Separation of VOC Gaseous Mixtures Using an Adsorption-Desorption Device

被引:0
|
作者
Gabrisova, Ludmila [1 ]
Macho, Oliver [1 ]
Juriga, Martin [1 ]
Gabrisova, Zuzana [2 ]
Valent, Ivan [3 ]
Kabat, Juraj [4 ]
Blasko, Jaroslav [4 ]
Kubinec, Robert [4 ]
机构
[1] Slovak Univ Technol Bratislava, Inst Proc Engn, Fac Mech Engn, Namestie Slobody 17, Bratislava 81231, Slovakia
[2] Slovak Univ Technol Bratislava, Inst Technol & Mat, Fac Mech Engn, Namestie Slobody 17, Bratislava 81231, Slovakia
[3] Comenius Univ, Fac Nat Sci, Dept Phys & Theoret Chem, Ilkovicova 6, Bratislava 84215, Slovakia
[4] Comenius Univ, Fac Nat Sci, Dept Analyt Chem, Ilkovicova 6, Bratislava 84215, Slovakia
关键词
ethanol; adsorption; desorption; stripping; granulated activated carbon; FERMENTATION BROTH; ACTIVATED CARBON; ETHANOL-PRODUCTION; LIQUID-MIXTURES; MODEL SOLUTIONS; AROMA COMPOUNDS; WATER; RECOVERY; ADSORBENTS; MEMBRANE;
D O I
10.3390/pr11092572
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The aim of this work was to separate ethanol in an experimental adsorption-desorption device. We focused on concentrating ethanol by adsorption onto granulated activated carbon in its gaseous phase, which was produced by stripping a matrix with different ethanol concentrations (2, 5, 10, and 15% v/v). For adsorption, three kinds of granulated activated carbon (GAC) were used, marked as GAC1, GAC2, and GAC3. The separation product had a higher ethanol concentration than the initial ethanol concentration before the adsorption-desorption process. The enrichment factor was, in the case of the initial ethanol concentration, 2% v/v at the level of 10. With our new adsorption-desorption device, it is possible to achieve a product with an ethanol concentration of 59.0% v/v with stripping, adsorption, desorption, and condensation. To verify the separation efficiency, a real matrix (fermentation broth) was used. The ethanol concentration in the real matrix was, at the beginning of the separation process, 0.65% v/v; after using our separation device, it was 11.35% v/v. Using a real matrix, the enrichment factor was at the level of 18. The main advantage is the use of our new adsorption-desorption device for the continuous separation of ethanol from fermentation broth. A mathematical model was created, based on which it is possible to calculate the ethanol concentration in the product of the separation process with high accuracy.
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页数:17
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