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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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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1716793414432849920 |