Dowex 1X4 and Dowex 1X8 as substitute of Diaion MA03SS in simulated moving bed chromatographic separation of sulfuric acid and sugars in concentrated sulfuric acid hydrolysates of bamboo

doi:10.1016/j.seppur.2016.04.023

Title: Dowex 1X4 and Dowex 1X8 as substitute of Diaion MA03SS in simulated moving bed chromatographic separation of sulfuric acid and sugars in concentrated sulfuric acid hydrolysates of bamboo

Full Record
Other Related Research

Authors:: Sun, Zhao-Yong; Ura, Tetsuya; Matsuura, Hirotaka; Kida, Kenji; Jyo, Akinori

Publication Date:: 2016-06-01

Sponsoring Org.:: USDOE

OSTI Identifier:: 1424799

Resource Type:: Publisher's Accepted Manuscript

Journal Name:: Separation and Purification Technology

Additional Journal Information:: Journal Name: Separation and Purification Technology Journal Volume: 166 Journal Issue: C; Journal ID: ISSN 1383-5866

Publisher:: Elsevier

Country of Publication:: United Kingdom

Language:: English

Citation Formats


                    Sun, Zhao-Yong, Ura, Tetsuya, Matsuura, Hirotaka, Kida, Kenji, and Jyo, Akinori. Dowex 1X4 and Dowex 1X8 as substitute of Diaion MA03SS in simulated moving bed chromatographic separation of sulfuric acid and sugars in concentrated sulfuric acid hydrolysates of bamboo.  United Kingdom: N. p., 2016. 
        Web.  doi:10.1016/j.seppur.2016.04.023.

Copy to clipboard


                    Sun, Zhao-Yong, Ura, Tetsuya, Matsuura, Hirotaka, Kida, Kenji, & Jyo, Akinori. Dowex 1X4 and Dowex 1X8 as substitute of Diaion MA03SS in simulated moving bed chromatographic separation of sulfuric acid and sugars in concentrated sulfuric acid hydrolysates of bamboo.  United Kingdom.  doi:10.1016/j.seppur.2016.04.023.

Copy to clipboard


                    Sun, Zhao-Yong, Ura, Tetsuya, Matsuura, Hirotaka, Kida, Kenji, and Jyo, Akinori. Wed .  
        "Dowex 1X4 and Dowex 1X8 as substitute of Diaion MA03SS in simulated moving bed chromatographic separation of sulfuric acid and sugars in concentrated sulfuric acid hydrolysates of bamboo".  United Kingdom.  doi:10.1016/j.seppur.2016.04.023.

Copy to clipboard


                    
@article{osti_1424799,

  title        = {Dowex 1X4 and Dowex 1X8 as substitute of Diaion MA03SS in simulated moving bed chromatographic separation of sulfuric acid and sugars in concentrated sulfuric acid hydrolysates of bamboo},

  author       = {Sun, Zhao-Yong and Ura, Tetsuya and Matsuura, Hirotaka and Kida, Kenji and Jyo, Akinori},

  abstractNote = {},

  doi          = {10.1016/j.seppur.2016.04.023},

  journal      = {Separation and Purification Technology},

  number       = C,

  volume       = 166,

  place        = {United Kingdom},

  year         = {2016},

  month        = {6}

}

Copy to clipboard

Journal Article:

Free Publicly Available Full Text

Accepted Manuscript (Publisher)

Publisher's Version of Record
DOI: 10.1016/j.seppur.2016.04.023

Other availability

Search WorldCat to find libraries that may hold this journal

Citation Metrics:

Cited by: 1 work

Citation information provided by
Web of Science

Save / Share:

Export Metadata

Save to My Library

Similar Records in DOE PAGES and OSTI.GOV collections:

THE PROCESSING OF PLUTONIUM BY ION EXCHANGE. I. THE CONCENTRATION DEPENDENCE OF DISTRIBUTION COEFFICIENTS ON DOWEX 1X4 FROM 7M NITRIC ACID

Technical Report James, D B

An expression was derived and experimentally confirmed for the change in the volume distribution coefficient for Pu(IV) on Dowex 1X4 from 7M HNO/sub 3/) with varying concentrations of Pu(IV) in the aqueous phase. A few experimerts wfth other sorbable species indicate the equations may be applicable to other systems. These calculations require one measurement of the volume distribution coefficient at a trace level of resin loading. These trace level coefficients were determined for many elements. (auth)
EQUILIBRIUM ANION EXCHANGE OF URANIUM(VI) ON DOWEX 1X4 FROM NITRIC ACID SOLUTIONS.

Technical Report James, D B
DOI: 10.2172/4452420

Full Text Available
KINETICS OF THE ANION EXCHANGE OF URANIUM(VI) ON DOWEX 1X4 FROM NITRIC ACID SOLUTIONS.

Technical Report James, D B
DOI: 10.2172/4451632

Full Text Available
DMR (deacetylation and mechanical refining) processing of corn stover achieves high monomeric sugar concentrations (230 g L^-1) during enzymatic hydrolysis and high ethanol concentrations (>10% v/v) during fermentation without hydrolysate purification or concentration

Journal Article Chen, Xiaowen ; Kuhn, Erik ; Jennings, Edward W. ; ... - Energy & Environmental Science

Distilling and purifying ethanol and other products from second generation lignocellulosic biorefineries adds significant capital and operating costs to biofuel production. The energy usage associated with distillation negatively affects plant gate costs and causes environmental and life-cycle impacts, and the lower titers in fermentation caused by lower sugar concentrations from pretreatment and enzymatic hydrolysis increase energy and water usage and ethanol production costs. In addition, lower ethanol titers increase the volumes required for enzymatic hydrolysis and fermentation vessels increase capital expenditure (CAPEX). Therefore, increasing biofuel titers has been a research focus in renewable biofuel production for several decades. In thismore »« less
Cited by 12
DOI: 10.1039/C5EE03718B

Full Text Available
Optimization of the countercurrent moving-bed chromatographic separator

Journal Article Fish, B B ; Carr, R W ; Aris, R - AIChE Journal (American Institute of Chemical Engineers); (United States)

A dispersionless, adsorption equilibrium, plug-flow model of a countercurrent moving-bed chromatographic separator operating at steady state is investigated. The flux of the constituents of a binary mixture is examined via concentration-phase plane plots, which reveal a complex behavior depending on a parameter [sigma], the ratio of solid- and fluid-phase flow of the mobile phase. When the model is modified by incorporating finite mass-transfer rates, axial concentration profiles exhibit behavior that is characteristic of experimental observations, rather than the predictions of the ideal model. Numerical simulations with the finite mass-transfer model reveal an optimum operating condition.
DOI: 10.1002/aic.690391006

Similar Records