L9- Membranes & Other Technology Flashcards

1
Q

Filtration

A

Separation of particulate and colloidal matter from liquid

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2
Q

Membrance process - define streams

A

Feed water - influent water to membrance
Permeate - compounds passing through membrane
Retentate - compounds not passing through membrane

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3
Q

Pressure driven membrane- Size of separation

A

Low P: Microfiltration (MF) & Ultrafiltration (UF)
High P: Nanofiltration (NF) & Reverse Osmosis (RO)

Smallest size filtered: RO < NF < UF < MF

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4
Q

Membrane configuration types and materials

A

Tubular, hollow fine fibre, spiral wound, plate and frame

Materials: symmetric, asymmetric, thin-film composites

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5
Q

Driving force of membrane separation

A

Hydraulic pressure or vacuum

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6
Q

Desalination

A

Mineral components from saline water (salty)
Desalinated for human consumption or irrigation

Dis: High operation costs, produces salty brine, no materials in water

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7
Q

Cross-flow operational mode

A

Feed water tangental to membrane

Ptm = [(Pf + Pr)/2] - Pp

Ptm = transmembrane pressure gradient (bar)
Pf, Pr, Pp = pressure of feed, retentate, permeate (bar)

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8
Q

Dead-end operational mode

A

All feed water passes through membrane

Ptm = Pf - Pp

Ptm = transmembrane pressure gradient (bar)
Pf, Pp = pressure of feed, permeate (bar)

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9
Q

Recovery, r(%) - define variables

A

r(%) = (Vp/Vf)100 (Also (Qp/Qf)100)

Vp, Vf = volumetric flow of permeate and feed (m3/d)

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10
Q

Permeate flowrate, Qp - define variables

A

Qp = Fw*A

Fw = transmembrane water flux rate (m/h)
A = membrane are (m2)

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11
Q

Rejection of contaminant, R(%) - define variables

A

R(%) = [1-(Cp/Cf)]100 (Also [(Cf-Cp)/Cf]100)

Cp, Cf = concentrations of permeate and feed (kg/m3)

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12
Q

Log rejection, LR - define variables

A

LR = -log(1-R) = log(Cf/Cp)

Cp, Cf = concentrations of permeate and feed (kg/m3)

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13
Q

Membrane mass balance

A

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)

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14
Q

Membrane fouling types

A

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

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15
Q

Osmotic pressure of solution - define variables

A

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)

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16
Q

Feed water flux, Fw - define variables

A

Fw = kw*(Delta P - Delta PI) = Qp/A

Fw = feed water flux (L/m2h)
kw = mass transfer coefficient for water flux (L/m2
h*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)

17
Q

Silt Density Index (SDI) - define variaibles

A

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

18
Q

Management of retentate

A

Concentrated brine solution: heavy metals, sals, organics, m/o
Treatment: solar evaporator, spray dryers
Disposal: deep well injection, to WWTP, to ocean

19
Q

Control of membrane fouling

A

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

20
Q

Summary of other treatment technologies

A

Advanced oxidation processes (AOPs), phytoremediation, distillation

21
Q

Advanced oxidation processes (AOPs) purpose, types and applications

A

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

22
Q

Describe types of AOPs

A

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

23
Q

Design considerations of AOPs

A

HO(radical) + R -> byproducts
rR = -kCHOCR

24
Q

Phytoremediation purpose, targets and factors affecting

A

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

25
Q

Distillation (importance of evaporation and condensation) & disadvantages

A

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

26
Q

Phytoremediation advantages and disadvantages

A

Adv: low cost, low environmental impact, preserve soil health, ease process monitoring

Dis: long treatment time, leaching of contaminants into ground water