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. 2021 May 18;11(5):368. doi: 10.3390/membranes11050368

Table 2.

Summary of developed models for permeate flux prediction in which osmotic pressure is considered.

No. Model Authors Ref. Validation Matrix Main Transport Mechanism Configuration Module Type Number of Citations Model Validation in Publications
(2.1) J=|ΔP|-|Δπ|μRm Osmotic pressure Keden and Katchalsky (1958) [112] Water Convective Dead-end - 442 [113,114,115,116,117]
(2.2) J=A(ΔP-Δπ) Goldsmith (1971) [118] Dextran fractions (polysaccharides) - Cross-flow
Dead-end
Tubular
Stirred cell
138 -
(2.3) J=ΔP-acbnexp(nJ/k)Rm
Model parameters: a, n
Wijmans et al. (1984) [111] - - - - 201 [80,119]
(2.4) RP(t)=Rma1σΔπmΔPRma=Rma(Jwυw1) Bhattacharjee and Bhattacharya (1992) [58] BSA Convective Dead-end Unstirred cell 36 [17]
(2.5) J=ΔPΔπ[Rm+(V/AJ*t)α(cbcp)]μ
Model parameter: α
Bhattacharjee and Bhattacharya (1992) [25] PEG Convective Dead-end Unstirred cell 50 -
(2.6) J=υpo1+Rps*[1-e(-K1t)]
Model parameters: Rps*, K1
Bhattacharya et al. (2001) [21] Sugar cane Convective Dead-end Stirred cell 42 [120]
(2.7) J=ΔPΔπi1Rm i1+(Rm*ΔttR)+(miΔtJi1)
Model parameters: tR, mi
Kanani and Ghosh (2007) [121] HSA Convective Dead-end Stirred cell 28 -
(2.8) J=ΔP+σRTV1[ln(ρpolCmρpolCp)+{(11n)+X12Cm+Cpρpol}CmCpρpol]μRm
Model parameters: α, n, X12
Sarkar et al. (2010) [122] PEG-6000 Diffusive-Convective Dead-end Stirred cell 2 -
(2.9) J=ko(μbμo)1/3CbCw(μoμ)(MpRT)(dΠdC)dCC Binabaji et al. (2015) [123] Protein solution Diffusive Cross-flow Tangential flow filtration (TFF) Cassette 6 -

HSA: Human serum albumin solution; BSA: Bovine serum albumin; PEG: Polyethylene glycol.