“…Accordingly, there is a range of d p falling between the inertially-dominant and diffusive-dominant regimes, where neither the inertial nor diffusive mechanisms are effective, resulting in a minimum in E, often referred to as the "Greenfield gap" (Greenfield, 1957). This minimum falls, again, within 0:1 μm≲d p ≲10 μm as reported by several researchers (Gemci & Ebert, 1992;Kim et al, 2001;Lai, Dayan & Kerker, 1978;Lim, Lee & Park, 2006;Raj Mohan et al, 2008). Summarizing, the micron scale particle diameters that are most harmful to human lungs are the least effectively removed by wet scrubbers.…”
Section: Introductionmentioning
confidence: 55%
“…While generally effective, experimental and theoretical studies of wet scrubbers show that they perform poorly in the removal of micron-scale particles (Gemci & Ebert, 1992, Raj Mohan, Jain & Meikap, 2008. Plots of E versus particle diameter d p for wet scrubbers typically show a minimum in the micron scale region.…”
a b s t r a c tRan et al., 2014 developed the ultrasonic scrubber, a device which combines an ultrasonic standing wave field and a water spray to eliminate particles from a gas flow. This device, which is essentially a wet scrubber enhanced by ultrasound, was shown to significantly improve the scavenging of micron-scale particles compared to the use of a water spray alone. Herein a simulation of trajectories of the particles and spray drops in the ultrasonic scrubber are presented. These simulations and an associated model of the process are used to provide a mechanistic understanding of the enhanced scavenging observed in the ultrasonic scrubber.
“…Accordingly, there is a range of d p falling between the inertially-dominant and diffusive-dominant regimes, where neither the inertial nor diffusive mechanisms are effective, resulting in a minimum in E, often referred to as the "Greenfield gap" (Greenfield, 1957). This minimum falls, again, within 0:1 μm≲d p ≲10 μm as reported by several researchers (Gemci & Ebert, 1992;Kim et al, 2001;Lai, Dayan & Kerker, 1978;Lim, Lee & Park, 2006;Raj Mohan et al, 2008). Summarizing, the micron scale particle diameters that are most harmful to human lungs are the least effectively removed by wet scrubbers.…”
Section: Introductionmentioning
confidence: 55%
“…While generally effective, experimental and theoretical studies of wet scrubbers show that they perform poorly in the removal of micron-scale particles (Gemci & Ebert, 1992, Raj Mohan, Jain & Meikap, 2008. Plots of E versus particle diameter d p for wet scrubbers typically show a minimum in the micron scale region.…”
a b s t r a c tRan et al., 2014 developed the ultrasonic scrubber, a device which combines an ultrasonic standing wave field and a water spray to eliminate particles from a gas flow. This device, which is essentially a wet scrubber enhanced by ultrasound, was shown to significantly improve the scavenging of micron-scale particles compared to the use of a water spray alone. Herein a simulation of trajectories of the particles and spray drops in the ultrasonic scrubber are presented. These simulations and an associated model of the process are used to provide a mechanistic understanding of the enhanced scavenging observed in the ultrasonic scrubber.
“…However, in those cases where a high desulfurization ratio is required (e.g. desulfurization efficiency >95%, reported by Rajmohan et al [6][7][8] and Meikap et al [9,10]), a wet scrubber can be applied. Fig.…”
Section: Ca/s Molar Ratio Influence On Desulfurization Efficiencymentioning
confidence: 99%
“…Among these, the wet FGD process is the main technology used for flue gas desulfurization, which has the advantages of high desulfurization efficiency, high utilization rate of desulfurization reagents, and a stable operating environment [3][4][5]. Rajmohan et al reported the removal of SO 2 , as well as particulate pollutants, with an almost 99.99% efficiency [6][7][8]. Meikap et al achieved 100% SO 2 removal efficiency when employing a modified multi-stage bubble column scrubber [9,10].…”
“…These are critically discussed here for the broad interests of the future researchers in this chosen field of air pollution control. Particulate scrubbing in a countercurrent spray scrubber (Mohan, Biswas, et al 2008;Mohan, Jain, et al 2008), SO 2 scrubbing in a spray-cum-bubble column (Rajmohan et al 2008) and particulate scrubbing in a spray-cum-bubble column (Mohan and Meikap 2009) were reported that were questionable. On peer scrutiny of all these research studies revealed that these contained serious technical deficiencies coupled with language problems.…”
Industrialization tends to be accompanied by growing population and increasing awareness on environmental problems, making the use of pollution control equipment imperative. However, the air pollution is a complex phenomenon, as the pollutants distributed in the air are molecularly more random than in other media (soil and water). The control of air pollution, therefore, often becomes a more energy intensive process, leading to increased CO 2 emissions. Further, air pollution comprises particulate and gaseous pollutions requiring different control philosophies. When the control of both particulate and gaseous pollutants is required in a single step, the selection of equipment is further complicated. This article outlines how such complications could be avoided by developing an understanding on the criteria of selecting air pollution control devices. The advantages and disadvantages of all generic control devices are critically appraised for the better understanding by both the designers and users. Emission trading, bubble policy, and the recommendations of the World Bank Guidelines for controlling particulates, SO 2 , and NO X pollution are highlighted. The recent research on the development of air pollution control devices are appraised critically. Finally, the criteria on selecting equipment for controlling particulate-laden-gaseous pollution in a single step are critically elucidated with few case studies.
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