{"currentpage":1,"firstResult":0,"maxresult":10,"pagecode":5,"pageindex":{"endPagecode":5,"startPagecode":1},"records":[{"abstractinfo":"研究了PVDF中空纤维膜为核心的CMF系统在海水淡化预处理应用中的工艺优化问题.经过长期的运行实验表明:最佳运行工艺条件是工作时间35 min,气水双洗30 s,反冲洗25 s,排污15 s.在气水双洗工艺中,当压缩空气储罐压力大于0.5 MPa时清洗效果最好.使用CMF进水配制的清洗剂中,NaClO和HCl相结合的化学清洗效果最好.CMF系统的出水浊度始终稳定在0.06～0.07 NTU之间,SDI值一直稳定在1～2之间,系统收率维持在96.3%.","authors":[{"authorName":"李璟","id":"2ec13b2d-8cc5-4cf6-a4ce-1e91a839d271","originalAuthorName":"李璟"},{"authorName":"吕晓龙","id":"d2cebefe-4757-41b5-a867-3e6fb3ca838a","originalAuthorName":"吕晓龙"},{"authorName":"马世虎","id":"aac79266-21cb-4486-890e-43a926725f38","originalAuthorName":"马世虎"}],"doi":"10.3969/j.issn.1007-8924.2006.03.014","fpage":"65","id":"ea0d4045-4c32-415d-b221-06f9f5af194b","issue":"3","journal":{"abbrevTitle":"MKXYJS","coverImgSrc":"journal/img/cover/MKXYJS.jpg","id":"54","issnPpub":"1007-8924","publisherId":"MKXYJS","title":"膜科学与技术   "},"keywords":[{"id":"b7971ad3-3498-4359-b0dd-b8d6c798b0f5","keyword":"<span style=\"color:red\">连续</span><span style=\"color:red\">膜过滤</span>","originalKeyword":"连续膜过滤"},{"id":"05b2d1bd-69f8-442a-9b79-9e5b41371ca3","keyword":"海水淡化","originalKeyword":"海水淡化"},{"id":"0f40f1ca-c41f-4fdb-ab4e-26ab9075346b","keyword":"工艺优化","originalKeyword":"工艺优化"}],"language":"zh","publisherId":"mkxyjs200603014","title":"海水淡化中<span style=\"color:red\">连续</span><span style=\"color:red\">膜过滤</span>技术的工艺优化研究","volume":"26","year":"2006"},{"abstractinfo":"介绍了聚偏氟乙烯(PVDF)中空纤维膜的制备工艺,讨论了PVDF含量、添加剂、纺丝温度、干程及卷绕速度对膜性能的影响.并就PVDF中空纤维膜3种应用方法--<span style=\"color:red\">连续</span><span style=\"color:red\">膜过滤</span>、膜生物反应器、双向流<span style=\"color:red\">过滤</span>的技术原理及应用作了介绍.","authors":[{"authorName":"杜启云","id":"c3d17907-3b1d-4145-9bec-380f69e40b1b","originalAuthorName":"杜启云"}],"doi":"10.3969/j.issn.1007-8924.2003.04.016","fpage":"80","id":"c7a81084-599c-4f68-9452-b078bd6fe3a4","issue":"4","journal":{"abbrevTitle":"MKXYJS","coverImgSrc":"journal/img/cover/MKXYJS.jpg","id":"54","issnPpub":"1007-8924","publisherId":"MKXYJS","title":"膜科学与技术   "},"keywords":[{"id":"61dea724-b228-4e19-b7e2-fa5f1c756ab0","keyword":"聚偏氟乙烯","originalKeyword":"聚偏氟乙烯"},{"id":"3c276873-e1ed-4281-92ca-972e573fe2f1","keyword":"中空纤维","originalKeyword":"中空纤维"},{"id":"e001471b-a8e7-46fc-8f09-b33352eaca51","keyword":"膜","originalKeyword":"膜"},{"id":"57aeaa75-b079-4035-acff-825d337b6ec9","keyword":"<span style=\"color:red\">连续</span><span style=\"color:red\">膜过滤</span>","originalKeyword":"连续膜过滤"},{"id":"395b33cb-c3b8-4cdc-9e53-6c33a8724974","keyword":"膜生物反应器","originalKeyword":"膜生物反应器"},{"id":"76f1fb4a-f280-44e5-bcf9-d520d6c86f02","keyword":"双向流<span style=\"color:red\">过滤</span>","originalKeyword":"双向流过滤"}],"language":"zh","publisherId":"mkxyjs200304016","title":"聚偏氟乙烯中空纤维膜的研制和应用","volume":"23","year":"2003"},{"abstractinfo":"海水淡化是环渤海地区经济发展的重大课题.