Fort Walton Beach Council agenda — 06-09-09 regular — reading text

STATE OF FLORIDA COUNTY OF OKALOOSA This instrument was acknowledged before me this day of 2009 by Mike Anderson as Mayor, and Helen Spencer, as City Clerk, for the City of Fort Walton Beach, a political subdivision. They are personally known to me or have produced as identification. Signature of Notary Name of Notary typed, printed or stamped 15- Approved as to form: OKALOOSA COUNTY, FLORIDA M Attorney for Okaloosa County William J. Roberts, III, Chairman ATTEST: Clerk of Okaloosa County STATE OF FLORIDA COUNTY OF OKALOOSA This instrument was 2009 by William J. Roberts, the State of Florida, and Commissioners. He /she acknowledged before me this day of III on behalf of Okaloosa County, a political subdivision of as Chairman of the Okaloosa County Board of County is personally known to me or has produced as identification. Signature of person taking notary Name of notary typed, printed or stamped 16-  00 NN nn NN AmAm 00 ryry GG 7 m btj o 2 3H1A' 1 NI121V UZO v o z N o li pp Z d a t m Wya LL W w $ Wo= fix y U a E Eo m Q i hz a m8 s a Q 4f m W m O ; cQ Z 3! Q H ca J O 3 J L a Q C 3 r V F- 0 C O co LL v a L d vi o0 A+ LL J o  Appendix C List of Displace City of Ft. Walton Beach Employees, with Position Titles Joseph Jones Class " A" Wastewater Superintendent Larry Kilburn Class " B" Wastewater Supervisor Dan Enfield Class " C" Operator James Brown Class " C" Operator Bruce Burford Class " C" Operator Dean Crane Class " C" Operator Danon Austin Class " C" Operator Melissa Woodall Class " C" Laboratory Manager  r- l"— Luz cl jg, CL u ca C0: 0 0. 44 IS g Zo W Z; 0_ 0 Ol 4 rl*" tq 41 Ul 5 0 0 LO LU a CK; 6 N T3 F W C 0 z z z at am LLJ j ra LL C, 0 cr CL a tA co 6 to a, j Z f, v ir 01, Wn 0 14 vJ cl) 14 -W ' A L? ci 2 i 0 ".) . c m M 8 0 cz 5 i fl di m IN 41 01 0) E n wi L3 - C3 C' l- 282' S x:i o w v4 w w In ol Vn w UI V Ln 41 i CL  FOVALI are mom CL 140 0 Am w rp tll*m 411 a, ZV Ii") In In " P 10 ta zl U-1 All 0 r- Lf) C104 uj z OMMO z z t, M 4A aC tw Ll. Cr. CL U4 Z Z z : ui  APPENDIX E ARBENNIE PRITCHETT WRF Appendix E - The Arbennie Pritchett Water Reclamation Facility Okaloosa County is implementing a $ 65M program to construct the new 10 million gallon per day (mgd) Arbennie Pritchett Water Reclamation Facility (WRF) that will replace the aging Garniers Wastewater Treatment Plant (WWTP). The new WRF will provide new and improved technology, will have the capacity to serve a larger service area, will provide enhanced operational performance, and will remove the existing Garniers WWTP from the ever increasing residential congestion at its current location. The new WRF is under construction at the existing Garniers spray field property that is located on Eglin Air Force Base (AFB) property that is leased from the Air Force for this use. Construction is expected to be completed in September 2009. This program includes several elements Design -Build of the 10 mgd Arbennie Pritchett WRF Design and Construction of the 25 mgd Garniers Re -pump Station Design and Construction of 200 acres of rapid infiltration basins ( RIBs) Design and Construction of "tie -ins" and new piping and valves to convert 2 -20 -inch diameter reclaimed water force mains to raw sewer mains Design and Construction of new 36 -inch diameter raw sewer force main to the new Arbennie Pritchett WRF The new WRF will be designed to treat an influent average daily flow of 10 mgd and a peak hourly flow of 25 mgd, based on USEPA Class 1 Reliability Requirements. Provisions for future expansion to 15 mgd and 37.5 mgd respectively, have been incorporated in the design and construction of the headworks, ultra -violet light (UV) disinfection, and effluent pumping facilities. The new WRF will consist of four major process areas and support facilities as described below: Pretreatment Process Biological Treatment Process Effluent Management Biosolids Management Support Facilities Pretreatment Process The pretreatment processes are intended to provide gross removal of large solids and grit to protect downstream equipment. Pretreatment process components consist influent flow monitoring, influent composite sampling, mechanical and manual screening, screenings washing and dewatering equipment, grit removal and handling equipment, odor control, and septage receiving equipment. The pretreatment facilities have been designed and constructed to provide complete redundancy and have the hydraulic capacity to meet an average daily flow of 15 mgd and the future peak hourly flow of 37. 5 mgd. Biological Treatment Process The biological treatment process is intended to remove or reduce organic constituents, nutrients, and suspended solids from the wastewater. Treatment includes activated sludge bioreactors, secondary clarification, and return activated sludge ( RAS) and waste activated sludge (WAS) pumping. The process is designed and constructed to meet the influent loadings based on an average daily flow of 10 mgd and the future peak hourly flow of 25 mgd. The activated sludge bioreactor system is furnished to provide necessary biological treatment of the wastewater to meet permit conditions, and is designed to reduce carbonaceous biochemical oxygen demand ( CBOD), ammonia, nitrite, and nitrate to the prescribed effluent treatment levels,