• <tr id="yyy80"></tr>
  • <sup id="yyy80"></sup>
  • <tfoot id="yyy80"><noscript id="yyy80"></noscript></tfoot>
  • 99热精品在线国产_美女午夜性视频免费_国产精品国产高清国产av_av欧美777_自拍偷自拍亚洲精品老妇_亚洲熟女精品中文字幕_www日本黄色视频网_国产精品野战在线观看 ?

    Fate of nitrogen in subsurface in filtration system for treating secondary ef fluent

    2017-11-20 05:25:13YinghuLiHiLiXinyngXuSiyoXioSiqiWngShucongXu
    Water Science and Engineering 2017年3期
    關(guān)鍵詞:對(duì)角線意見專家

    Ying-hu Li,Hi-o Li,*,Xin-yng Xu,Si-yo Xio,Si-qi Wng,Shu-cong Xu

    aSchool of Resources and Civil Engineering,Northeastern University,Shenyang 110004,China bSchool of Material Science and Engineering,Shandong University,Ji'nan 250002,China

    Received 28 December 2016;accepted 23 March 2017 Available online 13 October 2017

    Fate of nitrogen in subsurface in filtration system for treating secondary ef fluent

    Ying-hua Lia,Hai-bo Lia,*,Xin-yang Xua,Si-yao Xiaoa,Si-qi Wanga,Shu-cong Xub

    aSchool of Resources and Civil Engineering,Northeastern University,Shenyang 110004,ChinabSchool of Material Science and Engineering,Shandong University,Ji'nan 250002,China

    Received 28 December 2016;accepted 23 March 2017 Available online 13 October 2017

    The concentration of total nitrogen(TN)is reported to vary between 20 and 35 mg/L in domestic wastewater.In raw wastewater,ammonia nitrogenis the main nitrogen form,accounting for 70%-82%of the TN concentration.Organic nitrogen,nitrite nitrogenand nitrate nitrogenare present as well.For years,due to the lack of regulatory limits on nitrogen concentration in surface waters,nitrogen from secondary ef fluent has posed a signi ficant threat to the health of aquatic ecosystems.Researchers have made substantial efforts to reduce the nitrogen concentration in secondary ef fluent.As a kind of advanced wastewater treatment technology,the subsurface in filtration(SI)system has been widely used,owing to its advantages,which include low operation cost,easy maintenance,and low energy consumption.This review discusses the fate of various forms of nitrogen in SI treatment,including organic nitrogen,Major biological processes involved in nitrogen removal and the main factors in fluencing its transformation are suggested.Finally,it is shown that ammoni fication followed by nitri fication-denitri fication plays a major role in nitrogen removal.Further research needs to focus on the emission characteristics of gaseous nitrogen(generated from the nitri fication,denitri fication,and completely autotrophic nitrogen-removal over nitrite(CANON)processes)with respect to their greenhouse effects.

    ?2017 Hohai University.Production and hosting by Elsevier B.V.This is an open access article under the CC BY-NC-ND license(http://creativecommons.org/licenses/by-nc-nd/4.0/).

    Wastewater treatment;Natural treatment technology;Subsurface in filtration;Nitrogen;Biological process

    1.Introduction

    In China,thousands of scientists and engineers have made substantial efforts in water pollution control.A number of technologies and procedures for municipal wastewater treatment have been developed and applied(Yuan and He,2015).Of those,the activated sludge technology and bio film treatment method are most commonly used for centralized wastewater treatment in big cities.

    However,due to the lack of legal restraints,conventional sewage treatment processes,such as activated sludge and trickling filters,are known to be less ef ficient for nitrogen removal,compared with the removal ef ficiency of organic matter.Therefore,after a secondary treatment,wastewater discharge can be a major source of nutrients that cause eutrophication in lakes and rivers.Various physio-chemical processes such as filtration or adsorption have been employed for nutrient removal,but such processes are often costly and dif ficult to maintain(Bali et al.,2010;Curia et al.,2011).In an increasingly restrictive economic climate,especially in rural areas,capital resources for implementation and operation of such wastewater treatment infrastructure and facilities are limited.Therefore,natural treatment systems,such as wetlands,oxidation ponds,and subsurface in filtration(SI)systems,have emerged as appropriate alternatives.Compared with conventional systems,natural systems require less energy and less skilled labor(Sun et al.,2006).In SI,a kind of natural treatment system,wastewater is first treated by conventional physicochemical and/or biological treatment and then allowed to in filtrate through the aerated unsaturated zone,where it gets puri fied through processes such as filtration,adsorption,chemical processes,and biodegradation(Ji et al.,2012).SI systems have the advantages of low construction and operation costs,no aeration,low energy consumption,the ability to utilize fertilizer resources in wastewater,and simultaneous wastewater treatment and ecological service.Since 1990,large-scale SI systems have been developed in many countries to treat municipal wastewater(Phuong et al.,2014).Some demonstration treatment systems have also been established.Table 1 summarizes the treatment ef ficiency of SI systems.

    In SI systems,the wastewater moves upwards slowly under capillary action,passing through the aerobic distribution layer,then the unsaturated and saturated substrate layers.During this movement,it is generally accepted that organic molecules are broken down by the microbiota through fermentation and/or respiration,and mineralized as a source of energy or assimilated into biomass(Qin et al.,2014),while the main removal mechanisms of phosphorus are short-term or long-term storage in soil/sediments and(to a lesser extent)plant uptake.More controversially,nitrogen can be removed through ammonia volatilization,soil adsorption,nitri fication-denitri fication,and anaerobic ammonium oxidation(Anammox).This paper reviews the forms and fates of nitrogen in secondary ef fluent,as well as the biological processes involved in nitrogen removal via SI treatment.

    2.Nitrogen forms and levels in secondary ef fluent

    Nitrogen levels in secondary ef fluent change with local lifestyle,local economic level,secondary treatment methods,and other factors.Generally,the secondary ef fluent from a municipal wastewater treatment plant is characterized by a low carbon-to-nitrogen ratio in China(Wang et al.,2015).Kim et al.(2011)suggested that 2mg/L is the lowest concentration for total nitrogen(TN),which can be removed from a treated wetland without additional chemical and mechanical treatments.If TN concentration in the in flow does not exceed this limit,the treatment system(e.g.,wetland and SI)may not remove TN effectively.Li et al.(2013)reported that ammonia nitrogenwas a dominating form of nitrogen in secondary ef fluent,accounting for 85.1%±1.2%of TN.The concentration of nitrate nitrogenwas only 0.1-0.2 mg/L,less than 1%of TN.Meanwhile,in the ef fluent of the SI system,theconcentration increased to 1.8-3.2 mg/L,accounting for 33.5%±2.3%of TN.On the other hand, theconcentration decreased to 2.0-3.7 mg/L,accounting for 64.4%±1.9%of TN.In the research presented by Boonchai and Seo(2015),TN mostly occurred in the form ofin secondary ef fluent from the Jinhae Sewage Treatment Plant in Changwon City,South Korea,with a concentration of 18.8 mg/L.Consistent with this conclusion,Jin et al.(2015)suggested that,in secondary ef fluent,nitrogen is mainly composed of inorganic nitrogen,i.e.,accounted for 65%of the TN in their study.The concentration of dissolved organic nitrogen changed little via secondary treatment,accounting for 15%-20%of TN.In raw water,the proportions of dissolved nitrogen and particulate nitrogen existed almost at the same level,with concentrations of 39.2 and 41.2 mg/L,respectively.Dissolved nitrogen was mainly composed of inorganic nitrogen,at a proportion of 93.2%(36.6 mg/L),but the concentration of dissolved organic nitrogen was relatively low(2.7mg/L).For particulate nitrogen,organic nitrogen was the main form(96.2%).Dissolved organic nitrogen was signi ficantly removed by anaerobic microbial degradation in the anaerobic and anoxic compartments of the secondary treatment,whereas a slight increase of dissolved organic nitrogen concentrations was observed in the aerobic compartment.

