食品科学 ›› 2022, Vol. 43 ›› Issue (16): 53-60.doi: 10.7506/spkx1002-6630-20211021-227

• 食品化学 • 上一篇    下一篇

糖用脱色树脂吸附己糖碱性降解色素传质机理解析

李文,焦丽,廖春玉,余海清,肖尧,邢卫红,李凯,彭文博   

  1. (1.江苏久吾高科技股份有限公司,江苏省博士后创新实践基地,江苏 南京 211808;2.广西民族大学化学化工学院,广西林产化学与工程重点实验室,广西 南宁 530008;3.南京工业大学化工学院,江苏 南京 211816;4.广西大学轻工与食品工程学院,广西 南宁 530004)
  • 出版日期:2022-08-25 发布日期:2022-08-31
  • 基金资助:
    国家自然科学基金青年科学基金项目(32001741);广西自然科学基金青年科学基金项目(2021GXNSFBA076002)

Mass Transfer Mechanisms for Decolorizing Resin Adsorption of Alkaline Degradation Products of Hexose

LI Wen, JIAO Li, LIAO Chunyu, YU Haiqing, XIAO Yao, XING Weihong, LI Kai, PENG Wenbo   

  1. (1. Postdoctoral Innovation Practice Base of Jiangsu Province, Jiangsu Jiuwu Hi-Tech Co. Ltd., Nanjing 211808, China; 2. Guangxi Key Laboratory of Chemistry and Engineering of Forest Products, School of Chemistry and Chemical Engineering, Guangxi Minzu University, Nanning 530008, China; 3. College of Chemical Engineering, Nanjing Tech University, Nanjing 211816, China; 4. College of Light Industry and Food Engineering, Guangxi University, Nanning 530004, China)
  • Online:2022-08-25 Published:2022-08-31

摘要: 以回溶糖浆代表性色素——己糖碱性降解色素为吸附模型底物,考察糖用脱色树脂对其吸附性能,并采用4 种新型吸附传质现象学模型,即外部传质阻力(external mass transfer resistance,EMTR)、内部传质阻力(internal mass transfer resistance,IMTR)、活性位点吸附(adsorption on active sites,AAS)及EMTR-IMTR组合模型,解析树脂吸附色素传质机理。在色素初始质量浓度为60、90 mg/L及120 mg/L条件下,树脂对色素平衡吸附量分别为190、270 mg/g及326 mg/g,对应脱色率分别为95%、90%及82%。树脂吸附色素限速步骤由EMTR和IMTR共同决定,但AAS步骤不可忽略。EMTR-IMTR组合模型可准确求解吸附体系任意时刻树脂周围液膜及其内部孔道对色素吸附量,AAS模型可准确计算吸附过程任意时刻物理及化学吸附速率大小,可为阐明吸附传质机理提供新视角。

关键词: 己糖碱性降解色素;脱色树脂;吸附;回溶糖浆;传质机理

Abstract: 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 EMTR-IMTR, 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.

Key words: alkaline degradation products of hexose; decolorizing resin; adsorption; remelt syrup; mass transfer mechanism

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