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MEMBRANE CLEANING COST EFFECTIVE SOLUTION
Kimberlite Chemicals India Private Limited
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Over view of the Presentation
Kimberlite an introduction of production &
R&D Lab
Types of Membrane fouling
Basic chemistry of membrane fouling
General Membrane Cleaning procedures
Kimberlite cleaning solution
Advantages
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Vision
With the vision to be a
leading, globalspecialty chemicals
company in the world
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Mission
We satisfy our customers by delivering
results through quality chemical products
and services. Our desire to grow drives ourpassion to win in the marketplace. With a
unified, economical operating structure, we
will remain competitive across specialty
Chemicals business and in every geographic
region.
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Values
We act with integrity and honesty.
We focus on customer .
We drive innovation and results by
understanding the market and its opportunities. We are committed to the values of responsibility,
sustainability and transparency.
We create safe and health-conscious work
environments, require compliance and embraceenvironmental stewardship.
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Company overview
Established in 1997
Operations in 3 countries
India,
Singapore and
UAE
More than 500 Clients in 18 Countries
Australia, New Zealand, Spain, Chile, Argentina, SouthAfrica, Turkey, Kuwait, Malaysia, Mauritius, Kenya,
Bangladesh, Thailand, Singapore, Oman, Bahrain,
Philippines, UAE and India
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Head quarters : Bangalore, INDIA
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Kimberlite Chemicals
Production Unit
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Manufacturing & R&D facility at Malur, Karnataka,INDIA
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Liquid Products 16 tons per Shift
Powder Products 6 tons per shift
PRODUCTION CAPACITY
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Laboratory for Q.C and R & D
Q.C and R&D facility at Malur, Karnataka,INDIA
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Ware HouseKimberlite Chemicals
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Industries we serve with our Specialties
Water /waste water treatmentReverse Osmosis / Desalination
Sugar
Paint / Coatings / Dyes & Inks
Biocides / preservatives
Construction
Mining
Leather
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Base Line Products
Acrylic Dispersing Polymer
-Acrylic Homo Polymers
- Acrylic Co-polymers
-Acrylic Ter Polymers
Non Oxidising Biocides
-Di thio Carbamate Based
-Quaternary Ammonium
-Isothiozoline based
-DBNPA Based
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Main Line of ProductsFormulations
Membrane Treatment and Cleaning Chemicals
CoolingWater Treatment
Boiler Water TreatmentSugar Process
De-foamers
MiningPaint Additives
Construction Chemicals
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Quality
ISO 9001-2008 Certification from TUV
ANSI /NSF 60 certification for Membrane Antiscalants
from UL )Underwriters Laboratories) , USA
Non-toxicology certification from National Toxicology
Center, Pune INDIA. For Sugar Process Products
Membrane Manufacturers Approval Saehan
Membranes, Korea
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Membrane Treatment Products
1. Antiscalants
2. Cleaners
3. Biocides
4. De-chlorination
5. Coagulants & Floculants
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LAB FACILITY AT AWRTC
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LAB FACILITY AT AWRTC
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Membrane fouling
Accumulation of certain constituents in the feed water on thesurface of the membrane or in membrane matrix.
Membrane fouling is a complicated phenomenon andtypically results from multiple causes.
Electrostatic interactions occur among functional groups ofmembranes, fouling materials and water, primarily throughdissociation which strongly depend on the pH, ionic strength,and concentrations of multivalent cations in the solution
Hydrophobic/ hydrophilic interactions are functions ofstructure similarities between membranes and foulingmaterials
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Type of Membrane Fouling
Generally recognized by four categories &
mechanism of fouling.
inorganic fouling/scaling,
particle/colloids fouling,
microbial fouling,
organic fouling.
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Inorganic Fouling/Scaling
accumulation of inorganic precipitates such as metal
hydroxides, and scales on membrane surface or
within pore structure.
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Inorganic Fouling/Scaling
RO and NF membranes reject inorganic species.
Those species form a concentrated layer in the
vicinity of membrane-liquid interface - aPhenomenon referred to
concentration polarization.
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Particulate/colloid Fouling
Algae, bacteria, and certain natural organic matters
fall into the size range of particle and colloids.
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Particulate/colloid Fouling
In most cases, particles and colloids do not
really foul the membrane because the flux
decline caused by their accumulation on themembrane surface is largely reversible by
hydraulic cleaning measures such as backwash
and air scrubbing.
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Microbial/Biological Fouling
formation of bio films on membrane surfaces. Once bacteria
attach to the membrane, they start to multiple and produce
extra cellular polymeric substances (EPS) to form a viscous,
slimy, hydrated gel.Kimberlite Chemicals
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Organic Fouling
Organic fouling because of relatively high natural organicmatters (NOM) in source water.
For source water high in NOM, organic fouling is believed to bethe most significant factor contributed to flux decline
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Organic Fouling
Surface Waters:Natural Organic Matter (NOM)
Mostly humic substances
Complex, poorly defined anionic macromolecules
Wastewaters:Effluent Organic Matter (EfOM)
Soluble microbial products (polysaccharides, proteins)
Other organic matter
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Membrane fouling
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Membrane fouling
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Effects of Operating Strategies on
Membrane Fouling
Type of fouling Effects of Operating Strategy
Hydraulic
Cleaning
Feed
Chlorination
Feed
Acidification
Chemical
Cleaning
Inorganic
_ _ ++ ++Particulate ++ _ _ ++Microbial + ++ +* ++
Organic _ + _ ++
Note: - No effects or have negative effects.
