控释掺混肥对麦玉轮作体系作物产量和温室气体排放的影响

为探究控释掺混肥一次性施肥对华北平原麦玉（冬小麦和夏玉米）轮作体系作物产量和温室气体排放的影响,于2020~2022年在德州市现代农业科技园区开展田间试验.冬小麦和夏玉米均设不施氮对照（CK）、农户习惯施氮（FFP）、优化施氮（OPT）、CRU1（包膜尿素与普通尿素在冬小麦和夏玉米上的掺混比例分别为5∶5和3∶7）、CRU2（包膜尿素与普通尿素在冬小麦和夏玉米上的掺混比例分别为7∶3和5∶5）共5个处理.对比分析了不同处理的作物产量、氮肥利用效率、施肥经济效益和温室气体排放的差异.结果表明,施氮可显著提高麦玉轮作系统单季和周年作物产量（P<0.05）.与FFP相比,CRU1和CRU2处理的夏玉米、冬小麦和周年产量分别提高了0.4%~5.6%、-5.4%~4.1%和-1.1%~3.9%（P>0.05）;氮肥吸收利用率、氮肥农学利用率和氮肥偏生产力分别提高了-8.6%~43.4%、2.05~6.24 kg·kg^-1和4.24~10.13 kg·kg^-1;周年净收益提高了0.2%~6.3%.施氮显著增加了麦玉轮作体系的土壤N₂O和CO₂的周年排放（P<0.05）,但对CH₄周年排放没有影响（第1年FFP处理除外）.CRU1和CRU2处理的土壤N₂O周年排放总量较FFP处理显著降低了23.4%~30.2%（P<0.05）.施氮显著增加了麦玉轮作体系的周年全球增温潜势（GWP）（P<0.05）,但各施氮处理通过提高作物产量降低了温室气体排放强度.与FFP相比,CRU1和CRU2处理的周年GWP降低了9.6%~11.5%（P<0.05）,周年温室气体排放强度（GHGI）降低了11.2%~13.8%（P>0.05）.综上所述,一次性减量施用控释掺混肥在减少氮肥和人工投入、提高作物产量、经济效益和降低温室气体排放方面具有积极作用,是促进华北平原粮食作物清洁生产的有效氮肥管理措施.     

Controlling various contaminants in wastewater effluent through membranes and engineered wetland

For effective wastewater reclamation and water recovery, the treatment of natural and effluent organic matters (NOM and EfOM), toxic anions, and micropollutants was considered in this work. Two different NOM (humic acid of the Suwannee River, and NOM of US and Youngsan River, Korea), and one EfOM from the Damyang wastewater treatment plant, Korea, were selected for investigating the removal efficiencies of tight nanofiltration (NF) and ultrafiltration (UF) membranes with different properties. Nitrate, bromate, and perchlorate were selected as target toxic anions due to their well known high toxicities. Tri-(2-chloroethyl)-phosphate (TCEP), oxybenzone, and caffeine, due to their different K _ow and pK _a values, were selected as target micropollutants. As expected, the NF membranes provided high removal efficiencies in terms of all the tested contaminants, and the UF membrane provided fairly high removal efficiencies for anions (except for nitrate) and the relatively hydrophobic micropollutant, oxybenzon. Through the wetlands, nitrate was successfully removed. Therefore, a fair process of combining membranes with an engineered wetland could be proposed for sustainable wastewater reclamation and optimum control of contaminats.     

荷电纳滤膜研究进展

根据所带电荷性质不同,荷电纳滤膜可分为荷正电纳滤膜、荷负电纳滤膜和荷电镶嵌膜。所带电荷不同,其分离模型也不同,荷正（负）电纳滤膜的分离模型有Donnan模型、固定电荷模型、空间电荷模型、静电位阻模型和杂化模型等。荷电镶嵌膜主要通过离子交换进行分离。因此,荷电纳滤膜的分离具有较高的选择性。目前,国内外制作荷电纳滤膜的方法主要有L—S法、表面改性法、共混法和复合法几类,其中表面改性是最常用的方法。     

动、静态超滤处理碱法草浆黑液的超滤膜特性比较

通过静、动态试验,考察了不同截留分子量的PES、PEK、SPES、SPK、PAN等5种超滤膜处理碱法草浆黑液的超滤特性结果表明,静态接触条件下,PEK膜受黑液组份的污染程度最重,PAN、SPES及SPK膜次之,PES膜的污染程度最轻;PAN膜不适宜于碱性黑液的处理;荷负电性较高的康化类膜及低截留分子量的超滤膜具有较好的黑液超滤特性;动态试验膜的超滤特性优于静态试验．本研究结果为超滤技术在碱法草浆黑液处理中的应用提供了基础性资料     

卷式超滤膜在蓝藻收集中的应用

利用微孔滤布-卷式超滤膜组合工艺,构建蓝藻收集中试系统,用于处理高藻期富营养化水体。考察了高藻期该工艺的蓝藻收集效率、膜通量变化及膜污染状况。结果表明,该组合工艺在进水泵频率40 Hz,进水压力0.2 MPa的条件下,定期排蓝藻浓缩液实验和蓝藻连续浓缩实验的蓝藻截留率均能达到95%以上;6 d后定期排蓝藻浓缩液实验最低...     

