Yes. We supply MF/UF, NF/RO, and membrane distillation systems, as well as electrodialysis systems and equipment for gas permeation testing, among other products.
Yes. All equipment can be supplied with or without data acquisition, and with partial or full automation.
Yes. Our equipment allows for quick module replacement and comparative performance evaluation.
· MF: removes suspended solids, particles, and some microorganisms.
· UF: removes colloids, macromolecules, and viruses.
· NF: removes hardness, color, some salts, and low-molecular-weight organic compounds.
· OI: removes virtually all salts, ions, and micropollutants.
When the goal is to reduce COD, refractory organic matter, and hardness, thereby preparing the effluent for subsequent treatment stages (such as advanced treatment). In cases where pretreatment is effective at removing nutrients—particularly ammonia—NF may serve as the final treatment stage.
Yes. Technologies such as UF + NF + RO or NF alone are effective at reducing COD, ammonia, color, salts, and refractory organics.
Yes. We provide services ranging from research and development to complete industrial plants.
Yes, with both in-person and remote support.
Yes, subject to availability and the scope of the project.
Yes. All services can be accompanied by a comprehensive technical report upon request.
CHARACTERISTICS OF HOLLOW ULTRAFILTRATION FIBERS:
a) Membranes with a cylindrical geometry, of the hollow-fiber type (Figure 1);
b) Material of the hollow fibers: poly(ether sulfone);
c) Outer diameter of the fibers: between 0.8 and 0.9 mm;
d) Fibers with a selective outer layer;
e) UF fibers exhibit 95.0% effective retention for compounds with a molecular weight greater than 50 kDa;
f) Filtration occurs from the outside to the inside of the fibers;
g) The ultrafiltrated extract flows through the interior of the fibers;
h) Module construction material: weldable PVC;
i) Operating pressure: depends on the extract to be processed in the equipment. The critical pressure for each type of extract must be determined;
j) Maximum operating pressure: 5 bar;
l) Maximum operating temperature: up to 55.0°C;
m) pH: 2.0 to 13.0.

CHARACTERISTICS OF HOLLOW MICROFILTRATION FIBERS:
a) Membranes with a cylindrical geometry, of the hollow-fiber type;
b) Material of the hollow fibers: poly(imide);
c) Outer diameter of the fibers: between 0.9 and 1.0 mm;
d) Fibers with a selective outer layer;
e) Average pore size on the outer surface of the fibers: 0.4 µm (Figure 1);
f) Retention of 99.99% of the microorganisms and suspended solids present in the extract to be processed;
g) Filtration occurs from the outside to the inside of the fibers;
h) The microfiltrate flows through the interior of the fibers;
i) Operating pressure: dependent on the stream to be processed by the equipment. The critical pressure for each type of feed stream must be determined;
j) Maximum operating pressure: 5 bar;
l) Maximum operating temperature: up to 55.0°C;
m) pH: 2.0 to 13.0.

Devices that use a membrane to create a large contact area between two phases (gas-liquid) without allowing them to disperse.
One phase flows through one side of the membrane and the other through the other side. Mass transfer occurs through the pores without the phases mixing.
Water degassing (removal of O2 and CO2), carbonation of beverages, liquid-liquid extraction without emulsification.
A process for separating liquid mixtures in which the permeate is removed as vapor; effective for azeotropic mixtures.
A component preferentially permeates through the membrane and evaporates on the permeate side, which is maintained under vacuum.
Solvent dehydration (ethanol, isopropanol), removal of volatile organic compounds (VOCs) from water, separation of organic-organic mixtures.
The process with the highest rejection capacity. It removes virtually all dissolved salts and contaminants, producing water of the highest purity.
It applies pressure greater than the solution's osmotic pressure, forcing water to pass through the membrane in the opposite direction of the natural flow, leaving the salts behind.
Seawater desalination, production of ultrapure water for industries (pharmaceutical, semiconductor), and purification of water for consumption.
An intermediate process between UF and reverse osmosis, with pore sizes ranging from 1 to 10 nanometers. It removes multivalent ions (hardness) and low-molecular-weight organic molecules.
It operates at higher pressures than UF. It separates components based on size and electric charge, allowing monovalent ions to pass through.
Water softening, partial desalination, pesticide removal, wastewater recycling.
Similar to microfiltration, but with smaller pores (0.01 to 0.1 micrometer), capable of retaining viruses and macromolecules such as proteins.
It uses hydrostatic pressure to force the solvent through the membrane, while high-molecular-weight solutes are retained.
A membrane separation process that removes suspended particles, bacteria, and colloidal solids in the range of 0.1 to 10 micrometers. It operates at low pressures.
Water or a fluid is forced to pass through a microporous membrane. Particles larger than the pores are retained on the surface of the membrane.
✅ High flow rate
✅ Low energy consumption
✅ Effective removal of bacteria
✅ Easy to use