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Impingement scrubber

An impingement scrubber is designed to make the dust particles impinge and adhere to water droplets. Gas is introduced at the bottom and passes up through water-covered perforated trays, where dust is removed by the scrubbing liquid. [Pg.1247]

Figure 4-60. Impingement scrubber. Courtesy of Peabody Engineering Corp. Figure 4-60. Impingement scrubber. Courtesy of Peabody Engineering Corp.
Total enclosure Wet scrubbing Absorption tower Fluidized bed scrubber Impingement scrubber Irrigated target scrubber Pressure spray scrubber Rotary scrubber ... [Pg.350]

FGD is used to control S02 emissions from coal and oil combustion from electric utilities and industrial sources. Impingement scrubbers are one wet scrubber configuration used to bring exhaust gases into contact with a sorbent designed to remove the S02. On occasion, wet scrubbers have been applied to S02 emissions from processes in the primary non-ferrous metals industries (e.g., copper, lead, and aluminum), but sulfuric acid or elemental sulfur plants are more popular control devices for controlling the high S02 concentrations associated with these processes. [Pg.232]

The most common types of wet scrubbers are spray towers, venturi scrubbers, packed bed scrubbers and impingement scrubbers. Spray towers are the simplest, least expensive, however not very efficient, tar separation devices [23]. [Pg.337]

Entrainment separation is accomplished with inertial separators, which are usually cyclones or impingement separators of various forms. If properly designed, these devices can remove virtually all droplets of the sizes produced in scrubbers. However, reentrainment of liquid can take place in poorly designed or overloaded separators. [Pg.1591]

Smelt tanks Particulates (mist or dust) Demisters, venturi, packed tower, or impingement-type scrubbers... [Pg.2176]

These scrubbers have had limited use as part of flue gas desulfurization (FGD) systems, but the scrubbing solution flow rate must be carefully controlled to avoid flooding. When absorption is used for VOC control, packed towers are usually more cost effective than impingement plate towers (discussed later). [Pg.448]

PM Impingement-plate tower collection efficiencies range from 50 to 99 percent, depending upon the application. This type of scrubber relies almost exclusively on inertial impaction for PM collection. Therefore, collection efficiency decreases as particle size decreases. Short residence times will also lower scrubber efficiency for small particles. Collection efficiencies for small particles (< 1 fim in aerodynamic diameter) are low for these scrubbers hence, they are not recommended for fine PM control. [Pg.455]

PM Control - An impingement-plate scrubber is a vertical chamber with plates mounted horizontally inside a hollow shell. Impingement-plate scrubbers operate as eountercurrent PM collection devices. The scrubbing liquid flows down the tower while the gas stream flows upward. Contact between the liquid and the particle-laden gas occurs on the plates. The plates are equipped with openings that allow the gas to pass through. Some plates are perforated or slotted, while more complex plates have valve-like openings. [Pg.457]

The simplest impingement-plate scrubber is the sieve plate, which has round... [Pg.457]

Scrubbers Wet Cyclonic, Packed Tower, Impingement, and Venturi... [Pg.1244]

Operation Concentration Particle Sizes Gravity Impinge- ment Cyclone Scrubbers Electrical... [Pg.235]

Sizing, 451, 453, 455, 459, 462 Sonic flow, 461 Types, illustrations, 411-421 Rupture disk, liquids, 462, 466 Rupture disk/pressure-relief valves combination, 463 Safely relief valve, 400 See Relief valve Safety valve, 400, 434 Safety, vacuum, 343 Scale-up, mixing, 312, 314—316 Design procedure, 316-318 Schedules/summaries Equipment, 30, 31 Lines, 23, 24 Screen particle size, 225 Scrubber, spray, 269, 270 Impingement, 269, 272 Separator applications, liquid particles, 235 Liquid particles, 235 Separator selection, 224, 225 Comparison chart, 230 Efficiency, 231... [Pg.630]

In wet scrubbing the dust is removed by counter-current washing with a liquid, usually water, and the solids are removed as a slurry. The principal mechanism involved is the impact (impingement) of the dust particles and the water droplets. Particle sizes down to 0.5 /i.m can be removed in suitably designed scrubbers. In addition to removing solids, wet scrubbers can be used to simultaneously cool the gas and neutralise any corrosive constituents. [Pg.459]


See other pages where Impingement scrubber is mentioned: [Pg.531]    [Pg.70]    [Pg.408]    [Pg.724]    [Pg.1060]    [Pg.1066]    [Pg.1068]    [Pg.1293]    [Pg.337]    [Pg.85]    [Pg.50]    [Pg.1074]    [Pg.1082]    [Pg.1084]    [Pg.1268]    [Pg.531]    [Pg.70]    [Pg.408]    [Pg.724]    [Pg.1060]    [Pg.1066]    [Pg.1068]    [Pg.1293]    [Pg.337]    [Pg.85]    [Pg.50]    [Pg.1074]    [Pg.1082]    [Pg.1084]    [Pg.1268]    [Pg.1430]    [Pg.1593]    [Pg.1596]    [Pg.471]    [Pg.440]    [Pg.442]    [Pg.455]    [Pg.457]    [Pg.530]    [Pg.254]    [Pg.642]    [Pg.235]    [Pg.213]   
See also in sourсe #XX -- [ Pg.1247 , Pg.1248 , Pg.1450 ]




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