光谱学与光谱分析
光譜學與光譜分析
광보학여광보분석
SPECTROSCOPY AND SPECTRAL ANALYSIS
2013年
12期
3312-3317
,共6页
曾晓岚%韩乐%刘建栋%丁文川%张勤%江岸
曾曉嵐%韓樂%劉建棟%丁文川%張勤%江岸
증효람%한악%류건동%정문천%장근%강안
垃圾渗滤液%光谱分析%反渗透膜%预处理%溶解性有机物
垃圾滲濾液%光譜分析%反滲透膜%預處理%溶解性有機物
랄급삼려액%광보분석%반삼투막%예처리%용해성유궤물
Leachate%Spectral analysis%Reverse osmosis%Pretreatment%Dissolved organic matter
考查反渗透(RO )膜处理渗滤液前所采用的预处理工艺对致膜有机污染物的去除效果,为RO膜预处理工艺的选择提供参考,采用同步荧光光谱、三维荧光光谱、紫外-可见全光谱对某垃圾焚烧厂渗滤液原液及其经“生化(UASB+A/O)+超滤”预处理工艺各级出水进行不同分子量分布区间的分析。同步荧光光谱表明,预处理工艺总体能有效去除波长在250~320 nm各分子量区间的以及波长>320 nm、分子量>1KDa的DOM ;三维荧光光谱表明,预处理工艺总体能有效去除低激发波长类酪氨酸、低激发波长类色氨酸及高激发波长类色氨酸及分子量>1KDa的类富里酸和高激发波长类酪氨酸;紫外-可见全光谱表明,预处理工艺总体能有效去除分子量>1KDa带π-π*跃迁的DOM 和各分子量区间的带多个共轭体系苯环结构的DOM。结果显示,将“生化(UASB+A/O)+超滤”组合工艺作为RO膜法处理焚烧厂渗滤液的预处理工艺时,还需加强同步荧光范围>320 nm、分子量<1 KDa、带π-π*跃迁的类富里酸及高激发波长类酪氨酸的去除。
攷查反滲透(RO )膜處理滲濾液前所採用的預處理工藝對緻膜有機汙染物的去除效果,為RO膜預處理工藝的選擇提供參攷,採用同步熒光光譜、三維熒光光譜、紫外-可見全光譜對某垃圾焚燒廠滲濾液原液及其經“生化(UASB+A/O)+超濾”預處理工藝各級齣水進行不同分子量分佈區間的分析。同步熒光光譜錶明,預處理工藝總體能有效去除波長在250~320 nm各分子量區間的以及波長>320 nm、分子量>1KDa的DOM ;三維熒光光譜錶明,預處理工藝總體能有效去除低激髮波長類酪氨痠、低激髮波長類色氨痠及高激髮波長類色氨痠及分子量>1KDa的類富裏痠和高激髮波長類酪氨痠;紫外-可見全光譜錶明,預處理工藝總體能有效去除分子量>1KDa帶π-π*躍遷的DOM 和各分子量區間的帶多箇共軛體繫苯環結構的DOM。結果顯示,將“生化(UASB+A/O)+超濾”組閤工藝作為RO膜法處理焚燒廠滲濾液的預處理工藝時,還需加彊同步熒光範圍>320 nm、分子量<1 KDa、帶π-π*躍遷的類富裏痠及高激髮波長類酪氨痠的去除。
고사반삼투(RO )막처리삼려액전소채용적예처리공예대치막유궤오염물적거제효과,위RO막예처리공예적선택제공삼고,채용동보형광광보、삼유형광광보、자외-가견전광보대모랄급분소엄삼려액원액급기경“생화(UASB+A/O)+초려”예처리공예각급출수진행불동분자량분포구간적분석。동보형광광보표명,예처리공예총체능유효거제파장재250~320 nm각분자량구간적이급파장>320 nm、분자량>1KDa적DOM ;삼유형광광보표명,예처리공예총체능유효거제저격발파장류락안산、저격발파장류색안산급고격발파장류색안산급분자량>1KDa적류부리산화고격발파장류락안산;자외-가견전광보표명,예처리공예총체능유효거제분자량>1KDa대π-π*약천적DOM 화각분자량구간적대다개공액체계분배결구적DOM。결과현시,장“생화(UASB+A/O)+초려”조합공예작위RO막법처리분소엄삼려액적예처리공예시,환수가강동보형광범위>320 nm、분자량<1 KDa、대π-π*약천적류부리산급고격발파장류락안산적거제。
In order to examine the removal of organic matter in the leachate which results in reverse osmosis (RO) membrane fouling ,and to provides a reference to select appropriate pretreatment processes of RO ,synchronous-scan fluorescence ,three-di-mensional excitation emission matrix fluorescence spectroscopic and UV-Vis spectrum of the dissolved organic matter (DOM ) in different molecular weight range in effluent from each leachate process of “biochemical (UASB+A/O)and UF” pretreatment in some incineration plant were examined .The results of synchronous fluorescence spectra analysis showed that DOM in the wave-length range of 250~320 nm with all the molecular weight and in the wavelength>320 nm with molecular weight>1 KDa was removed obviously by the pretreatment processes .The results of three-dimensional excitation-emission matrix (3D-EEM ) fluo-rescence spectra showed that the pretreatment processes removed low-excitation wavelength tyrosine-like ,low-excitation wave-length tryptophan-like and high-excitation wavelength tryptophan-like with all the molecular weight off ,and fulvic-like matter and high-excitation wave length tyrosine-like with molecular weight>1 KDa effectively .The results of UV-Vis spectra analysis showed that the pretreatment processes removed DOM of molecular weight >1 KDa withπ-π* transition and DOM of all molec-ular weight with conjugated system of the benzene ring structure .It was concluded that the removal of both fulvic-like matter and high-excitation wave length tyrosine-like with the wavelength>320 nm ,molecular weight<1 KDa and withπ-π* transition should be strengthened for controlling (RO) membrane fouling ,when leachate was treated by RO with the pretreatment proces-ses of “biochemical(UASB+A/O)and UF”.