日光温室番茄-西瓜轮作系统不同水氮处理氨挥发特征

为探究黄土高原地区日光温室果蔬栽培中氨挥发特征,在陕西省杨凌区选择当地典型的日光温室,设置4个不同的水氮处理,采用密闭式间歇抽气法监测番茄-西瓜轮作季的氨挥发特征.结果表明: 日光温室栽培土壤氮素转化快,施氮处理施肥后第1～2天氨挥发出现峰值,氨挥发峰值为0.26～2.02 kg N·hm^-2·d^-1,7 d左右各处理氨挥发通量相近;施氮处理间氨累积排放量无显著差异;相同施氮量条件下,降低灌溉量氨累积排放量两季平均增加了46.7%;不同种植季氨平均排放通量和累积排放量均表现为西瓜季高于番茄季,西瓜季高温促进了氨排放;土壤铵态氮含量、土壤孔隙含水量、0～5 cm地温和温室气温均对氨排放通量有极显著影响,而土壤pH值与氨挥发通量呈显著负相关关系.不同种植季氨挥发通量和累积排放量存在差异,降低施氮量可减少氨排放,相同施氮量条件下降低灌溉量增加了氨排放.     

土壤盐渍化对尿素与磷酸脲氨挥发的影响

氨挥发是肥料氮素损失的重要途径之一,肥料类型、土壤类型、肥料用量以及土壤全盐量均影响氨挥发损失率及挥发特征。本文采用通气法测定了磷酸脲和尿素两种肥料六个施肥量处理分别施入六个不同盐渍化程度（1.7、9.9、16.4、23.2、29.1、37.9 g/kg）的土壤后氨挥发累积状况和动力学特性,以及土壤氨挥发累积量与土壤电导值之间的相关性。结果表明：（1）在土壤总盐介于1.66 -37.9 g/kg的范围内,随着土壤含盐量增加,尿素与磷酸脲处理的氨挥发累积量显著增加;土壤含盐量对氨挥发速率有显著的促进作用。（2）各处理二次线性函数拟合的二项式系数a均为负值,表明：在不同盐渍化条件下肥料的挥发速率是随着时间增长而降低的;一次线性函数和Elovich 方程的斜率a随土壤含盐量增加而增大,表明：土壤盐渍化将加剧土壤的氨挥发速率。（3）土壤氨挥发累积量与电导值拟合结果符合logistic方程（︱R︱分别为0.9732,0.9815,0.965,0.9182,0.9817,0.9971︱R︱>r0.01=0.9172, n=6）,氨挥发累积量随土壤电导值呈“S”型增长。     

施用南荻生物炭对不同类型土壤氨挥发的影响

在洞庭湖区农田施用秸秆生物炭不仅能实现秸秆资源化利用,还可降低环境污染压力。本研究于2020年采用水稻盆栽试验,研究了不同南荻秸秆生物炭施用量对土壤氨挥发速率、累积氨挥发量、表面水pH值和NH₄⁺-N浓度的影响。供试土壤为第四纪红土发育的红黄泥和花岗岩发育的麻砂泥水稻土,设置6个南荻秸秆生物炭添加处理,即分别以土柱0～20 cm土壤重量的0%、1%、2%、4%、6%和8%比例添加生物炭,每盆施用复合肥200 kg N·hm^-2。结果表明: 施用生物炭导致两种土壤之间或不同生物炭处理之间的氨挥发速率和累积量均存在显著差异。麻砂泥施用生物炭处理在施肥后第2天出现氨挥发峰值,且较不施生物炭处理峰值降低了23.6%～53.4%;红黄泥氨挥发峰值出现在施肥后第7～13天,且其峰值随着生物炭添加量的增加而升高。整体上,麻砂泥土壤的氨挥发速率均高于红黄泥。麻砂泥土壤＜4%生物炭添加量能抑制土壤氨挥发速率及累积量,其中以2%处理降幅最大(46.9%),但生物炭添加对水稻生长前期表面水pH值的影响不显著;红黄泥土壤随着南荻生物炭用量的增加,表面水中pH值和NH₄⁺-N浓度增加,导致氨挥发速率及累积量增幅达1.3～10.5倍。回归分析显示,生物炭添加量是影响两种土壤氨挥发的关键因素。Elo-vich方程能较好地拟合两种土壤的氨挥发累积量随时间的变化动态,各施炭处理的相关系数均达极显著水平。总体上,对于偏中性的麻砂泥土壤,施用一定量的南荻生物炭对氨排放有一定的抑制作用,而对于酸性的红黄泥土壤,增施南荻生物炭会通过提高表面水的pH值和NH₄⁺-N浓度促进氨挥发,因此针对不同类型土壤施用南荻秸秆生物炭应注意选择适宜用量,以降低氮素损失。     