Enhanced sorption of perfluorooctane sulfonate (PFOS) on carbon nanotube-filled electrospun nanofibrous membranes

Multi-walled carbon nanotube-filled electrospun nanofibrous membranes (MWCNT-ENFMs) were prepared by electrospinning. The addition of MWCNTs (0.5 wt.% vs. ENFMs) doubled the specific surface area and tensile strength of the ENFMs. The MWCNT-ENFMs were used to adsorb perfluorooctane sulfonate (PFOS) in aqueous solutions. The sorption kinetics results showed that the sorption rate of PFOS onto the MWCNT-ENFMs was much higher than the sorption rate of PFOS onto the pure ENFMs control, and the pseudo-second-order model (PSOM) described the sorption kinetics well. The sorption isotherms indicated that the sorption capacity of the MWCNT-ENFMs for PFOS (16.29 ± 0.26 μmol g⁻¹) increased approximately 18 times, compared with the pure ENFMs (0.92 ± 0.06 μmol g⁻¹). Moreover, the solution pH significantly affected the sorption efficiency and sorption mechanism. The MWCNT-ENFMs were negatively charged from pH 2.0–10.0, but the electrostatic repulsion between the MWCNT-ENFMs and PFOS was overcome by the hydrophobic interactions between PFOS and the MWCNTs or nanofibers. The strong hydrophobic interactions between PFOS and the MWCNTs played a dominant role in the sorption process. For the pure ENFMs, the electrostatic repulsion was conquered by the hydrophobic interactions between PFOS and the nanofibers at pH > 3.1. In addition to the hydrophobic interactions, an electrostatic attraction between PFOS and the pure ENFMs was involved in the sorption process at pH < 3.1.     

原油对纳米SiO2/聚偏氟乙烯离子膜的污染及清洗技术研究

聚偏氟乙烯(PVDF)膜的疏水性限制了其在水处理领域的应用.采用纳米SiO2/PVDF离子膜电渗析对含原油高矿化度污水进行膜污染试验.结果表明,纳米SiO2/PVDF离子膜抗油珠污染的能力较强于PVDF膜.乳化油珠在电场的作用下向阴离子膜表面迁移,并在阴离子膜表面浓集、聚并,形成油膜,堵塞离子通道,少量原油以憎水膜的形式覆盖于活性基团上.扫描电镜和能谱分析表明,膜面有机污染物主要是石油类污染物,无机污染物主要是CaCO3等无机物污垢.原油污染的纳米Si02/PVDF离子膜的较佳清洗方法为碱-表面活性剂法.     

Effect of synthesis parameters on single gas permeation through T-type zeolite membranes

In this research, nanoporous zeolite T membranes were synthesized at three levels of synthesis temperature: 100, 120 and 140 °C and synthesis time: 15, 30 and 50 h and characterized by gas permeation. Effects of synthesis parameters on CO₂ and CH₄ permeances and CO₂/CH₄ ideal separation factors were studied. All experiments were conducted at 1 bar feed pressure and 30 °C module temperature. Normally, it is anticipated that increasing synthesis temperature and synthesis time increase gas permeances and consequently decrease ideal separation factor. This prediction was not observed in the case of synthesis temperature increase from 100 to 120 °C as well as synthesis time increase from 15 to 30 h, due to the dual effect of increasing synthesis temperature and synthesis time on gas permeances and ideal separation factor. More zeolites are deposited and larger crystals are formed at higher synthesis temperatures and times. Forming the larger crystals accelerates the rate of zeolite layer integration, which is responsible for gas separation, in one hand and reduces the density of deposited zeolite layer on the support, due to the formation of more voids, on the other hand. In terms of maximizing the CO₂/CH₄ ideal separation factor, medium synthesis temperature and synthesis time (120 °C and 30 h) can be selected, however, maximum gas permeances are obtained at low levels of synthesis temperature and time (100 °C and 15 h). According to the ranges of gas permeances (10⁻¹¹ to 10⁻⁶ mol/m² s Pa) and CO₂/CH₄ ideal separation factors (1.4–70.3), it is concluded that the zeolite T membranes synthesized at optimum conditions can be employed for membrane separation of CO₂/CH₄ mixtures.     

用盐桥支撑双分子层脂膜模拟研究锌离子跨细胞膜输运

采用盐桥支撑技术制备镶嵌胆固醇的双分子层卵磷脂(脑磷脂)膜,用以模拟细胞膜.用正辛烷做溶剂,对不同卵磷脂(脑磷脂)与胆固醇配比进行制膜,膜的稳定性均超过100h.实验发现,纯脂质体不能输运重金属离子,胆固醇能输运重金属离子.胆固醇与重金属离子之间存在吸附作用,无化学反应.采用电化学工作站对双分子层脂膜的稳定性、离子通透性、双层膜中胆固醇对离子通透性的影响等进行了研究,并利用实验制备的双分子层脂膜模拟研究锌离子跨细胞膜的输运过程,建立了锌离子跨细胞膜的吸附-扩散模型,该模型计算值与实验值基本吻合.