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1.
灭多威的超声降解研究   总被引:12,自引:0,他引:12       下载免费PDF全文
研究了灭多威模拟废水在超声作用下的降解反应动力学、降解产物、降解途径、以及影响降解速率的因素等问题.结果表明,灭多威经超声作用35min,可被完全转换为无机物,其降解过程为假一级反应;浓度增加时,降解减慢;Fe  相似文献   

2.
超声在废水处理中的应用   总被引:17,自引:2,他引:15       下载免费PDF全文
超声波处理废水是一项新兴的废水处理技术,具有操作简单方便、降解速度快等优点,在处理毒性高、难降解的有机废水应用表现出广阔的前景。  相似文献   

3.
在超声波降解有机物溶液过程中,超声空化产生的高温高压以及空化泡振荡产生的激波在有机物溶液的降解中发挥重要作用.本文通过对超声波作用下气泡动力学的研究,讨论了超声波声压、频率、气泡初始半径等参量对有机物溶液降解效率的影响.研究发现.存在使降解效率极大的声压和频率.在空化稳定的情况下,存在一个使降解效率极大的气泡初始半径,降解效率随着黏滞系数的增大而减小.研究还发现,双频超声作用的空化效果比单频超声作用时强,与双频超声作用下有机物溶液降解率较大这一实验结果一致.  相似文献   

4.
功率超声在废水处理中的应用   总被引:5,自引:0,他引:5       下载免费PDF全文
熊宜栋 《应用声学》2002,21(4):33-35,32
采用不同强度和频率的超声波,对几种生物难降解的有毒污染物(苯胺,硝基苯)废水进行超声处理,实验表明,降解效果主要取决于超声波在反应液中的声强及处理时间,同时,若辅以通氧气或加入催化剂,处理效果更好,这就为设计相应的超声废水处理设备提供了实验基础。  相似文献   

5.
超声处理有机废水的现状与进展   总被引:2,自引:1,他引:1       下载免费PDF全文
从超声降解有机废水的机理入手,对当前单频和多频(二维正交和三维)超声以及超声技术与其他技术联用降解污水的原理、影响因素和效果和国内外研究现状进行了总结和回顾,同时对该技术在处理有机废水方面的研究趋势进行了展望。  相似文献   

6.
超声方法对于海藻酸钠的降解反应研究   总被引:1,自引:0,他引:1  
用超声方法对海藻酸钠溶液进行了降解研究,研究了各种因素对降解效果的影响,得出了聚合物溶液特性粘度与降解时间的经验公式。  相似文献   

7.
本文考察了用超声波降解水中溴苯的动力学与脱卤效应,并研究了重要的操作参数如强度与饱和气体,以及环境干扰因素如悬浮物、地表水其他杂质的影响。结果表明,超声波可以有效地处理溴苯,在20kHz,7.5W/cm2下一级反应常数达0.044/min,脱卤效率达58%。本研究范围内,声强度越高,反应越快。氧气和氩气下降解速率高于空气下。超声降解不受地表水中杂质、纳米级微粒、无机颗粒的影响,但有机悬浮物能在一定程度上干扰溴苯的超声降解。  相似文献   

8.
尹峰 《光谱实验室》2012,29(4):2531-2532
通过分光光度法测定了亚硝酸盐氮的含量,并从培养条件优化和游离氨抑制作用两方面考察了河底活性淤泥对水体中亚硝酸盐氮的生物降解情况;在最佳条件下,河水中亚硝酸盐氮的降解在2天内降解率可达83.7%.  相似文献   

9.
以东北某油田区内地下输油管道的泄漏区域作为典型研究区,通过静态降解实验模拟研究了石油类污染物在土著微生物作用下的自然降解规律。实验结果显示,天然情况下包气带介质中的生物降解效率可以达到67.03%,而含水层介质的生物降解效率为56.72%。石油类污染物在介质中的降解符合一级动力学方程,包气带介质中的降解速率常数为0.0298d-1,含水层介质中的降解速率常数为0.0226d-1。上述实验结果为开展研究区地下水土中石油污染的生物修复工作提供了可靠的理论依据。  相似文献   

10.
针对现有超声协同臭氧降解农药的研究多集中在20kHz至50kHz的频段内,而效果一直不够理想,以及目前民用的超声协同臭氧蔬果药残降解装置较少的问题,设计了一种160kHz超声协同臭氧蔬果药残降解仪。超声波发生器采用SG3525芯片驱动半桥式功率放大电路,并运用小范围扫频技术。臭氧发生器使用市场上量产的小型臭氧机。本文利用该降解仪进行了乙酰甲胺磷农药降解实验,对160kHz超声波协同臭氧的农药降解效果进行了初步研究,结果表明仪器对降解乙酰甲胺磷有效。  相似文献   

