• <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 ?

    Analysis of Dry Fermentation Process for Treating Food Waste

    2014-10-30 07:33:18ATTAEWUSIAmaXiangyuMAZonghuWANGLi

    ATTA-EWUSI Ama, Lü Xiang-yu, MA Zong-hu, WANG Li

    (1.University of Cape Coast,Cape Coast 00233,Ghana;2.Shenyang University of Chemical Technology,Shenyang 110142,China;3.China Huadian Engineering CO.,LTD.,Beijing 100160,China)

    Food waste is the domestic waste of residents living consumption of life,and it easy to be rotten extremely,diffuses fetid and spreads bacteria and viruses.The production of food waste in China has over 6 000 000 tons every year.With the larger population density in adding the meal time concentrated and waste serious,the food waste production is larger.While due to the cafeteria mismanagement,lots of food waste are used to feed pigs and produce cooking oil.It has a strong impact on our health.

    Food waste accounts for a high proportion of municipal solid waste in Asian countries,Visvanathan et al[1]reported the wet weight ratio of several compositions of municipal solid waste in Asian countries as shown in Fig.1.Degrade food waste has a crucial role in handing municipal waste.

    Fig.1 Materials'wet weight ratio of municipal solid waste in Asia countries

    1 Determination of Food Waste Components

    The food waste main ingredients include rice,vegetables,flour food,meat,bone,animal and plant oil,from the chemical composition's point of view,it has starch,cellulose,protein,lipid and inorganic salt[2].As the food waste composition is complex,its material properties are varied.

    1.1 Materials

    The sampling materials of food waste are taken from the restaurant at every Monday for many weeks and sampling times at half an hour after dinner as shown in Fig.2.Stir evenly before sampling in the food waste tank and jetting-out the tons,chopsticks,plastic bags and so on.Smash the food waste into 2~5 mm using food grinder and stir evenly.

    Fig.2 Experiment material

    1.2 Test Items and Method

    All test items use standard methods,the results as shown in Table 1.

    Table 1 The main project measuring method and evidence of food waste

    1.3 Food Waste Properties Analysis

    From outside,the food waste of breakfast main include egg shells,pickles,porridge,steamed stuffed buns,deep-fried dough sticks,deep-fried dough cakes and so on,the lunch and the dinner almost similar,which also include rice,noodle,vegetables,meat and so on.By contrast,the breakfast,lunch and dinner contain more oil and salt.

    1.3.1 Changes of TS,VS,TC,TN and C/N

    Carbon source and nitrogen source are necessary for microbial growth and development,and TS,VS,TC,TN and C/N play an important role in fermentation.

    Cho et al[3]reported that a text about methane yields of cooked meat,cellulose,boiled rice,fresh cabbage and mixed food waste,with the same TS from 15%to 30%,were 482,356,294,277 and 472 mL/g VS added respectively,and anaerobic biodegradability based on the stoichiometric methane yield were 82% ,92% ,72% ,73%and 86%,respectively.

    Hashimoto[4]reported at both mesophilic(35℃)and thermophilic(55℃).The batch tests could smoothly start-up with 0.49 m3/g VS fed.While thermophilic operation was not stable at an effluent substrate concentration of 62.5 m3/kg VS.Chea Eliyan[5]found that as the VS increased,the bio-gas production decreased.The methane bio-gas production rate of 140.35 L/kg VS when reactor loading rate at 2 kg/m3d.However,when loading was increased to 2.5 kg/m3d,the significant deterioration of biogas composition as well as production was only 62.55 L/kg VS.

    C/N make a very important effect on anaerobic digestion.The most suitable C/N proportion(molar ratio)for anaerobic digestion is(10~20)∶1,Polprasert[6]also gave an optimum(C/N)ratio(molar ratio)about(25 ~30)∶1,which is considered suitable for an anaerobic digester.If the C/N proportion too high might be due to acid accumulation and ammonia inhibition when proportion low.If the C/N of material is not suitable,we can mix food waste with other materials,and there are some materials C/N ratio as follows Table 2.

    Table 2 C/N ratio of some materials

    1.3.2 Inorganic Salt Ions

    Food waste contains many complicated nutrients,there is more amount of salt.While the amount of salt might affect performance of anaerobic digestion,so we determine the water-solubility salt.Some studies indicated that it made no difference for methane bacteria under low Na+、Ca2+、C1-concentration.The salt content of food waste of breakfast,lunch and dinner was shown in Table 3.High concentration has clear evidence to restrain the growing of methane bacterial.The inoculation sludge was taken from process maturity anaerobic reaction tank,bacterial domestication as well,so it's feasible for food waste digestion.

    From the result of the analysis about food waste in Table 4 shown,there are abundant nutriments in food waste and C/N、VS/TS rate are all in the appropriate rang,and inorganic salt concentration also haven't reached the degree of inhibition.Comprehensive analysis of the food waste has enormous potential for anaerobic digestion.

    Table 3 The salt content of the food waste

    Table 4 The TS、VS、TC、kjeldahl nitrogen-N、TN of the food waste and the C/N、TS/VS

    Table 4 The TS、VS、TC、kjeldahl nitrogen-N、TN of the food waste and the C/N、TS/VS

    Notes:B—breakfast;L—lunch;D—dinner.

