Page 5 - Dairy Dimension - Mar-Apr 2025
P. 5

| Volume 1 | Issue 3 | Mar-Apr 2025  SUSTAINABILITY FOCUS                       | Volume 1 | Issue 3 | Mar-Apr 2025







 Non-Biofouling



 Membranes Using Positive


 and Negative Charges for Dairy


 Wastewater Streams




 Dairy wastewater management presents a significant
 challenge due to its complex composition, high organic
 load, and potential for biofouling in conventional
 treatment systems. The presence of fats, proteins,
 lactose, and other suspended solids contributes to rapid
 membrane fouling, which reduces efficiency and
 increases operational costs. Biofouled membranes
 require frequent cleaning, increased chemical usage,
 and have shorter lifespans, all of which raise overall
 treatment expenses.
          2.  General Plant Wastewater                           contaminant loads and pH conditions while
 To address these challenges, non-biofouling membranes
 with positive and negative charge configurations have   ·  This category includes a mixture of several waste   maintaining high efficiency.
 emerged as an effective solution. These membranes   streams such as Clean-in-Place (CIP) solutions, CIP   3.  Membrane Fouling and Cleaning Requirements
 mitigate fouling by leveraging electrostatic interactions   flush water, product losses from silos, and NF      Conventional membranes require frequent cleaning
 that prevent the adhesion of organic and biological   permeate.  due to irreversible fouling caused by organic matter,
 contaminants. This innovative approach enhances   ·  The variability in composition makes it difficult to   microorganisms, and inorganic scaling. Repeated
 Prof. Lalit Vashista  membrane longevity, reduces maintenance costs, and   implement a uniform treatment approach.  cleaning reduces membrane lifespan and increases
 Diva Envitec  improves water recovery—making it a sustainable and   ·  Depending on the processing stage, this   downtime and operational expenses.
 economically viable solution for dairy wastewater   wastewater can exhibit fluctuating pH levels, high   4.  High Chemical and Operational Costs
 treatment.     chemical oxygen demand (COD), and varying         Traditional membrane systems rely on chemical
 Dairy Wastewater Streams  concentrations of fats, proteins, and lactose.  dosing to control fouling, resulting in higher use of
 Dairy wastewater is generated from various stages of   Challenges in Dairy Wastewater Treatment  detergents, acids, and alkalis. Energy-intensive
 processing and cleaning operations within dairy plants.   1.  Protein Denaturation and Biofouling  processes like high-pressure filtration also contribute
 The primary sources include:     Proteins in dairy wastewater tend to denature when   to rising operational costs.
 1.  Ultrafiltration (UF) Permeate and Nanofiltration   exposed to heat or chemicals. Upon denaturation,   Solution: Non-Biofouling Membranes with Positive
 (NF) Permeate  they form hydrophobic aggregates that strongly   and Negative Charges
    These streams contain lower concentrations of   adhere to membrane surfaces, causing biofouling.   Non-biofouling membranes are engineered to resist
 organics but still pose a risk of membrane fouling if   This increases filtration resistance, lowers permeate   organic and biological fouling through surface charge
 not properly managed. UF permeate typically   flux, and requires frequent cleaning, thus raising   modifications. These membranes use alternating
 consists of small molecules such as lactose and   operational costs.  positive and negative charges to prevent contaminant
 minerals, while NF permeate includes slightly larger   2.  Variability in Wastewater Composition  adhesion via electrostatic repulsion. This mechanism
 organic compounds and dissolved solids. Effective      The composition of dairy wastewater varies based on   significantly reduces fouling buildup and enhances
 treatment of these streams is essential to maintain   product type, processing methods, and cleaning   membrane performance.
 high water recovery rates and prevent secondary   protocols. This variability necessitates a flexible   PROMEM-B membranes, for instance, are designed for
 contamination.  treatment system capable of adapting to different   high-strength wastewater applications with minimal risk




 04                                                                                                         05
   1   2   3   4   5   6   7   8   9   10