11.
《中国物理 B》2021,30(10):104302-104302
The present study analyzes the effect of stirring on ultrasonic degradation experiments through acoustic field distribution, which provides a guidance for further improvement of the degradation rate of organic solutions. It is known that in order to eliminate the standing wave field formed by ultrasonic radiation in the water tank, the liquid in the water tank needs to be stirred and the corresponding distribution of acoustic field is simulated by using the finite element method(FEM).The standing wave leads to an uneven distribution of the acoustic field when it is not stirred, and disappears after being stirred, which increases the cavitation area in the ultrasonic cleaning tank. Then, the degradation experiment with agitation is carried out. The experimental results show that the degradation rate of the solution is higher than that when there is no agitation, which confirms the importance of the acoustic field distribution to ultrasonic degradation. In addition, it is clear that with the increase of the stirring speed, the degradation rate increases first and reaches a maximum at 600 rpm before decreasing. Finally, the distribution of flow field is simulated and analyzed.  相似文献   

12.
Techniques such as solvent extraction, incineration, chemical dehalogenation, and biodegradation have been investigated for the degradation of hazardous organic compounds. We found ultrasound to be an attractive technology for the degradation of hazardous organic compounds in water. However, the effects of ultrasonic frequency on degradation rate constants were not investigated quantitatively. In this study, the degradation process of a model for hazardous organic compound methylene blue was investigated using ultrasonic irradiation. The study focused on the effects of ultrasonic frequency and ultrasonic power on the degradation rate constant. The apparent degradation rate constants were estimated based on time dependence of methylene blue concentration assuming pseudo-first-order kinetics for the decomposition. A linear relationship between the apparent degradation rate constant and ultrasonic power was identified. In addition, the apparent degradation rate constants at frequencies of 127 and 490 kHz were much larger than those at 22.8 kHz. A relationship between the apparent degradation rate constant and the sonochemical efficiency value (SE value) was also found. Based on these results, a simple model for estimating the apparent degradation rate constant of methylene blue based on the ultrasonic power and the SE value is proposed in this study.  相似文献   

13.
The present study comparatively investigated the ultrasonic degradation of ketoprofen (KET) and paracetamol (PCT) in water. Ultrasonic irradiation at 555 kHz achieved rapid degradation of KET and PCT in water, the removal efficiencies of KET (2.5–80 μM) and PCT (2.5–80 μM) reached 87.7%-100% and 50.6%-86.9%, respectively, after 10 min of reaction under an ultrasonic power of 60 W. The degradation behaviors of both KET and PCT followed the Langmuir-Hinshelwood model. KET was eliminated faster than PCT because of its higher hydrophobicity. Acidic media favored ultrasonic degradation of KET and PCT. Organic compounds in water matrices exerted a great negative effect on the ultrasonic degradation rates of KET and PCT major by competing with target compounds with the generated radicals at the bubble/water interfacial region. The effects of anions were species dependent. The introduction of ClO4 and Cl enhanced KET and PCT degradation to different extents, while the introduction of HCO3 posed a negative effect on both KET and PCT. KET and PCT degradation are accompanied by the generation of several transform intermediates, as identified via LC/MS/MS analysis, and corresponding reaction pathways have been proposed. A human umbilical vein endothelial cell (HUVEC) toxicity evaluation indicated that ultrasonic treatment was capable of controlling the toxicity of KET or PCT degradation. Of note, the enhanced formation of disinfection byproducts (DBPs), i.e., trichloromethane (TCM) and trichloronitromethane (TCNM), was found due to chlorination after ultrasonic treatment for both KET and PCT.  相似文献   

14.
A microbubble generator with a cylindrical hollow ultrasonic horn (HUSH), gas flow path, and an orifice inside it can produce high ultrasonic pressure around the generated microbubbles. We used this microbubble generator with a HUSH as a sonochemical reactor for the degradation of indigo carmine and evaluated the sonochemical reaction by simply inserting the horn end into a liquid. The experimental results revealed that the ultrasonic irradiation around ultrasonically generated microbubbles effectively degraded indigo carmine in water. In addition, degradation experiments performed by varying the ultrasonic power and gas flow rates indicated that a continuous gas supply and ultrasonic pressure were required for generating the microbubbles, without the generation of millimeter-scale bubbles, to enhance the sonochemical reaction in water.  相似文献   

15.
The degradation process and mechanism of p-chlorophenol in water using high frequency ultrasound (1.7 mHz) was investigated in this paper. The p-chlorophenol was degraded successfully in the high frequency ultrasonic device with low consumption of energy. The degradation effect was improved by increasing the solution concentration. No products or intermediate products were detected in the reaction mixture by the analytic methods of MS and 1H-NMR after ultrasonic irradiation. The dominant degradation mechanism is high temperature pyrolysis in ultrasonic cavities rather than free radical oxidation, and the experimental results can be explained completely according to pyrolysis mechanism.  相似文献   

