共查询到17条相似文献，搜索用时 171 毫秒
1.
采用天然碳酸钙中和烟气吸收酸性废水,研究中空纤维结晶膜蒸馏技术对中和后废水处理的效果。考察了料液温度、起始浓度、流速、pH值等因素对膜通量的影响。在选定的条件下对水样进行连续膜蒸馏处理。结果表明,在料液温度50℃,料液速度为18.5mL/min,pH值为7,运行18h后,浓缩溶液开始出现结晶,结晶效果较好。截留率均接近100%。 相似文献
2.
膜蒸馏处理糠醛废水的实验研究 总被引：2，自引：1，他引：1
采用中空纤维膜蒸馏技术研究了糠醛废水的膜蒸馏处理效果,考察了料液相的温度、醋酸浓度、流速、吸收液浓度等因素对处理效果的影响。结果表明：在温差为15℃、料液的浓度为0.306 mol/mL时,速度为8 mL/min;吸收液的质量浓度为25 g/L时,速度为3 mL/min。运行12 h后,料液的pH值由开始的1.9升高为5.1,醋酸的去除率为76.3％,糠醛的去除率为40.1％。此过程可降低料液中糠醛和醋酸的含量,减小了低分子量有机酸对微生物危害的影响,为后续生物处理奠定了基础。 相似文献
3.
以一体式膜生物反应器（SMBR）对生活污水进行处理，研究不同水力停留时间（HRT）条件下污泥浓度对有机物去除率的影响，并对所得试验数据进行曲线拟合，建立有机物去除率与污泥浓度的数学模型。试验结果表明：在溶解氧（DO）浓度为 2．0～3．0m g／L的条件下，HRT为3h、2h和 1h时，有机物去除率（η）随着污泥浓度的增大而增大，但当污泥浓度增大到 6000 m g／L时，η增大趋势逐渐减小，并趋于稳定。有机物去除率与污泥浓度的数学模型表明：有机物去除率（η）与水力停留时间（τ）、进水COD浓度（S0）和污泥负荷率（N S）等主要运行参数有关，并可以通过调节运行参数τ、S 0和 N S来达到所需要的COD去除率。 相似文献
4.
气态膜回收氰化物的研究 总被引：3，自引：0，他引：3
气态膜是一种新型的膜分离技术,适用于从水溶液中分离提取挥发性物质。本文对气态膜回收氰化物的迁移机理及各种影响因素进行了研究,结果表明：传质速率与料液浓度呈现线性递增关系;吸收液浓度、流速和料液浓度、流速在一定范围内影响传质速率;温度升高,传质加快;膜孔径及孔隙率增大,传质速率也随之增大。 相似文献
5.
若尔盖高原沼泽湿地CH4排放研究 总被引：26，自引：0，他引：26
若尔盖高原沼泽湿地海拔 3400 m，面积 4038km2，是我国面积最大的高原沼泽湿地分布区。2001年 5～9月的非冰冻期，其主要沼泽类型木里苔草沼泽的CH4排放通量范围是 0.51～ 8.20 m g/（m 2· h），平均值为 2.87 m g/（m 2· h）；乌拉苔草沼泽CH4排放通量范围是 0.36～10.04 m g/（m 2· h），平均值为 4.51 m g/（m 2· h）。在空间分布上，不同沼泽类型之间CH4排放通量具有一定的差异。在季节变化上，没有明显的排放高峰。根据代表性观测点的CH4平均排放量、日数和沼泽总面积推算，非冰冻期若尔盖高原沼泽湿地CH4的排放量为 0.052Tg/a。 相似文献
6.
以一体式膜生物反应器(SMBR)对生活污水进行处理,研究不同水力停留时间(HRT)条件下污泥浓度对有机物去除率的影响,并对所得试验数据进行曲线拟合,建立有机物去除率与污泥浓度的数学模型。试验结果表明:在溶解氧(DO)浓度为2.0～3.0mg/L的条件下,HRT为3h、2h和1h时,有机物去除率(η)随着污泥浓度的增大而增大,但当污泥浓度增大到6000mg/L时,η增大趋势逐渐减小,并趋于稳定。有机物去除率与污泥浓度的数学模型表明:有机物去除率(η)与水力停留时间(τ)、进水COD浓度(S_o)和污泥负荷率(N_s)等主要运行参数有关,并可以通过调节运行参数τ、S_o和N_s来达到所需要的COD去除率。 相似文献
7.
