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On-Site Wastewater Treatment and Disposal Systems - Forced ...

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Anionic polyelectrolytes can be used in combination with the aluminum<br />

<strong>and</strong> iron salts to improve settling, but may overly complicate the onsite<br />

treatment system.<br />

The required dosages of aluminum <strong>and</strong> iron compounds are generally re-<br />

ported as molar ratios of trivalent metal salt to phosphate phosphorus.<br />

Molar ratios currently used in practice today range from 1.5:1 to 4:1,<br />

depending upon wastewater characteristics, point of addition, <strong>and</strong> de-<br />

sired phosphorus removal (20)(62).<br />

Adding aluminum or iron salts to the raw wastewater prior to the septic<br />

tank has the advantage of using the existing septic tank for sedimenta-<br />

tion (70). Aluminum or iron salts may be metered to the raw wastewater<br />

with a chemical feed pump activated by electrical or mechanical impulse.<br />

Mixing of the chemical with the wastewater is provided in the sewer line<br />

to the septic tank. The quantity of metal salt added to.the wastewater<br />

is dependent upon wastewater characteristics. Since the impulse to the<br />

feed pump may come from any of a number of household events, it is not<br />

possible to precisely adjust metal dosage. An average dose of salt<br />

based on estimated phosphorus discharge is most practical.<br />

Addition of iron or aluminum salts following the septic tank may also be<br />

considered. A batch -feed system could be employed whereby a preset<br />

chemical dose is provided when the wastewater reaches a preset volume in<br />

a holding tank. Mixing may be provided by aeration or mechanical mixer,<br />

followed by a period of quiescence. Additional raw wastewater flow<br />

would be diverted to a holding tank until the precipitation-sedimenta-<br />

tion cycle is completed. This system may be employed after the septic<br />

tank <strong>and</strong> preceding the intermittent s<strong>and</strong> filter.<br />

The processes briefly described above represent a few of the many chemi-<br />

cal treatment processes that might be considered for onsite treatment.<br />

They may be designed <strong>and</strong> constructed to fit the specific needs of the<br />

site, or purchased as a proprietary device. Storage <strong>and</strong> holding of<br />

chemicals must be considered in the design of these systems. Details on<br />

chemical storage, feeding, piping, <strong>and</strong> control systems may be found<br />

elsewhere (20)(62). Attention must be given to appropriate materials<br />

selection, since many of the metal salts employed are corrosive in<br />

liquid form.<br />

b. Operation <strong>and</strong> Maintenance<br />

Every effort should be made to select equipment that is easily operated<br />

<strong>and</strong> maintained. Nonetheless, chemical precipitation systems require<br />

semi-skilled labor to maintain chemical feed equipment, mixers, pumps,<br />

196

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