16.
This paper describes the ultrasonic degradation of oxalic acid. The effects of ultrasonic power, H2O2, NaCl, external gases on the degradation of oxalic acid were investigated. Reactor flask containing oxalic acid was immersed in the ultrasonic bath with water as the coupling fluid. Representative samples withdrawn were analysed by volumetric titration. Degradation degree of oxalic acid increased with increasing ultrasonic power. It was observed that H2O2 has negative contribution on the degradation of oxalic acid and there was an optimum concentration of NaCl for enhancing the degradation degree of oxalic acid. Although bubbling nitrogen gave higher degradation than that for bubbling air, both gases (for 20 min before sonication and during sonication together) could not help to enhance the degradation of oxalic acid when compared with the degradation without gas passage.  相似文献   

17.
A simplified and energy-saving integrated device consisting of a microwave applicator and an ultrasonic homogenizer has been fabricated to generate liquid plasma in a medium possessing high dielectric factors, for example water. The microwave waveguide and the ultrasonic transducer were interconnected through a tungsten/titanium alloy stick acting both as the microwave antenna and as the horn of the ultrasonic homogenizer. Both microwaves and ultrasonic waves are simultaneously transmitted to the aqueous media through the tungsten tip of the antenna. The microwave discharge liquid plasma was easily generated in solution during ultrasonic cavitation. The simple device was evaluated by carrying out the degradation of the perfluorooctanoic acid (PFOA), a system highly recalcitrant to degradation by conventional advanced oxidation processes (AOPs). PFOA is 59% degraded in an aqueous medium after only 90 s of irradiation by the plasma. Intermediates were identified by electrospray mass spectral techniques in the negative ion mode.  相似文献   

18.
Sonolysis has been proposed as a promising treatment technology to remove per- and polyfluoroalkyl substances (PFASs) from contaminated water. The mechanism of degradation is generally accepted to be high temperature pyrolysis at the bubble surface with dependency upon surface reaction site availability. However, the parametric effects of the ultrasonic system on PFAS degradation are poorly understood, making upscale challenging and leading to less than optimal use of ultrasonic energy. Hence, a thorough understanding of these parametric effects could lead to improved efficiency and commercial viability. Here, reactor characterisation was performed at 44, 400, 500, and 1000 kHz using potassium iodide (KI) dosimetry, sonochemiluminescence (SCL), and sonoluminescence (SL) in water and a solution of potassium salt of PFOS (hereafter, K-PFOS). Then the degradation of K-PFOS (10 mg L−1 in 200 mL solution) was investigated at these four frequencies. At 44 kHz, no PFOS degradation was observed. At 400, 500, and 1000 kHz the amount of degradation was 96.9, 93.8, and 91.2%, respectively, over four hours and was accompanied by stoichiometric fluoride release, indicating mineralisation of the PFOS molecule. Close correlation of PFOS degradation trends with KI dosimetry and SCL intensity was observed, which suggested degradation occurred under similar conditions to these sonochemical processes. At 1000 kHz, where the overall intensity of collapse was significantly reduced (measured by SL), PFOS degradation was not similarly decreased. Discussion is presented that suggests a hydrated electron degradation mechanism for PFOS may occur in ultrasonic conditions. This mechanism is a novel hypothesis in the field of PFAS sonolysis.  相似文献   

19.
Degradation of Rhodamine B, a waste water dye effluent was studied under the influence of ultrasound. In the present study, optimization of this degradation was carried out with power parameters, namely, power density (W/ml) and power intensity (W/cm2) using different ultrasonic equipments. From the studies, it has been observed that the degradation does not increase indefinitely with an increase in the power parameters, but instead, it reaches an optimum value and then decreases with a further increase in the power parameters. Also, these optima were not the same in all the ultrasonic equipments in which these studies were carried out. Difference in the type of acoustic field generated may be responsible for the different power optima observed with different ultrasonic equipments. The comparative study of the degradation of Rhodamine B using various ultrasonic equipments establishes a relationship between the area-specific parameter (intensity) and the volume-specific parameter (density) of reactivity.  相似文献   

20.
Acoustic cavitation, induced by ultrasound, can be used to eliminate organic pollutants from water. This type of ultrasonic treatment of polluted water can be grouped with those generally referred to as advanced oxidative processes since it involves hydroxyl radicals. In this case these highly active species are generated from the dissociation of water and oxygen dissociation caused by cavitation bubble collapse. The cavitation induced degradation rates of organic compounds in water are mainly linked to their vapor pressure and solubility and here we will further explore these links by examining the degradation of a mixture of two materials with different physical properties, chlorobenzene and 4-chlorophenol. The results obtained when a dilute solution of a mixture of these compounds saturated with argon is subjected to sonication at 300 kHz, parallels previous observations achieved in an aerated aqueous medium at 500 kHz. The two compounds exhibit sequential degradation with the more volatile chlorobenzene entering the cavitation bubble and being destroyed first. The 4-chlorophenol degradation occurs subsequently only when the chlorobenzene has been completely destroyed. The two compounds exhibit different behavior when sonicated in water saturated with oxygen. Under these conditions the two compounds are degraded simultaneously, a remarkable result for which two explanations can be proposed, both of which are based on the formation of additional OH radical species: The ability to produce conditions for the simultaneous elimination of two organic compounds by the use of oxygen is of great importance in the developing field of ultrasonic water treatment.  相似文献   

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