    3.Nitrogen transformation process in SI systems

    Generally speaking,nitrogen in secondary ef fluent goes into SI systems in the form ofand organic nitrogen(ON),along with a small amount of nitrate and nitrite.After complex reactions in the system,as shown in Fig.1,there may emerge several gaseous forms of nitrogen,e.g.,N2,NO,and N2O.

    Table 1 Treatment ef ficiency of SI systems.

    Fig.1.Nitrogen transformation in SI system.

    3.1.Organic nitrogen removal

    In SI systems,organic nitrogen is mainly removed by reactions of sedimentation, filtration,and adsorption of soil.The remaining organic nitrogen hydrolyzes into soluble amino acids,and the assimilation of animals,plants,and microorganisms may utilize some of the solid organic nitrogen directly.Water-soluble organic nitrogen is transformed into ammonium by ammoni fiers.It then enters the nitrogen cycle,or is partly adsorbed by microorganisms(Heil et al.,2015).

    3.2.Ammonia nitrogen removal

    There are two methods of ammonia nitrogen removal:(1)Adsorption followed by biological oxidation:Because the soil comprises electronegative colloids,that exists in the form of a positive charge is first adsorbed by soil colloids and soil particles.Then,absorbed by soil particles is dif ficult to move(Pan and Yu,2015).The cation exchange capacity(CEC)of soil determines the adsorption capacity of.At the same time,nitri fication,temperature,humidity,and pH can also affect the adsorption capacity ofAfter absorption by soil colloidal particles,ammonia nitrogen is removed by microbial nitri fication-denitri fication.In an SI system,nitri fication is completed by nitrite bacteria and nitrate bacteria.Nitrite bacteria oxidizeobtaining the energy,thenis ready to be oxidized intoby nitrate bacteria.Because the organic nitrogen in in fluent merely constitutes 15%-25%of TN,the ammoni fication process of organics does not limit nitri fication signi ficantly.Nitrate bacteria can use CO2as a carbon source.Thus,the carbon source is not the limiting factor of nitri fication,either.In addition,pH,temperature,dissolved oxygen(DO),and humidity are factors in fluencing the nitri fication process.The most important factor among them in the control of the nitri fication rate is DO.Research by Llor■ens et al.(2011)showed that,in SI systems,most of the nitrogen is nitri fied at 0.3 m below the water distributor,but,owing to respiration or saturation causing the oxygen level to drop,nitri fication may be slowed and even stopped.Their study showed that,when the system holds water for too long,such that it becomes saturated,anaerobics will emerge at the bottom of percolation ditch,which will reduce oxygen exchange and the nitri fication capacity of soil.This can also explain why the nitri fication performance of the SI system is not very strong when permeability is poor;is barely absorbed by soil,except for when it is used by organisms;and it is therefore free to move in the soil.Whenis transformed intoby nitrate bacteria and nitrite bacteria,they are eluted.The negative charge of soil particles is released again,and theadsorption capacity is recovered.(2)Volatilization:Ammonia nitrogen can escape from the SI system in the same way as NH3,and this is particularly signi ficant in dry climatic regions.The main factors affecting this process are the pH of the soil solution,the escape velocity of ammonia,and the temperature.In general,there is less volatilization of ammonia with greater depth of the soil in the SI system.The removal ef ficiency decreases at the same time.There are also some results showing that,when the pH value of soil is lower than 8.0,the volatilization of ammonia can be neglected(Kumar et al.,2015;Oksana et al.,2015).

    3.3.Nitrate and nitrite removal

    InSIsystems,themethodsofnitrateandnitriteremovalfrom sewage include the following:(1)Biological effects:Denitrifying bacteria use nitrate and nitrite as electron acceptors,converting them into gas under anaerobic conditions.Even under aerobic conditions,the denitri fication process in SI systems can also occur.This may be because of the anaerobic environment that is created by the respiration of microorganisms.Kong et al.(2002)observed that,after wastewater enters soil,with the increase of soil saturation,the release rate of N2O increases.The reason is that the contact between nitrate and inorganics affects the distribution of oxygen and microbial activity.In addition,temperature,pH,nitrate content,and organic carbon content can affect the denitri fication.(2)Chemical reaction:When theof the soil accumulates to a certain extent,it can react with organics in the SI system,and produce N2,NO2,and N2O.Generally,the process of nitrite nitrogen being converted into nitrate nitrogen occurs much faster than that of ammonia being converted into nitrate.When nitrogen in thegaseousformincreaseintheSIsystem,itcausestheincrease of pH and restrains the activity of nitrate bacteria.However,it does not restrain the activity of nitrite bacteria signi ficantly;nitrite nitrogen may accumulate.In the denitri fication process,if the content of nitrate is relatively high,microorganisms will first use nitrite nitrogen as electron acceptors,causing the accumulation of nitrite nitrogen.Foran SI system,the chemical reaction process of gaseous nitrogen generation is always ignored,but when the denitri fication reaction is signi ficant,it cannot be ignored.(3)Absorption by plants:Whenandmove with the water,they can be absorbed and used by plant roots,and they become the necessary elements for plant growth.Stewart et al.(2010)analyzed the relationship between TN removal and the nitrogen intake by plants.The results show that,with the decrease of soil permeability,the intake of nitrogen increases.When the pollution load of BOD is 1735 kg/(hm2.year),about 46%of TN is absorbed by plants.

    4.Major biological processes involved in nitrogen removal

    As shown in Fig.1,many mechanisms are involved in the fate of nitrogen:uptake of inorganic nitrogen by bacteria,mineralization,sedimentation,volatilization of ammonia,and nitri fication coupled with denitri fication.

    For a long time,contradictory assumptions about the main mechanisms responsible for nitrogen removal have been proposed.Some researchers have argued that ammonia volatilization largely explains nitrogen removal by SI systems(O'Reilly et al.,2012).Other authors have reported that ammonia volatilization accounts for only a small fraction of nitrogen removal,even with a pH value as high as 8.5(Oksana et al.,2015).Most investigations have suggested that sedimentation and adsorption of ammonia are the major processes responsible for nitrogen removal in the start-up periods(Chen et al.,2014).For an SI system in stable performance periods,nitri fication coupled with denitri fication can be the major process of nitrogen removal,especially on warm days(Sun et al.,2012).Generally speaking,of the several methods of nitrogen removal by SI systems,nitri fication-denitri fication constitutes 69%-77%,the adsorption ofplantsconstitutes 14%-17%,and volatilization and other methods constitute 6%-17%(Bernadette et al.,2009).Biological effects are therefore the main form of nitrogen removal.During soil treatment of wastewater,organicnitrogeniseasilyconvertedintoammonifying bacteria in SI systems,can be adsorbed onto the soil because the zeta potential of the soil particles is negative,and the adsorption capacity of the soil can quickly return to the initial state due to nitri fication of intowhich is subsequently denitri fied to N2orN2O by the denitrifying biomass under the anoxic conditions.This is the circulation mode of nitrogen removal in SI systems.

    4.1.Ammoni fication

    The process of microorganisms decomposing organic nitrogen compounds into ammonia is called ammoni fication.It can also be called mineralization.In SI systems,the majority of ammonia produced through ammoni fication is converted into nitrate and nitrite,and the rest is absorbed by plants or escapes from the system.A lot of bacteria,fungi,and actinomycetes can secrete proteases,which can break down proteins into polypeptides,amino acids,and NH3.Of the microorganisms,those with the ability to decompose organic nitrogen are called ammonifying microorganisms,and are widely distributed in nature,including in aerobic,facultative,and anaerobic conditions.