    Item w(TS)/% w(VS)/%w(VS/TS)/%w(TC)/% w(KN)/% w(NO-3-N)/% w(TN)/% w(C/N)/%1 2 3 55 L 30.05 25.12 83.60 30.85 2.77 0.022 7 2.79 13.06 D 28.33 22.80 80.57 30.34 2.45 0.027 7 2.48 14.23 B 34.70 25.10 72.33 23.83 2.03 0.009 8 2.13 13.B 48.12 36.46 75.77 28.46 1.61 0.012 2 1.62 18.18 L 33.45 27.70 82.81 32.10 2.68 0.019 5 2.70 12.88 D 30.80 24.53 81.55 27.48 2.34 0.037 9 2.38 12.57 B 38.32 29.20 76.20 27.00 1.85 0.010 4 1.86 14.71 53 L 40.55 33.28 82.07 34.21 2.06 0.015 6 2.08 18.46 D 32.20 26.15 82.30 31.76 2.46 0.040 2 2.50 12.

    2 Dry Fermentation and Factors

    Dry fermentation,one of the most efficient and productive treatment technologies has received significant attention from researchers.Dry fermentation means organic solid concentration between 20%to 30%,and methane fermentation under no or little flow water condition.Contrast with the wet anaerobic digestion there are no or little fresh water by dry anaerobic digestion,it is only saving water but also save cost for digestive residue dehydration.Therefore dry anaerobic digestion has more high organic loading and bio-gas production efficiency.

    Food waste has abundant organic materials and water,using food waste as matrix for anaerobic digestion not only reduce waste emission but also provide cleaner energy.Zhang et al[7]sampled 500 food waste point location for investigation and bio-gas production study,find food waste is suitable matrix for anaerobic digestion,it has high biodegradability and methanogenesis performance.As shown in Table 5.

    Table 5 Several performance data of digestion for food waste and other solid[8]

    2.1 Temperature

    The optimum temperature is important for microorganism growth and metabolism,it's also important factor for enzyme activity.Generally,thermophilic fermentation and mesophilic fermentation are used for degradation waste.Though thermophilic fermentation have some advantages such as quick response,short digest time,high biogas production and so on.Baere[9]claimed that when thermophilic dry fermentation occurred and became attractive due to higher gas production and pathogen killed-off.A report shown that at a temperature of 35℃,the methane yield was increased by 43%compared to 25 ℃ .Chae et al[10].reported that the bio-gas composition differed according to digestion temperature.Methane contents in the biogas were 65.3%,64.0%and 62.0%at 35℃,30℃ and 25℃,respectively.In view of the geographical environment and climate conditions in northern China,thermophilic fermentation might increase fermentation costs.While mesophilic fer-mentation digests process stability,need less energy consumption,higher treatment ability and more mature technology.It's more suitable for northern Chinese food waste digestion.

    2.2 Hydrogen Concentration(pH)

    The activity of microorganisms is affected by pH value,so pH value affects the whole process of anaerobic digestion.In single-phase anaerobic process,as acid production and methane production in the same reactor,general pH range between 6.4~7.2 is most suitable for the anaerobic digestion process.Mace et al[11]reported at the range of 7.0 to 7.2 bacteria shows the highest performance.When the pH is too low,can make the acid producers occur irreversible inhibition,thus affect the entire digestive process.Lay et al reported that a pH less than 6.1 or more than 8.3 will cause bad performance,even failure of a digester.In two-phase anaerobic digestion process,acidification reactor can regulate the pH value for choosing particular acid producer microbial populations,thus to control acid producing approach and the subsequent methanogenesis process.The growths of methanogens have influenced by the pH value,too high or too low pH value will reduce the active of methanogens,and even kill them.

    2.3 Solid Holdup

    Dry anaerobic fermentation solid content rate can be raised to 20% ~40%,studies had shown that the initial use higher Total Solid(TS)concentration of food waste as anaerobic fermentation raw materials,in the early reaction the solid-phase hydrolysis acidification rapidly,a large number of Volatile Fatty Acids(VFA)can be produced and inhibit hydrolysis-acidification phase and subsequent methane-producing,even affected the speed and stability of the anaerobic fermentation seriously.Forster-Carneiro et al[12],using food waste as raw materials for dry fermentation experiments found that the TS was 20%,and the sludge was 30%,the yield of methane gas rate is 0.49 L·g-1VS.

    2.4 Ratio of Inocula

    The acidification phenomenon of food waste anaerobic digestion might due to the rate of hydrolysis acidification and methane-producing phase mismatch;anaerobic fermentation inocula not only provide a microbial but also plays an important role in regulating acid-base balance.Angelidaki[13]reported it is very important to find appropriate inocula containing the necessary bacteria for the degradation process to proceed,and another important factor is the amount of inocula.Studies had found that mesophilic fermentation under the condition of inoculation proportion between 10∶90 to 15∶85(volume ratio)could be starting and running normally,while when inoculation proportion over 50∶50(volume ratio)the volatile solid(VS)degradation rate and the methane production rate high-efficiency.Mesophilic fermentation in a ratio inocula of 90∶10(volume ratio),volatile solid degradation rate was 99%,the volatile solid methane-producing rate up to 519.3 mL/g,methane production rate can reach 94.5%.

