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渗滤

渗滤的相关文献在1985年到2023年内共计7234篇,主要集中在废物处理与综合利用、化学工业、环境污染及其防治 等领域,其中期刊论文113篇、会议论文2篇、专利文献7119篇;相关期刊99种,包括地质找矿论丛、农业工程学报、南京工业大学学报(自然科学版)等; 相关会议2种,包括中国科协2005年学术年会分论坛暨西部开发与生态环境保护研讨会、第一届全国化学工程与生物化工年会等;渗滤的相关文献由13113位作者贡献,包括彭永臻、刘军、刘伟等。

渗滤—发文量

期刊论文>

论文:113 占比:1.56%

会议论文>

论文:2 占比:0.03%

专利文献>

论文:7119 占比:98.41%

总计:7234篇

渗滤—发文趋势图

渗滤

-研究学者

  • 彭永臻
  • 刘军
  • 刘伟
  • 李红
  • 王淑莹
  • 席北斗
  • 冷超群
  • 刘洋
  • 黄开明
  • 赵由才
  • 期刊论文
  • 会议论文
  • 专利文献

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    • 曹军瑞; 王勋亮; 马宇辉; 王树勋; 赵瑾; 王文华; 姜天翔
    • 摘要: 为了有效控制道路微污染雨水径流污染,利用纤维柬-活性炭-沸石联用法对模拟雨水进行处理,考察该系统对浊度、TOC、氨氮及磷酸盐的去除效果.结果 表明,当浊度、TOC、氨氮及磷酸盐浓度分别在(3.85 ~ 25.60 NTU)、(4.58~17.80 mg/L)、(0.31 ~ 1.42 mg/L)和(0.05 ~0.36 mg/L)范围内时,该联用工艺对上述污染物去除率分别为(79.2% ~ 96.9%)、(82.7%~87.2%)、(87.5% ~94.0%)和(52.9%~65.6%).活性炭对TOC的吸附能力较强,其吸附过程符合Langmuir吸附等温线模型,单分子层最大吸附量为41.70 mg/g;沸石对氨氮和磷酸盐的吸附能力明显,其吸附过程同样符合Langmuir吸附等温线模型,单分子层最大吸附量分别为12.31和0.64 mg/g.该组合工艺是一种理想的净化城市污染雨水的方法.
    • 徐静远; 汤淑云; 邱运仁
    • 摘要: 用超滤膜采用连续渗滤法对聚丙烯酸钠(PAAS)进行预处理以去除PAAS溶液中的小分子.研究了PAAS浓度、pH值、跨膜压差(TMP)和预处理时间对透过液浓度和渗透通量的影响.结果表明,所需预处理时间(NPT)随着PAAS浓度的增加而增加,随着TMP的增加而减小.渗透通量随时间的变化趋势受pH值的影响,在pH为5.0、7.0和9.3时,渗透通量开始迅速下降,然后随着渗滤时间的延长逐渐增加直至稳定值;然而,在等电点pH值为3.0时,渗透通量随着渗滤时间的延长逐渐减小.在pH大于等电点(IEP)进行渗滤时,小分子比较容易去除.过滤电势随时间的变化趋势与渗透浓度的变化趋势相似,但前者对预处理效果的指示更便捷.%Thepretreatment for the removal of small molecules from poly(acrylic acid) sodium (PAAS) solution by continuous diafiltration was investigated using ultrafiltration membrane. The effects of PAAS concentration, pH, trans-membrane pressure and pretreatment time on the permeate concentration and permeate flux were studied. The results show that the necessary pretreatment time (NPT) increases with PAAS concentration, decreases with TMP. The change trend of permeate flux with time is affected by pH. The permeate fluxes rapidly decrease from the start, and then increase gradually to stable values at pH 5.0, pH 7.0 and pH 9.3. However, it decreases gradually with time till a state value at pH 3.0 (iso-electric point, IEP). The removal of small molecules is easy at pH greater than iso-electric point (IEP). The change of filtration potential with time indicates the similar trend to that of permeation concentration, but the former is more convenient for indication of NPT.
    • 徐静远1; 汤淑云1; 邱运仁1
    • 摘要: 用超滤膜采用连续渗滤法对聚丙烯酸钠(PAAS)进行预处理以去除PAAS溶液中的小分子。研究了PAAS浓度、pH值、跨膜压差(TMP)和预处理时间对透过液浓度和渗透通量的影响。结果表明,所需预处理时间(NPT)随着PAAS浓度的增加而增加,随着TMP的增加而减小。渗透通量随时间的变化趋势受pH值的影响,在pH为5.0、7.0和9.3时,渗透通量开始迅速下降,然后随着渗滤时间的延长逐渐增加直至稳定值;然而,在等电点pH值为3.0时,渗透通量随着渗滤时间的延长逐渐减小。在pH大于等电点(IEP)进行渗滤时,小分子比较容易去除。过滤电势随时间的变化趋势与渗透浓度的变化趋势相似,但前者对预处理效果的指示更便捷。
    • 李冰; 李晓
    • 摘要: 通过对2016—2017年晋江龙湖水质结果进行分析,发现龙湖氮磷常年存在超标现象,地下水较湖水超标更为严重,超标倍数4.69~9.09倍.在龙湖选取了4个孔进行抽水试验,对ZK1进行分析,氨氮在渗滤过程中发生吸附沉淀、阳离子交换吸附作用、硝化与反硝化作用,其中后两者起主要作用.总磷的迁移转化主要发生:吸附沉淀、离子交换吸附反应,与磷酸盐的沉淀溶解,而生物作用不明显.对水中磷的迁移转化影响较大的因素为:pH、水温、溶解氧含量、水动力条件.
    • 黑昆仑; 常志州; 陈广银; 叶小梅; 张应鹏
    • 摘要: High solid content anaerobic digestion is an environment friendly and cost efficient way to dispose the organic wastes because of little water added and renewable energy produced. In high solid digestion system, substrate has little free water so that the mass transfer is inhibited frequently, leading to volatile fatty acids (VFAs) accumulation and fermentation system failed easily. Many researchers report that leachate recirculation in reactors is an efficient way to enhance mass transfer leading the increase of anaerobic digestion