投加粉末活性炭对MBR运行性能的影响 总被引：4，自引：0，他引：4
试验研究比较了在相同的进水和运行条件下,反应器1(投加粉末活性炭,投加量为12.3 g,使其质量浓度达到1 100 mg/L)和反应器2(未投加粉末活性炭)的膜透水性及对污染物的去除效果,并分析了粉末活性炭可以提高膜过滤性能的相关机理。试验结果表明：反应器1的膜通量衰减速率明显小于反应器2;投加粉末活性炭改变了混合液的性质,也大大降低了混合液中胞外聚合物和微细胶体的含量,从而减缓了膜通量的下降速度,可以使系统长时间地以相对高的膜通量运行。 相似文献
8.
将混入污染物和杂质的地热尾水直接排向地表水体,会造成水、土环境污染,也会造成水资源的浪费。为高效减少地热尾水中污染物,实现供暖地热尾水的无害化排放,以林甸县花园镇供暖地热尾水为例,通过混凝沉淀、超滤、纳滤工艺开展供暖尾水处理的室内实验和中试试验研究,连续监测获取地热尾水各处理工艺运行参数,组合工艺稳定运行期间监测到溶解性总固体浓度由5 824.7 mg/L降为432.40 mg/L、氯化物浓度由3 010.13 mg/L降为194.16 mg/L、氟化物浓度由1.57 mg/L降为0.31 mg/L、硼浓度由4.04 mg/L降为1.62 mg/L。确定该区地热尾水处理的最佳组合工艺为采用超滤运行压力为0.1 MPa,纳滤膜为陶氏NF90,操作压力为0.60 MPa,进水量为0.8 m3/h。室内实验溶解性总固体去除率90.21%～92.49%,氯化物去除率91.63%～93.02%,氟化物去除率96.81%,硼去除率55.20%～55.69%。中试试验溶解性总固体去除率为92.62%;氯化物浓度200 mg/L,氯化物去除率为92.57%;硼浓度1.77 mg/L,硼去除率为55.7%,以上实验结果均达到相关规范标准。试验证明本工艺处理松嫩盆地北部林甸地热田供暖尾水是可行的,解决了供暖尾水处理中资源浪费和尾水回收利用的技术性问题,为地热资源可持续利用提供了新的途径。 相似文献
9.
实验以大洋多金属结核浸出渣(66%,质量分数)为主要原料、高岭土(21%)为粘结剂、蛭石(13%)为膨胀剂,研制出用于动态吸附废水中重金属离子的浸出渣颗粒。以造粒后的颗粒为吸附剂动态处理含Cu2 的模拟废水,研究发现溶液浓度、流速、pH值对动态吸附效果的影响,选定浸出渣颗粒动态处理重金属废水的工艺参数:造粒后浸出渣颗粒的比表面积为18.61 m2/g,当模拟废水中Cu2 溶液的初始浓度为27 mg/L、pH=5.35、出口流速为10 ml/h时,每克浸出渣颗粒可动态处理模拟废水114.3 ml,处理后溶液中阳离子的浓度≤0.5 mg/L,实验效果明显。 相似文献
10.
11.
A. H. Hassani Ph.D. R. Mirzayee S. Nasseri Ph.D. M. Borghei Ph.D. M. Gholami Ph.D. B. Torabifar M.Sc. 《International Journal of Environmental Science and Technology》2008,5(3):401-408
Dyestuffs removal from industrial wastewater requires special advanced technologies, since dyes are usually difficult to remove by biological methods. In this study nanofiltration process was used for removal of different dyestuffs from solutions. The rate of dye removal by spiral wound nanofiltration membrane in film thin composite MWCO=90 Dalton, was evaluated for four classes of dyes acidic, disperse, reactive and direct in red and blue dyes medium. Dye absorbance was measured by spectrophotometric method (2120 Standard Method 1998). Effects of feed concentration, pressure and total dissolved solids concentration were also studied. Results showed that increasing dye concentration lead to higher color removal up to 98 % and at different pressures for acidic and reactive blue were up to 99.7 %. Different types of dyes had no effect on dye removal and permeate flux. During 2 h. of the operation time, permeate flux decline was increased. Permeate fluxes for different types of red dyes were from 16.6 to 12.6 (L/m2/h.) and for blue dyes were from 16.6 to 10.45 (L/m2/h.). Presence of sodium chloride in dye solutions increased dye rejections nearby 100 %. Chemical oxygen demand removal efficiencies for reactive blue, disperse blue, direct and disperse red dyes were also approximately 100 %. 相似文献
12.
