Position: HOME > Product > Water purification equipment > Water Filter Element >
What is the Difference Between Anti-Fouling Reverse Osmosis Membrane LFC3-LD-4040 and Ordinary Reverse Osmosis Membranes? 4040 and 8080 Specification Selection Guide
  • What is the Difference Between Anti-Fouling Reverse Osmosis Membrane LFC3-LD-4040 and Ordinary Reverse Osmosis Membranes? 4040 and 8080 Specification Selection Guide

What is the Difference Between Anti-Fouling Reverse Osmosis Membrane LFC3-LD-4040 and Ordinary Reverse Osmosis Membranes? 4040 and 8080 Specification Selection Guide

Read 0 Reviews23 Q&As Write a Review
​ I. What is an Anti-Fouling Reverse Osmosis Membrane? What are its Core Differences from Ordinary Membranes? In the field of water treatment, membrane fouling is one of the main issues causing reduced system efficiency, and anti-fouling reverse osmosis membranes are specially designed membrane modules to address this pain point. Based on ordinary reverse osmosis membranes, they undergo material improvements and structural optimizations (such as surface hydrophilic treatment and refined pore size distribution) to reduce the adsorption and deposition of pollutants (e.g., organic matter, colloids, microorganisms) on the membrane surface, thereby extending cleaning cycles and lowering operating costs (Baidu Encyclopedia entry for "anti-fouling reverse osmosis membrane", 2024).

PARAMETER

Brand Name:
Model Number:
Nominal filtration rating:
Application:
Operating pressure:
Working temperature:
Replacement or not:Replacement

 I. What is an Anti-Fouling Reverse Osmosis Membrane? What are its Core Differences from Ordinary Membranes?  

In the field of water treatment, membrane fouling is one of the main issues causing reduced system efficiency, and anti-fouling reverse osmosis membranes are specially designed membrane modules to address this pain point. Based on ordinary reverse osmosis membranes, they undergo material improvements and structural optimizations (such as surface hydrophilic treatment and refined pore size distribution) to reduce the adsorption and deposition of pollutants (e.g., organic matter, colloids, microorganisms) on the membrane surface, thereby extending cleaning cycles and lowering operating costs (Baidu Encyclopedia entry for "anti-fouling reverse osmosis membrane", 2024).  

 

The core differences between anti-fouling reverse osmosis membranes and ordinary reverse osmosis membranes lie in three aspects:  

1. Surface Properties: Anti-fouling membranes typically have negative charges or hydrophilic groups on their surfaces, reducing electrostatic adsorption of negatively charged organic matter (e.g., humic acid) ( Principles of Membrane Separation Technology , 360 Library, 2023);  

2. Flow Channel Design: Anti-fouling membranes have wider water inlet channels (usually 30mil, compared to ordinary membranes~18-28mil) and faster water flow, which can promptly flush away pollutants;  

3. Material Toughness: Anti-fouling membranes use oxidation-resistant materials (e.g., enhanced polyamide), tolerating more frequent chemical cleaning (e.g., high-concentration NaOH solutions).  

 

For example, a comparative experiment at a municipal wastewater treatment plant showed: under the same raw water conditions, the operating cycle (interval between cleanings) of anti-fouling reverse osmosis membranes was 90 days, while that of ordinary membranes was only 45 days, reducing maintenance costs by approximately 40% (Case from third-party environmental forum "Green Valley Environment", 2024).  

 

 

 II. What is the LFC3-LD-4040 Reverse Osmosis Membrane? Core Parameters and Applicable Scenarios  

 2.1 Parameter Analysis of LFC3-LD-4040 Reverse Osmosis Membrane  

LFC3-LD-4040 reverse osmosis membrane is a typical low-pressure anti-fouling membrane model ("LFC" stands for "Low Fouling Composite", and "LD" stands for "Low Differential Pressure"). Its core parameters are as follows:  

- Standard water production: 365 gallons per day (GPD), equivalent to approximately 5.8 cubic meters per hour (based on standard conditions of 25°C and 100psi);  

- Salt rejection rate: 99.4% (initial rejection rate for sodium chloride);  

- Operating pressure: Recommended 80-150psi (lower than ordinary membranes150-300psi, more energy-efficient);  

- Temperature resistance range: 0-45°C (during operation), adapting to water temperature changes in different climatic regions;  

- Inlet water pH range: 2-11 (operation), 1-13 (cleaning), with strong compatibility.  

 

 2.2 Outstanding Advantages of LFC3-LD-4040 Reverse Osmosis Membrane  

1. Low-pressure energy efficiency: An operating pressure of 100psi is over 30% lower than ordinary membranes. After using this membrane, a food factory reduced its monthly electricity bill for the water treatment system by approximately 2,000 yuan (2023 enterprise practice data);  

2. Strong anti-fouling performance: The hydrophilic coating on the membrane surface results in a water contact angle 60° (ordinary membranes are approximately 80°), making it harder for pollutants to adhere ( Research on Surface Modification Technology of Anti-Fouling Membranes , academic paper, 2024);  

3. Stable water production: With raw water turbidity fluctuations 2NTU, the water production variation rate is 3%, suitable for scenarios with unstable water quality (e.g., surface water treatment).  

