河北农业科学
河北農業科學
하북농업과학
JOURNAL OF HEBEI AGRICULTURAL SCIENCES
2014年
5期
95-99
,共5页
薛慧玲%于家伊%赵晞瑛%周闯%邹亮
薛慧玲%于傢伊%趙晞瑛%週闖%鄒亮
설혜령%우가이%조희영%주틈%추량
阳离子交换树脂%餐厨废弃物%黄腐酸%脱盐%纯化%工艺条件优化
暘離子交換樹脂%餐廚廢棄物%黃腐痠%脫鹽%純化%工藝條件優化
양리자교환수지%찬주폐기물%황부산%탈염%순화%공예조건우화
Cation exchange resin%Kitchen waste%Biochemical fulvic acid%Desalination%Purification%Parameter optimization
对餐厨废弃物发酵产黄腐酸分离纯化的工艺条件进行研究,优化离子交换法的工艺参数,以获得高纯度的发酵产黄腐酸。利用单因素试验,采用 H +型和 NH4+型阳离子交换树脂对餐厨废弃物发酵产黄腐酸进行分离纯化,通过比较2种树脂对黄腐酸粗提液静态交换吸附的效果,筛选出用于黄腐酸溶液纯化的较适合的阳离子交换树脂类型;并利用三因素(上样流速、层析高径比、上样浓度)三水平的正交试验,对筛选出的阳离子交换树脂的纯化工艺参数进行了优化。结果表明:采用离子交换法纯化餐厨废弃物发酵产黄腐酸的最佳工艺条件是采用 NH4+型阳离子交换树脂,柱高径比5∶1,上样流速1 BV /h,上样浓度为Na +初始浓度≤700 mg /L (相当于原料0.1 g /mL)。利用该工艺对黄腐酸粗提液进行分离纯化,除杂效果最好, Na +去除率为95.90%,黄腐酸含量可达到82.10%。
對餐廚廢棄物髮酵產黃腐痠分離純化的工藝條件進行研究,優化離子交換法的工藝參數,以穫得高純度的髮酵產黃腐痠。利用單因素試驗,採用 H +型和 NH4+型暘離子交換樹脂對餐廚廢棄物髮酵產黃腐痠進行分離純化,通過比較2種樹脂對黃腐痠粗提液靜態交換吸附的效果,篩選齣用于黃腐痠溶液純化的較適閤的暘離子交換樹脂類型;併利用三因素(上樣流速、層析高徑比、上樣濃度)三水平的正交試驗,對篩選齣的暘離子交換樹脂的純化工藝參數進行瞭優化。結果錶明:採用離子交換法純化餐廚廢棄物髮酵產黃腐痠的最佳工藝條件是採用 NH4+型暘離子交換樹脂,柱高徑比5∶1,上樣流速1 BV /h,上樣濃度為Na +初始濃度≤700 mg /L (相噹于原料0.1 g /mL)。利用該工藝對黃腐痠粗提液進行分離純化,除雜效果最好, Na +去除率為95.90%,黃腐痠含量可達到82.10%。
대찬주폐기물발효산황부산분리순화적공예조건진행연구,우화리자교환법적공예삼수,이획득고순도적발효산황부산。이용단인소시험,채용 H +형화 NH4+형양리자교환수지대찬주폐기물발효산황부산진행분리순화,통과비교2충수지대황부산조제액정태교환흡부적효과,사선출용우황부산용액순화적교괄합적양리자교환수지류형;병이용삼인소(상양류속、층석고경비、상양농도)삼수평적정교시험,대사선출적양리자교환수지적순화공예삼수진행료우화。결과표명:채용리자교환법순화찬주폐기물발효산황부산적최가공예조건시채용 NH4+형양리자교환수지,주고경비5∶1,상양류속1 BV /h,상양농도위Na +초시농도≤700 mg /L (상당우원료0.1 g /mL)。이용해공예대황부산조제액진행분리순화,제잡효과최호, Na +거제솔위95.90%,황부산함량가체도82.10%。
Biochemical fulvic acid produced from kitchen waste was purificated in this paper, purification parameters were researched to obtain high-purity fulvic acid.Purification of biochemical fulvic acid was researched by H + and NH4 + cation exchange resin, through the comparison of exchange adsorption effect of 2 kinds of resin, screened out the cation exchange resin suitable for purification of biochemical fulvic acid by the single factor experiment, then the purification parameters of the selected cation exchange resin were optimized using the orthogonal test with three factors (injection velocity, aspect ratio, injection concentration) and three levels.The results showed that the optimum process conditions for purification of biochemical fulvic acid produced from kitchen waste by ion exchange were using NH4 + cation exchange resin, 5∶1 of aspect ratio, 1 BV /h of injection velocity, initial concentration of Na + ≤ 700 mg /L ( raw material 0.1 g /mL of injection concentration ) .Under the conditions, Na + desalination rate reached 95.90%, biochemical fulvic acid concentration could reach 82.10%.