{"title":"绿色技术在冷却剂废水过滤发展中的贡献","authors":"E. Yuliwati","doi":"10.22135/sje.2018.3.2.74-79","DOIUrl":null,"url":null,"abstract":"The aim of this study is the contribution of green technology in the sustainable development of oily wastewater from machining process. The cross-flow membranes has been performed for treating wastewater emulsion of oil derived from the automotive industry on the metal cutting section. The objective of this study is to treat liquid waste from machining process using membrane technology. The mechanism of ultrafiltration process is flow of small molecules pass through pore of membrane. The performance of the cellulose acetate hydrophilic membrane is determined by the permeate and rejection flux. The operation of this two-stage ultrafiltration membrane involves a 12% composite cellulose acetate membrane (CA-12) in phase I and 15% (15%) cellulose acetate membrane (CA-15) in phase II with a 90 minute operating time with pressure of 3.5 bar. Flux of phase I, without pretreatment and with pretreatment are 17,03 L / m 2 .h and 59,05 L / m 2 .h respectively. In phase II, the flux of treatment without and with preteeatment are 22.08 L / m 2 .h and 24.86 L / m 2 .h , respectively. COD and surfactant rejection for both membrane without pretreatment of 96.57% and 96.35%, whereas for waste feed with COD rejection of 98.56% and surfactant rejection of 97.44 %.","PeriodicalId":31278,"journal":{"name":"Sriwijaya Journal of Environment","volume":"238 1","pages":""},"PeriodicalIF":0.0000,"publicationDate":"2018-09-26","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Green Technology Contribution in Development of Coolant Wastewater Filtration\",\"authors\":\"E. Yuliwati\",\"doi\":\"10.22135/sje.2018.3.2.74-79\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"The aim of this study is the contribution of green technology in the sustainable development of oily wastewater from machining process. The cross-flow membranes has been performed for treating wastewater emulsion of oil derived from the automotive industry on the metal cutting section. The objective of this study is to treat liquid waste from machining process using membrane technology. The mechanism of ultrafiltration process is flow of small molecules pass through pore of membrane. The performance of the cellulose acetate hydrophilic membrane is determined by the permeate and rejection flux. The operation of this two-stage ultrafiltration membrane involves a 12% composite cellulose acetate membrane (CA-12) in phase I and 15% (15%) cellulose acetate membrane (CA-15) in phase II with a 90 minute operating time with pressure of 3.5 bar. Flux of phase I, without pretreatment and with pretreatment are 17,03 L / m 2 .h and 59,05 L / m 2 .h respectively. In phase II, the flux of treatment without and with preteeatment are 22.08 L / m 2 .h and 24.86 L / m 2 .h , respectively. COD and surfactant rejection for both membrane without pretreatment of 96.57% and 96.35%, whereas for waste feed with COD rejection of 98.56% and surfactant rejection of 97.44 %.\",\"PeriodicalId\":31278,\"journal\":{\"name\":\"Sriwijaya Journal of Environment\",\"volume\":\"238 1\",\"pages\":\"\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"2018-09-26\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Sriwijaya Journal of Environment\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://doi.org/10.22135/sje.2018.3.2.74-79\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Sriwijaya Journal of Environment","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.22135/sje.2018.3.2.74-79","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0
摘要
本研究旨在探讨绿色技术在机械加工含油废水可持续发展中的贡献。用横流膜法处理汽车工业的油类废水乳化液。本研究的目的是利用膜技术处理加工过程中的废液。超滤过程的机理是小分子通过膜孔的流动。醋酸纤维素亲水性膜的性能由渗透通量和排斥通量决定。该两级超滤膜的操作包括一期为12%复合醋酸纤维素膜(CA-12)和二期为15%(15%)醋酸纤维素膜(CA-15),操作时间为90分钟,压力为3.5 bar。第一期、未经预处理和经预处理的通量分别为17.03 L / m2 .h和59.05 L / m2 .h。第二期未预处理和预处理处理的通量分别为22.08 L / m 2. h和24.86 L / m 2. h。未经预处理的两种膜的COD和表面活性剂去除率分别为96.57%和96.35%,而废饲料的COD去除率为98.56%,表面活性剂去除率为97.44%。
Green Technology Contribution in Development of Coolant Wastewater Filtration
The aim of this study is the contribution of green technology in the sustainable development of oily wastewater from machining process. The cross-flow membranes has been performed for treating wastewater emulsion of oil derived from the automotive industry on the metal cutting section. The objective of this study is to treat liquid waste from machining process using membrane technology. The mechanism of ultrafiltration process is flow of small molecules pass through pore of membrane. The performance of the cellulose acetate hydrophilic membrane is determined by the permeate and rejection flux. The operation of this two-stage ultrafiltration membrane involves a 12% composite cellulose acetate membrane (CA-12) in phase I and 15% (15%) cellulose acetate membrane (CA-15) in phase II with a 90 minute operating time with pressure of 3.5 bar. Flux of phase I, without pretreatment and with pretreatment are 17,03 L / m 2 .h and 59,05 L / m 2 .h respectively. In phase II, the flux of treatment without and with preteeatment are 22.08 L / m 2 .h and 24.86 L / m 2 .h , respectively. COD and surfactant rejection for both membrane without pretreatment of 96.57% and 96.35%, whereas for waste feed with COD rejection of 98.56% and surfactant rejection of 97.44 %.