三江平原典型小叶章湿地土壤氨挥发特征及影响因素

采用通气法对三江平原典型草甸小叶章湿地和沼泽化草甸小叶章湿地土壤的氨挥发进行了原位测定,并对其主要影响因素进行了分析。结果表明,二者的氨挥发速率在生长季内的变化趋势基本一致,7月中旬前出现两次挥发高峰和一次低值,之后整体呈严格单调下降趋势,后者的氨挥发速率较高,平均为前者的1.35±0.53倍;二者累计氨挥发量的变化趋势也基本一致,7月中旬前增加迅速,且值比较接近;之后增加缓慢,但其值发生明显分异,表现为后者大于前者;生长季内,典型草甸小叶章湿地土壤的氨挥发总量为6.35 kg N.hm-2,而沼泽化草甸小叶章湿地则为6.87 kg N.hm-2,二者之比为1∶1.08;氮素物质基础不是影响二者氨挥发过程的重要限制因素,大气温度及其所引起的其它温度波动是影响氨挥发速率变化的重要因素;降水及土壤水分波动与散失是引起氨挥发速率局部波动的重要原因;土壤pH和质地是导致氨挥发速率普遍较低的根本原因;而各种因素综合作用的结果则是引起二者氨挥发速率和氨挥发量变化及差异的主要原因。     

新疆灰漠土区不同肥料配比土壤氨挥发原位监测

在17a的新疆国家灰漠土土壤肥力与肥料效益长期定位试验区,采用通气法对春小麦种植体系8种处理,即(1)对照(种植、不施肥,CK)、(2)施氮肥(N)、(3)施氮磷肥(NP)、(4)施氮钾肥(NK)、(5)施氮磷钾肥(NPK)、(6)施氮磷钾肥+有机肥增量(NPKM1)、(7)施氮磷钾化肥+有机肥常量(NPKM2)、(8)施氮磷钾化肥+秸秆还田(NPKS)的氨挥发损失与不同肥料配比、长期不同施肥土壤特性变化之间关系进行研究.结果表明:(1)在当地春小麦种植典型施肥模式,即"基肥撒施后机械翻耕,追肥撒施后灌水"下,在施氮量为84.97～241.5 kg · hm-2的条件下,不同处理基肥氨挥发累积量为0.194～2.236 kg N · hm-2之间;追肥氨挥发累积量在0.078～0.210 kg N · hm-2之间,远低于基肥氨挥发量;基肥和追肥氨挥发损失氮素之和占总施氮量的0.39%～1.23%.(2)相同施氮量241.5 kg · hm-2的N、NP、NK、NPK 4个处理,氨挥发累积量分别为1.017、0.944、1.988、2.437 kg N · hm-2,氨挥发量与不同处理土壤速效钾含量相关性达显著水平(r=0.951, P<0.05,n=4).(3)施氮量分别为151.8、84.9、216.7 kg · hm-2有机肥处理NPKM1、NPKM2、NPKS的氨挥发累积量分别为1.404、1.041、1.583 kg N · hm-2,氨挥发量与氮肥使用量呈显著正相关(r=0.581,P<0.05,n=18).以上结果表明,氨挥发不是新疆灰漠土长期定位试验春小麦体系氮肥损失的主要途径;不同肥料配比和长期不同肥料配比造成土壤特性的变化是7种施氮肥处理氨挥发差异的主要原因.     