 

 

 III. Specification Differences Between 4040 Reverse Osmosis Membrane and 8080 Reverse Osmosis Membrane: How to Match System Requirements?  

 3.1 Specification Parameter Comparison Table  

Specification Indicator

4040 Reverse Osmosis Membrane (Taking LFC3-LD-4040 as an Example)

8080 Reverse Osmosis Membrane (Taking LFC3-LD-8080 as an Example)

Size (inches)

Diameter 4 × Length 40

Diameter 8 × Length 80

Water production per unit (GPD)

365

3200

Membrane area (square feet)

85

400

Weight (kg)

Approximately 12

Approximately 45

Applicable system water production

1-8 tons/hour

10-50 tons/hour

 

(Source: Dow Anti-Fouling Membrane Technical Manual , compiled by third-party industrial materials platform "Material Library" in 2024)  

 

 3.2 Three Core Factors to Consider During Selection  

1. System scale: Small factories (e.g., cosmetics factories with a water production demand of 3 tons/hour) are suitable for 4040 reverse osmosis membranes (usually 3-4 in parallel); large-scale projects (e.g., industrial park wastewater treatment with a water production demand of 20 tons/hour) require 8080 reverse osmosis membranes (2-3 in parallel are sufficient).  

2. Installation space: The membrane housing of 4040 reverse osmosis membrane has a diameter of approximately 15cm and a length of approximately 1.2m, suitable for narrow machine rooms; the membrane housing of 8080 reverse osmosis membrane has a diameter of approximately 30cm and a length of approximately 2.5m, requiring more installation and maintenance space.  

3. Cost budget: A single 8080 reverse osmosis membrane is approximately 5-6 times the price of a 4040 reverse osmosis membrane , but the cost per unit water production is lower (e.g., 8080 membrane costs approximately 0.05 yuan per GPD, while 4040 membrane costs approximately 0.08 yuan), making long-term operation more economical (2023 quotation analysis from a water treatment engineering company).  

 

 

 IV. Pollution Types and Prevention of Reverse Osmosis Membranes: Practical Methods to Extend Service Life  

 4.1 Common Pollution Types and Judgment Basis  

Pollution Type

Causes

Manifestations

Colloidal pollution

Colloidal particles such as clay and iron oxides in raw water

Increased inlet pressure, decreased water production

Organic pollution

Humic acid, proteins, oils, etc.

Viscous attachments on the membrane surface, slightly decreased salt rejection rate

Microbial pollution

Growth of bacteria and algae on the membrane surface

Odor in produced water, biological mucosa in the concentrated water end

Scaling pollution

Excessive calcium magnesium carbonate, sulfate, etc.

Significantly decreased salt rejection rate, increased hardness of produced water

 

(Source: Diagnosis and Control of Reverse Osmosis Membrane Fouling , Wikipedia entry for "RO membrane fouling", 2024)  

 

 4.2 Targeted Prevention and Control Measures  

1. Enhanced pretreatment:  

   - Colloidal pollution: Add flocculants (e.g., PAC) and use ultrafiltration pretreatment to remove particles with a size 0.1μm;  

   - Microbial pollution: Add chlorine or use ultraviolet disinfection to ensure residual chlorine in inlet water is 0.1-0.5mg/L (but reducers must be added before the membrane to remove residual chlorine to avoid oxidizing the membrane material).  

2. Operating parameter control:  

   - Maintain stable inlet water temperature (fluctuation ≤±2°C) to avoid rapid microbial reproduction due to sudden temperature rise;  

   - Control recovery rate (produced water/inlet water): It is recommended to be 75% for brackish water systems and 45% for seawater systems. Excessively high recovery rates will cause excessive salinity on the concentrated water side, accelerating scaling.  

3. Scientific cleaning plan:  

   - Colloidal/organic pollution: Circulate and clean with 0.1% NaOH solution (pH12-13) for 60 minutes;  

   - Scaling pollution: Clean with 1% citric acid solution (pH2-3) at room temperature, and heat to 30°C if necessary to enhance effectiveness ( Industrial Reverse Osmosis Membrane Cleaning Guide , 360 Library, 2023).  

 

Case: An electronics factory used LFC3-LD-4040 reverse osmosis membrane to treat groundwater. Due to uncontrolled recovery rate (reaching 85%), calcium carbonate scaling appeared on the membrane surface after 3 months, and water production decreased by 25%. After cleaning with citric acid and adjusting the recovery rate to 70%, water production returned to normal, and no severe scaling occurred in the subsequent 6 months (2024 factory equipment maintenance report).  