    2.5 Ammonia Nitrogen

    Generally believes that mass concentration below 200 mg/L of ammonia nitrogen is good for anaerobic process,because nitrogen is one of the important nutrients in anaerobic microorganisms.And Gerardi[14]reported that ammonia concentration more than 1 500 mg·L-1at high pH may result into digester failure.Chynoweth and Pullammanappali[15]reported that the concentration of NH4-N between 200 to 1 000 mg·L-1had no adverse effect on digestion,while the concentration above 3 000 mg·L-1,it had toxic for bacteria.Ammonia inhibition concentration range is wide,cause methane production fell into 50%(half inhibition)of mass concentration range is 1.7~14 g·L-1.The effect of ammonia-nitrogen/ammonia in anaerobic digester was summarized in Table 6.Much higher concentrations could be accepted through acclimation.Ammonia inhibition concentration of significant differences can be attributed to the matrix,the inoculation sludge,environmental conditions,and the domestication time difference.

    Table 6 Effect of ammonia-nitrogen/ammonia in an anaerobic digester

    3 Dry Fermentation Kinetics Analysis

    In the 1970s,Bryant discovered originally referred to as“the methane-producing bacteria bacterium”is composed by two kinds of bacteria,one bacterial oxidation acetic acid into ethanol and H2,and another kind of bacteria use H2,CO2and acetic acid generate CH4.Thus he puts forward the theory of anaerobic digestion for three stages,namely hydrolysis-fermentation stage,producing hydrogen-production acetate stage and methaneproducing phase.First of all,through the fermentation of bacteria produce ethanol,propionic acid,butyric acid,lactic acid and so on.Schieder et al[16]found that hydrolysis is often the slowest and limiting-step in anaerobic degradation process for solid substrate.Mata-Alvarez claimed that the hydrolysis is considered to be the key step in the biodegradation of complex wastes.Then through the production of acetic,acid bacteria degradation functions to generate acetic acid,H2and CO2.Schink found that the accumulation of product such as lactate,ethanol,propionate,butyrate and higher volatile fatty acids(VFAs)is the bacteria's response to increased hydrogen concentration.Last by methane bacteria use materials converted to CH4and CO2eventually.

    3.1 Anaerobic Microbe Growth Dynamics

    Microbial growth of six typical periods for:delay phase, acceleration phase, logarithmic phase,deceleration phase,stagnation and death phase.

    In the logarithmic phase of growth rate dX/dt,growth rate μ and the biomass X has relationship as follows:

    μ is restricted production such as carbon source,nitrogen source.

    This is the Monod equation,[S]is the concentration of free organic substrate in reactor,the maximum growth rate of microbesm μmand the difference constant Kshas relationships as follows:the research has shown that the hydrolysis acidification phase and the degradation of propionic acid,butyric acid and the acetic acid reaction of methane bacteria ofpseudo-first-order kinetic model(Monod equation).

    The growth rate of cells equation as follows:

    rxis the absolute rate of cell growth;cxis the cell concentration.

    Two parameters of Monod equation are Ksand μm,respectively.Several kinds of common microorganisms'Ksand μm.were shown in Table 7.

    Table 7 Several kinds of common microorganisms'Ksand μm

    Later,people consider some of the specific problems of facts,such as matrix lack.So some deformation equation occur as follows[17-18]:

    Smis the threshold concentration;D is the actual growth rate;m is maintenance rate.

    The dynamics of death is represented mathematically as a decay of the population Kd[X].Incorporating Monod's concept and the kinetics of death into equation follows.

    [X]is total concentration of organisms in reactor.

    The rate of decrease of the concentration of the substrate is proportional to the rate of increase of the concentration of the organisms.The rate of decrease of the substrate is the equation.

    [K]is rate constant;U is the reciprocal of Y.

    In some cases,Monod equations become no longer applicable,such as high cell density.As a result,people have otherunstructured model(Table 8)is put forward.

    Table 8 Some unstructured model

    Teissier equation was considered as pure empirical formula;Moser equation described the high series reaction substrate consumption;Contois equation described in the high densityofcell growth;Blackman equation reflected in addition to the bottom store there may be other limiting factors;Logistic law belonged to the logic equations,it integrated said because of the lack of nutrients and toxic metabolite accumulation and cell concentration on the negative effectsofcell growth rate.

    3.2 Substrate Consumption Dynamics

    The substrate utilization rate or substrate decrease rate can be modeled with the following expression.

    d[S]/dt is the rate of formation.

    When matrix inhibited by its own bio-degradation,the Monod model above becomes unsatisfactory.In this case,someone made the following equation after their research.

    In some case,the effect of the cell growth is by a variety of substrates at the same time,its means the influence is also different.If there are two limiting substrate influence cellspecific growth rate at the same time,expressed by the following equation.

    μmis the maximum specific growth rate when the two substrates also enough;Ks1、Ks2is the two substrates saturated coefficient.

    If there are n kinds of restrictive substrates.

    If the two substrates can be used at the same time,and also can be substituted.

    μm1、μm2is the maximum specific growth rate at the two substrates,respectively.

    For n kinds of restrictive substrates.

    For more complex cases,the substrates can be divided into two kinds:one kind is necessary to cell growth,if lack of them,a cell cannot grow;another kind is promote cell growth,it can improve the specific growth rate of cells.

    [SI]is the promote cell growth substrate concentration;[SE]is the substrate concentration necessary to cell growth;μm0is the maximum specific growth rate when the promote growth substrates does not exist.