海水预处理是淡化的关键过程.文章结合渤海湾地区海水水质的特点,讨论了膜法海水淡化预处理工艺的选择,设计时对水温,浊度变化的考虑.对<span style=\"color:red\">连续</span><span style=\"color:red\">膜过滤</span>工艺的类型和特点作了介绍.","authors":[{"authorName":"杜启云","id":"69960709-38a7-483f-978e-646f314b5370","originalAuthorName":"杜启云"}],"doi":"10.3969/j.issn.1007-8924.2011.03.039","fpage":"243","id":"735596ad-ff52-4809-b1f0-e8813599db6b","issue":"3","journal":{"abbrevTitle":"MKXYJS","coverImgSrc":"journal/img/cover/MKXYJS.jpg","id":"54","issnPpub":"1007-8924","publisherId":"MKXYJS","title":"膜科学与技术   "},"keywords":[{"id":"8602d265-e296-46ad-9ce1-1cb007a01634","keyword":"海水淡化","originalKeyword":"海水淡化"},{"id":"56dcb20e-44f3-4b6d-975d-76fb93adca8a","keyword":"预处理","originalKeyword":"预处理"},{"id":"7546545f-c74c-4abc-a152-cac0e1de4fb5","keyword":"<span style=\"color:red\">连续</span><span style=\"color:red\">膜过滤</span>","originalKeyword":"连续膜过滤"}],"language":"zh","publisherId":"mkxyjs201103039","title":"环渤海地区膜法海水淡化预处理工艺探讨","volume":"31","year":"2011"},{"abstractinfo":"研究了产品模块划分、模块组合、模块化设计和管理技术及零部件参数化设计方法.将污水回用<span style=\"color:red\">连续</span>微滤膜系统分解成若干个不同层次的独立的功能模块,可实现其模块化设计和管理.","authors":[{"authorName":"温淑鸿","id":"ac1a731a-b9c0-497f-8010-8211708db0c2","originalAuthorName":"温淑鸿"},{"authorName":"李然","id":"d7a26795-0e74-4015-9b6e-8b5264fc1189","originalAuthorName":"李然"},{"authorName":"李祥得","id":"5d3e5596-5c7f-4d04-97b0-134481531a65","originalAuthorName":"李祥得"}],"doi":"10.3969/j.issn.1007-8924.2005.06.008","fpage":"32","id":"8ff71691-70e2-4602-be15-7e0b9d193dd2","issue":"6","journal":{"abbrevTitle":"MKXYJS","coverImgSrc":"journal/img/cover/MKXYJS.jpg","id":"54","issnPpub":"1007-8924","publisherId":"MKXYJS","title":"膜科学与技术   "},"keywords":[{"id":"4693d776-84e8-42ea-b031-59d920f310fb","keyword":"膜系统","originalKeyword":"膜系统"},{"id":"c0cccec4-8bb1-4141-bfc4-92c55d7c5040","keyword":"模块化设计","originalKeyword":"模块化设计"},{"id":"5e939828-08b1-4460-a41e-f440f26794e7","keyword":"参数化设计","originalKeyword":"参数化设计"}],"language":"zh","publisherId":"mkxyjs200506008","title":"<span style=\"color:red\">连续</span><span style=\"color:red\">膜过滤</span>系统的模块化设计与管理","volume":"25","year":"2005"},{"abstractinfo":"以改善一体式<span style=\"color:red\">膜过滤</span>器中<span style=\"color:red\">膜过滤</span>性能为目的,将搅拌引入<span style=\"color:red\">膜过滤</span>系统,设计新型的旋转切向流强化<span style=\"color:red\">膜过滤</span>.