+ Some positive effects, ++ Positive effects
* in conjunction of feed chlorination.Kimberlite Chemicals
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Membrane Fouling
Membrane fouling and cleaning is to
understand interactions
a) between fouling materials and membrane,
b) between cleaning chemicals and fouling
materials,
c) between cleaning chemicals and membrane,
d) among the fouling materials.
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Functionalized Colloidal Probe
Surface charge of membrane media isthe results of ionization of particularfunctional groups existed on themembrane surface (e.g., carboxyl andamine).
Ionization of a functional group &surface charge of a particularmembrane depends on pH.
On the other hand, colloids, particles,and dissolved organic matters typicallycarry negative charges at the pH ofnatural water.
Therefore, there is a tendency ofelectrostatic repulsion betweenmembranes and those constituents.
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Foulant Interactions in Membrane Filtration
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Organic Fouling
Organic Foulants: Humics
Model structure of humic acid
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Effect of Divalent Cations on RO
Humic Acid Fouling: Mg2+ vs. Ca2+
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Bridging Effect of Ca2+
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Effect of Divalent Cations on
Fouling: Other Divalent Cations
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Conceptual Model of Membrane
Fouling and CleaningFor membrane fouling dominated by the adsorption of natural organic
matter, and dominated by microbial causes to a less extent, the fouling and
cleaning can be illustrated by a simple conceptual model as
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Membrane fouling causes
Calcium carbonate scale Sulphate scale of Calcium, barium and strontium
Metal oxides (iron, manganese, copper, nickel,
aluminium, etc
Polymerized silica scale
Inorganic colloidal deposits
Natural organic colloidal deposits
Biological deposits
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Effect of non maintenance
Deposits will form on the membrane surface
Deposits become harder and tough to clean
RO membrane efficiency will come down drastically
Pressure drop across the membrane
Reduction of out put flow
Membrane life reduction
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Advantage of our cleaning solution
Rapid and efficient membrane cleaning
High flux and output levels
Minimal discharge of cleaning liquids Low consumption of water needed for membrane
cleaning operations (low foaming formulation)
Surfactant based formulation will lower the surface
tension loosening of the scale
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General protocol for cleaning
1. Acidic soak/circulation at temp.50-55 deg.C for 10
15 minutes. This will help to loosen any of the iron
and calcium scale present on the membrane, then
purge with water2. Alkaline solution soak for another 10 15 minutes to
loosen the organic scales
3. Subjecting the membrane with high velocity low
foaming alkaline solution for 10 15 minutes to
flush out the loosened scale
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Kimberlite product
(Tacelene Chem 8209)A product with a combination of
Alkali, Complexing agent,surfactant,etc
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Product Specification and test results
Name of the product Tacelene Chem 8209
Analytical report no. SKPL 0911002 / dt. 12/11/09
Batch No 002
Mfg. Date 11/11/09
Product Test ReportDescription Result Specification
Appearance Fine powder Fine powder
Colour off white White to off white
pH (1% solution withwater)
12.7 12.00 13.00
Solubility in water Completely
soluble
Completely
soluble in water
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Pilot Study on Membranes
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Tacelene Chem 8209
Permea e Reject % Recovery Feed Permeate %Reduction Permeate Reject % Recovery Feed Permeate %Reduction
001 2 min 65 600 9.8 1220 430 65 92 600 13.3 1220 380 69
5 min 65 600 9.8 1220 430 65 108 600 15.3 1220 320 74
10 min 65 600 9.8 1220 430 65 155 600 20.5 1220 210 83
15 min 65 600 9.8 1220 430 65 180 600 23.1 1220 185 85
20 min 65 600 9.8 1220 430 65 202 600 25.2 1220 140 89
Permeate Reject % Recovery Feed Permeate %Reduction Permeate Reject % Recovery Feed Permeate %Reduction
002 2 min 60 600 9.1 1220 480 61 65 600 9.8 1220 435 64
5 min 60 600 9.1 1220 480 61 92 600 13.3 1220 387 68
10 min 60 600 9.1 1220 480 61 126 600 17.4 1220 305 75
15 min 60 600 9.1 1220 480 61 165 600 21.6 1220 215 82
20 min 60 600 9.1 1220 480 61 198 600 24.8 1220 122 90
Permeate Reject % Recovery Feed Permeate %Reduction Permeate Reject % Recovery Feed Permeate %Reduction003 2 min 56 600 8.5 1220 455 63 68 600 10.2 1220 405 67
5 min 56 600 8.5 1220 455 63 100 600 14.3 1220 364 70
10 min 56 600 8.5 1220 455 63 138 600 18.7 1220 298 76
15 min 56 600 8.5 1220 455 63 175 600 22.6 1220 205 83
20 min 56 600 8.5 1220 455 63 210 600 25.9 1220 152 88
R.O
Membrane #
Time of
treatment
Before cleaning After cleaning (2.5% inDM water)
Flow rate (ml/min) TDS mg/l Flow r ate (ml/min) TDS mg/l
Pilot study of the cleaning powder
R.OMembrane # Time oftreatment
Before cleaning After cleaning (2.5% inDM water)
Flow rate (ml/min) TDS mg/l Flow r ate (ml/min) TDS mg/l
After cleaning (2.5% inDM water)
Flow rate (ml/min) TDS mg/lR.O
Membrane #
Time of
treatmentFlow rate (ml/min) TDS mg/l
Before cleaning
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