Recovery of Lignosulfonates from Spent Sulfite Liquor Using Ceramic Hollow-Fiber Membranes

Spent sulfite liquor is an abundant but currently less used wastewater stream from the pulp and paper industry. The recovery of lignin from this resource would provide an inexpensive raw material for the manufacture of fuels and fine chemicals. Here we investigated the suitability of ceramic hollow-...

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Main Authors: Daniel Humpert, Mehrdad Ebrahimi, Annika Stroh, Peter Czermak
Format: Article
Language:English
Published: MDPI AG 2019-03-01
Series:Membranes
Subjects:
Online Access:https://www.mdpi.com/2077-0375/9/4/45
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spelling doaj-add17aa28cbe461a9b6739935f7298602020-11-24T20:54:53ZengMDPI AGMembranes2077-03752019-03-01944510.3390/membranes9040045membranes9040045Recovery of Lignosulfonates from Spent Sulfite Liquor Using Ceramic Hollow-Fiber MembranesDaniel Humpert0Mehrdad Ebrahimi1Annika Stroh2Peter Czermak3Institute of Bioprocess Engineering and Pharmaceutical Technology, University of Applied Sciences Mittelhessen, 35390 Giessen, GermanyInstitute of Bioprocess Engineering and Pharmaceutical Technology, University of Applied Sciences Mittelhessen, 35390 Giessen, GermanyInstitute of Bioprocess Engineering and Pharmaceutical Technology, University of Applied Sciences Mittelhessen, 35390 Giessen, GermanyInstitute of Bioprocess Engineering and Pharmaceutical Technology, University of Applied Sciences Mittelhessen, 35390 Giessen, GermanySpent sulfite liquor is an abundant but currently less used wastewater stream from the pulp and paper industry. The recovery of lignin from this resource would provide an inexpensive raw material for the manufacture of fuels and fine chemicals. Here we investigated the suitability of ceramic hollow-fiber membranes for the concentration of spent sulfite liquor as an alternative to common membrane technologies. We tested three ceramic hollow-fiber membranes (3, 8, and 30 nm) in different membrane processes (fed-batch and total recycle mode) and compared their performance with the widely-used tubular membrane geometry. We also evaluated backflushing as a strategy to reduce membrane fouling during filtration. The juxtaposition of the two membrane geometries revealed that wall shear stress is the most important process parameter for the assessment of membrane performance according to permeate flux. The higher the wall shear stress, the higher the permeate flux. Due to the smaller inner diameter of the hollow-fiber membranes, higher wall shear stress can be achieved more easily. Backflushing had no effect on the permeate flux during the concentration experiments.https://www.mdpi.com/2077-0375/9/4/45ceramic hollow-fiber membranelignin treatmentlignin fractionationlignosulfonatespent sulfite liquorbackflushing
collection DOAJ
language English
format Article
sources DOAJ
author Daniel Humpert
Mehrdad Ebrahimi
Annika Stroh
Peter Czermak
spellingShingle Daniel Humpert
Mehrdad Ebrahimi
Annika Stroh
Peter Czermak
Recovery of Lignosulfonates from Spent Sulfite Liquor Using Ceramic Hollow-Fiber Membranes
Membranes
ceramic hollow-fiber membrane
lignin treatment
lignin fractionation
lignosulfonate
spent sulfite liquor
backflushing
author_facet Daniel Humpert
Mehrdad Ebrahimi
Annika Stroh
Peter Czermak
author_sort Daniel Humpert
title Recovery of Lignosulfonates from Spent Sulfite Liquor Using Ceramic Hollow-Fiber Membranes
title_short Recovery of Lignosulfonates from Spent Sulfite Liquor Using Ceramic Hollow-Fiber Membranes
title_full Recovery of Lignosulfonates from Spent Sulfite Liquor Using Ceramic Hollow-Fiber Membranes
title_fullStr Recovery of Lignosulfonates from Spent Sulfite Liquor Using Ceramic Hollow-Fiber Membranes
title_full_unstemmed Recovery of Lignosulfonates from Spent Sulfite Liquor Using Ceramic Hollow-Fiber Membranes
title_sort recovery of lignosulfonates from spent sulfite liquor using ceramic hollow-fiber membranes
publisher MDPI AG
series Membranes
issn 2077-0375
publishDate 2019-03-01
description Spent sulfite liquor is an abundant but currently less used wastewater stream from the pulp and paper industry. The recovery of lignin from this resource would provide an inexpensive raw material for the manufacture of fuels and fine chemicals. Here we investigated the suitability of ceramic hollow-fiber membranes for the concentration of spent sulfite liquor as an alternative to common membrane technologies. We tested three ceramic hollow-fiber membranes (3, 8, and 30 nm) in different membrane processes (fed-batch and total recycle mode) and compared their performance with the widely-used tubular membrane geometry. We also evaluated backflushing as a strategy to reduce membrane fouling during filtration. The juxtaposition of the two membrane geometries revealed that wall shear stress is the most important process parameter for the assessment of membrane performance according to permeate flux. The higher the wall shear stress, the higher the permeate flux. Due to the smaller inner diameter of the hollow-fiber membranes, higher wall shear stress can be achieved more easily. Backflushing had no effect on the permeate flux during the concentration experiments.
topic ceramic hollow-fiber membrane
lignin treatment
lignin fractionation
lignosulfonate
spent sulfite liquor
backflushing
url https://www.mdpi.com/2077-0375/9/4/45
work_keys_str_mv AT danielhumpert recoveryoflignosulfonatesfromspentsulfiteliquorusingceramichollowfibermembranes
AT mehrdadebrahimi recoveryoflignosulfonatesfromspentsulfiteliquorusingceramichollowfibermembranes
AT annikastroh recoveryoflignosulfonatesfromspentsulfiteliquorusingceramichollowfibermembranes
AT peterczermak recoveryoflignosulfonatesfromspentsulfiteliquorusingceramichollowfibermembranes
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