考察搅拌器的类型以及操作参数(搅拌速度、叶轮直径、膜管与搅拌轴之间的距离)对膜通量的影响,并比较旋转切向流<span style=\"color:red\">膜过滤</span>与错流<span style=\"color:red\">膜过滤</span>的能耗,为一体式<span style=\"color:red\">膜过滤</span>器的应用提供基础数据.","authors":[{"authorName":"陈日志","id":"afa4406d-9548-4f0b-af99-a0cdda877643","originalAuthorName":"陈日志"},{"authorName":"张利雄","id":"fed01087-8f53-42ca-a05b-43b114ee356f","originalAuthorName":"张利雄"},{"authorName":"徐南平","id":"beec6be5-dcfd-44dc-8712-b7f030ca8b18","originalAuthorName":"徐南平"}],"doi":"10.3969/j.issn.1007-8924.2006.01.002","fpage":"3","id":"18e70f44-27b4-44ed-9946-60928d4eee70","issue":"1","journal":{"abbrevTitle":"MKXYJS","coverImgSrc":"journal/img/cover/MKXYJS.jpg","id":"54","issnPpub":"1007-8924","publisherId":"MKXYJS","title":"膜科学与技术   "},"keywords":[{"id":"bcd635e9-c598-4f85-a930-e281daa4e197","keyword":"一体式<span style=\"color:red\">膜过滤</span>器","originalKeyword":"一体式膜过滤器"},{"id":"6688ebc7-3d19-435e-94e0-0d1ba11cdda5","keyword":"陶瓷膜","originalKeyword":"陶瓷膜"},{"id":"9a0f73b6-e393-4795-a91a-9259f5bf8cd8","keyword":"旋转切向流","originalKeyword":"旋转切向流"},{"id":"df7ffb00-6ce1-4e06-89c7-106d84301693","keyword":"错流","originalKeyword":"错流"}],"language":"zh","publisherId":"mkxyjs200601002","title":"旋转切向流对一体式<span style=\"color:red\">膜过滤</span>器中<span style=\"color:red\">膜过滤</span>性能影响的研究","volume":"26","year":"2006"},{"abstractinfo":"研究了钛白行业中<span style=\"color:red\">过滤</span>物料浓废酸、淡废酸和转窑\"白水\"的物理性质,探讨<span style=\"color:red\">膜过滤</span>设备在钛白行业应用中存在的问题,并进行了分析和总结.","authors":[{"authorName":"金斌","id":"93565193-b4bc-4c2f-a4d3-5257126ddc49","originalAuthorName":"金斌"}],"doi":"10.3969/j.issn.1009-9964.2002.06.007","fpage":"25","id":"89205441-a9b5-461e-b3c4-a8556152af1a","issue":"6","journal":{"abbrevTitle":"TGYJZ","coverImgSrc":"journal/img/cover/TGYJZ.jpg","id":"60","issnPpub":"1009-9964","publisherId":"TGYJZ","title":"钛工业进展"},"keywords":[{"id":"60bd1502-34c7-4e79-ace7-5fc85764c0fe","keyword":"物料性质","originalKeyword":"物料性质"},{"id":"11abee09-442a-4b8c-b555-84a9845c7077","keyword":"<span style=\"color:red\">膜过滤</span>","originalKeyword":"膜过滤"},{"id":"07b9fa58-d0f4-4f5e-9314-b8e048c4e1c0","keyword":"钛白","originalKeyword":"钛白"}],"language":"zh","publisherId":"tgyjz200206007","title":"<span style=\"color:red\">膜过滤</span>设备在钛白行业应用探讨","volume":"","year":"2002"},{"abstractinfo":"研究微滤<span style=\"color:red\">膜过滤</span>阻力机理及其通量的变化是该工艺应用推广需要解决的关键.以Langmuir理论和Darcy定律为基础,从理论上证实了浓度极化阻力与凝胶层阻力是同一性质的阻力,并通过Langmuir关系式统一起来,推导了微滤<span style=\"color:red\">膜过滤</span>阻力的数学模型.然后采用一体式<span style=\"color:red\">膜过滤</span>反应器<span style=\"color:red\">过滤</span>乳化油实验对该模型进行了验证.实验结果与<span style=\"color:red\">膜过滤</span>阻力模型拟合得很好(R~2=0.991 2),膜表面极化浓度与相对<span style=\"color:red\">过滤</span>压差成线性关系,比例系数为凝胶层浓度.基于Langmuir理论的微滤<span style=\"color:red\">膜过滤</span>阻力模型能真实反映凝胶层阻力的形成过程.