L9- Membranes & Other Technology Flashcards
Filtration
Separation of particulate and colloidal matter from liquid
Membrance process - define streams
Feed water - influent water to membrance
Permeate - compounds passing through membrane
Retentate - compounds not passing through membrane
Pressure driven membrane- Size of separation
Low P: Microfiltration (MF) & Ultrafiltration (UF)
High P: Nanofiltration (NF) & Reverse Osmosis (RO)
Smallest size filtered: RO < NF < UF < MF
Membrane configuration types and materials
Tubular, hollow fine fibre, spiral wound, plate and frame
Materials: symmetric, asymmetric, thin-film composites
Driving force of membrane separation
Hydraulic pressure or vacuum
Desalination
Mineral components from saline water (salty)
Desalinated for human consumption or irrigation
Dis: High operation costs, produces salty brine, no materials in water
Cross-flow operational mode
Feed water tangental to membrane
Ptm = [(Pf + Pr)/2] - Pp
Ptm = transmembrane pressure gradient (bar)
Pf, Pr, Pp = pressure of feed, retentate, permeate (bar)
Dead-end operational mode
All feed water passes through membrane
Ptm = Pf - Pp
Ptm = transmembrane pressure gradient (bar)
Pf, Pp = pressure of feed, permeate (bar)
Recovery, r(%) - define variables
r(%) = (Vp/Vf)100 (Also (Qp/Qf)100)
Vp, Vf = volumetric flow of permeate and feed (m3/d)
Permeate flowrate, Qp - define variables
Qp = Fw*A
Fw = transmembrane water flux rate (m/h)
A = membrane are (m2)
Rejection of contaminant, R(%) - define variables
R(%) = [1-(Cp/Cf)]100 (Also [(Cf-Cp)/Cf]100)
Cp, Cf = concentrations of permeate and feed (kg/m3)
Log rejection, LR - define variables
LR = -log(1-R) = log(Cf/Cp)
Cp, Cf = concentrations of permeate and feed (kg/m3)
Membrane mass balance
Water: Qf = Qr + Qp
Contaminant: QfCf = QpCp + Qr*Cr
Recovery = Qp/Qf
Cp, Cf, Cr = concentrations of permeate, feed and retentate (kg/m3)
Qp, Qf, Qr = volumetric flow of permeate, feed and retentate (m3/d)
Membrane fouling types
Particulate fouling: Build-up of substances
Scaling: precipitation of salts
Organic fouling: presence of organics
Biological fouling: presence of m/o
Chemicals that react with membranes = permanent damage
Osmotic pressure of solution - define variables
PI = sum(iMRT)
PI = osmotic pressure (atm)
i = van’t Hoff factor of solute
M = molar concentration of solute (mol/L)
R = universal gas constant (0.08206 Latm/molK)
T = temperature (K)
Feed water flux, Fw - define variables
Fw = kw*(Delta P - Delta PI) = Qp/A
Fw = feed water flux (L/m2h)
kw = mass transfer coefficient for water flux (L/m2h*bar)
Qp = permate flowrate (L/h)
A = membrane area (m2)
Delta P = average applied pressure gradient, [(Pf+Pr)/2] - Pp (bar)
Delta PI = osmotic pressure gradient, [(PIf+PIr)/2] - PIp (bar)
Silt Density Index (SDI) - define variaibles
SDI = [100*(1-(ti/tf))]/t
SDI = treatability of given water/wastewater with NF/RO membranes
ti, tf,t = time to collect initial, final samples of 500mL and total time for running the test
Management of retentate
Concentrated brine solution: heavy metals, sals, organics, m/o
Treatment: solar evaporator, spray dryers
Disposal: deep well injection, to WWTP, to ocean
Control of membrane fouling
Pre-treatment of feed water: reduce TSS, colloids and bacteria (water conditioning)
Membrane backflushing: with water/air
Chemical cleaning: removes substances not removed by backflushing
Summary of other treatment technologies
Advanced oxidation processes (AOPs), phytoremediation, distillation
Advanced oxidation processes (AOPs) purpose, types and applications
Chemical oxidation aiming at mineralisation of contaminants to CO2, water and inorganics or at least transformation into harmless products
Types: Fenton, Photo-Fenton, electrodialysis
Applications: Polishing step in WWTP, remove persistent organic pollutants (POPs), disinfection
Describe types of AOPs
Wet oxidation: oxygen/air to achieve pollutant oxidation at high T&P - high operating costs
Fenton’s reagent: Destroy toxic compounds in WW using hydrogen peroxide with iron - low pH
Photo-Fenton: UV-Vis at 300nm> (control pH, dose, irradiation time)
Electrolysis: Uses DC to drive non-spontaneous chemical reaction; for WW with high alkalinity/salinity; no pH restriction
Design considerations of AOPs
HO(radical) + R -> byproducts
rR = -kCHOCR
Phytoremediation purpose, targets and factors affecting
Use living plants to clean up soil, air and water contaminated with hazardous contaminants (hyperaccumulators)
Targets: toxic heavy metals and organic pollutants
Factors: type of plants, type & conc. of pollutants, climate
Distillation (importance of evaporation and condensation) & disadvantages
Separate and extract clean water by vaporisation and condensation, i.e. Solar distillation
Evaporation to remove impurities; Condensation to collect water
Dis: scaling and corrosion problems, disposal of concentrated waste, high energy requirements
Phytoremediation advantages and disadvantages
Adv: low cost, low environmental impact, preserve soil health, ease process monitoring
Dis: long treatment time, leaching of contaminants into ground water