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WWTPs

Holly s (Holly, Michigan) original Wastewater Treatment Plant, WWTP, was built a trickling filter plant built in 1957 and had a design flow of 500,000 gallons per day. As the community grew it became necessary to construct a new plant. The... [Pg.596]

Industrial park WWTP Cooling and low pressure Taiwan... [Pg.115]

The viability of producing regenerated water for industrial reuse purposes by means of tertiary treatment of WWTP effluents is illustrated in this section, through examples in N Spain. The demonstration has been performed in Spain. The industrial activities in the selected region showed that the potential industrial demand of regenerated wastewater accounted for 5.2 Hm yr which could be obtained from WWTP facilities located 5 km away of the industrial consumers,... [Pg.116]

As expected for a WWTP effluent, turbidity and E. coli are higher than the specific standards for industrial wastewater reuse included in the new Spanish Regulation of Regenerated Wastewater (RD 1620/2007). Other parameters, such as conductivity or TDS may result in too much high level considering some specific industrial uses of water [11]. Therefore further treatment of the WWTP effluent is needed before reuse. [Pg.117]

Table 3 Vuelta Ostrera WWTP effluent characterisation... Table 3 Vuelta Ostrera WWTP effluent characterisation...
Fig. 1 Integral hybrid process flow diagram MFAJV/NF for regeneration of WWTP effluents... Fig. 1 Integral hybrid process flow diagram MFAJV/NF for regeneration of WWTP effluents...
Table 4 Efficiency of the hybrid system MFAJV/NF in the reclamation process of WWTP wastewater for industrial reuse... Table 4 Efficiency of the hybrid system MFAJV/NF in the reclamation process of WWTP wastewater for industrial reuse...
Parameter WWTP effluent average value ME effluent UV effluent Regenerated water average value Average reduction (%)... [Pg.119]

The use of UV light has been selected as disinfection agent in this case study. The advantages of this technique have been explained previously [27], Total inactivation of the E. coll present in the WWTP effluent was achieved, as can be seen in Table 4 and pressure drop in the water line was increased in 0.1 bar. [Pg.119]

Although certain variability in the quality of the WWTP effluent was found, regenerated wastewater by the selected process resulted of a good constant composition in the measured parameters, with important reduction of all the measured pollutants. Disinfection by UV achieved almost 100% of effectiveness in the destruction of microorganisms ( . coll). Conductivity, turbidity or TDS parameters... [Pg.119]

Effluent pretreatment is necessary when RO is used as tertiary treatment in order to prevent membranes filters form being blocked or abraded. UF offers a powerful tool for the reduction of fouling potential of RO/NF membranes [57]. A typical pretreatment consist of a MF allowing the removal of the large suspended solids form the WWTP effluent followed by UF unit which removes thoroughly suspended solids, colloidal material, bacteria, viruses and organic compounds from the filtrated water. The UF product is sent to the RO unit where dissolved salts are removed. [Pg.121]

Table 5 Membrane specifications and operation conditions for UF stage in WWTP hybrid process for industrial reuse water reclamation... Table 5 Membrane specifications and operation conditions for UF stage in WWTP hybrid process for industrial reuse water reclamation...
Table 6 Efficiency of the hybrid system UF/RO in the reclamation of WWTP wastewater for ... Table 6 Efficiency of the hybrid system UF/RO in the reclamation of WWTP wastewater for ...
The opportunities offered by the state of the art in the development and apphca-tion of advanced technologies for water reclamation have been presented and illustrated by means of a general example representative of the abihty of using WWTP effluents as regenerated water source by means of combination of advanced technologies. [Pg.123]

Janssen AN, van Agtmaal J, van den Broek WBP et al (2008) Monitoring of SUR to control and enhance the performance of dead-end ultraflltration installations treating WWTP effluent. Desalination 231 99-107... [Pg.126]

Minutes/hours for example, storms affecting sewer systems, punctual discharges, river flow rate variations due to hydroelectric plants, residence time in a WWTP, etc. [Pg.131]

Months/years elicitation of works, percolation of spills into the soil, WWTP building/upgrading, annual rainfall regime, etc. [Pg.131]

While some of these dynamics are natural, others are due to technological systems, or to cultural/social behavior or changes. While some of them can be described with high precision (e.g., fluid dynamics in a pipe or WWTP efficiencies), others can be approached (e.g., prevision of water demand) or estimated with low precision (e.g., rainfall regime of next years). [Pg.131]

Effects of WWTP Inputs on Water and Nutrient Loads. 178... [Pg.174]

Effects of WWTP Inputs on In-Stream Nutrient Retention. 179... [Pg.174]

This chapter aims to review current knowledge on the effects of wastewater treatment plant (WWTP) inputs (as major nutrient point sources) on stream nutrient dynamics, with major emphasis on nutrient loads and in-stream nutrient retention, and to discuss its implications within the context of actual and future scenarios of water scarcity conditions. Following this introduction, the second section of this chapter describes water quality problems associated with wastewater inputs from urban areas and how they are faced within the context of increasing urbanization across the world and its higher impact on water availability. In the third section, we... [Pg.174]

Inputs from WWTP effluents can also affect the hydrologic and nutrient concentration regimes of recipient streams at different temporal scales. Daily variations of these parameters may be exacerbated in streams below the WWTP input by the diel patterns of the effluent discharge associated with plant operation [46]. In contrast, at the annual scale, seasonal variations of physical and chemical parameters upstream of the WWTP may be dampened by the constant input of additional water and nutrients from the WWTP. At its extreme, naturally intermittent or ephemeral streams may turn into permanent streams downstream of WWTPs [28, 30]. In these effluent-dominated streams, the relative contribution of WWTP inputs may vary widely on an annual basis, as shown by the 3-100% range measured in a Mediterranean stream [47]. Finally, WWTP inputs also cause shifts in the relative availability of N and P as well as in the relative importance of reduced and oxidized forms of N in the stream [30, 47]. The magnitude of these shifts depends on the level of wastewater treatment (i.e., primary, secondary, or tertiary treatment), the type of WWTP infrastructure (e.g., activated sludge reactor. [Pg.178]


See other pages where WWTPs is mentioned: [Pg.597]    [Pg.90]    [Pg.107]    [Pg.108]    [Pg.108]    [Pg.112]    [Pg.117]    [Pg.117]    [Pg.117]    [Pg.118]    [Pg.120]    [Pg.122]    [Pg.123]    [Pg.137]    [Pg.173]    [Pg.174]    [Pg.174]    [Pg.175]    [Pg.175]    [Pg.176]    [Pg.177]    [Pg.178]    [Pg.178]    [Pg.179]    [Pg.179]   
See also in sourсe #XX -- [ Pg.112 , Pg.173 , Pg.197 ]

See also in sourсe #XX -- [ Pg.319 ]




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Energy balances for WWTPs

Process trains for WWTPs

WWTPs removal rates

WWTPs water/nutrient loads

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