TY - JOUR
T1 - Effectiveness of adjustable-volume packed-bed reactor with an ion-exchange resin catalyst for continuous production
AU - Yamazaki, Kota
AU - Shibasaki-Kitakawa, Naomi
AU - Nakashima, Kazunori
AU - Yonemoto, Toshikuni
N1 - Funding Information:
This work was financially supported by the Ministry of Education, Culture, Sports, Science and Technology of Japan through a Grant-in- Aid for Scientific Research (A) (No. 24246127).
Publisher Copyright:
© 2016 The Society of Chemical Engineers, Japan.
PY - 2016
Y1 - 2016
N2 - Packed-bed reactors filled with ion-exchange resin catalysts are very effective for the continuous production of various chemicals. However, the resin tends to swell or shrink depending on the composition of the surrounding solution, and this can greatly alter the resin bed height and the volume of the liquid phase above the resin in a fixed-volume reactor. Because this liquid phase does not contribute to the production of chemicals in the reaction, it is important to minimize the liquid-phase volume to increase the productivity. In the present study, an adjustable-volume packed-bed reactor system was developed, and its effectiveness for the continuous production of fatty acid esters and regeneration of the resin were evaluated. The column height was adjusted by controlling the position of a movable plunger to minimize the liquid-phase volume in the upper part of the column. In fatty acid ester production using the adjustable-volume reactor, the residence time of the reactants in the liquid phase was shorter than that in a fixed-volume reactor, and the solution was rapidly eluted from the column, which improved productivity. For resin regeneration, minimization of the liquidphase volume in the adjustable-volume reactor reduced the effect of dilution on the performance of the regeneration solutions compared to that in the fixed-volume reactor, and less regeneration solution was required. The adjustable volume reactor could allow for more efficient and environment-friendly production of chemicals than a fixed-volume reactor.
AB - Packed-bed reactors filled with ion-exchange resin catalysts are very effective for the continuous production of various chemicals. However, the resin tends to swell or shrink depending on the composition of the surrounding solution, and this can greatly alter the resin bed height and the volume of the liquid phase above the resin in a fixed-volume reactor. Because this liquid phase does not contribute to the production of chemicals in the reaction, it is important to minimize the liquid-phase volume to increase the productivity. In the present study, an adjustable-volume packed-bed reactor system was developed, and its effectiveness for the continuous production of fatty acid esters and regeneration of the resin were evaluated. The column height was adjusted by controlling the position of a movable plunger to minimize the liquid-phase volume in the upper part of the column. In fatty acid ester production using the adjustable-volume reactor, the residence time of the reactants in the liquid phase was shorter than that in a fixed-volume reactor, and the solution was rapidly eluted from the column, which improved productivity. For resin regeneration, minimization of the liquidphase volume in the adjustable-volume reactor reduced the effect of dilution on the performance of the regeneration solutions compared to that in the fixed-volume reactor, and less regeneration solution was required. The adjustable volume reactor could allow for more efficient and environment-friendly production of chemicals than a fixed-volume reactor.
KW - Continuous production
KW - Ion-Exchange resin
KW - Packed-Bed reactor
KW - Resin regeneration
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U2 - 10.1252/jcej.15we243
DO - 10.1252/jcej.15we243
M3 - Article
AN - SCOPUS:84978755558
SN - 0021-9592
VL - 49
SP - 668
EP - 672
JO - Journal of Chemical Engineering of Japan
JF - Journal of Chemical Engineering of Japan
IS - 7
ER -