    3.3 Product Inhibition Growth Dynamics

    When microbial growth inhibited by its metabolites,expressed by the dynamics equations as follows:

    Kifor response inhibition constant,[P] is product concentration.

    Bryant is indicted that produce hydrogen-acetic-acid bacteria generate hydrogen increase hydrogen partial pressure suppresses the production of acetic-acid bacteria metabolic activity,if a large number of hydrolysis acid accumulation will lead to methane-producing bacteria activity decrease and even kill the bacteria.So build a new reactor online monitoring system to realize the real-time control of the reaction,ensure the anaerobic digestion progress smoothly.

    Some of the main empirical formulas is as follows.

    Aiba et al:

    KPIis the product inhibition constant.

    Hinshelwood:

    kPis the product inhibition rate constant.

    Levenspeil:

    [Pm]is the product concentration when the cells stop growing;n is the product toxicity indexis the apparent maximum specific growth rate.

    From Levenspiel equation,when [P] =[Pm]=0,cell stop growth,and when[P]=0,μm=

    4 Conclusions

    Food waste output increased dramatically in recent years.Its proportion of household waste becomes more and vaster,and organic matter content in the food waste is higher and the composition is more and more complex.Food waste dry anaerobic fermentation for waste reduction,harmless and recycling is great significance.Focus on the colder winter in northern China and low rate of gas,this article first analyzes the using probability of the food waste,and then sets about experimental study,optimizes the fermentation equipment and heating preservation method as the reference of the northern city life on the dry fermentation of the food waste.

    [1] Visvanathan C,Trankler J,Joseph K,et al.Municipal Solid Waste Management in Asia:Asian Regional Research Program on Environmental Technology(ARRPET)[M].Pathum Thani:Asian Institute of Technology Publication,2004:34-36.

    [2] You Y,Ren N Q,Wang A J,et al.Use of Waste Fermenting Liquor to Produce Bioflocculants with I-solated Strains[J].International Journal of Hydrogen Energy,2008,33(13):3295-3301.

    [3] Cho J K,Park S C.Biochemical Methane Potential and Solid State Anaerobic Digestion of Korean Food Wastes[J].Bioresource Technology,1995,52(3):245-253.

    [4] Hashimoto A G.Thermophilic and Mesophilic Anaerobic Fermentation of Swine Manure[J].Agric Wastes,1983,6(3):175-191.

    [5] Chea Eliyan.Anaerobic Digestion of Municipal Solid Waste in Thermophilic Continuous Operation[J/OL].(2007-04-27).http://www.faculty.ait.ac.th/visu/Data/AIT-Thesis/Master%20Thesis%20final/chea%20combined.pdf.

    [6] Polprasert C.Organic Waste Recycling Technology and Management[M].America:John Wiley &sons,1996:78-80.

    [7] Zhang R H,EI-Mashad H M,Hartman K,et a1.Characterization of Food Waste as Feedstock for Anaerobic Digestion[J].Bioresource Technology,2007,98(4):929-935.

    [8] Jay Chand Shiv.Techno-economic Feasibility Evaluation of Conversion of Food Waste toEnergy Through Anaerobic Digestion and Gasification[EB/OL].(2009-08-10).http://www.uea.ac.uk/env/all/teaching/eiaams/pdf_dissertations/2009/Shiv_Jay.pdf.

    [9] De Baere L.Anaerobic Digestion of Solid Waste:State-of-the-art[J].Water Science and Technology,2000,41(3):283-290.

    [10] Chae K J,Jang A,Yim S K,et al.The Effect of Digestion Temperature and Temperature Shock on the Biogas Yields from the Mesophilic Anaerobic-digestion of Swine Manure[J].Bioresour Technol,2008,99(1):1-6.

    [11] Mace S,Bolzonella D,Cecchi F,et al.Comparison of the Biodegradability of the Grey Fraction of Municipal Solid Waste of Barcelona in Mesophilic and Thermophilic Conditions[J].Water Science and Technology,2000,48(4):21-28.

    [12] Forste-Carneiro T,Pérez M,Remero L I.Influence of Total Solid and Inoculum Concents on Performance of Anaerobic Reactors Treating Food Waste[J].Bioresource Technology,2008,99(15):6994-7002.

    [13] Jantsch T G,Angelidaki I,Schmidt J E,et al.Anaerobic Biodegradation of Spent Sulphite Liquor in a UASB Reactor[J].Bioresource Technology,2002,84(1):15-20.

    [14] Gerardi M.The Microbiology of Anaerobic Digesters[M].New Jersey:John Wiley and sons,Inc.,2003:186-189.

    [15] Chynoweth D P,Pullammanappallil P.Microbiology of Solid Waste[M].New york:Anaerobic Digestion of Solid Waste,1996:71-77.

    [16] Schieder D,Schneider R,Bischof F.Thermal Hydrolysis(TDH)as a Pretreatment Method for the Digestion of Organic Waste[J].Water Science and Technology,2000,41(3):181-187.

    [17] Goudar C,Strevett K,Grego J.Competitive Substrate Biodegradation During Surfactant-enhanced Remediation[J].Journal of Environmental Engineering,1999,125(12):1142-1148.

    [18] Goudar C T,Ganji S H,Pujar B G,et al.Substrate Inhibition Kinetics of Phenol Biodegradation[J].Water Environment Research,2000,72(1):50-55.

