Diffusion membrane generation of 1-cyclohexylpiperidinium bicarbonate

Birendra Adhikari; Christopher J. Orme; Michael G. Jones; Daniel S. Wendt; Gregory L. Mines; Aaron D. Wilson

doi:10.1016/j.memsci.2019.04.047

Diffusion membrane generation of 1-cyclohexylpiperidinium bicarbonate

Birendra Adhikari
, Christopher J. Orme
, Michael G. Jones
, Daniel S. Wendt
, Gregory L. Mines
, Aaron D. Wilson

Research output: Contribution to journal › Article › peer-review

6 Scopus citations

Abstract

Different methods of introducing CO₂ to a heterogeneous mixture of water and 1-cyclohexylpiperidine are explored in order to generate a single-phase aqueous 1-cyclohexylpiperidinium bicarbonate solution. Membrane gas contacting was found to be an effective method for CO₂ addition. This analysis varied solution temperature, gas pressure, solution pressure, solution flow rate, and membrane area to determine and minimize mass transport and chemical reaction limiting phenomena. Both mass transport limitations and chemical kinetic limitations were found for the industrially relevant membrane gas contacting process conditions explored in this study.

Original language	English
Pages (from-to)	258-266
Number of pages	9
Journal	Journal of Membrane Science
Volume	583
DOIs	https://doi.org/10.1016/j.memsci.2019.04.047
State	Published - Aug 1 2019

Keywords

Desalination
Draw solution
Forward osmosis
Osmotically driven membrane process
Switchable polarity solvents

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10.1016/j.memsci.2019.04.047

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title = "Diffusion membrane generation of 1-cyclohexylpiperidinium bicarbonate",

abstract = "Different methods of introducing CO2 to a heterogeneous mixture of water and 1-cyclohexylpiperidine are explored in order to generate a single-phase aqueous 1-cyclohexylpiperidinium bicarbonate solution. Membrane gas contacting was found to be an effective method for CO2 addition. This analysis varied solution temperature, gas pressure, solution pressure, solution flow rate, and membrane area to determine and minimize mass transport and chemical reaction limiting phenomena. Both mass transport limitations and chemical kinetic limitations were found for the industrially relevant membrane gas contacting process conditions explored in this study.",

keywords = "Desalination, Draw solution, Forward osmosis, Osmotically driven membrane process, Switchable polarity solvents",

author = "Birendra Adhikari and Orme, \{Christopher J.\} and Jones, \{Michael G.\} and Wendt, \{Daniel S.\} and Mines, \{Gregory L.\} and Wilson, \{Aaron D.\}",

note = "Publisher Copyright: {\textcopyright} 2019 Elsevier B.V.",

year = "2019",

month = aug,

day = "1",

doi = "10.1016/j.memsci.2019.04.047",

language = "English",

volume = "583",

pages = "258--266",

journal = "Journal of Membrane Science",

issn = "0376-7388",

publisher = "Elsevier B.V.",

}

TY - JOUR

T1 - Diffusion membrane generation of 1-cyclohexylpiperidinium bicarbonate

AU - Adhikari, Birendra

AU - Orme, Christopher J.

AU - Jones, Michael G.

AU - Wendt, Daniel S.

AU - Mines, Gregory L.

AU - Wilson, Aaron D.

PY - 2019/8/1

Y1 - 2019/8/1

N2 - Different methods of introducing CO2 to a heterogeneous mixture of water and 1-cyclohexylpiperidine are explored in order to generate a single-phase aqueous 1-cyclohexylpiperidinium bicarbonate solution. Membrane gas contacting was found to be an effective method for CO2 addition. This analysis varied solution temperature, gas pressure, solution pressure, solution flow rate, and membrane area to determine and minimize mass transport and chemical reaction limiting phenomena. Both mass transport limitations and chemical kinetic limitations were found for the industrially relevant membrane gas contacting process conditions explored in this study.

AB - Different methods of introducing CO2 to a heterogeneous mixture of water and 1-cyclohexylpiperidine are explored in order to generate a single-phase aqueous 1-cyclohexylpiperidinium bicarbonate solution. Membrane gas contacting was found to be an effective method for CO2 addition. This analysis varied solution temperature, gas pressure, solution pressure, solution flow rate, and membrane area to determine and minimize mass transport and chemical reaction limiting phenomena. Both mass transport limitations and chemical kinetic limitations were found for the industrially relevant membrane gas contacting process conditions explored in this study.

KW - Desalination

KW - Draw solution

KW - Forward osmosis

KW - Osmotically driven membrane process

KW - Switchable polarity solvents

UR - https://www.scopus.com/pages/publications/85065093896

U2 - 10.1016/j.memsci.2019.04.047

DO - 10.1016/j.memsci.2019.04.047

M3 - Article

AN - SCOPUS:85065093896

SN - 0376-7388

VL - 583

SP - 258

EP - 266

JO - Journal of Membrane Science

JF - Journal of Membrane Science

ER -

Diffusion membrane generation of 1-cyclohexylpiperidinium bicarbonate

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Keywords

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