TY - JOUR
T1 - 糖用脱色树脂吸附己糖碱性降解色素传质机理解析
AU - Li, Wen
AU - Jiao, Li
AU - Liao, Chunyu
AU - Yu, Haiqing
AU - Xiao, Yao
AU - Xing, Weihong
AU - Li, Kai
AU - Peng, Wenbo
N1 - Publisher Copyright:
© 2022, China Food Publishing Company. All right reserved.
PY - 2022/8/25
Y1 - 2022/8/25
N2 - Alkaline degradation products of hexose (HADP) were prepared as a representative colorant in remelt syrup to evaluate their adsorption performance onto a decolorizing resin. Four novel phenomenological adsorption mass transfer models, namely, external mass transfer resistance (EMTR), internal mass transfer resistance (IMTR), combined EMTRIMTR, and adsorption on active sites (AAS), were used to decipher the mass transfer mechanisms for the resin adsorption of HADP. At the initial colorant concentrations of 60, 90, and 120 mg/L, the equilibrium adsorption capacities of the resin for HADP were 190, 270, and 326 mg/g, and the corresponding decolorization rates were 95%, 90%, and 82%, respectively. EMTR combined with IMTR was the rate-limiting step for HADP adsorption onto the resin, and AAS could not be neglected. The dynamic characteristics of HADP adsorption through the liquid film around the resin and the pores inside the resin could be described well using the combined EMTR-IMTR model. The AAS model could accurately calculate the physisorption and chemisorption rates during the whole adsorption process. These models can help provide new insights into the mass transfer behaviors of the adsorption system.
AB - Alkaline degradation products of hexose (HADP) were prepared as a representative colorant in remelt syrup to evaluate their adsorption performance onto a decolorizing resin. Four novel phenomenological adsorption mass transfer models, namely, external mass transfer resistance (EMTR), internal mass transfer resistance (IMTR), combined EMTRIMTR, and adsorption on active sites (AAS), were used to decipher the mass transfer mechanisms for the resin adsorption of HADP. At the initial colorant concentrations of 60, 90, and 120 mg/L, the equilibrium adsorption capacities of the resin for HADP were 190, 270, and 326 mg/g, and the corresponding decolorization rates were 95%, 90%, and 82%, respectively. EMTR combined with IMTR was the rate-limiting step for HADP adsorption onto the resin, and AAS could not be neglected. The dynamic characteristics of HADP adsorption through the liquid film around the resin and the pores inside the resin could be described well using the combined EMTR-IMTR model. The AAS model could accurately calculate the physisorption and chemisorption rates during the whole adsorption process. These models can help provide new insights into the mass transfer behaviors of the adsorption system.
KW - Adsorption
KW - Alkaline degradation products of hexose
KW - Decolorizing resin
KW - Mass transfer mechanism
KW - Remelt syrup
UR - http://www.scopus.com/inward/record.url?scp=85138208975&partnerID=8YFLogxK
U2 - 10.7506/spkx1002-6630-20211021-227
DO - 10.7506/spkx1002-6630-20211021-227
M3 - 文章
AN - SCOPUS:85138208975
SN - 1002-6630
VL - 43
SP - 53
EP - 60
JO - Shipin Kexue/Food Science
JF - Shipin Kexue/Food Science
IS - 16
ER -