efficiency. Most of the investigators are keen on making mathematics model to indicate the movement of leachate in substrates, these mathematical models require skillful person to play a key role in practices. Therefore, it is important to have better and easier understanding of leachate distribution characteristics in substrates. The trial was designed to determine such distribution. Lithium-Ion tracing method and contour map were used to achieve these goals. A batch wheat straw anaerobic digestion experiment was conducted at 14% total solid content and mesophilic conditions in special designed batch fermentation device, three treatments (T1, T2 & T3) were set to investigate the leachate distribution characteristics, and anaerobic digestion substrates for T1, T2 & T3 were all same. For T1, we divided the substrates into three equal parts by two separator plates. T2 was divided into two equal parts by one separator plate. T3 was not divided but as a whole. A certain amount of lithium chloride solution instead of leachate was circulated in T1, T2 & T3 at the end of fermentation. When the circulation process was over (no water dropped from the fermentation device bottom), we took the inner part of fermentation device out and froze them. The substrate profile was obtained by sawing off the substrate. Samples for measuring residue-lithium-Ion and Extracellular Polymeric Substances (EPS) were taken from profile substrate regularly. The distribution characters of leachate in substrates were expressed by the contour map obtained by SUFER 8.0 based on residue-Lithium-Ion and EPS data. At the same time, the daily biogas production, methane content, layer wet bulk density before and after digestion were analyzed. The results showed that there were no significant differences among total biogas production, accumulation of TS biogas production, and methane content in T1, T2 & T3 treatments. At the end of fermentation, the layer wet bulk density of T1, T2 and T3 was high at the top layer and decreased generally. The wet bulk density of T3 decreased in substrate depth before reaching a constant of 0.6 g/cm3, but it was larger than the initial substrate wet bulk density of 0.58 g/cm3. From the Li+-residue contour map, the area of residue Li+ content below 2 mg/kg in T1, T2 and T3 profile took up 2.32%, 12.69% and 20.66% of total profile area respectively, indicating that the "leachate dead zone" existed in three treatments. The conclusions drawn from profile EPS contour map were the same as these conducted from Li+-residual contour map, they both showed leachate recirculation was not homogeneous substrates high in straw solid content anaerobic digestion. These results provided scientific evidences on improvement of leachate recirculation technologies in high straw solid anaerobic digestion.%探明秸秆高固厌氧发酵回流液剖面渗滤特征,对提高秸秆高固厌氧发酵产气效率十分重要.该研究以搓揉麦秸为底物,在(37±1)°C、TS为14%的发酵条件下,通过隔板将发酵罐中物料均分成3层(T1)、2层(T2)与不分层(T3)3个处理,以氯化锂为示踪剂,分析了剖面上物料残留锂离子、物料胞外多聚物(extracellular polymeric substances,EPS)含量、各处理产气以及发酵前后物料湿容重的变化.结果表明:各处理总产气量、累积总固体产气量与甲烷含量差异不显著;不同处理纵剖面各层物料湿容重,呈现上低下高的趋势,其中T3处理物料湿容重随高度的降低先增加后基本稳定,稳定在0.6 g/cm3左右,大于初始发酵物料湿容重0.58 g/cm3;T1、T2、T3剖面残留锂离子质量分数低于2 mg/kg的区域面积占比为2.32%、12.69%、20.66%,表明3个处理回流液淋滤存在着"回流液死区",EPS等值线图与物料残留锂离子等值线图相互印证,表明秸秆高固厌氧发酵中,回流液的淋滤在剖面上表现出非均态性特性.该研究为改善秸秆高固厌氧发酵回流液回流技术提供了科学依据.
    • 李刚; 崔燕平; 张浩; 李玲; 岳建芝; 焦有宙