T. M. Patel K. Nath 《International Journal of Environmental Science and Technology》2014,11(5):1237-1248
Nanofiltration of ternary mixtures of sodium chloride and aqueous solutions of Reactive Black-5 was studied in two different modules, namely, flat sheet and spiral wound over a wide range of operating conditions. Hydrophilized polyamide membrane with molecular weight cutoff of 150 was used for the experiments. Combined effect of dye and salt concentration, trans-membrane pressure drop, initial pH of feed solution on the permeate flux, and observed retention were investigated. Extent of color removal, chemical oxygen demand (COD), total dissolved solid (TDS), and conductivity were determined to assess performance of the membrane. The experimental results showed that both the permeate flux and observed retention decreased with increase in dye as well as salt concentration in the feed. Permeate fluxes were lower at higher pH values. Substantial removal of color was achieved in the nanofiltration experiments with a marked reduction in COD and TDS. The process allowed the production of permeate stream with great reutilization possibilities. 相似文献
13.
J. L. Lin C. D. Dong C. W. Chen S. H. Chen T. E. Hsieh C. M. Kao 《International Journal of Environmental Science and Technology》2017,14(9):1919-1930
A two-stage system for octachlorinated dibenzo-p-dioxin (OCDD)-contaminated soil remediation was developed. Soil washing using emulsified oil (EO) was applied in the first stage for OCDD extraction followed by the second stage of bioremediation using P. mendocina NSYSU for remaining OCDD biodegradation. The major tasks included (1) determination of optimal soil washing conditions for OCDD extraction by EO, (2) evaluation of feasibility of OCDD biodegradation by P. mendocina NSYSU under aerobic cometabolic conditions using EO as the primary substrate, and (3) assessment of the effectiveness of OCDD removal using the two-stage system. During the soil washing stage, EO with two different oil-to-water ratios (1:50 and 1:200) and pore volumes were tested with initial soil OCDD concentration of 21,000 µg/kg. Results indicate that EO could effectively improve the solubility and desorption of OCDD in soils. Up to 74% of OCDD removal could be obtained after washing with 60 PVs of EO and dilution factor of 50. After the soil washing process, enriched P. mendocina NSYSU solution was added into the reactor to enhance the aerobic biodegradation of remaining OCDD in soils. P. mendocina NSYSU could use adsorbed EO globules as substrates and caused significant OCDD degradation via the aerobic cometabolic mechanism. Approximately 82% of the remaining OCDD could be removed after 50 days of operation, and P. mendocina NSYSU played important roles in OCDD biodegradation. Up to 87% of OCDD was removed through the EO washing and biodegradation process. The two-stage system is a potential technology to remediate dioxin-contaminated soils. 相似文献
14.
