MEMBRAN - nuristianah.lecture.ub.ac.idnuristianah.lecture.ub.ac.id/files/2016/09/KP2_Membran.pdf ·...

14
MEMBRAN Nur Istianah-KP2-2016

Transcript of MEMBRAN - nuristianah.lecture.ub.ac.idnuristianah.lecture.ub.ac.id/files/2016/09/KP2_Membran.pdf ·...

MEMBRAN

Nur Istianah-KP2-2016

is a VERY THIN film that allows some types of

matter to pass through while leaving others behind

Membran = materials which have voids in them letting some molecules

pass more conveniently than some other molecules

semi-permeable membrane

Retentate

Permeate Membrane

Feed

Konsep dasar

Nur Istianah-KP2-2016

Driving force :

3. Voltage difference,

1. Pressure difference

2. Concentration difference

4. Temperature difference,

RO

UF

MF

Pervaporation

Dialysis

Membrane extraction

Electrodialysis

Membrane distillation

Nur Istianah-KP2-2016

Nur Istianah-KP2-2016 Diffusivity

Membrane

thickness

Conceentration and molar

volume of solvent

K (ΔP – Δπ ) Osmotic pressure

applied pressure

Flux (in kg/h.m2)

J =NA

Water flux increases with an increase in applied pressure, increased permeability of the membrane and lower solute concentration in the feed stream.

Jw(kg/h) = solvent (water) flux,

K(kg / m2.h.Pa) = mass transfer coefficient/permeability const.

A(m2) = cross area of the membrane,

Δ P(Pa) = applied pressure and

Δπ(Pa) = change in osmotic pressure.

Osmotic pressure is found for dilute solutions using:

π = MRT

Jw = kA (ΔP – Δπ)

Nur Istianah-KP2-2016

................... (2)

................... (3)

M=molarity, T(K), R= 8.314 kPa.m3mol-1K-1

Larger solutes become concentrated at the membrane

surface. The flux is therefore controlled by the applied

pressure, and the solute concentrations in the bulk of the

liquid and at the membrane surface:

Js= solute flux

c1= concentration of solutes at the membrane (initial)

c2= concentration of solutes in the liquid (final)

Nur Istianah-KP2-2016

................... (4) Js = kA ln (c1 / c2)

Nur Istianah-KP2-2016

Contoh soal

Jus buah yang mengandung 9% w/w partikel padat

(solid) telah diberi perlakuan pre-concentration

pada 35°C dengan reverse osmosis untuk

kemudian dilakukan ‘concentration’ pada

evaporator. Jika tekanan operasi RO adalah 4000

kPa dan koefisien transfer massa sebesar 6.3x10-3

kg.m-2h-1kPa-1, hitung luasan area membran yang

diperlukan untuk menghilangkan 5 ton permeate

selama 8 jam. (asumsikan mayoritas partikel padat

berbentuk sucrose dan konstanta gas universal (R=

8.314 kPa.m3mol-1K-1)

Nur Istianah-KP2-2016

Penyelesaian:

Molar concentration (M) = concentration (kg/m3) : molecular weight

M = 90/342 = 264 mol m-3 = 0.264 mol/L

Tekanan osmotic (persamaan 3)

π = 0.264 x 8.314 (35+273) = 676 kPa

Flux (kg/jam feed): J = 5000 kg / 8 jam = 625 kg/jam

Persamaan 2:

625 = 6.3x10-3. A (4000 – 676)

A = 29.9 m2 = 30 m2

Nur Istianah-KP2-2016

Latihan soal

Sebuah membran cellulose-acetate dengan area

4x10-3 m2 digunakan pada suhu 25°C untuk

menentukan konstanta permeabilitas RO larutan

garam yang mengandung 12 kg NaCl/m3 (ρ=1005.5

kg/m3) dan dihasilkan produk larutan dengan

konsentrasi 0.486 kg NaCl/m3 (ρ=997.3 kg/m3). Flow

rate produk adalah 3.84x10-8 m3/s dan tekanan

operasi sebesar 56.0 atm. Hitunglah konstanta

permeabilitas RO tersebut!

Densitas air pada 25°C adalah 997 kg/m3

#Bagaimana pengaruh kenaikan suhu sebesar 30 K

pada flow rate produk jika dioperasikan pada tekanan

sama!

Nur Istianah-KP2-2016

Series resistance

Nur Istianah-KP2-2016

Gas permeation

Nur Istianah-KP2-2016

Gas permeation

Nur Istianah-KP2-2016

Gas permeation

THANKS FOR YOUR ATTENTION

The best person is one give something useful always

Nur Istianah-KP2-2016