用该模型得到的沉积平衡系数Φ反映了混合液的浓度、颗粒大小、温度和黏度等<span style=\"color:red\">过滤</span>特性,并把极限通量J_(Vlim)与混合液<span style=\"color:red\">过滤</span>特性联系起来,极限通量与<span style=\"color:red\">过滤</span>压差无关.","authors":[{"authorName":"曹占平","id":"dd19ee70-4805-47e8-9f28-a99cd283fd3f","originalAuthorName":"曹占平"},{"authorName":"张景丽","id":"afc01ec5-eeb1-455f-b840-d8d896f31872","originalAuthorName":"张景丽"},{"authorName":"张宏伟","id":"53270788-6a0f-4ea5-aa11-5245e3e8c4b5","originalAuthorName":"张宏伟"}],"doi":"10.3969/j.issn.1007-8924.2010.01.004","fpage":"18","id":"e375da00-90b6-4016-aaa8-f49e44715dfd","issue":"1","journal":{"abbrevTitle":"MKXYJS","coverImgSrc":"journal/img/cover/MKXYJS.jpg","id":"54","issnPpub":"1007-8924","publisherId":"MKXYJS","title":"膜科学与技术   "},"keywords":[{"id":"6135d368-5afa-4b55-b4ae-d14dd0968b73","keyword":"微滤","originalKeyword":"微滤"},{"id":"5784b6b6-a8d4-4d94-bd84-063b177a0e1c","keyword":"<span style=\"color:red\">过滤</span>模型","originalKeyword":"过滤模型"},{"id":"3d2f4d77-2657-4532-96b1-7ebea9c688fc","keyword":"Langmuir理论","originalKeyword":"Langmuir理论"},{"id":"09451ae5-13d6-4d03-ae2f-565f382c5c32","keyword":"极限通量","originalKeyword":"极限通量"}],"language":"zh","publisherId":"mkxyjs201001004","title":"微滤<span style=\"color:red\">膜过滤</span>阻力机理及模型研究","volume":"30","year":"2010"},{"abstractinfo":"超声技术可有助于控制膜污染的形成,采用超声波辅助陶瓷<span style=\"color:red\">膜过滤</span>氧化铝悬浮液体系,考察超声在不同颗粒的粒径、浓度以及<span style=\"color:red\">膜过滤</span>操作压力下对膜过程的影响规律,以及超声功率、超声方式等对<span style=\"color:red\">膜过滤</span>过程的影响;分析了超声波对强化颗粒体系<span style=\"color:red\">过滤</span>的机理.结果表明,超声可使陶瓷膜微滤通量提高10%左右,且对粒径大的颗粒体系影响增大;合适的超声功率为8 W,<span style=\"color:red\">连续</span>超声对通量的提高率大于间歇超声.","authors":[{"authorName":"舒莉","id":"b74f5c8a-24ea-41e0-bf7f-5c3980e90133","originalAuthorName":"舒莉"},{"authorName":"邢卫红","id":"103cbdc8-e44d-4a99-831d-2dac89ee07a3","originalAuthorName":"邢卫红"}],"doi":"10.3969/j.issn.1007-8924.2009.05.002","fpage":"6","id":"66c114d4-03ca-4537-a119-861bdaaa23ac","issue":"5","journal":{"abbrevTitle":"MKXYJS","coverImgSrc":"journal/img/cover/MKXYJS.jpg","id":"54","issnPpub":"1007-8924","publisherId":"MKXYJS","title":"膜科学与技术   "},"keywords":[{"id":"961bf575-21b8-44a9-afb3-ef4d5e5bd4aa","keyword":"超声","originalKeyword":"超声"},{"id":"d6e5455d-c0bc-471c-a5dd-216b090be22b","keyword":"陶瓷膜","originalKeyword":"陶瓷膜"},{"id":"df5e8df9-fdaa-4d65-aba5-1611d7d1c06f","keyword":"颗粒","originalKeyword":"颗粒"}],"language":"zh","publisherId":"mkxyjs200905002","title":"超声在陶瓷<span style=\"color:red\">膜过滤</span>氧化铝悬浮体系中的应用","volume":"29","year":"2009"},{"abstractinfo":"探讨了超滤-微滤<span style=\"color:red\">膜过滤</span>传质理论的研究状况,重点介绍了超滤-微滤膜过理论模型、非牛顿液体膜堵塞<span style=\"color:red\">过滤</span>以及动态<span style=\"color:red\">过滤</span>等常规<span