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WATER REMOVAL FROM SLUDGE IN A HORIZONTAL ELECTRIC FIELD 总被引:2,自引:0,他引:2
A new method for sludge dewatering was proposed, in which a horizontal electric field was applied in order to facilitate the dissipation of gases produced at electrodes and to keep the anode soaked in water during the dewatering process. The effects of operation conditions such as the magnitude of electric field strength, pH of aqueous phase, the pretreatment procedures including flocculation, freezing and heating on the water removal were examined, respectively. The morphological difference between the concentrated sludge produced by electrodewatering and by vacuum filtration was revealed with scanning electron microscopy, which shown that electrodewatering was effective in removing the capillary water in the sludge floc. At electric field strength of 1200 V/m, the sludge concentration could be increased from 3 to 8%(w/w), indicating that over 60% of water was removed from the sludge. Compared to those operated in a vertical electric field, the method described in the present study has the advantages in terms of high eficiency, simple structure and ease of operation. 相似文献
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《Drying Technology》2013,31(3-4):627-638
A new method for sludge dewatering was proposed, in which a horizontal electric field was applied in order to facilitate the dissipation of gases produced at electrodes and to keep the anode soaked in water during the dewatering process. The effects of operation conditions such as the magnitude of electric field strength, pH of aqueous phase, the pretreatment procedures including flocculation, freezing and heating on the water removal were examined, respectively. The morphological difference between the concentrated sludge produced by electrodewatering and by vacuum filtration was revealed with scanning electron microscopy, which shown that electrodewatering was effective in removing the capillary water in the sludge floc. At electric field strength of 1200 V/m, the sludge concentration could be increased from 3 to 8%(w/w), indicating that over 60% of water was removed from the sludge. Compared to those operated in a vertical electric field, the method described in the present study has the advantages in terms of high eficiency, simple structure and ease of operation. 相似文献
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Horizontal pipeline and tubular loop aerators are of interest for fermentation and waste water treatment and are ideally suited for continuous processing. A major drawback is that these pipeline contactors invariably operate in the “elongated bubble and plug” regime in which the mass transfer rate is low. This article evaluates the performance of a horizontal pipeline aerator fitted with nozzles equispaced along its length to enhance mass transfer rates by promoting turbulence and augmenting effective interfacial area. Such devices can also be advantageously used in long pipe lines as in the case of treating waste while it is being transported. Pressure drop and overall liquid-side mass transfer coefficient data are reported as functions of liquid (water) and gas flow rates and nozzle size and spacing. It is shown that for all the conditions studied, kLa = 0.026(ΔP/L)1.036 and that the pressure gradient is given by a simple correlation, provided an empirical parameter which characterises a nozzle is known. Preliminary investigations on the effect of surfactant ad the presence of suspended solids (size 75 μm) on mass transfer coefficient are also reported. Very high values of power dissipation can be achieved in such aerators without mechanically moving parts and high values of mass transfer coefficient can be realized. 相似文献
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Horizontal pipeline and tubular loop aerators are of interest for fermentation and waste water treatment and are ideally suited for continuous processing. A major drawback is that these pipeline contactors invariably operate in the “elongated bubble and plug” regime in which the mass transfer rate is low. This article evaluates the performance of a horizontal pipeline aerator fitted with nozzles equispaced along its length to enhance mass transfer rates by promoting turbulence and augmenting effective interfacial area. Such devices can also be advantageously used in long pipe lines as in the case of treating waste while it is being transported. Pressure drop and overall liquid-side mass transfer coefficient data are reported as functions of liquid (water) and gas flow rates and nozzle size and spacing. It is shown that for all the conditions studied, kLa = 0.026(ΔP/L)1.036 and that the pressure gradient is given by a simple correlation, provided an empirical parameter which characterises a nozzle is known. Preliminary investigations on the effect of surfactant ad the presence of suspended solids (size 75 μm) on mass transfer coefficient are also reported. Very high values of power dissipation can be achieved in such aerators without mechanically moving parts and high values of mass transfer coefficient can be realized. 相似文献
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陶瓷喷砂嘴的冲蚀磨损机理研究 总被引:3,自引:0,他引:3
以B4C和Al203/(W,Ti)C陶瓷材料制备喷砂嘴,以SiC和Al2O3作为冲蚀磨料进行了喷砂冲蚀试验。研究了陶瓷喷嘴材料的冲蚀磨损机理以及不同冲蚀磨科对陶瓷喷嘴冲蚀磨损的影响。结果表明:喷嘴材料的硬度对陶瓷喷嘴的冲蚀磨损起重要作用。在相同条件下,具有高硬度的B4C陶瓷喷砂嘴的磨损率较小,相对硬度较低的Al2O3/(W,Ti)C陶瓷喷嘴磨损率较大。B4C陶瓷喷嘴的主要磨损机理为脆性断裂,而Al2O3/(W,Ti)C陶瓷喷嘴的主要磨损机理为微观切削。冲蚀用磨科的硬度和粒度对陶瓷喷嘴的磨损也有一定的影响,磨料的硬度和粒度越大,陶瓷喷嘴的磨损速度加快。 相似文献
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The subject of this paper is the evaluation of the applicability of constant temperature anemometry (CTA) with a modified version of Delhaye's method to aerated stirred tanks. A calibration technique that takes into account the variation in medium temperature was developed and verified experimentally. The directional sensitivity of the conical film probe was investigated in a streamline flow field as well as in the impeller discharge stream in an stirred tank.