《Applied Geochemistry》2005,20(3):569-585
Constructed and natural wetlands can accumulate elevated levels of Se; however, few data are available on cost-effective methods for remobilization and removal of Se from these areas. A field experiment was conducted to assess the effectiveness of flooding on the removal of Se from dry surface sediments. The 83-m2 flood-experiment plot contained 10 monitoring wells, a water-quality minimonitor (continuous measurement of pH, specific conductance, water temperature, and dissolved O2), a down-hole Br electrode, and 2 pressure transducers. Flooding was initiated on August 27, 2002, and a Br tracer was added to water delivered through a pipeline to the flood plot during the first 1.2 h. Standing water depth in the flood plot was maintained at 0.3 m through September 1, 2002. The Br tracer data indicate a dual porosity system that includes fracture (mud cracks) and matrix flow components. Mean vertical water velocities for the matrix flow component were estimated to range from 0.002 to 0.012 m/h. Dissolved (less than 0.45 μm) Se increased from pre-flood concentrations of less than 10 μg/L to greater than 800 μg/L during flooding in samples from deep (2.0 m below land surface) ground water. Selenium concentrations exceeded 5500 μg/L in samples from shallow (0.8 m below land surface) ground water. Ratios of Se to Br in water samples indicate that Se moved conservatively during the experiment and was derived from leaching of near-surface sediments. Cumulative Se flux to the deep ground water during the experiment ranged from 9.0 to 170 mg/m2. Pre- and post-flood surface soil sampling indicated a mean Se flux of 720 mg/m2 through the top 15 cm of soil. Ground-water samples collected 8 months after termination of the flood experiment contained Se concentrations of less than 20 μg/L. The minimonitor data indicate a rapid return to chemically reducing conditions in the deep ground water, limiting the mobility of the Se dissolved in the water pulse introduced during the flood experiment. Ratios of Se to Br in deep ground-water samples collected 8 months after the experiment confirmed the removal of Se from the aqueous phase. Based on the median Se flux rate estimated during the experiment of 0.65 mg/h/m2 (n = 52), 7 flooding cycles would be required to meet the 4 μg/g remediation goal in surface soils from the SLWMA wetland. 相似文献
15.
胞外聚合物对膜生物反应器运行性能的影响 总被引：3，自引：1，他引：3
膜生物反应器处理污水过程中,依据胞外聚合物(EPS)、蛋白质、多糖、粘度等参数随时间的变化趋势以及对膜通量的影响,求出上述参数及蛋白质/多糖的比值与膜通量间的相关系数分别为0.28、0.57、0.38、0.14、0.70。结果表明:蛋白质/多糖的比值与膜通量的衰减速度两者相关系数最大。 相似文献
16.
采用Tween80溶液冲洗修复萘污染地下水,分析了Tween80溶液质量浓度和冲洗流速对修复效果的影响,并考察了Tween80溶液对萘的增溶效果及对萘在介质上吸附特性的影响。结果表明：萘和Tween80在中砂介质上的吸附分别符合线性吸附和F型吸附;Tween80增溶萘效果较好,10.0 g/L Tween80溶液中,萘的表观溶解度达到500 mg/L,约为水相饱和溶解度的17倍;确定Tween80洗脱萘的临界解吸质量浓度为2.0 g/L;不同质量浓度、不同冲洗流速修复萘污染地下水实验结果表明,10.0 g/L Tween80溶液、3.0 mL/min流速为最佳冲洗修复参数,萘的去除率达到90%以上。 相似文献
17.
A semi-empirical treatment of isothermal element partitioning caused by flow rate-dependent calcite growth from hydrothermal solutions yields element/Ca ratios that are qualitatively similar to those observed in calcite bands of the Pb-Zn banded ores from the Harz Mountains, Germany. The comparison of the calculations with the analytical results suggests that flow rates varied between episodes of calcite precipitation as well as during formation of individual bands. Based on a flow rate-dependent element partition coefficient, changing element/Ca ratios in precipitates from a hydrotherm are therefore not necessarily indicative of changing compositions of the fluid. The variations in element/Ca ratios to be envisaged could be as much as a factor of three.Notation
A
defined by Eq. 8
-
a, b
individual values of any element in Eq. 1
-
c
concentration in moles/m3
-
C
0
initial concentration moles/m3
-
i
running parameter
-
F
area of precipitation in m2
-
k
p
rate constant of pth order reaction in s · m3/molesp
-
R
linear (one-dimensional) growth rate in moles/m2 · s
-
p
order of growth reaction
-
s
distance from entry of solution in m
-
s
0
vertical extension of a vein in m
-
t
time in s
- v
flow rate of hydrothermal solution in m/s
- v0
standard flow rate in m/s
-
r
relative flow rate in multiple of v0
-
fraction of total precipitation
- 0
fraction of precipitation under reference conditions when the hydrothermal solution leaves the vein
-
defining the sign in Eq. 1 for elements that are en riched (= +1) or impoverished (= -1)
-
logarithmic partition coefficient in Eq. 10
-
(R)
logarithmic partition coefficient as a function of variable growth rate
- [ ], { }
concentration ratios of fluids and solids, respectively
-
EL/Ca
calculated ratio of El/Ca in the calcite surface zone after Eq. 11 相似文献