    In SI systems,the factors affecting ammoni fication mainly include the following:(1)Temperature:Within the range of 25°C-35°C,the velocity of ammoni fication grows with the increase of temperature,but the absorption of plants rises at the same time.(2)Moisture content of the substrate:Ammoni fication is enhanced with the rise of water content of soil,but when the water content rises to some certain extent,the velocity of ammoni fication drops quickly.(3)Organic matter:Ammoni fication velocity is positively correlated with the content of organic matter.(4)Soil depth:In general,the velocity of ammoni fication drops with the rise of soil depth.The amount of organic matter at different depths of soil is also the main factor affecting ammoni fication.Within the range of 0-120 cm,ammoni fication is different at different soil depths.This is because,with the increase of soil depth,the breathability of microorganisms and mineralization extent of organic matter always change.With the breathability of soil dropping gradually,less organic matter can be degraded,the amount of microorganisms drops quickly,and the ammoni fication rate decreases.(5)Other factors:The physical state of soil,like the water content in the soil and the degree of compaction,affects the condition of soil breathability.Any changes in these factors affect the ammoni fication performance of SI systems.

    4.2.Nitri fication

    Nitri fication is completed by autotrophs in stages(Pan et al.,2013).The first stage is nitrosation,which is the stage of converting ammonia into nitrite.There are mainly five species of nitrite bacteria taking part in this stage:Nitrosomonas,Nitrosocytis,Nitrosococcus,Nitrosospira,and Nitrosogloea.The second stage is nitri fication,during which nitrite is oxidized into nitrate.There are mainly three species taking part in this stage:Nitrobacter,Nitrospina,and Nitrococcus.As shown in Fig.2,N2O and NO are produced as reaction byproducts during the process in whichis oxidized intowhere N is an electron acceptor(Kong et al.,2002):

    Fig.2.Nitri fication process for gaseous nitrogen production.

    The factors affecting nitri fication in SI systems include temperature,DO,pH,carbon-to-nitrogen ratio(C/N ratio),and toxic substances(Zhao et al.,2013):(1)Temperature:Temperature affects nitri fication mainly by affecting the fluidity of microbial cells and the activity of biological macromolecules.On one hand,the reactive velocity of microbial cells accelerates,and the metabolism and growth are accordingly accelerated.On the other hand,with the rise of temperature,biologically active substances change,the functioning of cells drops,and the microorganisms may even die.Biological nitri fication can occur within the range of 4°C-45°C,the most suitable temperature for nitrate bacteria is 35°C,and the most suitable temperature range for nitrite bacteria is 35°C-42°C.Temperature not only affects the growth rate of nitrate bacteria,but also the activity of bacteria.Jin et al.(2014)showed that nitri fication is limited at temperatures below 10°C,and stops below 6°C.Thus,low temperature limits nitri fication.When the temperature rises from 5°C to 30°C,the velocity of nitri fication also rises.(2)DO:Nitri fication is generally carried out under aerobic conditions.The concentration of DO can also affect the velocity of nitri fication,which generally should be above 2 mg/L.For SI systems,DO is not as sensitive as it is to activated sludge and bio film systems.However,in order to ensure adequate nitri fication,the DO level must be high,generally greater than 3mg/L,because 4.6 mg/L of DO is needed to oxidize 1.0 mg ammonia.(3)pH:Nitrate bacteria are generally thought to be pH-sensitive.The most suitable pH range is from 6.6 to 8.0,and the best value is 8.0.When the pH value is less than 6.0,the nitri fication rate will drop,and when the pH value is below 4.5,nitri fication will stop.Fan et al.(2013)argued that the most suitable range of pH values for nitrate bacteria is 7.2-8.0 when the system is under acidic conditions,and the activity of nitrite bacteria as well as nitrate bacteria is limited signi ficantly.(4)C/N ratio:The C/N ratio is an important factor in the velocity and process of nitri fication.If the BOD concentration is high in sewage,heterotrophic bacteria will compete with nitrate bacteria for substrate and oxygen,restricting the growth of nitrate bacteria.(5)Toxic substances:High levels of NH3-N,heavy metals,toxic substances,and organics will suppress nitri fication.There are two main interventions that suppress nitri fication:interfering with the metabolism of cells,and destroying the original oxidation ability of bacteria.Generally speaking,for a toxic substance,the effect of nitrite bacteria is more signi ficant than that of nitrate bacteria.There are two reasons that organics suppress nitri fication(Rodriguez-Caballeroa et al.,2014).The first is that,when the organic concentration is high,the amount of heterotrophic bacteria will be much greater than that of nitrite bacteria,and get in the way of ammonia passing to nitrite bacteria.The number of nitrate bacteria is also reduced because of the existence of heterotrophic bacteria.Another reason is that some organics are toxic or suppressive to nitrite bacteria.

    The nitri fication potential,an indicator of nitrifying bacteria activity,was measured as in Kadlec et al.(2010).20 g soil samples were added to 100 mL of NH4Cl solution with a nitrogen concentration of 500mg/L.The mixture was incubated at 25°C for 24 h.The amount of nitri fied ammonium nitrogen was determined by Eq.(1):

    where ω is the rate of nitrate nitrogen production(mg/(kg.h)),ρiis the initialconcentration of substrate solution(mg/L),ρtis theconcentration of the solution after incubation time t(mg/L),ρbis theconcentration of the blank sample after incubation time t(mg/L),V is the volume of substrate solution(L),M is the mass of the soil sample(kg),w is the water content of the soil sample(fraction),and ρ is the density of water at 25°C(0.997 kg/L).

    In nitri fication depths,the Pearson correlation coef ficients of functional genes amoA-nxrA,amoA-napA,nxrA-napA,amoA-nirK,amoA-nosZ,nirK-nosZ,nxrA-nosZ,napA-nosZ,nxrA-nirK,and napA-nirK were all greater than 0.6(P<0.05).Thus,associated enrichments between amoA,nxrA,napA,nirK,and nosZ existed.Based on this in-depth analysis,it was found that amoA,nxrA,napA,nirK,and nosZ genes could be expressed under aerobic conditions and had similar ecological adaptability during the nitri fication process(Ji et al.,2012).

    4.3.Denitri fication

    Denitri fication is the process,in which denitrifying bacteria deoxygenate nitrite,with N2or N2O released under hypoxic conditions.Most denitrifying bacteria are facultative anaerobes,such as Achromobacter,Aerobacter,Alcaligenes,and Pseudomonas.These denitrifying bacteria use many kinds of organic substrate as electron donors,deoxygenatinginto N2by stages.According to Jacobs and Harrison(2014),N2O is produced as an intermediate product during the denitri fication process in whichis converted into N2(Fig.3).

    In SI systems,the main factors that affect denitri fication are the following:(1)Temperature:The most suitable temperature range for denitri fication is 20°C-40°C.When the temperature is below 15°C,the velocity of denitri fication will drop dramatically,and when the temperature is below 3°C,the denitri fication process will stop.(2)DO:Denitri fication generally occurs under conditions of hypoxia.DO will restrain the denitri fication process,because DO will compete with nitrate for electron donors,which can also restrain the mixture and the activity of nitrate reductase.(3)pH:The most suitable pH values for denitri fication are 6.5-7.5.Unsuitable pH values will affect the growth of denitrifying bacteria and the activity of enzymes.When the pH value is below 6.0 or above 8.0,it will restrain the denitri fication process signi ficantly.The denitri fication process will produce alkalinity,which is helpful to maintaining the pH value within a suitable range.(4)Carbon source:Generally,when the BOD/total Kjeldahl nitrogen(TKN)ratio is above 3 to 5 in SI systems,the carbon sources are suf ficient.If organics are in shortage in wastewater,carbon sources,like methanol,ethanol,citric acid,and molasses,need to be added.Municipal wastewater and some industrial wastewater can also serve as the carbon sources of denitri fication.The term solid-phase denitri fication came into existence in recent years,where solid substrates were used as a constant carbon source for denitri fication and also to provide a platform for microbial biomass development.Materials such as starch,polycaprolactone,and polybutylene succinate have been widely used due to their excellent denitri fication ef ficiencies in short time periods(Ashok and Hait,2015).The donor species or technologies can be adopted,depending on environmental,physical,and biological conditions of the environment,and should not lead to pollution swapping.

    Fig.3.Denitri fication process for gaseous nitrogen production.