    日本欧美视频一区| 最近2019中文字幕mv第一页| freevideosex欧美| 日本黄色片子视频| 一级毛片 在线播放| 精品国产露脸久久av麻豆| 精品亚洲乱码少妇综合久久| 久久韩国三级中文字幕| 日本午夜av视频| 亚洲色图av天堂| 国产大屁股一区二区在线视频| 久久午夜福利片| 免费不卡的大黄色大毛片视频在线观看| 大话2 男鬼变身卡| 午夜免费观看性视频| 人妻少妇偷人精品九色| 欧美性感艳星| 国产午夜精品久久久久久一区二区三区| 精品少妇黑人巨大在线播放| 老熟女久久久| 中文乱码字字幕精品一区二区三区| 亚洲欧洲日产国产| 亚洲真实伦在线观看| 亚洲色图av天堂| 男人添女人高潮全过程视频| 水蜜桃什么品种好| 国产黄片视频在线免费观看| 色婷婷av一区二区三区视频| 国产男女超爽视频在线观看| 国产高清三级在线| 亚洲国产色片| 日本av手机在线免费观看| 国产成人91sexporn| 大话2 男鬼变身卡| 亚洲无线观看免费| 99热这里只有精品一区| videossex国产| 免费久久久久久久精品成人欧美视频 | 欧美xxⅹ黑人| 国产在线男女| 亚洲av综合色区一区| 久久国产亚洲av麻豆专区| 十分钟在线观看高清视频www | 亚洲精品乱码久久久v下载方式| 最后的刺客免费高清国语| 大片电影免费在线观看免费| 婷婷色麻豆天堂久久| 亚洲最大成人中文| tube8黄色片| 秋霞在线观看毛片| 免费观看性生交大片5| 男女免费视频国产| 干丝袜人妻中文字幕| 日日摸夜夜添夜夜爱| 亚洲怡红院男人天堂| 永久免费av网站大全| 久久女婷五月综合色啪小说| 久久 成人 亚洲| 国产成人免费无遮挡视频| 婷婷色综合www| 18禁在线无遮挡免费观看视频| 日本vs欧美在线观看视频 | 看免费成人av毛片| 国产黄片美女视频| av在线蜜桃| 性高湖久久久久久久久免费观看| 中文资源天堂在线| 久久精品国产亚洲av涩爱| 99国产精品免费福利视频| 韩国高清视频一区二区三区| 18禁在线无遮挡免费观看视频| 春色校园在线视频观看| 久久久久性生活片| 18禁动态无遮挡网站| 久久久久久久大尺度免费视频| 麻豆精品久久久久久蜜桃| 国产人妻一区二区三区在| 春色校园在线视频观看| 国产精品伦人一区二区| 国产视频内射| 91在线精品国自产拍蜜月| 国产黄片视频在线免费观看| 亚洲,一卡二卡三卡| 在线观看三级黄色| 国产视频首页在线观看| 久久韩国三级中文字幕| 好男人视频免费观看在线| 日本欧美国产在线视频| 秋霞在线观看毛片| 国产精品久久久久久久久免| 九九爱精品视频在线观看| 成年av动漫网址| 亚洲国产精品国产精品| 久久久久久久大尺度免费视频| 精品亚洲乱码少妇综合久久| 亚洲国产毛片av蜜桃av| 亚洲av成人精品一区久久| 80岁老熟妇乱子伦牲交| 亚洲精品一二三| 欧美区成人在线视频| 久久久亚洲精品成人影院| 亚洲精品亚洲一区二区| 国产爱豆传媒在线观看| 欧美精品一区二区大全| 久久国产乱子免费精品| 日韩制服骚丝袜av| 我要看日韩黄色一级片| 嫩草影院入口| 亚洲成人手机| 天堂8中文在线网| 美女国产视频在线观看| www.av在线官网国产| 亚洲av中文av极速乱| 色吧在线观看| 深爱激情五月婷婷| 一级av片app| 国产日韩欧美在线精品| 久久久久久久久久人人人人人人| 男女边吃奶边做爰视频| 亚洲国产色片| 亚洲性久久影院| 久久久亚洲精品成人影院| 精品久久久久久电影网| 国产精品久久久久久av不卡| 亚洲精品456在线播放app| 精品亚洲成a人片在线观看 | 美女xxoo啪啪120秒动态图| 大香蕉97超碰在线| 国产又色又爽无遮挡免| 蜜臀久久99精品久久宅男| 99久久中文字幕三级久久日本| 国内精品宾馆在线| 国产日韩欧美亚洲二区| 精品国产一区二区三区久久久樱花 | 国产av精品麻豆| 久久久午夜欧美精品| 精品午夜福利在线看| 日本一二三区视频观看| 成人美女网站在线观看视频| 久久国产精品大桥未久av | 97超视频在线观看视频| av卡一久久| 麻豆精品久久久久久蜜桃| 黄色欧美视频在线观看| 全区人妻精品视频| 欧美少妇被猛烈插入视频| 国产亚洲精品久久久com| 国产在线一区二区三区精| 91狼人影院| 国内少妇人妻偷人精品xxx网站| 日本vs欧美在线观看视频 | av卡一久久| 国产乱来视频区| 乱码一卡2卡4卡精品| 欧美激情极品国产一区二区三区 | 黄片wwwwww| 中国国产av一级| 国产精品久久久久成人av| 亚洲av不卡在线观看| av不卡在线播放| av线在线观看网站| 国产精品不卡视频一区二区| 国产成人freesex在线| .