Your privacy is important to us. It is Pam Membranas Seletivas’ policy to respect your privacy regarding any information we may collect from you on thePam Membranas Seletivas website and other websites we own and operate.
We request personal information only when we truly need it to provide you with a service. We do so through fair and lawful means, with your knowledge and consent. We also explain why we are collecting it and how it will be used.
We retain the information we collect only for as long as necessary to provide the requested service. When we store data, we protect it using commercially reasonable measures to prevent loss and theft, as well as unauthorized access, disclosure, copying, use, or modification.
We do not share personally identifiable information publicly or with third parties, except when required by law.
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Your continued use of our website will be considered acceptance of our privacy and personal information practices. If you have any questions about how we handle user data and personal information, please contact us.
The user agrees to make appropriate use of the content and information provided by Pam Membranas Seletivas on the website, including, but not limited to:
We hope this clarifies the matter, and as mentioned earlier, if there’s anything you’re unsure about whether or not you need, it’s generally safer to leave cookies enabled in case you interact with one of the features you use on our website.
This policy is effective as of November 29, 2025, at 9:12 p.m.
For questions, requests, or to exercise your rights under the LGPD:
📧 Email: vendas@pam-membranas.com.br
📞 Phone: (21) 3733-1988
📍 Address: MP Building, Rua Sydney Martins Gomes dos Santos, 52, Unit 01, Cidade Universitária, Rio de Janeiro, RJ.
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