| 膜集成技术精制回收乙二醇-水混合液的探索 |
| 作者: 天津工业大学材料科学与工程学院 |
| 单位: 天津工业大学材料科学与工程学院 |
| 关键词: 膜集成技术;回收醇水混合液;纳滤技术;反渗透技术;离子交换树脂. |
| DOI号: |
| 分类号: TQ09;X783 |
| 出版年,卷(期):页码: 2014, 34(5):84-88 |
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摘要: |
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本文剖析了乙二醇生产环节的废液—多醇贫液及其蒸馏馏分的主要化学物质,确定了引起馏分味浓、色重和电导率高的原因。经工艺筛选,聚酰胺纳滤膜在1.5MPa下流速45L/m2.h将混合液完全脱色。活性炭吸附柱以0.5L/m2.h可脱除体系N、S化合物。聚酰胺反渗透膜在1.8MPa下流速35L/m2.h可将低粘度液体电导率降低至20µS/cm;经酸、碱凝胶离子交换柱可将高粘度液体电导率降至10µS/cm。根据产品性质和工厂实际情况设计了用于乙二醇-水混合液精制的膜集成技术工艺路线。 |
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The ingredients of blending waste liquid of ethylene glycol/water were analyzed, which came from ethylene glycol commercial manufactory company. The main reason had been identified which cause heavy smell, dark color and high conductivity for. Under 1.5MPa pressure, concentrate glycol liquids were filtrated by polyamide nanofiltration membrane in velocity of 45L/m2.h to be bleached. Volatile small organic molecules were deodorized by active carbon filled column under 0.5L/m2.h. Organic electrolytes dissolving in glycol-water mixtures were removed by reverse osmosis for low viscosity liquid with the speed of 35L/m2.h under 1.8MPa and ion exchange resin columns for high viscosity liquid. The process conditions and factors of each unit were also investigated and discuss, and the operation route was designed for whole purification process according to the actual situation of the nature of products and factory integration technology. |
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基金项目: |
| 国家高技术研究发展计划(863计划), “高性能分离膜材料的规模化关键技术(一期)”项目之“高通量纳滤膜材料的规模化制备技术”课题资助(2012AA03A602). |
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作者简介: |
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The ingredients of blending waste liquid of ethylene glycol/water were analyzed, which came from ethylene glycol commercial manufactory company. The main reason had been identified which cause heavy smell, dark color and high conductivity for. Under 1.5MPa pressure, concentrate glycol liquids were filtrated by polyamide nanofiltration membrane in velocity of 45L/m2.h to be bleached. Volatile small organic molecules were deodorized by active carbon filled column under 0.5L/m2.h. Organic electrolytes dissolving in glycol-water mixtures were removed by reverse osmosis for low viscosity liquid with the speed of 35L/m2.h under 1.8MPa and ion exchange resin columns for high viscosity liquid. The process conditions and factors of each unit were also investigated and discuss, and the operation route was designed for whole purification process according to the actual situation of the nature of products and factory integration technology. |
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参考文献: |
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[1] 殷伊琳. 环氧乙烷/乙二醇技术进展及市场分析[J]. 天津化工, 2012, 26 (5): 1—3. |
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