不同施肥与灌水量对槟榔土壤氨挥发的影响

利用通气法田间原位试验,研究了不同施肥模式、灌溉量对槟榔土壤氨挥发速率和挥发量的影响。结果表明：槟榔恢复期和出花期追肥灌水后,不同施肥处理均在第3天出现氨挥发速率峰值（0.50-3.42 kg.hm-2.d-1）,而后迅速下降并进入低挥发阶段。出花期氨挥发速率峰值（1.50-4.42 kg.hm-2.d-1）比恢复期氨挥发速率峰值明显高。灌水量小(300 m3. hm-2)的氨挥发率和总量比灌水量大(600 m3. hm-2)的明显减小。在同一氮水平下,有机质含量较低的氨挥发率较高。在同一有机质含量条件,氨挥发率随着N肥含量增加而升高。与单施N肥处理相比,有机肥与N肥配施可明显减少氨挥发速率和总量,可减少氮损失。     

城市河道底泥污染生物修复技术研究

城市河道受污染底泥对水体产生大的二次污染,为有效的控制底泥污染物的释放和开发有效的水体治理技术方法,本研究利用人工模拟河道在连续流条件下,对河道污染底泥的生物修复及其对水体生物修复的影响进行了试验研究。研究结果表明:采用曝气增氧和投加底泥生物修复制剂联合处理的方式能达到好的底泥生物修复效果,能有效的提高底泥的生物降解活性(G值),削减底泥氮磷污染物的释放量,底泥G值与底泥氮、磷污染物释放量呈显著负相关性:单独采用曝气增氧和投加土著微生物制剂联合实施的生物修复方法对河道污染水体均具有良好的修复效果,但底泥的生物修复将对河道水体生物修复的效果产生大的影响。底泥生物修复后,对水体进行生物修复的处理效果更加显著,在相同实验条件下,对水体COD、氨氮的最大去除率由65.0%和16.30%提高到72.0%和41.0%,水体生物修复的周期由13 d缩短为6 d。     

不同尿素配施处理下土壤氨挥发特性

采用室内恒温模拟培养方法,以单施尿素处理为对照,研究了减量尿素配施玉米秸秆、配施脲酶抑制剂NBPT和硝化抑制剂DMPP组合、配施玉米秸秆+抑制剂组合等处理对棕壤氨挥发特性的影响,分析了不同处理土壤的p H、铵态氮、硝态氮含量与氨挥发速率的相关性。结果表明:单施尿素处理氨挥发速率在第3天即达到峰值;减量尿素配施玉米秸秆处理的氨挥发速率峰值出现时间延迟至施肥后第5天;在配施玉米秸秆的土壤中添加抑制剂组合后,氨挥发速率峰值延迟至第11天出现。与单施尿素相比,减量尿素配施玉米秸秆并添加抑制剂组合可显著降低氨挥发速率峰值74.27%,培养18 d可减少氨挥发累积损失量43.96%。不同处理的氨挥发速率与土壤的铵态氮浓度、p H呈正相关,与土壤的硝态氮浓度呈负相关。配施玉米秸秆并添加抑制剂组合的土壤中铵态氮浓度达到高峰后可长时间保持较高水平(350 mg·kg-1),并可有效减少硝态氮的浓度。     

氮添加对沙质草地氨挥发及硝态氮淋溶的影响

采用密闭室法和离子交换树脂袋法,研究了科尔沁沙质草地不同处理(水添加、氮添加、水氮添加)氧挥发的损失量和硝态氮的淋溶量.结果表明:氮添加处理和水氮添加处理显著促进了氨挥发(P＜0.05),最大氨挥发速率显著高于对照;氮添加处理和水氮添加处理的氨挥发累积量为111.80和148.64 mg·m-2,分别占氮添加量的1.1％和1.5％;水氮同时添加条件下,氨挥发累计量显著高于氨添加处理(P＜0.05),水添加处理和对照相比没有显著差异(P＞0.05);水氮添加处理显著增加了土壤深度20 cm处的硝态氮淋溶量(P＜0.05),氮添加处理和水氮添加处理的硝态氮淋溶量分别是对照的1.96和4.22倍,然而在土壤深度40 cm处各处理硝态氮淋溶量差异不显著(P＞0.05);可见,氮添加和水氮添加均促进了土壤的氧挥发,对硝态氮的淋溶没有显著影响.     