style=\"color:red\">过滤</span>理论的研究进展,评述了超滤-微滤<span style=\"color:red\">膜过滤</span>传质机理的动态,指出了超滤-微滤<span style=\"color:red\">膜过滤</span>基本理论模型需进一步研究解决的问题.","authors":[{"authorName":"许振良","id":"c2070030-6cc6-431c-aa92-014e576e8ff5","originalAuthorName":"许振良"},{"authorName":"李鲜日","id":"4672d7e6-698b-4a9f-8c9a-abf134811049","originalAuthorName":"李鲜日"},{"authorName":"周颖","id":"a769edcc-28fd-4564-a068-1c5656c9c93c","originalAuthorName":"周颖"}],"doi":"10.3969/j.issn.1007-8924.2008.04.001","fpage":"1","id":"1e5c351b-1f97-4002-926d-aeaaad8eba8a","issue":"4","journal":{"abbrevTitle":"MKXYJS","coverImgSrc":"journal/img/cover/MKXYJS.jpg","id":"54","issnPpub":"1007-8924","publisherId":"MKXYJS","title":"膜科学与技术   "},"keywords":[{"id":"c5cb8b84-9cde-4d0f-b996-e1876dc65f19","keyword":"超滤-微滤","originalKeyword":"超滤-微滤"},{"id":"749d587b-a77d-4c19-9606-d8f04fbc6172","keyword":"传质理论","originalKeyword":"传质理论"},{"id":"d60ca294-e3ea-4935-a145-fffbe3609e44","keyword":"非牛顿液体","originalKeyword":"非牛顿液体"},{"id":"1b4e06bd-2b5f-4e63-be01-905fe2d6d341","keyword":"错流","originalKeyword":"错流"}],"language":"zh","publisherId":"mkxyjs200804001","title":"超滤-微滤<span style=\"color:red\">膜过滤</span>传质理论的研究进展","volume":"28","year":"2008"},{"abstractinfo":"对UF膜处理某厂生活污水出水时膜污染的机理进行了研究.实验结果表明,在<span style=\"color:red\">膜过滤</span>过程中,沉积层的形成是膜污染的主要来源.压力越大,沉积阻力所占总阻力比例越大.投加混凝剂后沉积阻力所占总阻力比例下降.同时,<span style=\"color:red\">过滤</span>总阻力也显著减小.<span style=\"color:red\">膜过滤</span>原水初期,膜污染过程不受堵塞的控制.<span style=\"color:red\">膜过滤</span>原水过程符合沉积<span style=\"color:red\">过滤</span>定律.混凝后<span style=\"color:red\">膜过滤</span>初期,截留分子量为3万的UF膜污染过程不受堵塞的控制,而10万和14万UF<span style=\"color:red\">膜过滤</span>混凝出水初期时膜污染过程虽然受堵塞的控制,但时间很短,混凝后<span style=\"color:red\">膜过滤</span>过程主要受沉积层的控制.","authors":[{"authorName":"孙德栋","id":"66fa2e39-0dd0-468d-9942-a17516c29f89","originalAuthorName":"孙德栋"},{"authorName":"张启修","id":"f71dbdf9-5602-4f9f-abfa-7e6976e7db14","originalAuthorName":"张启修"}],"doi":"10.3969/j.issn.1007-8924.2004.05.009","fpage":"37","id":"22d04657-73c8-473b-8b07-a182b254b879","issue":"5","journal":{"abbrevTitle":"MKXYJS","coverImgSrc":"journal/img/cover/MKXYJS.jpg","id":"54","issnPpub":"1007-8924","publisherId":"MKXYJS","title":"膜科学与技术   "},"keywords":[{"id":"30105d4a-aebc-45ca-b73e-3a431aaa3b5e","keyword":"UF膜","originalKeyword":"UF膜"},{"id":"57ed7845-301f-4861-8193-d81c182f8f68","keyword":"膜污染","originalKeyword":"膜污染"},{"id":"d9bd3ebb-78ab-4a31-b308-6f3d3ee52658","keyword":"膜阻力","originalKeyword":"膜阻力"}],"language":"zh","publisherId":"mkxyjs200405009","title":"某厂生活污水站出水用UF<span style=\"color:red\">膜过滤</span>的污染试验研究","volume":"24","year":"2004"}],"totalpage":751,"totalrecord":7508}