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'Tws":'l <br /> of the the media, no sludge rising concerns, and withstanding shock loads better than the <br /> suspended growth process. The disadvantages of an attached growth process include poorer <br /> effluent quality in terms of BOD and TSS, odor production, clogging of distributors or bed, <br /> sloughing of biofilm, snail, mosquito and insect problems. <br /> The MBBR system is an enhanced activated sludge process with biomass attached on small bio- <br /> media suspended in mixed liquor. The MBBR combines the advantages of a suspended growth <br /> process and an attached growth process. Compared to the conventional activated sludge <br /> system, the MBBR has the advantage of providing a greater biomass concentration therefore <br /> increasing treatment capacity, no sludge bulking concerns, having more process operation <br /> stability, reduced sludge production, enhanced sludge settleability, and lower costs for <br /> operation and maintenance. Compared to the attached growth process, the MBBR has <br /> advantages in providing a good quality effluent, easily designed for nitrogen and phosphorus, <br /> more opportunities for contact with organic matter nutrients and air, no odor or mosquito/insect <br /> problems. <br /> Since there are no sludge bulking concerns and no odor and insect concerns, thus, LESS <br /> TECHNICAL SUPPORT AND OPERATING SKILLS ARE REQUIRED FOR DAILY OPERATION. This is <br /> critical for a small scale wastewater treatment facility, like the WCMCRWWTP. It is economically <br /> not reasonable to hire a professional management team for daily operations. <br /> The performance of the MBBR can be easily controlled by the sludge retention time (SRT) and <br /> oxygen supply. Basically, the inline DO monitoring controls the blower operation to provide <br /> enough oxygen. The amount of sludge wasting can control the biological system growth and <br /> normal functioning. The daily operation of the MBBR process can be automatically controlled <br /> and executed by the PLC. <br /> In our MBBR design for the WCMCRWWTP, the dissolved air floatation (DAF) was introduced to <br /> separate the microorganisms from the treated effluent. This completely solved the concerns of <br /> the solid water separation. <br /> The effluent from the secondary wastewater treatment process is being polished by the <br /> California Title 22 Water Recycling Criteria (WRC) accepted membrane filters. Since the <br /> previous secondary wastewater treatment process units have significantly removed the organic <br /> matter (BODS) and TSS, the membrane filter can expect lower organic loading, less biofouling <br /> concerns, less backwash and chemical cleanings. The membrane filter will screen most of the <br /> turbidity and microorganisms out of the system and produce tertiary recycling quality water (<_2 <br /> NTU) for irrigation use. <br /> The California Title 22 Water Recycling Criteria (WRC) accepted chlorination process will be <br /> used to disinfect the filtration effluent. The disinfected water is going to be discharged effeite-to <br /> . S4&4a. P1¢*G2 o H StrO ..V <br /> Wine Cup Motor Coach Resort WWTP Page 4 of 10 8/22/2007 <br /> Preliminary Design Report <br />