不同施肥方式对土壤氨挥发和氧化亚氮排放的影响

采用密闭室间歇通气法和静态箱法对不同施肥方式(撒施后翻耕、条施后覆土、撒施后灌水)下的土壤氨挥发和氧化亚氮排放进行了研究.结果表明:不同施肥方式显著影响了土壤中的氨挥发和氧化亚氮排放.撒施后灌水处理明显促进了氨挥发,其最大氨挥发速率明显高于其它处理,氨挥发累计达2.465 kg N·hm-2.不同施肥方式下氧化亚氮排放通量存在显著差异(P《0.05),且峰值出现时间也不同.施肥后第2天,撒施后灌水处理达到峰值,为193.66 μg·m-2·h-1,而条施后覆土处理在施肥后第5天才出现峰值,为51.13 μg·m-2·h-1,且其排放峰值在3种施肥方式中最低.撒施后灌水处理的氧化亚氮累积净排放量达121.55 g N·hm-2,显著大于撒施后翻耕和条施后覆土处理.撒施后翻耕和条施后覆土处理能有效抑制氨挥发和氧化亚氮排放损失,是较为合理的施肥方式.     

硝化细菌群的富集及其去除城镇寡营养河道中氨氮污染的应用

[背景]随着工农业的发展,污水排放导致的氨氮超标逐渐成为水体污染的重要因素,脱氮已成为人们研究的重点.目前脱氮方法主要集中于硝化细菌的硝化作用,其将氨氮转化为硝酸盐氮,从而减少水体中氨氮的污染.由于工业废水和农业污水中的有机物含量较高,而且异养硝化细菌具有生长较快等优势,因此对异养菌的研究多于自养菌.然而现有的异养硝化...     

Remediation of Urban River Water by Pontederia Cordata Combined with Artificial Aeration: Organic Matter and Nutrients Removal and Root-Adhered Bacterial Communities

Macrophyte combined with artificial aeration is a promising in situ remediation approach for urban rivers polluted with nutrients and organic matter. However, seasonal variations and aeration effects on phytoremediation performance and root-adhered microbial communities are still unclear. In this study, Pontederia cordata was used to treat polluted urban river water under various aeration intensities. Results showed that the highest removal efficiencies of chemical oxygen demand (COD_Cr) and total nitrogen (TN) were attained under aeration of 30 L min^?1 in spring and summer and 15 L min^?1 in autumn, while total phosphorus (TP) removal reached maximum with aeration of 15 L min^?1 in all seasons. Moderate aeration was beneficial for increasing the diversity of root-adhered bacteria communities, and the shift of bacterial community structure was more pronounced in spring and autumn with varying aeration intensity. The dual effect, i.e. turbulence and dissolved oxygen (DO), of aeration on the removal of COD_Cr and TN prevailed over the individual effect of DO, while DO was the most influential factor for TP removal and the root-adhered bacterial community diversity. P. cordata combined with 15 L min^?1 aeration was deemed to be the best condition tested in this study.     

Nitrogen removal from polluted river by enhanced floating bed grown canna

Floating beds of canna can remove nitrogen from polluted river water, but the removal efficiency is not very high in a short time, so some enhanced methods must be used to improve nitrogen removal efficiency by the system. Immobilized denitrifying bacteria and aeration were added into the canna floating bed. The experimental results showed that these enhancements substantially improved the nitrogen removal efficiency of the floating beds. With the enhancements, total nitrogen removal was 72.1%, ammonia nitrogen oxidation was 100%, nitrate nitrogen removal was 75.8%, nitrite nitrogen removal was 95.9%, and COD removal was 94.6% in 5 days. Without the enhancements, the canna floating bed system removed only 50.4% of the total nitrogen, 22.4% of the nitrate nitrogen, 5.3% of the nitrite nitrogen and 39.9% of the COD, respectively, in 5 days, but did accomplish 100% oxidation of the ammonia nitrogen. The experimental results provide an improved method for the treatment of polluted river water.     

