scholarly journals Integrating external costs with life cycle costs of emissions from tertiary treatment of municipal wastewater for reuse in cooling systems

2016 ◽  
Vol 112 ◽  
pp. 4733-4740 ◽  
Author(s):  
Ranjani B. Theregowda ◽  
Radisav Vidic ◽  
Amy E. Landis ◽  
David A. Dzombak ◽  
H. Scott Matthews
2013 ◽  
Vol 3 (3) ◽  
pp. 224-238 ◽  
Author(s):  
Ranjani Theregowda ◽  
Ming-Kai Hsieh ◽  
Michael E. Walker ◽  
Amy E. Landis ◽  
Javad Abbasian ◽  
...  

Life cycle costs (LCC) calculated using standard databases and first-stage cost estimation methods were used to compare selected tertiary treatment processes used to treat secondary treated municipal wastewater (MWW) for reuse in thermoelectric power plant cooling systems. Use of MWW increases challenges such as scaling, bio-fouling and corrosion. Tertiary treatment coupled with chemical inhibitors can enable use of MWW in cooling systems. To determine LCC for different treatment options, a life cycle conceptual costing (LC3) tool was developed to estimate costs within conceptual accuracy range (15–40%), defined by the International Association for the Advancement of Cost Engineering. LCC estimation showed that treatment alternatives with higher chemical consumption were most expensive. Operational phase of tertiary treatment and use of chemical conditioning agents dominates annual costs. Of various tertiary treatment alternatives evaluated, range of total costs to treat 7.75 million gallon/day (1 gallon = 3.79 L) – amount of water required by a 550 MW thermoelectric power plant recirculating cooling system – was estimated to be $0.91–1.32/kgal (2009 USD) excluding taxes and overhead costs. This range was found to lie between rate charged for river water withdrawal with filtration and chemical conditioning, i.e. an average of $0.74/kgal (2009 USD) for some areas of the USA, and the national average rate for potable city water, i.e. $2.95/kgal (2009 USD).


2003 ◽  
Author(s):  
Shayne Brannman ◽  
Eric W. Christensen ◽  
Ronald H. Nickel ◽  
Cori Rattelman ◽  
Richard D. Miller

2003 ◽  
Vol 3 (4) ◽  
pp. 145-152 ◽  
Author(s):  
H. Heinonen-Tanski ◽  
P. Juntunen ◽  
R. Rajala ◽  
E. Haume ◽  
A. Niemelä

Municipal treated wastewater has been tertiary treated in a pilot-scale rapid sand filter. The filtration process was improved by using polyaluminium coagulants. The sand-filtered water was further treated with one or two UV reactors. The quality changes of wastewater were measured with transmittance, total phosphorus, soluble phosphorus, and somatic coliphages, FRNA-coliphages, FC, enterococci and fecal clostridia. Sand filtration alone without coagulants improved slightly some physico-chemical parameters and it had almost no effect on content of microorganisms. If coagulants were used, the filtration was more effective. The reductions were 88-98% for microbial groups and 80% for total phosphorus. The wastewater would meet the requirements for bathing waters (2,000 FC/100 ml, EU, 1976). UV further improved the hygiene level; this type of treated wastewater could be used for unrestricted irrigation (2.2 TC/100 ml, US.EPA 1992). The improvement was better if coagulants were used. The price for tertiary treatment (filtration + UV) would have been 0.036 Euro/m3 according to prices in 2001 in 22 Mm3/a. The investment cost needed for the filtration unit was 0.020 Euro/m3 (6%/15a). Filtration with coagulants is recommended in spite of its costs, since the low transmittance of unfiltered wastewater impairs the efficiency of the UV treatment.


Water ◽  
2021 ◽  
Vol 13 (10) ◽  
pp. 1339
Author(s):  
Javier Bayo ◽  
Sonia Olmos ◽  
Joaquín López-Castellanos

This study investigates the removal of microplastics from wastewater in an urban wastewater treatment plant located in Southeast Spain, including an oxidation ditch, rapid sand filtration, and ultraviolet disinfection. A total of 146.73 L of wastewater samples from influent and effluent were processed, following a density separation methodology, visual classification under a stereomicroscope, and FTIR analysis for polymer identification. Microplastics proved to be 72.41% of total microparticles collected, with a global removal rate of 64.26% after the tertiary treatment and within the average retention for European WWTPs. Three different shapes were identified: i.e., microfiber (79.65%), film (11.26%), and fragment (9.09%), without the identification of microbeads despite the proximity to a plastic compounding factory. Fibers were less efficiently removed (56.16%) than particulate microplastics (90.03%), suggesting that tertiary treatments clearly discriminate between forms, and reporting a daily emission of 1.6 × 107 microplastics to the environment. Year variability in microplastic burden was cushioned at the effluent, reporting a stable performance of the sewage plant. Eight different polymer families were identified, LDPE film being the most abundant form, with 10 different colors and sizes mainly between 1–2 mm. Future efforts should be dedicated to source control, plastic waste management, improvement of legislation, and specific microplastic-targeted treatment units, especially for microfiber removal.


Author(s):  
Shuyan Zhang ◽  
Shuyin Duan ◽  
Fushuan Wen ◽  
Farhad Shahnia ◽  
Qingfang Chen ◽  
...  

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