasonal variability to be documented
Technology High-pressure SWRO on a skid
Pre-treatment Multimedia, cartridge, dosing or ultrafiltration depending on the intake
Control system Control, safety functions, flushing and conductivity monitoring according to the project
Cleaning CIP loop to be provided according to criticality and required availability
Energy Power and voltage confirmed once the hydraulic selection is made
Options Containerisation, storage, UV, remineralisation and remote monitoring

Important: these figures set the framework for the study. The final bill of materials, power draw, recovery rate, permeate quality and dimensions are confirmed at quotation, once the raw water and the site have been validated.

Schéma des cinq étapes du dessalement par osmose inverse

Operation and consumables

For a professional installation, Flocea recommends an operating plan: simple daily checks, condition-based cartridge replacement, conductivity monitoring, CIP cleaning and a minimum stock of critical consumables.

  • pre-filter cartridges, replaced according to turbidity and running hours;
  • antiscalant or conditioning chemicals where the analysis justifies them;
  • membrane cleaning and preservation chemicals for extended shutdowns;
  • reverse osmosis membranes, whose life depends on pre-treatment and how the unit is run;
  • seals, sensors and pump wear parts, per the maintenance schedule.

Compare the Flocea range

Solution Nominal flow Raw water Typical project
Marine 30 30 L/h Seawater Sailing boat and small craft, building autonomy
Marine 100 100 L/h Seawater Large yacht with a full crew
SWRO 250 250 L/h Seawater Coastal villa, guest accommodation, small camp
SWRO 1000 1,000 L/h Seawater Hotel, farm, construction site, small authority
BWRO 500 500 L/h Brackish water Saline borehole, smallholding, process water
BWRO 2000 2,000 L/h Brackish water Agriculture, industry, community site
Informations nécessaires au dimensionnement d’un dessalinisateur

Frequently asked questions

Can a 1,000 L/h plant run continuously?

It can be designed for long operating windows, but the strategy depends on storage, maintenance, the intake and the level of redundancy expected.

Is a containerised installation necessary?

Not always. A suitable plant room can be enough. A container makes sense when the set has to be protected, pre-assembled and shipped to a remote site.

What happens to the salt concentrate?

It has to be discharged according to the site, the flow rate and local rules. That environmental constraint is part of the study that precedes the quotation.