新型脱氮微生物与水体脱氮新工艺研究进展

氨氮是河流等淡水资源有机污染的主要污染指标之一。生物脱氮具有低成本、高效、无二次污染和易操作等优点,极具发展前景。重点概述了水体净化系统中新型脱氮微生物的种类及研究进展,介绍了厌氧氨氧化、短程硝化-反硝化和分段进水生物脱氮等高效节能新工艺的工艺原理。     

Microbial nitrogen removal of ammonia wastewater in poly (butylenes succinate)-based constructed wetland: effect of dissolved oxygen

Constructed wetland (CW) is popular in wastewater treatment for its prominent advantage of low construction and operation cost. However, the nitrogen removal in conventional CW is usually limited by the low dissolved oxygen (DO) and insufficient electron donor. This paper investigated the nitrogen removal performance and mechanisms in the poly (butylenes succinate)-based CW (PBS-CW) while treating ammonia wastewater under different DO levels. The average DO contents in limited-aeration and full-aeration phases were 1.68 mg L⁻¹ and 5.71 mg L⁻¹, respectively. Results indicated that, with the ammonia nitrogen loading rate of 25 g N m⁻³ day⁻¹, total nitrogen removal ratios in the PBS-CW under the limited-aeration and full-aeration phases were 72% and 99%, respectively. Combined analyses revealed that simultaneous nitrification and denitrification (SND) via nitrite/nitrate were the main microbial nitrogen removal pathways in the aeration phase of the PBS-CW (> 89%). The microbial carrier of biodegradable material was believed to play a significant role in prompting SND performance while dealing with low C/N wastewater. Due to the coexistence of micro-anaerobic zone and carbon supply inside the coated biofilm, the high DO level in the PBS-CW increased the abundance of the nitrifying bacteria (amoA and nxrA), denitrifying bacteria (narG, nirK, nirS, and nosZ), and even anammox bacteria (anammox 16s rRNA). These features are beneficial to many microbial processes which require the simultaneous aerobic, anoxic, and anaerobic environment.

     

Enhanced biological nitrogen removal and N<Subscript>2</Subscript>O emission characteristics of the intermittent aeration activated sludge process

Enhanced biological nitrogen removal processes are necessarily required to cope with more stringent wastewater discharging regulations, especially for wastewater with low level of organic carbon to nitrogen ratios. The intermittent aeration activated sludge process has been received comprehensive attention over the past decades, due to its excellent performance in nitrogen removal and remarkable reduction of energy consumption. Recent advances for this technology was reviewed from aspects of characteristics of system, factors affecting nitrogen removal, nitrous oxide (N₂O) emission and its control, and application of the technology and its operation control. Finally, future development was proposed. In the intermittent aeration activated sludge process, aeration duration should be controlled for adequate nitrification and non-aeration duration should be adequate for complete denitrification, and these would benefit both nitrogen removal and N₂O mitigation. The step feed strategy could be applied to enhance the better utilization of influent organic carbon for nitrogen removal. Dissolved oxygen (DO) and aerobic duration both affected nitrogen removal in particular that via nitrite in the intermittent aeration process. Nitrite should be removed efficiently to avoid a high N₂O emission under both anoxic and aerobic conditions. Intermittent aeration activated sludge process has been applied in the treatment of various wastewaters, such as municipal wastewater, swine wastewater, anaerobic effluents and landfill leachate. For practical application, DO, pH and oxidation–reduction potential could be used as indices for controlling nitrogen removal and N₂O mitigation. Microbial ecology in the intermittent aeration activated sludge process should be specifically focused in future studies.     