    The method of determining the denitri fication potential of the soil medium developed by Kadlec et al.(2010)was used with slight modi fications.A 10 g soil sample was incubated with a 100 mL KNO3substrate solution in each 250 mL flask,and the flasks were shaken at 180 rpm for 48 h at 37°C.After the incubation,soil suspension was filtered through a 0.45 μm-membrane filter for further analysis ofandconcentrations.The denitri fication potentialwas calculated by Eq.(2).

    where ω′isthe rate ofgaseousnitrogen production(mg/(kg.h)),is the initialconcentration of the substrate solution(mg/L),is theconcentration of the solution after incubation time t(mg/L),is theconcentration of the solution after incubation time t(mg/L),represents theconcentrations of blank samples after incubation time t(mg/L),V1is the volume of the substrate solution(L),V2is the water content of the soil sample(L),m is the mass of the soil sample(kg),and k is the moisture coef ficient of the matrix at 25°C.

    Li et al.(2013)reported that denitri fiers increased with soil depth.In contrast,nitri fiers decreased with the increase in soil depth.Ji et al.(2012)found that the associated enrichments between narG and qnorB genes existed in anaerobic areas.Based on the depth analysis,they insisted that narG and qnorB could be expressed under anaerobic conditions and they had similarecologicaladaptability during the denitri ficaiton process.

    4.4.CANON and Anammox

    Nitrogen removal from municipal wastewater via the traditional nitri fication-denitri fication has become a key process in biological treatment over recent decades.However,the implementation of conventional nitrogen removal,i.e.,the aerobic conversion of ammonia to nitrate combined with the anaerobic conversion of nitrate to nitrogen gas,is energyintensive,mainly because of aeration costs(Susanne et al.,2014).In recent years,a new pathway for ammonium removal has been discovered and widely studied:completely autotrophic nitrogen-removal over nitrite(CANON)and anaerobic ammonium oxidation(Anammox).

    CANON is closely related to the Anammox process,in whichis first partially oxidized into nitrite nitrogen before being transformed with the remaining ammonium into dinitrogen gas by planctomycetes-like bacteria.These planctomycetes-like bacteria grow in the anaerobic zones of treatment systems.The stoichiometry of the CANON process is described by Eq.(3):

    Because the CANON process generates dinitrogen gas,the loss of TN in the sewage is a natural result.According to the research by Zhang et al.(2015),theconcentration decreases and theconcentration increases with soil depth.In comparison,TN concentration is unceasingly reduced.Above the soil depth of 1.30 m,30.5%of the nitrogen disappeared.Through mass balance analysis,it was observed that the CANON process was responsible for transforming nitrogen into a gaseous form.In addition,47.5%of theparticipated in the CANON process,and the rest played a role in nitration.At depths of 1.30-2.00 m,more than 90%of the TN was composed ofwhich indicated that the removal of TN occurred via denitri fication.

    Kuypers et al.(2003),who found Anammox bacteria at the bottom of Black Sea,have shown that the Anammox process is promising for the treatment of low-ammonium content wastewater.The reaction equation for Anammox is Eq.(4):

    To date,there are no reports suggesting that Anammox is of high importance in nitrogen removal via SI treatment.With respect to constructed wetlands(CWs),there exist controversial conclusions about whether or not Anammox is as importantasnitri fication-denitri fication fornitrogen removal.Through molecular biological analyses,research by Zhi and Ji(2014)showed that aerobic ammonia oxidation was the dominant ammonium removal path when the C/N ratio was less than or equal to six.However,when the C/N ratio was greater than six,the importance of Anammox was notably enhanced,resulting in another primary ammonium removal pathway,in addition to the aerobic ammonia oxidation.He et al.(2012)examined the effects of pH and seasonal temperature variation on simultaneous partial nitri fication and Anammox in two free-water surface wetlands.Fluorescence in situ hybridization analysis found that aerobic ammonium oxidizing bacteria and Anammox bacteria accounted for 42%-73%of the bacterial populations in the wetlands.A seasonal temperature variation of more than 6°C would affect simultaneous partial nitri fication and Anammox signi ficantly.Signi ficant pH effects were identi fied when the temperatures were below 18.9°C.Anammox was the limiting stage of simultaneous partial nitri fication and Anammox in the wetlands.In comparison,Takaaki et al.(2011)suggested that,although Anammox bacteria were detected by molecular methods,Anammox activity could not be measured and therefore that this process appears to be of low importance in nitrogen transformations in these wastewater eco-treatment systems.Due to the differences between operations of a SI system and CW,e.g., flow-moving paths,hydraulic retention time,substrate composition,and construction,Anammox should be another future research focus relating to the nitrogen removal process via SI systems.

    5.Conclusions

    (1)During the wastewater treatment process using SI systems,mineralization,volatilization,adsorption,nitri fication,and denitri fication are the main paths of organic nitrogen,ammonia nitrogen,removal.

    (2)With respect to TN removal,ammoni fication followed by nitri fication and denitri fication constitutes 69%-77%,adsorption of plants 14%-17%,and volatilization and other methods 6%-17%,showing that biological effects are the main method of nitrogen removal.

    (3)The CANON process could be responsible for transforming nitrogen into a gaseous form in upper layers of SI systems.Both denitri fication and the CANON reaction transform in fluent nitrogen into a gaseous form,expressed by N2O,N2,and NO.

    (4)Further research needs to focus on the emission characteristics of gaseous nitrogen and its spatial distribution in soil.

    Ashok,V.,Hait,S.,2015.Remediation of nitrate-contaminated water by solidphase denitri fication process:A review.Environ.Sci.Pollut.Res.22(11),8075-8093.https://doi.org/10.1007/s11356-015-4334-9.

    Bali,M.,Gueddari,M.,Boukchina,R.,2010.Treatment of secondary wastewater ef fluents by in filtration percolation.Desalination 258(1-3),1-4.https://doi.org/10.1016/j.desal.2010.03.041.

    Bernadette,P.,Tahina,A.,D■ebora,P.O.,Wang,X.Z.,Qiu,J.P.,Fran?ois,B.,2009.Nitrogen removal in wastewater stabilization ponds.Desalination Water Treat.4(1-3),103-110.https://doi.org/10.5004/dwt.2009.363.

    Boonchai,R.,Seo,G.,2015.Microalgae membrane photobioreactor for further removal of nitrogen and phosphorus from secondary sewage ef fluent.Korean J.Chem.Eng.32(10),2047-2052.https://doi.org/10.1007/s11814-015-0043-9.

    Chen,P.Z.,Cui,J.Y.,Hu,L.,2014.Nitrogen removal improvement by adding peat in deep soil of subsurface wastewater in filtration system.J.Integr.Agric.13,1113-1120.https://doi.org/10.1016/S2095-3119(13)60401-3.

    Curia,A.C.,Koppe,J.C.,Costa,J.F.C.L.,F■eris,L.A.,Gerber,W.D.,2011.Application of pilot-scale-constructed wetland as tertiary treatment system of wastewater for phosphors and nitrogen removal.Water,Air,Soil Pollut.218(1-4),131-143.https://doi.org/10.1007/s11270-010-0629-0.

    Duan,J.J.,Geng,C.G.,Li,X.,Duan,Z.Q.,Yang,L.Z.,2015.The treatment performance and nutrient removal of a garden land in filtration system receiving dairy farm wastewater.Agric.Water Manag.150,103-110.https://doi.org/10.1016/j.agwat.2014.12.003.

    Fan,J.L.,Zhang,B.,Zhang,J.,Guo,W.S.,Liu,F.F.,Guo,Y.Y.,Wu,H.M.,2013.Intermittent aeration strategy to enhance organics and nitrogen removal in subsurface flow constructed wetlands.Bioresour.Technol.141,117-122.https://doi.org/10.1016/j.biortech.2013.03.077.