The reliability of the setup and the technique was verified through the comparison of the vertical and radial velocity profiles of water in a stirred tank with those obtained from the literature. The directional response of the conical probe follows the cosine law for intersection angles smaller than 45° in a streamline flow field, but the directional sensitivity in the impeller discharge stream is rather poor, owing to the rolling characteristics of flow in this region. Due to the inability to detect bubbles smaller than the sensing element of the conical probe, the CTA usually gives lower values of local gas holdup. However, this discrepancy is considered to have no influence on the velocity measurement. 相似文献
The reliability of the setup and the technique was verified through the comparison of the vertical and radial velocity profiles of water in a stirred tank with those obtained from the literature. The directional response of the conical probe follows the cosine law for intersection angles smaller than 45° in a streamline flow field, but the directional sensitivity in the impeller discharge stream is rather poor, owing to the rolling characteristics of flow in this region. Due to the inability to detect bubbles smaller than the sensing element of the conical probe, the CTA usually gives lower values of local gas holdup. However, this discrepancy is considered to have no influence on the velocity measurement. 相似文献
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采用浸没式超滤系统取代传统工艺中的砂滤系统处理西江原水,对比了新工艺(混凝沉淀+浸没式超滤工艺)与传统工艺(混凝沉淀+砂滤工艺)的出水水质,考察了浸没式超滤系统的对COD、氨氮、浊度和颗粒物的去除,研究了试验期间系统跨膜压力(TMP)变化,最后考察了化学清洗对膜污染的控制。结果表明,混凝沉淀+浸没式超滤工艺出水CODMn和氨氮含量略高于混凝沉淀+砂滤工艺,但均达到了GB 5749-2006和CJ 94-2005要求;对浊度处理效果优于混凝沉淀+砂滤工艺;系统运行48 d,TMP从16 kPa升高到34.5 kPa;采用HCl和NaClO进行化学清洗,可有效控制膜污染。 相似文献
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应用热膜风速仪测定搅拌槽内气—液两相流的流体力学参数 总被引:1,自引:0,他引:1
开发应用了恒温热膜风速仪(简称CTA)来测定搅拌槽内气-液两相流的局部气含率、液体的时均速度及脉动速度的均方根值。根据柱形热膜探头以及气-液搅拌槽内流体流动特性,改进了用电压概率密度法^[1]划分气-液搅拌槽内气液两相信号的方法,在此基础上得到了局部气含率、液体的时均速度及脉动脉动速度均方根值的计算公式。研究了热膜探头偏角及流体介质温度变化对热膜风速仪测量精度的影响,并对流体介质温度的影响进行了校 相似文献
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A model is proposed for interpreting micromixing experiments in a semi-batch reactor. In these experiments, a fast consecutive-competing reaction system is used A + B → R, R + B → S, B being added either dropwise or as a pulse into an excess of A. A segregation index Xs = 2ns/nB0 is measured after completion of the reaction for various locations of the injection point. The macroscopic flow pattern is assumed to be known, essentially characterized by the recirculation time tc. Micromixing then takes place within the cloud via a mechanism of interaction with the mean environment (IEM model, micromixing time tm). Experimental results published by Barthole et al. (precipitation of barium sulphate) and Bourne et al. (diazo coupling) are successfully interpreted by this model. The influence of stirring speed, injection volume, concentration of species and mode of injection (pulse or dropwise) are especially well accounted for. This model provides a simple method for predicting the influence of mixing on selectivity in semi-batch reactors. 相似文献
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The effect of acetic acid on the corrosion behavior of X 65 and C 1018 carbon steel in vapor-water two-phase stratified flow (Vsg: 2 m/s; Vsl: 0.1 m/s) at 2 bars total pressure, 1.54 bars CO2 partial pressure, pH 5.5, and 80°C was studied in a low pressure-high temperature multiphase flow horizontal loop using electrochemical and mass loss techniques. The liquid phase is composed of 1% NaCl aqueous solution containing different concentrations of acetic acid (500 to 5000 ppm total acetic acid), and the gas phase is composed of CO2-acetic acid-water vapor mixture. The corrosion rates, on both the top and bottom of the line, increase with increase in acetic acid concentration, which was attributed to the contribution of hydrogen ions by the free acetic acid to the cathodic reaction. Partial coverage of the metal surface by FeCO3 on both the top and bottom of the line is reported to be responsible for the observed localized corrosion. Surface analysis investigated with SEM and XRD is reported.
A vapor-liquid equilibrium model was developed for the system studied. 相似文献
A vapor-liquid equilibrium model was developed for the system studied. 相似文献
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污水处理厂UASB污泥处理的试验研究 总被引:5,自引:0,他引:5
UASB反应器已广泛用于处理各种废水,但用于处理污泥的方法尚未见有报道。本文讨论了常温下用活性污泥作种泥,培养颗粒污泥的可行性,并且得到了USAB反应器处理污泥的运行参数。 相似文献