国产精品久久| 尾随美女入室| 欧美97在线视频| 久久国产精品男人的天堂亚洲 | 亚洲中文av在线| 人人妻人人看人人澡| 欧美日本视频| 国产在线免费精品| .国产精品久久| 亚洲国产高清在线一区二区三| 99视频精品全部免费 在线| 欧美精品人与动牲交sv欧美| 亚洲真实伦在线观看| 午夜福利在线观看免费完整高清在| 亚洲精品aⅴ在线观看| 亚洲av男天堂| 免费观看的影片在线观看| 亚洲美女搞黄在线观看| 日韩国内少妇激情av| 久久久久久九九精品二区国产| 色婷婷av一区二区三区视频| 2021少妇久久久久久久久久久| 99热这里只有精品一区| 高清午夜精品一区二区三区| 日本午夜av视频| 大香蕉97超碰在线| 观看免费一级毛片| 国产av码专区亚洲av| 久久99热这里只有精品18| 大片免费播放器 马上看| 欧美日韩亚洲高清精品| 欧美激情极品国产一区二区三区 | 久久6这里有精品| 欧美精品亚洲一区二区| 成人亚洲欧美一区二区av| 菩萨蛮人人尽说江南好唐韦庄| 国产精品一区www在线观看| 大又大粗又爽又黄少妇毛片口| 一级毛片黄色毛片免费观看视频| 国产亚洲最大av| 最近的中文字幕免费完整| 少妇精品久久久久久久| 精品人妻视频免费看| 99九九线精品视频在线观看视频| 一级av片app| 亚洲成人av在线免费| 男女下面进入的视频免费午夜| 久久综合国产亚洲精品| 成人美女网站在线观看视频| av在线观看视频网站免费| 欧美国产精品一级二级三级 | 99热这里只有精品一区| 夜夜看夜夜爽夜夜摸| 中国国产av一级| 麻豆乱淫一区二区| 青春草视频在线免费观看| 少妇人妻一区二区三区视频| 欧美xxxx黑人xx丫x性爽| 99热这里只有精品一区| 日韩av不卡免费在线播放| 一级片'在线观看视频| 一本一本综合久久| h日本视频在线播放| 国产成人91sexporn| 久久午夜福利片| 欧美日本视频| 国产一区二区在线观看日韩| av国产久精品久网站免费入址| 简卡轻食公司| 又爽又黄a免费视频| 制服丝袜香蕉在线| 成人漫画全彩无遮挡| 国产大屁股一区二区在线视频| 精品熟女少妇av免费看| 狂野欧美激情性xxxx在线观看| 老熟女久久久| 大话2 男鬼变身卡| 日日摸夜夜添夜夜爱| 中文字幕人妻熟人妻熟丝袜美| .国产精品久久| 成人18禁高潮啪啪吃奶动态图 | 色婷婷av一区二区三区视频| 国产老妇伦熟女老妇高清| 亚洲国产日韩一区二区| 色婷婷av一区二区三区视频| 久热久热在线精品观看| av天堂中文字幕网| 欧美日韩视频精品一区| 狂野欧美白嫩少妇大欣赏| 久久毛片免费看一区二区三区| 久久久成人免费电影| 日本一二三区视频观看| 性高湖久久久久久久久免费观看| 国产精品人妻久久久影院| 性色avwww在线观看| 久久婷婷青草| 街头女战士在线观看网站| 我要看黄色一级片免费的| 成人美女网站在线观看视频| 精品国产乱码久久久久久小说| 亚洲性久久影院| 日韩欧美 国产精品| 一边亲一边摸免费视频| 中文字幕人妻熟人妻熟丝袜美| 日本av免费视频播放| 国内精品宾馆在线| 九九在线视频观看精品| 18禁在线无遮挡免费观看视频| 中国美白少妇内射xxxbb| 亚洲av福利一区| 亚洲国产成人一精品久久久| 久久热精品热| av不卡在线播放| 看免费成人av毛片| xxx大片免费视频| 女性被躁到高潮视频| 久久女婷五月综合色啪小说| 国国产精品蜜臀av免费| 久久国产精品男人的天堂亚洲 | 午夜老司机福利剧场| 国产成人a区在线观看| 寂寞人妻少妇视频99o| 国产精品国产三级国产av玫瑰| 亚洲国产精品一区三区| 久久 成人 亚洲| 一本一本综合久久| 18禁动态无遮挡网站| h视频一区二区三区| 久久女婷五月综合色啪小说| 免费人妻精品一区二区三区视频| 又粗又硬又长又爽又黄的视频| 黄色怎么调成土黄色| 丰满少妇做爰视频| 天堂俺去俺来也www色官网| 成人综合一区亚洲| 精品酒店卫生间| 国产黄频视频在线观看| 国产精品免费大片| 99久久精品国产国产毛片| 直男gayav资源| 九草在线视频观看| 国产精品国产三级专区第一集| 在线观看美女被高潮喷水网站| 直男gayav资源| 国产高清不卡午夜福利| 日韩成人av中文字幕在线观看| 