    Gunduz,M.A.O.,2013.Comparison of organic matter removal from synthetic and real wastewater in a laboratory-scale soil aquifer.Water,Air,Soil Pollut.224,1467-1474.https://doi.org/10.1007/s11270-013-1467-7.

    He,Y.L.,Tao,W.D.,Wang,Z.Y.,Walid,S.,2012.Effects of pH and seasonal temperature variation on simultaneous partial nitri fication and anammox in free-water surface wetlands.J.Environ.Manag.110,103-109.https://doi.org/10.1016/j.jenvman.2012.06.009.

    Heil,J.,Liu,S.R.,Vereecken,H.,Bru¨ggemann,N.,2015.Abiotic nitrous oxide production from hydroxylamine in soils and their dependence on soil properties.Soil Biol.Biochem.84,107-115.https://doi.org/10.1016/j.soilbio.2015.02.022.

    Jacobs,A.E.,Harrison,J.A.,2014.Effects of floating vegetation on denitrifi cation,nitrogen retention,and greenhouse gas production in wetland.Biogeochemistry 119(1-3),51-66.https://doi.org/10.1007/s10533-013-9947-9.

    Ji,G.D.,Zhi,W.,Tan,Y.F.,2012.Association of nitrogen micro-cycle functional genes in subsurface wastewater in filtration systems.Ecol.Eng.44,269-277.https://doi.org/10.1016/j.ecoleng.2012.04.007.

    Jin,H.O.,Park,J.Y.,Timothy,G.E.,2014.Septic wastewater treatment using recycled rubber particles as bio filtration media.Environ.Technol.35(5-8),637-644.https://doi.org/10.1080/09593339.2013.840337.

    Jin,P.K.,Song,L.,Ren,W.A.,2015.Transformation characteristics of different forms of nitrogen nutrients in process of wastewater treatment.Chin.J.Environ.Eng.9(9),4193-4198(in Chinese).

    Kadlec,R.H.,Roy,S.B.,Munson,R.K.,Charlton,S.,Brownlie,B.,2010.Water quality performance of treatment wetlands in the Imperial Valley,California.Ecol.Eng.36(8),1093-1107.https://doi.org/10.1016/j.ecoleng.2010.04.028.

    Kandra,H.,McCarthy,D.,Deletic,A.,2015.Assessment of the impact of stormwater characteristics on clogging in stormwater filters.Water Resour.Manag.29(4),1031-1048.https://doi.org/10.1007/s11269-014-0858-x.

    Kim,D.G.,Park,J.,Lee,D.,Kang,H.,2011.Removal of nitrogen and phosphorus from ef fluent of a secondary wastewater treatment plant using a pond-marsh wetland system.Water,Air,Soil Pollut.214(1-4),37-47.https://doi.org/10.1007/s11270-010-0399-8.

    Kong,H.N.,Kimochi,Y.,Mizuochi,M.,2002.Study of the characteristics of CH4and N2O emission and methods of controlling their emission in the soil-trench wastewater treatment process.Sci.Total Environ.290(1-3),59-67.https://doi.org/10.1016/S0048-9697(01)01058-0.

    由判斷矩陣特征可知,對(duì)m個(gè)因子進(jìn)行次兩兩比較可以確定判斷矩陣,各專家意見由相應(yīng)的判斷矩陣的上半(下半)矩陣(不包括對(duì)角線)即可體現(xiàn)。

    Kumar,D.,Asolekar,S.,Sharma,S.,2015.Post-treatment and reuse of secondary ef fluents using natural treatment systems:The Indian practices.Environ.Monit.Assess.187(10),1-15.https://doi.org/10.1007/s10661-015-4792-z.

    Kuypers,M.M.M.,Sliekers,A.O.,Lavik,G.,Schmid,M.,J?rgensen,B.B.,Kuenen,J.G.,Damst■e,S.,Strous,M.,Jetten,M.S.M.,2003.Anaerobic ammonium oxidation by Anammox bacteria in the Black Sea.Nature 422(6932),608-611.https://doi.org/10.1038/nature01472.

    Li,Y.H.,Li,H.B.,Wang,H.,Wang,X.,Zou,Y.,Sun,T.H.,2013.Comparison of the treatment performance of bio-substrate based and meadow brown soil based subsurface in filtration systems for domestic wastewater treatment.Water Sci.Technol.67(3),506-513.https://doi.org/10.2166/wst.2012.576.

    Llor■ens,M.,P■erez-Marín,A.B.,Aguilar,M.I.,S■aez,J.,Ortu~no,J.F.,Meseguer,V.F.,2011.Nitrogen transformation in two subsurface in filtration systems at pilot scale.Ecol.Eng.37,736-743.https://doi.org/10.1016/j.ecoleng.2010.06.033.

    Oksana,C.,Peter,K.,Uwe,K.,Oliver,S.,Marion,M.,Mike,S.M.J.,Kay,K.,2015.Nitrogen transforming community in a horizontal subsurface- flow constructed wetland.Water Res.74,203-212.https://doi.org/10.1016/j.watres.2015.02.018.

    O'Reilly,A.M.,Wanielista,M.P.,Chang,N.B.,Xuan,Z.,Harris,W.G.,2012.Nutrient removal using biosorption activated media:Preliminary biogeochemical assessment of an innovative stormwater in filtration basin.Sci.Total Environ.432,227-242.https://doi.org/10.1016/j.scitotenv.2012.05.083.

    Pan,J.,Yu,L.,Li,G.Z.,Huang,L.L.,Jin,H.T.,2013.Characteristics of microbial populations and enzyme activities in non-shunt and shunt subsurface wastewater in filtration systems during nitrogen removal.Ecol.Eng.61,127-132.https://doi.org/10.1016/j.ecoleng.2013.09.025.

    Pan,J.,Yu,L.,2015.Characteristics of subsurface wastewater in filtration systems fed with dissolved or particulate organic matter.Int.J.Environ.Sci.Technol.12(2),479-488.https://doi.org/10.1007/s13762-013-0408-8.

    Phuong,T.V.O.,Huu,H.N.,Guo,W.S.,Zhou,J.L.,Phuoc,D.N.,Andrzej,L.,Wang,X.C.,2014.A mini-review on the impacts of climate change on wastewater reclamation and reuse.Sci.Total Environ.494-495,9-17.https://doi.org/10.1016/j.scitotenv.2014.06.090.

    Qin,W.,Dou,J.F.,Ding,A.Z.,2014.A study of subsurface wastewater in filtration systems for distributed rural sewage treatment.Environ.Technol.35(16),2115-2121.https://doi.org/10.1080/09593330.2014.894579.

    Rodriguez-Caballeroa,I.,Aymericha,M.,Pochb,M.P.,2014.Evaluation of process conditions triggering emissions of green-house gases from a biological wastewater treatment system.Sci.Total Environ.15,384-391.https://doi.org/10.1016/j.scitotenv.2014.06.015.

    Stewart,M.,Oakleya,A.J.,Goldb,A.J.,2010.Nitrogen control through decentralized wastewater treatment:Process performance and alternative management strategies.Ecol.Eng.36,1520-1531.https://doi.org/10.1016/j.ecoleng.2010.04.030.

    Sun,T.H.,Li,X.F.,Song,Y.F.,2006.Natural Systems for Municipal Wastewater Treatment and Reclamation.Chemical Industry Press,Beijing(in Chinese).

    Sun,Z.,Mou,X.,Sun,J.,2012.Nitrogen biological cycle characteristics of seepweed(Suaeda salsa)wetland in intertidal zone of Huanghe(Yellow)River estuary.Chin.Geogr.Sci.22,15-28.https://doi.org/10.1007/s11769-012-0511-7.

    Susanne,L.,Eva,M.G.,Siegfried,E.V.,Adriano,J.,Harald,H.,van Loosdrecht,M.C.M.,2014.Full-scale partial nitritation/anammox experiences:An application survey.Water Res.55,292-303.https://doi.org/10.1016/j.watres.2014.02.032.

