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Wet electrostatic precipitators

E. Bakke, "The AppHcation of Wet Electrostatic Precipitators for Control of Eiue Particulate Matter," Preprint, Symposium on Control of Tine Particulate Emissions from Industrial Sources, Joint U.S.-USSR Working Group, Stationay Source Air Pollution ControlTechnology, San Francisco, Calif, Jan. 15—18, 1974. [Pg.417]

Pot charging Particulates (dust), CO, HF, SO, CF4, and hydrocarbons High-efficiency cyclone, baghouse, spray towers, floating-bed scrubber, electrostatic precipitators, chemisorption, wet electrostatic precipitators... [Pg.2175]

Give preference to fabric filters over wet scrubbers or wet electrostatic precipitators (ESPs) for dust control. [Pg.134]

WET ELECTROSTATIC PRECIPITATOR (ESP) WIRE-PIPE TYPE AND OTHERS... [Pg.426]

Continuous-spray, parallel-plate, wet electrostatic precipitators... [Pg.427]

The power consumed to operate a wet electrostatic precipitator is much less than that required by most other methods of control. There are four areas in which power is consumed (1) electrostatic power, (2) fan power, (3) insulator heating power, and (4) pump power. The total electrostatic power input required for operation is 0.8 to 1.0 kW/1,000 ft of collection area. A comparable piece of equipment is a venturi scrubber with 50-in.wg pressure drop. The power required for this installation would be 6 to 7 kW/1,000 cfm. This would mean that approximately seven times the power would be needed to achieve the same amount of cleaning with a venturi scrubber as opposed to using a precipitator. [Pg.432]

E. Bakke, On the Application of Wet Electrostatic Precipitators for Control of Emissions from Soderberg Aluminum Reduction Cells, A.I.M.E. Meeting, Dallas, Texas, February 1974. [Pg.492]

A very important parr of the gas-deatimg process is the removal of the collected particles from the cleaning system. This should be as controlled as possible in order to avoid particle reenrrainmenr to the gas flow. This can be accomplished in the case of liquid particles such as acid fume or tar or oil smoke. olid particles are normally removed by periodic rapping of discharge and collection electrodes. Solid particles can also be removed with the aid of water, as is done in wet electrostatic precipitators. [Pg.1214]

There are three classes of electrostatic precipitators dry electrostatic precipitators (ESP), wet electrostatic precipitators (WEP), and ionizing wet scrubbers (IWS). [Pg.149]

Anonymous, Wet Electrostatic Precipitator Tames Oils, Gases and Fines, Chem. Engineering, July 23, 1973, p. 74. [Pg.286]

Wet Electrostatic Precipitator (ESP) Wire-Pipe Type and Others... [Pg.200]

Continuous-spray wet electrostatic precipitators have been applied on many applications, including ... [Pg.203]

Wet electrostatic precipitators (WESP) are used for removal of liquid contaminants such as sulfuric acid mist, aerosols, and particulate matter. The acid mist and aerosols are typically formed in a WGS by condensation of SO3. Unlike dry precipitators, wet precipitators do not require rapping to remove the dust. The collected mist and particulate matter form a liquid film that runs down a vertical collecting plate. In some cases, a continuous spray of liquid is used to prevent solids deposition on the collecting plates. [Pg.373]

Its dust is removed by aqueous scrubbing and wet electrostatic precipitation. [Pg.54]

The feed gases come from wet electrostatic precipitation... [Pg.68]

Particulate control is by means of either a wet scrubber or a wet electrostatic precipitator located after the condensing heat exchanger. The choice of particulate control equipment depends on the degree of control required. The particulate slurry collected by the scrubber or precipitator is circulated through a pug mill that de-waters and pelletizes the ash. The ash pellets are spread on the tree fields as a fertilizer. The ash content of the wood is less than 1% so that a maximum of 5 t/day are collected and pelletized. The particulate emission standard to be met for new wood fired power plants in the State of Wisconsin, for exan le, is based on best available control technology (BACT) and can be expected to be about 21 g/ 10 kj. [Pg.817]

If a wet method for collection is selected, such as a wet electrostatic precipitator, fiber-type self-draining mist eliminator, or wet scrubber, ammonia can be regenerated from the salt solution by reaction with a readily available metal oxide such as lime or zinc oxide with formation of a stable sulfur product for disposal. These metal oxides, however, as well as their reaction products, are insoluble and could cause deposition on heat transfer surfaces and/or clogging in the regenerating equipment. Therefore, as indicated in Figure 2, to ensure continuity and reliability of the process, a soluble metal oxide was utilized (in the form of sodium hydroxide solution) to regenerate the ammonia in the experimental work described. This procedure also allows more eflFective utilization of the metal oxide the soluble oxide (NaOH) can be regenerated in batch equipment outside the continuous portion of the process by reaction with either the aforestated insoluble reactants, lime, or zinc oxide. Better control is aflForded in a batch reactor with more eflBcient use of reactants. However, in full-scale equipment undersirable deposition of reactant and product may be controllable so that batch operation may not be necessary. [Pg.197]

List the advantages and disadvantages of wet electrostatic precipitator (WEP) usage. Solution... [Pg.365]


See other pages where Wet electrostatic precipitators is mentioned: [Pg.143]    [Pg.429]    [Pg.48]    [Pg.12]    [Pg.273]    [Pg.1175]    [Pg.40]    [Pg.55]    [Pg.812]    [Pg.820]    [Pg.363]    [Pg.363]    [Pg.365]    [Pg.381]    [Pg.445]    [Pg.1397]    [Pg.112]   
See also in sourсe #XX -- [ Pg.373 ]

See also in sourсe #XX -- [ Pg.154 ]




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