2005
DOI: 10.1016/j.desal.2004.09.017
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Studies on ultrafiltration of spent sulfite liquor using various membranes for the recovery of lignosulphonates

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Cited by 60 publications
(41 citation statements)
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“…Lignosulphonates represent a polydispersed system with a wide molecular mass distribution from 200 to 15,000 kg mol À1 . Pore blocking and adsorption would be expected to occur when filtration is carried out using a 20 kg mol À1 MMCO membrane (Bhattacharya et al, 2005). Weis et al (2005) found that the phenolic compounds and acids in the SSL contribute significantly to the fouling problems during the filtration of lignosulphonates.…”
Section: Ultrafiltration Of Ssl Feedmentioning
confidence: 99%
“…Lignosulphonates represent a polydispersed system with a wide molecular mass distribution from 200 to 15,000 kg mol À1 . Pore blocking and adsorption would be expected to occur when filtration is carried out using a 20 kg mol À1 MMCO membrane (Bhattacharya et al, 2005). Weis et al (2005) found that the phenolic compounds and acids in the SSL contribute significantly to the fouling problems during the filtration of lignosulphonates.…”
Section: Ultrafiltration Of Ssl Feedmentioning
confidence: 99%
“…UF has been shown to have the potential to separate LS fractions with low polydispersity, whether it is applied to commercial LS (Gardon and Mason 1955;Tsapiuk et al 1989;Buchholz et al 1992;Zhou et al 2006;Yang et al 2008) or directly to the spent sulfite liquor (SSL) (Bhattacharya et al 2005;Ringena et al 2005). LS can also be fractionated based on their solubility in ethanol (EtOH)/ water solutions: low MW fractions were found to be soluble in highly concentrated EtOH solutions, whereas high MW fractions were only soluble in diluted solutions (Luh and Frederick 1992;Fredheim et al 2002).…”
Section: Introductionmentioning
confidence: 98%
“…The fouling flux decline curves for all cycles and protocols over time showed a steep decline which developed into a lower steady state flux (results not shown). Previous workers have shown that the flux decline during SSL filtration is due to a range of fouling phenomena such as concentration polarisation, irreversible fouling, pore blocking, and gel layer formation (11,15,20). The composition of SSL can be seen in Table 1.…”
Section: Results and Discussion Flux Measurementsmentioning
confidence: 98%
“…The composition of SSL can be seen in Table 1. It contained 5.9 wt.% lignosulphonates, which represents a polydisperse system with a wide range of molar mass distribution from 200 to 15,000 g mol À1 (20). Therefore, pore blocking and adsorption would be expected to occur during separation using a 20 kg mol À1 MMCO membrane.…”
Section: Results and Discussion Flux Measurementsmentioning
confidence: 99%