    Takaaki,T.,Hideyo,Y.,Sosuke,N.,Motoyuki,Y.,Wiebe,A.,2011.Application of the nitritation and anammox process into inorganic nitrogenous wastewaterfrom semiconductorfactory.J.Environ.Eng.137(2),146-154.https://doi.org/10.1061/(ASCE)EE.1943-7870.0000303.

    Wang,S.H.,Liang,P.,Wu,Z.Q.,Su,F.F.,Yuan,L.L.,Sun,Y.M.,Wu,Q.,Huang,X.,2015.Mixed sulfur-iron particles packed reactor for simultaneous advanced removal of nitrogen and phosphorus from secondary ef fluent.Environ.Sci.Pollut.Res.22(1),415-424.https://doi.org/10.1007/s11356-014-3370-1.

    Yuan,H.P.,He,Z.,2015.Integrating membrane filtration into bioelectrochemical systems as next generation energy-ef ficient wastewater treatment technologies for water reclamation:A review.Bioresour.Technol.195,202-209.https://doi.org/10.1016/j.biortech.2015.05.058.

    Zhang,J.,Huang,X.,Liu,C.X.,2002.Pilot study on subsurface wastewater in filtration system applied in rural sewage treatment.Environ.Sci.23(6),57-61(in Chinese).

    Zhang,L.Y.,Ye,Y.B.,Wang,L.J.,2015.Nitrogen removal processes in deep subsurface wastewater in filtration system.Ecol.Eng.77,275-283.https://doi.org/10.1016/j.ecoleng.2015.01.008.

    Zhao,H.G.,Xu,X.G.,Ke,F.,Li,W.C.,Feng,M.H.,Zhang,H.H.,2013.Nitrogen removal from wastewater plant secondary ef fluent in a compound natural treatment system.Ecol.Eng.57,361-365.https://doi.org/10.1016/j.ecoleng.2013.04.026.

    Zhi,W.,Ji,G.D.,2014.Quantitative response relationships between nitrogen transformation rates and nitrogen functional genes in a tidal flow constructed wetland under C/N ratio constrains.Water Res.64,32-41.https://doi.org/10.1016/j.watres.2014.06.035.

    This work was supported by the National Natural Science Foundation of China(Grants No.41571455 and 51578115)and the Basic Science Research Fund of Northeastern University(Grant No.N160104004).

    *Corresponding author.

    E-mail address:graceli_2003@163.com(Hai-bo Li).

    Peer review under responsibility of Hohai University.