一级爰片在线观看| 午夜日本视频在线| 嫩草影院入口| 蜜桃久久精品国产亚洲av| 在线观看免费日韩欧美大片 | 1000部很黄的大片| 黄色怎么调成土黄色| 18+在线观看网站| 美女主播在线视频| 国产人妻一区二区三区在| 久久亚洲国产成人精品v| 婷婷色综合大香蕉| 特大巨黑吊av在线直播| 国产精品一区二区性色av| 久久综合国产亚洲精品| 国产成人精品一,二区| 人妻夜夜爽99麻豆av| 国产精品精品国产色婷婷| 国产欧美日韩一区二区三区在线 | 精品久久久久久久末码| 精品视频人人做人人爽| 国产精品一及| 最近2019中文字幕mv第一页| 日韩国内少妇激情av| 99热网站在线观看| 黄色视频在线播放观看不卡| 午夜免费观看性视频| 国产亚洲91精品色在线| 国产精品国产三级国产专区5o| 五月开心婷婷网| 丰满人妻一区二区三区视频av| 国产乱来视频区| 色综合色国产| 精品久久久久久电影网| a 毛片基地| 国产伦在线观看视频一区| 精品久久久久久久久亚洲| 春色校园在线视频观看| 国产成人freesex在线| 国产一区亚洲一区在线观看| 久久久久久久久久久丰满| 亚洲激情五月婷婷啪啪| 精品久久久久久久末码| 蜜桃在线观看..| 欧美日韩在线观看h| 国产亚洲一区二区精品| 老司机影院毛片| 少妇的逼好多水| 男人狂女人下面高潮的视频| 夜夜看夜夜爽夜夜摸| 国产视频首页在线观看| 亚洲无线观看免费| 亚洲熟女精品中文字幕| 色婷婷久久久亚洲欧美| 亚洲在久久综合| 日韩av免费高清视频| 国产无遮挡羞羞视频在线观看| 欧美三级亚洲精品| 在线观看免费高清a一片| 精品人妻在线不人妻| 观看av在线不卡| 曰老女人黄片| 啦啦啦 在线观看视频| 人人妻人人添人人爽欧美一区卜| 国产一区有黄有色的免费视频| 免费看十八禁软件| 免费在线观看视频国产中文字幕亚洲 | 亚洲精品一区蜜桃| 大型av网站在线播放| 精品一区二区三区av网在线观看 | 老司机影院毛片| 亚洲成人手机| 高清视频免费观看一区二区| 爱豆传媒免费全集在线观看| 欧美 日韩 精品 国产| 只有这里有精品99| 天天躁日日躁夜夜躁夜夜| 欧美黄色片欧美黄色片| 一本—道久久a久久精品蜜桃钙片| 亚洲精品在线美女| 亚洲美女黄色视频免费看| 亚洲自偷自拍图片 自拍| 亚洲欧美精品自产自拍| 国产激情久久老熟女| 美女中出高潮动态图| 日本av免费视频播放| 欧美 日韩 精品 国产| 婷婷色麻豆天堂久久| 不卡av一区二区三区| 国产三级黄色录像| 两个人看的免费小视频| www日本在线高清视频| 久久久久精品人妻al黑| 激情五月婷婷亚洲| 99re6热这里在线精品视频| 日韩av免费高清视频| 赤兔流量卡办理| 国产麻豆69| 日韩制服丝袜自拍偷拍| 久久精品亚洲av国产电影网| 久久精品亚洲熟妇少妇任你| 午夜福利在线免费观看网站| 久久99热这里只频精品6学生| 午夜免费观看性视频| 黄色片一级片一级黄色片| av在线app专区| 国产精品偷伦视频观看了| 老司机在亚洲福利影院| 肉色欧美久久久久久久蜜桃| 久久国产精品人妻蜜桃| 国产在线免费精品| 在线观看国产h片| 性色av一级| 亚洲天堂av无毛| 老司机在亚洲福利影院| 欧美日韩综合久久久久久| 亚洲av电影在线观看一区二区三区| 精品少妇黑人巨大在线播放| 欧美精品av麻豆av| 欧美日韩视频精品一区| 建设人人有责人人尽责人人享有的| 老熟女久久久| 别揉我奶头~嗯~啊~动态视频 | 久久精品久久久久久噜噜老黄| www.熟女人妻精品国产| 97精品久久久久久久久久精品| 一二三四社区在线视频社区8| 国产亚洲欧美精品永久| 女人高潮潮喷娇喘18禁视频| 亚洲综合色网址| 男人舔女人的私密视频| 欧美精品一区二区免费开放| 久久久久网色| 这个男人来自地球电影免费观看| 欧美精品啪啪一区二区三区 | 午夜免费男女啪啪视频观看| 精品欧美一区二区三区在线| 国产日韩欧美亚洲二区| e午夜精品久久久久久久| 97精品久久久久久久久久精品| 中文字幕人妻丝袜制服| 热re99久久国产66热| 欧美+亚洲+日韩+国产| 成年美女黄网站色视频大全免费| 男男h啪啪无遮挡| 久久精品aⅴ一区二区三区四区| 欧美精品av麻豆av| 80岁老熟妇乱子伦牲交| 日韩中文字幕视频在线看片| 久久毛片免费看一区二区三区| 成人国语在线视频| 在线观看人妻少妇| 伦理电影免费视频| 精品国产一区二区三区四区第35| 国产成人一区二区三区免费视频网站 | 婷婷色综合www| 欧美人与善性xxx| 久久久国产一区二区| 亚洲少妇的诱惑av| 后天国语完整版免费观看| 欧美日韩精品网址| 黄色一级大片看看| 国产精品久久久久成人av| videosex国产| 丁香六月欧美| 精品免费久久久久久久清纯 | 天天躁日日躁夜夜躁夜夜| 18禁国产床啪视频网站| 一区二区av电影网| 欧美国产精品va在线观看不卡| 亚洲精品久久久久久婷婷小说| 又黄又粗又硬又大视频| 大香蕉久久网| 最近手机中文字幕大全| 日韩熟女老妇一区二区性免费视频| 看免费av毛片| 国产av一区二区精品久久| 免费在线观看日本一区| 久久久久精品人妻al黑| 欧美精品av麻豆av| 久久女婷五月综合色啪小说| 久久久久久久精品精品| 人人妻人人爽人人添夜夜欢视频| 激情五月婷婷亚洲| 五月开心婷婷网| 国产一区二区 视频在线| 久久天堂一区二区三区四区| 亚洲国产欧美在线一区| 高清视频免费观看一区二区| 男女边吃奶边做爰视频| 亚洲欧洲精品一区二区精品久久久| 老司机在亚洲福利影院| 亚洲国产精品一区二区三区在线| 亚洲欧洲日产国产| av在线老鸭窝| 国产高清videossex| 亚洲第一av免费看| 一本色道久久久久久精品综合| 亚洲国产欧美日韩在线播放| 男人操女人黄网站| 建设人人有责人人尽责人人享有的| 大话2 男鬼变身卡| 黄网站色视频无遮挡免费观看| 久久久亚洲精品成人影院| 色婷婷久久久亚洲欧美| 亚洲人成77777在线视频| 亚洲,一卡二卡三卡| 亚洲久久久国产精品| 国产男女内射视频| 在线观看一区二区三区激情| 丰满迷人的少妇在线观看| 亚洲人成网站在线观看播放| 多毛熟女@视频| 在线亚洲精品国产二区图片欧美| 成人三级做爰电影| 国产日韩欧美亚洲二区| 欧美在线一区亚洲| 亚洲精品av麻豆狂野| 亚洲视频免费观看视频| 在线观看国产h片| 一区福利在线观看| 两个人看的免费小视频| 亚洲,欧美,日韩| 精品第一国产精品| 亚洲人成网站在线观看播放| 午夜福利视频精品| 久久精品人人爽人人爽视色| 久久国产精品人妻蜜桃| 成在线人永久免费视频| 91九色精品人成在线观看| 亚洲av电影在线进入| 国产精品久久久久久精品电影小说| 国产av精品麻豆| 亚洲精品国产av成人精品| 赤兔流量卡办理| 大码成人一级视频| 青春草视频在线免费观看| 成人国产av品久久久| 秋霞在线观看毛片| 母亲3免费完整高清在线观看| 国产精品99久久99久久久不卡| 大话2 男鬼变身卡| 在线亚洲精品国产二区图片欧美| 爱豆传媒免费全集在线观看| 国产真人三级小视频在线观看| 久久精品久久精品一区二区三区| 老汉色av国产亚洲站长工具| 在现免费观看毛片| 在线看a的网站| 国产成人欧美| 日本一区二区免费在线视频| h视频一区二区三区| av一本久久久久| 最近中文字幕2019免费版| 午夜福利视频精品| 亚洲精品日韩在线中文字幕| 黄网站色视频无遮挡免费观看| 18禁裸乳无遮挡动漫免费视频| 少妇粗大呻吟视频| 美女扒开内裤让男人捅视频| 午夜影院在线不卡| 看免费av毛片| 19禁男女啪啪无遮挡网站| 黄色视频在线播放观看不卡| 成年美女黄网站色视频大全免费| 99国产精品一区二区三区| 别揉我奶头~嗯~啊~动态视频 | 午夜91福利影院| 国产精品偷伦视频观看了| 亚洲国产成人一精品久久久| 午夜老司机福利片| 激情视频va一区二区三区| 麻豆国产av国片精品| 久久人人97超碰香蕉20202| 一区在线观看完整版| 99久久综合免费| 1024香蕉在线观看| 日韩大片免费观看网站| 一个人免费看片子| 久久精品久久久久久噜噜老黄| 2021少妇久久久久久久久久久| 免费高清在线观看日韩| 大片免费播放器 马上看| 又大又爽又粗| 美女视频免费永久观看网站| 婷婷色综合大香蕉| 久久精品aⅴ一区二区三区四区| 久久影院123| 男女床上黄色一级片免费看| 久久精品亚洲熟妇少妇任你| 国产成人精品久久久久久| 男人爽女人下面视频在线观看| 观看av在线不卡| 国产爽快片一区二区三区| 久久精品久久久久久噜噜老黄| 国产黄色视频一区二区在线观看| 亚洲av国产av综合av卡| 亚洲精品一卡2卡三卡4卡5卡 | 亚洲av成人不卡在线观看播放网 | 日韩人妻精品一区2区三区| 91九色精品人成在线观看| 亚洲美女黄色视频免费看| 午夜视频精品福利| 亚洲欧美成人综合另类久久久| 蜜桃在线观看..| 国产av国产精品国产|