壳聚糖絮凝回收分级等电沉淀后鱼糜漂洗水中蛋白质

    Recovering protein from surimi wash water after isoelectrically precipitate by chitosan flocculation

    • 摘要: 为实现鱼糜漂洗水中蛋白质的洁净回收,同时达到净化鱼糜漂洗水及提高资源利用率的目的,该文针对分级等电沉淀回收蛋白质之后的低蛋白浓度废水,研究了蛋白-壳聚糖絮凝过程,探索了主要动力学和热力学因素对絮凝过程的影响;并根据Box-Benhnken设计进行了优化试验。结果表明,狭鳕鱼鱼糜漂洗水中蛋白质等电点主要集中在4.30和5.50,分级回收后蛋白质的回收率达到77.7%。其中絮凝时间、壳聚糖用量和脱乙酰度、絮凝温度和pH值对壳聚糖絮凝蛋白质均有影响,而絮凝温度的影响更多体现在50℃以上的较高温度区域。根据响应面分析结果,在脱乙酰度95%,反应时间90 min,pH值8.04,壳聚糖用量369 mg/L,温度19.6℃的条件下,可获得94.75%的蛋白总回收率,废水中蛋白质量浓度降至0.37 mg/mL以下。研究结果为富蛋白生产废水处理提供了技术参考。

       

      Abstract: Abstract: As a wastewater, surimi wash water is rich in nutrients, mainly protein. It means both waste of material and pollution to environment. To maximize protein recovery from surimi wash water by eco-friendly techonolgies, purify surimi wash water and increase the utilization efficiency of aquatic resources simultaneously, a combined protein-recovery technology of fractional isoelectric precipitation and chitosan ?occulation was adopted. The surimi wash water produced from Alaska pollock processing was isoelectrically precipitated fractionally in two points of pH values, which were determined by isoelectric focusing result tested in polyacrylamide gels before. And then the low-concentration supernatant protein was ?occulated using chitosan. Influences of some dynamic (flocculation time) and thermodynamic (internal factors such as dosage and deacetylation degree of chitosan, and external factors such as temperature and pH value of solution) factors on the ?occulating process were explored centrally. Thereafter, a 3-factor 3-level experiment of Box-Benhnken design was executed, so as to find out if there was any interactive influence between the factors and obtain optimal ?occulating conditions. It showed that the isoelectric points of proteins in surumi wash water of Alaska pollock were located around 4.30 and 5.50, which indicated that fractional isoelectric precipitation was feasible in the solution. Total protein recovery up to 77.70% was recorded from isoelectric precipitation fractionally at the pH values of 5.50 and 4.30, which was more efficient than single isoelectric precipitation as reported before. Herein the protein content was decreased from 7.00 to 1.56 mg/mL, and the chemical oxygen demand (COD) was cut down from 8 960 to 3 916 mg/L. Single-factor experiments in the pretreated surimi wash water of 1.56 mg/mL protein showed that, in chitosan ?occulating process, the increase of flocculation time had a positive effect before 90 min. However, after 90 min, protein flocculating recovery lowered down with time increasing. Chitosan dosage rising led to flocculating recovery increasing before 250 mg/L, almost the same as used in original surimi wash water, and then the influence of this factor became to be a little negative. As to deacetylation degree of chitosan, higher degree gave out more flocculating recovery. The pH value of solution was a key factor of the chitosan ?occulation, and proper pH value, such as 8.0, got 87.8% flocculating recovery, other than pH values of 4.0-4.5, flocculation could hardly be achieved. As an important thermodynamic factor, temperature of solution had a remarkable effect only when it was above 50℃. Finally flocculating time and deacetylation degree of chitosan were fixed at 90 min and 95% respectively, and Box-Benhnken experiment was designed with 3 factors i.e. chitosan dosage, pH value and temperature (the range was limited to <40℃ under consideration for industrial practice) of solution. According to results of response surface analysis, there were significant interactive influences between dosage and pH value, and dosage and temperature respectively. The condition was optimized as pH value of 8.04, chitosan dosage of 369 mg/L and temperature of 19.6℃. Under the condition, protein recovery up to 94.75% could be achieved, while content of residue protein was decreased to 0.37 mg/mL. Meanwhile 3 040 mg/L COD remained in the cleaned water, which indicated that there were other materials contributing to COD value.

       

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