    猜你喜歡
    對(duì)角線意見專家
    用活平行四邊形對(duì)角線的性質(zhì)
    致謝審稿專家
    評(píng)“小創(chuàng)”,送好禮
    沒有反對(duì)意見
    評(píng)“小創(chuàng)”,送好禮
    請(qǐng)叫我專家
    邊、角、對(duì)角線與平行四邊形的關(guān)系
    看四邊形對(duì)角線的“氣質(zhì)”
    專家面對(duì)面
    母雞下蛋
    19禁男女啪啪无遮挡网站| 18禁裸乳无遮挡动漫免费视频| 亚洲黑人精品在线| 亚洲精品自拍成人| 国产精品免费一区二区三区在线 | ponron亚洲| 亚洲精品成人av观看孕妇| 久久国产精品影院| 丝袜在线中文字幕| 婷婷精品国产亚洲av在线 | 免费久久久久久久精品成人欧美视频| 亚洲在线自拍视频| 精品久久久精品久久久| 精品少妇一区二区三区视频日本电影| 精品一区二区三区av网在线观看| av电影中文网址| 91在线观看av| 亚洲精品成人av观看孕妇| 手机成人av网站| 成人特级黄色片久久久久久久| 久久婷婷成人综合色麻豆| 国产精品综合久久久久久久免费 | 在线观看免费视频网站a站| 在线永久观看黄色视频| 五月开心婷婷网| 捣出白浆h1v1| 黑人巨大精品欧美一区二区蜜桃| 精品久久久久久,| 亚洲欧美激情在线| 窝窝影院91人妻| 在线播放国产精品三级| svipshipincom国产片| 精品无人区乱码1区二区| 亚洲中文av在线| 亚洲精品在线美女| 国精品久久久久久国模美| svipshipincom国产片| aaaaa片日本免费| 中国美女看黄片| 天堂中文最新版在线下载| 亚洲熟妇熟女久久| 黄色 视频免费看| 成人永久免费在线观看视频| 日日摸夜夜添夜夜添小说| 久久ye,这里只有精品| 欧美中文综合在线视频| 亚洲av美国av| 99精品欧美一区二区三区四区| 午夜免费成人在线视频| avwww免费| 国产日韩欧美亚洲二区| 亚洲精品中文字幕在线视频| 亚洲欧美精品综合一区二区三区| 久久影院123| 女人精品久久久久毛片| 在线观看日韩欧美| 一区二区三区精品91| 亚洲精品粉嫩美女一区| 丰满的人妻完整版| 新久久久久国产一级毛片| 天天躁夜夜躁狠狠躁躁| 久久婷婷成人综合色麻豆| 国产一区有黄有色的免费视频| 国产成人影院久久av| 亚洲色图 男人天堂 中文字幕| 黄色视频不卡| 日韩欧美一区二区三区在线观看 | 一级a爱片免费观看的视频| 丝瓜视频免费看黄片| 亚洲国产欧美日韩在线播放| 国产成人av激情在线播放| 大香蕉久久网| 不卡av一区二区三区| 黑人操中国人逼视频| 久久午夜综合久久蜜桃| av网站在线播放免费| 很黄的视频免费| 一区二区三区精品91| 亚洲熟妇熟女久久| 亚洲精品国产色婷婷电影| 中国美女看黄片| 最近最新免费中文字幕在线| 成人黄色视频免费在线看| 99热网站在线观看| 久久热在线av| 中文字幕最新亚洲高清| 脱女人内裤的视频| 成人18禁在线播放| 免费在线观看视频国产中文字幕亚洲| 天天躁夜夜躁狠狠躁躁| 十八禁网站免费在线| 99国产精品一区二区蜜桃av | 精品乱码久久久久久99久播| 一二三四社区在线视频社区8| 91av网站免费观看| 丁香欧美五月| 黄色视频不卡| 黄片大片在线免费观看| 精品熟女少妇八av免费久了| 久久国产精品人妻蜜桃| 亚洲色图av天堂| av不卡在线播放| 好男人电影高清在线观看| 一区福利在线观看| 国产午夜精品久久久久久| 黄色视频不卡| 成年人黄色毛片网站| 亚洲免费av在线视频| 9色porny在线观看| 激情在线观看视频在线高清 | 成在线人永久免费视频| 亚洲精品成人av观看孕妇| 欧美日韩av久久| 乱人伦中国视频| 999精品在线视频| 热re99久久精品国产66热6| 正在播放国产对白刺激| xxx96com| 亚洲欧美日韩高清在线视频| 久久热在线av| 91大片在线观看| 伦理电影免费视频| 在线观看午夜福利视频| 操出白浆在线播放| 超色免费av| 亚洲五月色婷婷综合| 黄片播放在线免费| 黑丝袜美女国产一区| 两个人免费观看高清视频| 韩国精品一区二区三区| 丝瓜视频免费看黄片| 男女高潮啪啪啪动态图| 国产黄色免费在线视频| 少妇裸体淫交视频免费看高清 | 欧美久久黑人一区二区| 亚洲免费av在线视频| 精品国产一区二区久久| 啦啦啦视频在线资源免费观看| 国产单亲对白刺激| av片东京热男人的天堂| 日本vs欧美在线观看视频| 无人区码免费观看不卡| 午夜精品在线福利| 69精品国产乱码久久久| bbb黄色大片| 久久久久国产一级毛片高清牌| 亚洲第一欧美日韩一区二区三区| 可以免费在线观看a视频的电影网站| 视频在线观看一区二区三区| 中国美女看黄片| 国产欧美日韩一区二区精品| 女警被强在线播放| 亚洲精品中文字幕一二三四区| av线在线观看网站| 国产精品国产高清国产av | 9色porny在线观看| 人人妻人人添人人爽欧美一区卜| 日日夜夜操网爽| svipshipincom国产片| 色尼玛亚洲综合影院| 国产精品亚洲av一区麻豆| 国产精品久久久久久人妻精品电影| 久久天躁狠狠躁夜夜2o2o| 成人手机av| 亚洲成a人片在线一区二区| 最近最新中文字幕大全电影3 | 国产av又大| 亚洲精品国产一区二区精华液| 午夜福利影视在线免费观看| 国产精品香港三级国产av潘金莲| 日韩人妻精品一区2区三区| 婷婷丁香在线五月| 手机成人av网站| 十八禁网站免费在线| 欧美在线一区亚洲| 老司机午夜福利在线观看视频| 美国免费a级毛片| 久久人人97超碰香蕉20202| 91精品三级在线观看| 十八禁人妻一区二区| 欧美日韩亚洲国产一区二区在线观看 | 日韩视频一区二区在线观看| 无人区码免费观看不卡| 免费观看精品视频网站| 激情视频va一区二区三区| 另类亚洲欧美激情| 51午夜福利影视在线观看| av超薄肉色丝袜交足视频| 成人三级做爰电影| 老司机在亚洲福利影院| 欧美av亚洲av综合av国产av| 大型av网站在线播放| 精品欧美一区二区三区在线| 亚洲综合色网址| 9色porny在线观看| 97人妻天天添夜夜摸| 搡老岳熟女国产| 一夜夜www| 99香蕉大伊视频| 欧美黄色淫秽网站| 夜夜躁狠狠躁天天躁| 亚洲人成伊人成综合网2020| 精品高清国产在线一区| 高潮久久久久久久久久久不卡| 国产精品电影一区二区三区 | 极品人妻少妇av视频| svipshipincom国产片| 黄色怎么调成土黄色| 亚洲国产精品合色在线| 纯流量卡能插随身wifi吗| 纯流量卡能插随身wifi吗| 日韩 欧美 亚洲 中文字幕| 婷婷精品国产亚洲av在线 | 99国产精品一区二区三区| 日本黄色视频三级网站网址 | 午夜影院日韩av| 男人舔女人的私密视频| 成人av一区二区三区在线看| 女人久久www免费人成看片| cao死你这个sao货| 精品欧美一区二区三区在线| 久久久精品区二区三区| 国产一卡二卡三卡精品| 午夜精品在线福利| 久久影院123| 丝袜美足系列| 欧美性长视频在线观看| 国产深夜福利视频在线观看| 91字幕亚洲| 亚洲精品一卡2卡三卡4卡5卡| 午夜福利乱码中文字幕| 久久亚洲真实| 亚洲欧美一区二区三区黑人| 精品福利永久在线观看| 国产精品秋霞免费鲁丝片| 国产99久久九九免费精品| 国产亚洲精品久久久久久毛片 | 国产精华一区二区三区| 制服人妻中文乱码| 国产精品免费视频内射| 亚洲伊人色综图| 亚洲av成人av| 三级毛片av免费| 脱女人内裤的视频| 久久人人97超碰香蕉20202| 亚洲中文av在线| 久久久久国内视频| 人妻久久中文字幕网| 国产精品一区二区精品视频观看| 999久久久国产精品视频| 国产av又大| 人人澡人人妻人| 国产99白浆流出| 亚洲精品一二三| 午夜福利在线观看吧| 久久国产精品人妻蜜桃| 午夜精品国产一区二区电影| 亚洲av美国av| 女警被强在线播放| 亚洲午夜理论影院| 久久国产精品男人的天堂亚洲| 久久人妻福利社区极品人妻图片| 丝袜人妻中文字幕| 国产男女内射视频| 一边摸一边做爽爽视频免费| 三上悠亚av全集在线观看| 欧美黑人精品巨大| 亚洲,欧美精品.