    • 摘要: 为解决生物质灰渣利用和沼液排放引起的污染环境问题,以生物质灰渣为滤料采用自然渗滤对沼液进行了净化处理试验.结果表明:灰渣对沼液具有较好的净化能力,粒径是影响灰渣对沼液净化效果的重要因素,灰渣粒径越小净化效果越明显,相同质量灰渣粒径>3 mm时,渗滤速率为4.17 mL/s,出水COD为1 880 mg/L,出水TS为1.46 g/L,COD和TS去除率为58.71%和67.69%;而粒径<0.5 mm时,渗滤速率为0.46 mL/s,出水COD为221 mg/L,出水TS为0.61 g/L,COD和TS去除率达到94.07%和87.16%.净化柱的高径比直接影响沼液流通路径,以COD去除率作为评价指标时,为获得较好的沼液净化效果,不同粒径灰渣(<0.5、0.5~1、>1~1.5、>1.5~2、>2~3 mm)所采用净化柱的高径比应不小于1.34、2.3、2.68、5.01、10.66,此时对应出水COD值分别为236、276、305、315、342 mg/L,COD去除率分别达到94.82%、93.94%、93.3%、93.08%和92.49%,出水水质接近农田灌溉用水要求.不同粒径(<0.5、0.5~1.0、>1.0~1.5、>1.5~2.0、>2.0~3.0)灰渣对沼液的最大的过滤能力分别为9~10、10~11、8~9、4~5、3~4 mL/g.%In order to avoid environmental pollution caused by biomass ash piled up on the open air and digested slurry discharged directly,and explore the utilization way,biomass ash was used as filter material to clarify digested slurry in infiltration.The results show that biomass ash can be used as filter material to clarify digested slurry.Particle size is the major influence factor for the cleaning of digested slurry,and the small particles have the better cleaning effect than large particles due to their specific surface area and spatial structure.Under the same experimental conditions,when particle size is large than 3 mm,infiltration rate is 4.17 mL/s,COD (chemical oxygen demand) of clarified digested slurry is 1 880 mg/L,TS (total solid) content of clarified digested slurry is 1.46 g/L,and the removal rates of COD and TS in digested slurry are 58.71% and 67.69%,respectively.When particle size is less than 0.5 mm,infiltration rate is 0.46 mL/s,COD of clarified digested slurry is 221 mg/L and TS of clarified digested slurry is 0.61 g/L,and the removal rates of COD and TS in digested slurry are 94.07% and 87.16%,respectively.The ratio of height to diameter of clarification column not only affects the flow path of digested slurry,but also affects its clarifying effect.When COD removal ratio is used as evaluating indicator,in order to get better cleaning effect,the height-diameter ratio of clarification column is more than 1.34 when particle size of biomass ash is less than 0.5 mm,is not less than 2.3 when particle size ofbiomass ash is between 0.5 and 1 mm,is not less than 2.68 when particle size ofbiomass ash is between 1 and 1.5 mm,is not less than 5.01 when particle size of biomass ash is between 1.5 and 2 mm,and is not less than 10.662 when particle size ofbiomass ash is greater than 3 mm,the COD values of clarified digested slurry were 236,276,305,315 and 342 mg/L respectively,and the removal rates of COD were 94.82%,93.94%,93.3%,93.08% and 92.49%,respectively.The clarified digested slurry quality is close to agricultural irrigation water requirements.The clarifying capacity ofbiomass ash in different particle sizes is 9-10 mL/g when particle size of biomass ash is less than 0.5 mm,10-11 mL/g when particle size of biomass ash is between 0.5 and 1 mm,8-9 mL/g when particle size of biomass ash is between 1 and 1.5 mm,4-5 mL/g when particle size of biomass ash is between 1.5 and 2 mm,and 3-4 mL/g when particle size of biomass ash is greater than 3 mm,respectively.
    • 李刚; 崔燕平; 李玲; 岳建芝; 焦有宙
    • 摘要: 在对生物质灰渣特性进行分析的基础上以活性炭为对照,研究不同粒径灰渣对沼液的净化效果.结果表明:灰渣水浸液呈较强的碱性,pH值在8.35 ~9.78之阀.不同取样时间的样品中粒径分布不同,但主要分布在0.5 ~2 mm范围内,约占总质量的80%.生物质灰渣粒径大小对其容重、孔隙度和其它物质的吸附性能有较大影响,生物质灰渣的容重、通气孔隙度和总孔隙度随着粒径的增加而减小.生物质灰渣容重介于0.55 g·cm-3.(>3 mm) ~0.83 g·cm-3(<0.5 mm)之间,通气孔隙度介于28.76%(>3 mm) ~47.29%( <0.5 mm),总孔隙度介于36.52%(>3 mm) ~58.96%( <0.5 mm)之间.生物质灰渣对沼液具有较好的过滤净化效果,COD、TS的去除率分别达到87.35%和63.5%,沼液净化后的电导率和浊度比净化前分别降低了79.31%和52.95%.
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