請用此 Handle URI 來引用此文件: http://hdl.handle.net/11455/5881
標題: 界面活性劑淋洗整治EDC-tar污染之評估
Evaluation of Surfactant Flushing for Remediating EDC-tar Contamination
作者: 謝承霖
Hsieh, Cheng-Lin
關鍵字: 氯化有機溶劑
chlorinated solvent
二氯乙烷焦油
質量傳輸
動力模式
地下水污染
EDC-tar
mass transfer
kinetics
groundwater contamination
出版社: 環境工程學系所
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摘要: Ethylene dichloride tar (EDC-tar)是氯乙烯單體製程所產生的焦油狀廢棄物,棕黑色且具臭味的重質非水相液體。此廢棄物成份大部分皆為單鍵及雙鍵的氯化脂肪族碳氫化合物,但是仍約有20%來自無法蒸餾之物質。本研究探討採用界面活性劑淋洗技術用以整治EDC-tar之可行性。首先,分析確認EDC-tar之成份組成,並針對此一污染物篩選合適之界面活性劑。研究過程探討界面活性劑單獨/混合使用及溶液pH對EDC-tar溶解度之影響,再藉由管柱淋洗實驗了解污染物去除之機制以及評估整治效益,並針對洗出廢水以鹽析法進行EDC-tar之分離,達到整治之目的。 EDC-tart成分分析結果顯示,1,1,2-三氯乙烷及1,2-二氯乙烷是EDC-tar之主要成份,佔EDC-tar總值量之57%。界面活性劑篩選試驗結果顯示,混合SDS/Tween 80兩種界面活性劑,當其濃度採用8 mM/16 mM之配比時對EDC-tar不僅有較佳的溶解能力(溶解度約32000 mg/L vs. 4000 mg/L於純水中),且此溶液之表面張力亦較純水之數值為低(SDS/Tween 80: 24.6 dyne/cm vs.純水: 70 dyne/cm),此外,當以氫氧化鈉調整溶液至鹼性條件時,能進一步提昇EDC-tar之溶解度。管柱實驗結果顯示,SDS之添加能提昇EDC-tar於管柱中之移動性,當使用鹼性界面活性劑淋洗時,其呈現較佳之移除效率。進一步藉由淋洗動力模式分析,成功模擬本實驗之EDC-tar藉由溶解機制之去除量(預測移除量/實際移除量= 0.89 ± 0.1)。本研究另針對EDC-tar/界面活性劑溶液分離之可行性予以探討,結果顯示EDC-tar能夠藉由鹽析作用進行分離,當氯化鈉的濃度達20 wt%時能夠分離濃縮溶液中約90%的EDC-tar,使其沈降於容器底部,有利於收集淋洗溶液中之EDC-tar。本研究之成果可作為整治EDC-tar污染土壤及地下水之技術選項。
Ethylene dichloride tar (EDC-tar) is a tar-like waste originated from the process of vinyl chloride production. This tar is a dense non-aqueous liquid with brown-black color and bad smells. EDC-tar is consisted of ~20% of undistilled components and the major constituents include chlorinated aliphatic and aromatic hydrocarbons. This study investigated the feasibility of surfactant enhanced aquifer remediation technique for treating EDC-tar contaminated aquifer. Initial experiments were to identify the components of EDC-tar consitituents and to select an appropriate surfactant to remediate EDC-tar contamination. This study investigated the potential to enhance solubility of EDC-tar using single surfactant or mixed surfactants systems also and the effect of solution pH. Furthermore, effectiveness and mechanisms of EDC-tar removed were examined in column studies. Regarding treatment of EDC-tar flushing solution, “salting out” effect was employed for separation of EDC-tar from contaminant/surfactant mixed solution. Results of EDC-tar qualitative analysis shows that 1,1,2-trichloroethane and 1,2-dichloroethane are main components of EDC-tar. The proportion of these two compounds in EDC-tar is 57%. Results of surfactants screening test show that SDS/Tween 80 at the mixing molar ratio of 8/16 exhibited better EDC-tar solubility (32000 mg/L vs. 4000 mg/L in pure water) and lower surface tension (24 dyne/cm vs. 70 dyne/cm in pure water). In addition, alkaline pH enhanced EDC-tar solubility comparing to that in neutral condition. Column studies show that addition of SDS enhanced EDC-tar mobility. Alkaline surfactant, SDS/Tween 80 with mixing molar ratio of 8 mM/16 mM, show better removals in column studies than other experimental conditions evaluated. Analysis of mass transfer kinetic behavior shows high correlation to actual mass removal of EDC-tar by solubilization mechanism. The ratio of simulated mass removed/actual mass removed is 0.89 ± 0.1. The separation of EDC-tar/surfactant mixed solution results show that EDC-tar can be separated by adding 20% of NaCl by weight (i.e., salting out effects). Ninety percent of EDC-tar could be separated and sunk at the bottom of vessel, which can be used as a way to collect EDC-tar from solution. The results obtained in this study would be helpful as a reference for remediation of EDC-tar contamination.
URI: http://hdl.handle.net/11455/5881
其他識別: U0005-1806201316180400
文章連結: http://www.airitilibrary.com/Publication/alDetailedMesh1?DocID=U0005-1806201316180400
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