MEMBRANE DISTILLATION FOULING CONTROL STRATEGIES ON XYLITOL CRYSTALIZATION
Xylitol is a sugar alcohol that can be used as a low calorie sweetener substitute for surcrose. Xylitol can be produced with biotechnology process by fermenting Oil Palm Empty Fruit Bunches (OPEFB) hydrolysate. The fermentation process produce impurities that need to be separated. Commercially, x...
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id-itb.:692342022-09-21T08:27:21ZMEMBRANE DISTILLATION FOULING CONTROL STRATEGIES ON XYLITOL CRYSTALIZATION Fadlika, Egi Indonesia Final Project xylitol, membrane distillation, fouling, fermentation, OPEFB INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/69234 Xylitol is a sugar alcohol that can be used as a low calorie sweetener substitute for surcrose. Xylitol can be produced with biotechnology process by fermenting Oil Palm Empty Fruit Bunches (OPEFB) hydrolysate. The fermentation process produce impurities that need to be separated. Commercially, xylitol is available in the form of crystalline powder. Therefore a downstream process is required to conduct for the fermentation solution. The downstream process consist of pre-treatment for separation and purification, concentration, and crystallization of the solution. One of the most efficient and potential way to concentrate and crytallize the solution is by using membrane distillation, but there is a major obstacle in the use of it, named fouling. Fouling phenomenon can reduce xylitol production and reduce membrane lifespan. Therefore, the purpose of this study is to provide recommendations on strategies for preventing and controlling membrane distillation’s fouling in the xylitol crystallization process. In this study, the separation and purification process include centrifugation, activated carbon adsorption, filtration using UF membrane, and a variation consist of zeolite adsorption. The concentration and crystallization process are done by using MD. The feed will be made from fermented OPEFB hydrolysate. Mitigation experiments consist of aeration with flow variation (0,1; 0,15; 0,2 L/minutes) and air backwash with periodic time variation (30, 60, and 90 minutes). This study shows that the zeolite adsorption (after UF filtration) produce a clearer crystal and produce higher yield (34,08%) compared to UF permeate (31,68%), and needs shorter operation time. The main experiment of aeration and air backwash can reduce fouling, with air backwash once per 60 minutes as the best variation. The variation produce 34% yield and reach the saturated concentration by 8.5 hours. text |
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Xylitol is a sugar alcohol that can be used as a low calorie sweetener substitute
for surcrose. Xylitol can be produced with biotechnology process by fermenting Oil Palm
Empty Fruit Bunches (OPEFB) hydrolysate. The fermentation process produce impurities
that need to be separated. Commercially, xylitol is available in the form of crystalline
powder. Therefore a downstream process is required to conduct for the fermentation
solution.
The downstream process consist of pre-treatment for separation and purification,
concentration, and crystallization of the solution. One of the most efficient and potential
way to concentrate and crytallize the solution is by using membrane distillation, but there
is a major obstacle in the use of it, named fouling. Fouling phenomenon can reduce xylitol
production and reduce membrane lifespan. Therefore, the purpose of this study is to
provide recommendations on strategies for preventing and controlling membrane
distillation’s fouling in the xylitol crystallization process.
In this study, the separation and purification process include centrifugation,
activated carbon adsorption, filtration using UF membrane, and a variation consist of
zeolite adsorption. The concentration and crystallization process are done by using MD.
The feed will be made from fermented OPEFB hydrolysate. Mitigation experiments
consist of aeration with flow variation (0,1; 0,15; 0,2 L/minutes) and air backwash with
periodic time variation (30, 60, and 90 minutes).
This study shows that the zeolite adsorption (after UF filtration) produce a clearer
crystal and produce higher yield (34,08%) compared to UF permeate (31,68%), and needs
shorter operation time. The main experiment of aeration and air backwash can reduce
fouling, with air backwash once per 60 minutes as the best variation. The variation
produce 34% yield and reach the saturated concentration by 8.5 hours. |
format |
Final Project |
author |
Fadlika, Egi |
spellingShingle |
Fadlika, Egi MEMBRANE DISTILLATION FOULING CONTROL STRATEGIES ON XYLITOL CRYSTALIZATION |
author_facet |
Fadlika, Egi |
author_sort |
Fadlika, Egi |
title |
MEMBRANE DISTILLATION FOULING CONTROL STRATEGIES ON XYLITOL CRYSTALIZATION |
title_short |
MEMBRANE DISTILLATION FOULING CONTROL STRATEGIES ON XYLITOL CRYSTALIZATION |
title_full |
MEMBRANE DISTILLATION FOULING CONTROL STRATEGIES ON XYLITOL CRYSTALIZATION |
title_fullStr |
MEMBRANE DISTILLATION FOULING CONTROL STRATEGIES ON XYLITOL CRYSTALIZATION |
title_full_unstemmed |
MEMBRANE DISTILLATION FOULING CONTROL STRATEGIES ON XYLITOL CRYSTALIZATION |
title_sort |
membrane distillation fouling control strategies on xylitol crystalization |
url |
https://digilib.itb.ac.id/gdl/view/69234 |
_version_ |
1822005988912267264 |