| 久久久久久久午夜电影 | 精品一品国产午夜福利视频| 精品人妻在线不人妻| 日韩欧美免费精品| 欧美成狂野欧美在线观看| 亚洲成国产人片在线观看| 亚洲成国产人片在线观看| 高清毛片免费观看视频网站 | 久久久精品国产亚洲av高清涩受| 亚洲欧美一区二区三区久久| 亚洲精品国产区一区二| 美女高潮喷水抽搐中文字幕| 大型av网站在线播放| 一级作爱视频免费观看| 男人操女人黄网站| 亚洲成a人片在线一区二区| 91九色精品人成在线观看| 91成人精品电影| 男女床上黄色一级片免费看| 久久精品成人免费网站| 日韩人妻精品一区2区三区| 久久影院123| 午夜视频精品福利| 久久中文字幕一级| 亚洲综合色网址| 91大片在线观看| 亚洲一区二区三区不卡视频| 国产精品久久久久成人av| 黄色 视频免费看| 91在线观看av| 女同久久另类99精品国产91| tube8黄色片| 性色av乱码一区二区三区2| 免费不卡黄色视频| 国产97色在线日韩免费| 国产精品乱码一区二三区的特点 | 亚洲人成电影观看| 50天的宝宝边吃奶边哭怎么回事| 亚洲午夜精品一区,二区,三区| 午夜免费观看网址| 人人妻人人澡人人看| 无限看片的www在线观看| 日韩欧美一区视频在线观看| 母亲3免费完整高清在线观看| 精品国产乱子伦一区二区三区| videos熟女内射| 天天添夜夜摸| 麻豆国产av国片精品| 夜夜躁狠狠躁天天躁| 一二三四在线观看免费中文在| 他把我摸到了高潮在线观看| 国产欧美日韩综合在线一区二区| 欧美国产精品一级二级三级| 超碰97精品在线观看| 国产无遮挡羞羞视频在线观看| 国产精品一区二区在线观看99| 亚洲国产中文字幕在线视频| 欧美丝袜亚洲另类 | 日本欧美视频一区| 一级,二级,三级黄色视频| 国产成人av激情在线播放| 成人国产一区最新在线观看| 女人爽到高潮嗷嗷叫在线视频| 亚洲 国产 在线| 性色av乱码一区二区三区2| 欧美日韩成人在线一区二区| 国产精品秋霞免费鲁丝片| 91老司机精品| 中文字幕精品免费在线观看视频| 亚洲色图av天堂| 在线天堂中文资源库| 亚洲免费av在线视频| 成年人午夜在线观看视频| 一边摸一边做爽爽视频免费| 搡老熟女国产l中国老女人| 国产成人欧美在线观看 | 天天躁日日躁夜夜躁夜夜| 露出奶头的视频| 日本精品一区二区三区蜜桃| 色婷婷久久久亚洲欧美| 777米奇影视久久| 丰满人妻熟妇乱又伦精品不卡| 午夜福利免费观看在线| 精品国产乱码久久久久久男人| 丝袜美腿诱惑在线| 怎么达到女性高潮| 午夜免费鲁丝| 欧美性长视频在线观看| 国产99白浆流出| 一区在线观看完整版| 免费少妇av软件| 国产又爽黄色视频| 午夜免费成人在线视频| av线在线观看网站| 国产欧美亚洲国产| 久久精品成人免费网站| 一区在线观看完整版| 黄色片一级片一级黄色片| 女警被强在线播放| 两人在一起打扑克的视频| 国产精品秋霞免费鲁丝片| 色婷婷av一区二区三区视频| 色综合欧美亚洲国产小说| 国产高清国产精品国产三级| 成人18禁在线播放| 免费在线观看黄色视频的| 免费在线观看黄色视频的| 国产欧美日韩综合在线一区二区| 大码成人一级视频| 无人区码免费观看不卡| 国产亚洲欧美98| 国产精品亚洲av一区麻豆| 可以免费在线观看a视频的电影网站| 制服人妻中文乱码| 高清在线国产一区| 啦啦啦视频在线资源免费观看| 少妇猛男粗大的猛烈进出视频| www日本在线高清视频| 免费一级毛片在线播放高清视频 | 深夜精品福利| 亚洲精品一二三| 在线天堂中文资源库| 亚洲精品一二三| 欧美午夜高清在线| 一a级毛片在线观看| 日韩精品免费视频一区二区三区| 欧美老熟妇乱子伦牲交| 美女高潮喷水抽搐中文字幕| 一二三四社区在线视频社区8| 成年人免费黄色播放视频| 日本精品一区二区三区蜜桃| 岛国毛片在线播放| 一夜夜www| 十八禁人妻一区二区| 很黄的视频免费| 久久精品成人免费网站| 18禁裸乳无遮挡免费网站照片 | 不卡av一区二区三区| 精品久久久精品久久久| 岛国在线观看网站| 黑人猛操日本美女一级片| 日本一区二区免费在线视频| 十八禁人妻一区二区| 十八禁网站免费在线| 国产一区在线观看成人免费| 一区福利在线观看| 亚洲熟妇熟女久久| 中亚洲国语对白在线视频| 午夜精品久久久久久毛片777| 精品国内亚洲2022精品成人 | 国产精品亚洲av一区麻豆| 91大片在线观看| 亚洲精品一卡2卡三卡4卡5卡| 三上悠亚av全集在线观看| 国产成人系列免费观看| 国产一区二区激情短视频| 免费女性裸体啪啪无遮挡网站| 午夜精品在线福利| 亚洲在线自拍视频| 欧美国产精品va在线观看不卡| 欧美亚洲日本最大视频资源| 精品亚洲成a人片在线观看| 亚洲中文字幕日韩| 日本欧美视频一区| 亚洲中文av在线| 18禁裸乳无遮挡免费网站照片 | 99热只有精品国产| 夜夜爽天天搞| 久久天躁狠狠躁夜夜2o2o| 亚洲 国产 在线| av线在线观看网站| 搡老岳熟女国产| 久久久水蜜桃国产精品网| 中文字幕另类日韩欧美亚洲嫩草| 日韩欧美免费精品| 国产精品久久久av美女十八| 18禁国产床啪视频网站| 久久中文字幕一级| 久久人妻福利社区极品人妻图片| 久久国产精品大桥未久av| 国产精品 国内视频| 亚洲人成电影观看| 国内久久婷婷六月综合欲色啪| 国产精品一区二区免费欧美| www日本在线高清视频| 久久久久久久国产电影| 一边摸一边做爽爽视频免费| 在线观看www视频免费| 亚洲精品久久成人aⅴ小说| 在线天堂中文资源库| 99riav亚洲国产免费| 在线观看一区二区三区激情| 黑人巨大精品欧美一区二区蜜桃| 精品国产美女av久久久久小说| 久久久久久久精品吃奶| 日本撒尿小便嘘嘘汇集6| 亚洲午夜理论影院| 激情在线观看视频在线高清 | 国产男靠女视频免费网站| 日本黄色日本黄色录像| 桃红色精品国产亚洲av| 国产男女内射视频| 咕卡用的链子| 欧美成人午夜精品| 18禁国产床啪视频网站| 18禁裸乳无遮挡免费网站照片 | 亚洲久久久国产精品| 麻豆av在线久日| 精品国产乱子伦一区二区三区| 99国产精品一区二区三区| 999精品在线视频| 老汉色av国产亚洲站长工具| 日本wwww免费看| 久久久久国产精品人妻aⅴ院 | 69av精品久久久久久| 自拍欧美九色日韩亚洲蝌蚪91| 国产免费男女视频| 老熟女久久久| 少妇裸体淫交视频免费看高清 | 91字幕亚洲| 成人亚洲精品一区在线观看| 一进一出抽搐动态| 久久精品亚洲精品国产色婷小说| 免费看a级黄色片| 91av网站免费观看| 一夜夜www| 搡老乐熟女国产| 老司机靠b影院| 国产免费现黄频在线看| 91老司机精品| 99国产极品粉嫩在线观看| 亚洲黑人精品在线| 午夜免费鲁丝| 亚洲专区国产一区二区| 国产淫语在线视频| 久久人妻熟女aⅴ| 亚洲国产中文字幕在线视频| 在线观看66精品国产| 日韩欧美一区视频在线观看| 国产精品久久视频播放| 老司机福利观看| 国产精品98久久久久久宅男小说| 亚洲国产欧美日韩在线播放| 日本精品一区二区三区蜜桃| 久久久国产成人免费| 在线国产一区二区在线| 91成人精品电影| 日本a在线网址| 国产欧美日韩综合在线一区二区| 国产精品免费大片| 一边摸一边做爽爽视频免费| 欧美激情 高清一区二区三区| tocl精华| 日日摸夜夜添夜夜添小说| 老熟妇乱子伦视频在线观看| 99re在线观看精品视频| 欧美乱妇无乱码| 99国产综合亚洲精品| 久久久久久亚洲精品国产蜜桃av| 亚洲一区二区三区不卡视频| av在线播放免费不卡| 国产色视频综合| 精品国产国语对白av| 高清视频免费观看一区二区| 99热国产这里只有精品6| 欧美乱色亚洲激情| 一进一出好大好爽视频| 国产国语露脸激情在线看| 一区二区三区国产精品乱码| 丝袜在线中文字幕| 国产欧美亚洲国产| 最新的欧美精品一区二区| 国产高清国产精品国产三级| 水蜜桃什么品种好| a级片在线免费高清观看视频| 久久午夜亚洲精品久久| 精品久久久久久久久久免费视频 | 国产精品免费大片| 9热在线视频观看99| 久热这里只有精品99| 免费看十八禁软件| 黄片播放在线免费| 新久久久久国产一级毛片| cao死你这个sao货| 午夜免费鲁丝| 天天躁夜夜躁狠狠躁躁| 天堂中文最新版在线下载| 18禁裸乳无遮挡动漫免费视频| 我的亚洲天堂| 欧美日韩亚洲高清精品| 大型av网站在线播放| 人人澡人人妻人| 黄色 视频免费看| 亚洲av电影在线进入| 亚洲国产中文字幕在线视频| 亚洲国产精品合色在线| 亚洲第一青青草原| 无人区码免费观看不卡| 精品卡一卡二卡四卡免费| 精品亚洲成a人片在线观看| 最近最新中文字幕大全免费视频| 久久国产精品人妻蜜桃| 妹子高潮喷水视频| 99国产精品免费福利视频| 久久精品91无色码中文字幕| 成人精品一区二区免费| 国产一区有黄有色的免费视频| 狠狠狠狠99中文字幕| 久久影院123| 一本大道久久a久久精品| 亚洲视频免费观看视频| aaaaa片日本免费| 天天躁夜夜躁狠狠躁躁| 69精品国产乱码久久久| 美女高潮喷水抽搐中文字幕| av超薄肉色丝袜交足视频| 亚洲午夜精品一区,二区,三区| 中亚洲国语对白在线视频| 亚洲三区欧美一区| 国产色视频综合| 免费在线观看影片大全网站| 久9热在线精品视频| 天天躁夜夜躁狠狠躁躁| 热99re8久久精品国产| 午夜免费成人在线视频| 欧美一级毛片孕妇| 精品人妻在线不人妻| av天堂久久9| 国产欧美日韩精品亚洲av| 精品国内亚洲2022精品成人 | 男女下面插进去视频免费观看| av免费在线观看网站| 欧美日韩视频精品一区| 亚洲专区中文字幕在线| 亚洲欧美激情综合另类| 午夜免费成人在线视频| 久久久久久亚洲精品国产蜜桃av| 日韩成人在线观看一区二区三区| 亚洲国产中文字幕在线视频| 18禁国产床啪视频网站| 脱女人内裤的视频| 国产免费现黄频在线看| 一本大道久久a久久精品| 久久99一区二区三区| 亚洲精品成人av观看孕妇| 国产欧美日韩一区二区精品| 黑人巨大精品欧美一区二区蜜桃|