 

 

 V. Performance Testing of Anti-Fouling Reverse Osmosis Membranes: Three Key Indicators and Testing Methods  

 5.1 Salt Rejection Rate Attenuation Speed  

Salt rejection rate is a core performance indicator of anti-fouling reverse osmosis membranes . For high-quality membranes, after 1 year of operation, the salt rejection rate attenuation should be 2% (e.g., from 99.4% to 97.4%). Testing method: Use a conductivity meter (accuracy 0.01μS/cm) to detect the conductivity of raw water and produced water respectively, calculate according to the formula "salt rejection rate = (1 - produced water conductivity / raw water conductivity) × 100%", and test and record the trend once a week.  

 

 5.2 Pressure Drop Increase  

The pressure difference (ΔP) between the inlet and outlet of the membrane module is an important indicator reflecting the degree of pollution. The ΔP of a new membrane is usually 5psi. For high-quality anti-fouling reverse osmosis membranes , after 6 months of operation, the ΔP increase should be 10psi (ordinary membranes may reach more than 20psi). The testing tool is a precision pressure gauge (accuracy ±0.5psi), and data comparison should be conducted under the same flow and temperature conditions.  

 

 5.3 Number of Chemical Cleaning Tolerances  

Anti-fouling membranes should withstand more chemical cleanings. Industry standards require that after 50 standard chemical cleanings (alternating acid and alkali), water production and salt rejection rate can still maintain more than 85% of the initial values. A laboratory test on LFC3-LD-4040 reverse osmosis membrane showed that it still met this standard after 60 cleanings ( Anti-Fouling Membrane Durability Test Report , 2024).  

 

 

 VI. System Design of Reverse Osmosis Membranes: How to Match Components for Optimal Performance?  

 6.1 Core Components of Pretreatment System  

1. Quartz sand filter: Removes large particles such as sediment and rust in raw water, reducing turbidity to 5NTU;  

2. Activated carbon filter: Adsorbs organic matter, residual chlorine, and odors to protect the membrane from oxidation (activated carbon iodine value should be 800mg/g to ensure adsorption capacity);  

3. Security filter: Uses 5μm precision PP cotton filter elements to intercept fine particles remaining after pretreatment, avoiding membrane surface scratches.  

 

 6.2 Membrane Module Arrangement  

- Parallel arrangement: Increases water production, suitable for scenarios with high treatment demand (e.g., 8 4040 reverse osmosis membranes in parallel, water production is approximately 8 times that of a single unit);  

- Series arrangement: Improves salt rejection rate. For example, connecting 2 groups of membranes in series, with the concentrated water of the first group as the inlet water of the second group, the total salt rejection rate can be increased to over 99.9% (suitable for high-purity water demand, such as electronic-grade pure water).  

 

 6.3 Auxiliary Equipment Configuration  

- High-pressure pump: Selected according to the operating pressure of the membrane. For example, LFC3-LD-4040 reverse osmosis membrane needs a high-pressure pump with a head of 120 meters (corresponding to 175psi);  

- Flow meter: Monitors produced water and concentrated water flow to calculate the recovery rate (recovery rate = produced water flow / inlet water flow × 100%);  

- Chemical cleaning device: Includes a cleaning water tank, cleaning pump, and filter to ensure clean and impurity-free cleaning fluid.  

 

 

 VII. Summary: Core Recommendations for Anti-Fouling Reverse Osmosis Membrane Selection and Application  

Anti-fouling reverse osmosis membranes (such as LFC3-LD-4040 reverse osmosis membrane ) outperform ordinary membranes in complex water quality treatment due to their anti-fouling and low-pressure energy-saving advantages. During selection, it is necessary to consider the system scale 4040 reverse osmosis membranes are flexibly adapted to small and medium-sized systems, while 8080 reverse osmosis membranes are more suitable for large-scale water treatment; at the same time, raw water quality (e.g., pollutant type, salinity) should be evaluated to design targeted pretreatment and operating parameters.  

 

In daily use, it is necessary to judge membrane performance by regularly testing indicators such as salt rejection rate and pressure drop, and conduct timely cleaning and maintenance. In the future, with the development of nano-coating technology, the service life of anti-fouling reverse osmosis membranes is expected to extend from the current 3-5 years to more than 7 years, further reducing water treatment costs ( Membrane Material Innovation and Development Report , industry white paper 2024).  

 

Whether for industrial pure water preparation or municipal reclaimed water reuse, selecting a suitable reverse osmosis membrane and conducting scientific operation and maintenance are crucial to ensuring efficient and stable system operation. As a mature model in the anti-fouling field, LFC3-LD-4040 reverse osmosis membrane has proven its performance in numerous practices and can be a priority choice for complex water quality scenarios.



{sval:sql sql='SELECT n_parameter FROM dede_addonarticle WHERE aid = ~aid~ ' } {/sval:sql}
{sval:sql sql='SELECT n_parameter FROM dede_addonarticle WHERE aid = ~aid~ ' } {/sval:sql}