Effects of temperature on simultaneous nitrification and denitrification via nitrite in a sequencing batch biofilm reactor

A laboratory scale experiment was described in this paper to enhance biological nitrogen removal by simultaneous nitrification and denitrification (SND) via nitrite with a sequencing batch biofilm reactor (SBBR). Under conditions of total nitrogen (TN) about 30 mg/L and pH ranged 7.15–7.62, synthetic wastewater was cyclically operated within the reactor for 110 days. Optimal operation conditions were established to obtain consistently high TN removal rate and nitrite accumulation ratio, which included an optimal temperature of 31 °C and an aeration time of 5 h under the air flow of 50 L/h. Stable nitrite accumulation could be realized under different temperatures and the nitrite accumulation ratio increased with an increase of temperature from 15 to 35 °C. The highest TN removal rate (91.9%) was at 31 °C with DO ranged 3–4 mg/L. Process control could be achieved by observing changes in DO and pH to judge the end-point of oxidation of ammonia and SND.     

Novel microbial nitrogen removal processes

The present-day wastewater treatment practices can be significantly improved through the introduction of new microbial treatment technologies. Recently, several new processes for nitrogen removal have been developed. These new nitrogen removal technologies provide practicable options for treating nitrogen-laden wastewaters. The new processes are based on partial nitrification of ammonium to nitrite combined with anaerobic ammonium oxidation. These processes include the single reactor system for high ammonia removal over nitrite (SHARON) process, which involves part conversion of ammonium to nitrite; the anaerobic ammonium oxidation (ANAMMOX) process, which involves anaerobic ammonium oxidation; and the completely autographic nitrogen removal over nitrite (CANON) process, which involves nitrogen removal within one reactor under oxygen-limited conditions. These new processes target the removal of nitrogen from wastewaters containing significant quantities of ammonium.     

Effect of COD/N ratio and salinity on the performance of sequencing batch reactors

The effects of COD/N ratio (3-6) and salt concentration (0.5-2%) on organics and nitrogen removal efficiencies in three bench top sequencing batch reactors (SBRs) with synthetic wastewater and one SBR with fish market wastewater were investigated under different operating schedules. The solids retention time (SRT, 20-100 days) and aeration time (4-10h) was also varied to monitor the performance. For synthetic wastewater, chemical oxygen demand (COD) removal efficiencies were consistently greater than 95%, irrespective of changes in COD/N ratio, aeration time and salt concentrations. Increasing the salt concentrations decreased the nitrification efficiency, while high COD/N ratio's favored better nitrogen removal (>90%). The treatment of real saline wastewater ( approximately 3.2%) from a fish market showed high COD (>80%) and nitrogen (>40%) removal efficiencies despite high loading rate and COD/N fluctuations, which is due to the acclimatization of the biomass within the SBR.     

Nitrification, denitrification, and dechlorination in bleached kraft pulp mill wastewater

This study deals with combining the biologi cal removal of organic halogens with the removal of nitrogen from bleached kraft pulp mill wastewater in fluidized-bed reactors under nitrifying and denitrifying conditions. Untreated and biotreated bleached kraft pulp mill wastewaters had no detrimental effect on nitrification or denitrification. The nitrifying biofilm reactor, pregrown on synthetic inorganic feed with ammonia, removed without a lag phase adsorbable organic halogens [7.2 mg Cl (g biomass volatile solids)⁻¹day⁻¹] from bleached kraft pulp mill wastewater and selected chlorophenols from synthetic wastewater. Electron microscopical examination of the biofilm showed that bacteria, morphologically similar to the nitrifying species Nitrosomonas or Nitrobacter, and Nitrosospira were dominant. The denitrifying fluidized-bed reactor, pregrown on nitrate and methanol, denitrified without a lag phase bleached kraft pulp mill wastewater. Under denitrifying conditions, 35% of the total organic carbon content of untreated bleached kraft pulp mill waste water was removed. The reducing power delivered by untreated bleached kraft pulp mill wastewater for denitrification was 2 mmol electrons/mmol carbon mineralized. Dechlorination under denitrifying conditions was negligible. Received: 21 November 1996 / Received revision: 27 January 1997 / Accepted: 1 February 1997