3Pengertian DAFProses pengolahan air limbah atau air lainnnya dengan cara memisahkan endapan seperti minyak atau solidPemisahan tercapai oleh udara yang terlarut di dalam air di bawah tekanan, lalu udara dilepaskan pada tekanan atmosferik didalam tangki flotasi
4How DAF WorksAir under pressure is dissolved into water according to Henry’s Law of Dissolution.Releasing the pressure back to standard temperature and pressure via a special device creates millions of “microbubbles” approximately 30 to 100 microns in diameter.At an 8 percent recycle flow at 70 psig saturation pressure, the number of 40-micron-diameter bubbles created at 40°F is 681 million per gallon. At 68°F the number of bubbles per gallon is 530 million
13Full Flow Pressurization The entire influent feed stream is pressurized by a pressurizing pump and held in the retention tankThe system is usually applicable to the feed stream with suspended solids exceeding 800 mg/L in concentrationIt is not susceptible to the shearing effects caused by the pressurizing pump and the high pressure drop at the pressure release valveSuspended solids will flocculate rapidly with the addition of chemical coagulants in the inlet compartment in the presence of the released air
14Partial Flow Pressurization Only about 30–50% of the influent feed stream is pressurized by a high- pressure pump and held in the retention tank.Materials with low specific gravity can be removed with the partial flow pressurization system.The increased hydraulic flow on the flotation chamber due to the flow recirculation must be taken into account in the flotation chamber design.
15Recycle Flow Pressurization A portion (15–50%) of the clarified effluent from the flotation chamber is recycled, pressurized, and semisaturated with air in the retention tank.The system is usually employed in applications where preliminary chemical addition and flocculation are necessary ahead of flotation.This system is not recommended for use when the suspended solids are susceptible to the shearing effects of the pressurizing pump and the high- pressure drop at the pressure release valve.The suspended solids concentrations are low.
16Faktor-Faktor Yang Mempengaruhi Kinerja DAF Sifat PartikelUkuran PartikelDispersing AgentsKomposisi dan sifat InfluentArus CairanRasio A/SFloat Removal
17Sifat PartikelThe specific gravity is a characteristic of the particle or liquid to be abated or separated.It can easily be accepted that sand, for example, cannot be floated while voluminous material, such as activated sludge, or a water immiscible liquid such as oil, can be floated.
18Ukuran PartikelGenerally, floatability increases with the size of the particle.In many cases,the size of particles can be increased by flocculation with various chemical coagulants.
19Dispersing AgentsCertain wastewaters and liquids contain unusual concentrations of various chemicals, resulting in specific flotation problems or advantages.Surfactants, such as detergents, tend to alter the physical properties of the sludge particle surface to be floated.
20Komposisi dan sifat Influent The composition and nature of the influent is most important.Equalization of composition and flow improves the performance of the flotation unit.
21Arus CairanThe liquid currents are governed by the physical design and hydraulics of the flotation unit.This becomes a consideration in the design of the tank and hydraulic loadings of the flotation unit.
22Rasio A/SThe amount of air and the method of mixing the air with the material to be floated are functions of the design of a particular flotation unit.For a specific application, a definite amount of air is necessary for flotation.In thickening applications it has been shown that increased performance is obtained at higher A/S ratios.
24Float RemovalA float-removal mechanism must be designed to have adequate capacity to remove water carryover.Various items to be considered in this design are the depth of submergence of the scooping mechanism and the speed of scoop operation.
25Gas to Solids Ratio : Full Flow Pressurized System GinGoutQCfXQCrQCeGCorrection factor, F or f, because complete gas saturation of liquid is often not achieved in a pressurized retention tankP ≥ 2 atmF = 0,5 – 1,0P < 2 atmf = 0,167 – 1,0Henry’s law
26Gas to Solids Ratio : Partial Flow Pressurized System QCfXGQnCfGinGoutQCeQpCrGP ≥ 2 atmF = 0,5 – 1,0P < 2 atmf = 0,167 – 1,0The Qp/Q ratio ranges between 0.3 and 0.5
27Gas to Solids Ratio : Recycle Flow Pressurized System QrCrQCeGCfXGinGoutP ≥ 2 atmF = 0,5 – 1,0R = Qr/QP < 2 atmf = 0,167 – 1,0
28Air Solubility in Water at 1 Atm (a) Temp. oCAir Sol. (mL/L)28,81023,52020,13017,9
31Design Parameters Hydraulic loading rate Solids loading rate Air to Solids ratioRetention Tank Pressure
32Basic Design Concept The ratio of Q/As is also defined as the hydraulic loading rateVH = horizontal velocity (m/s),Q = influent flow rate (m3/s),Ac = cross-sectional area of a flotation chamber (m2)VT = vertical rise rate of suspended solids (m/s),D = effective depth of the flotation chamber (m),T = detention time (s),Q = influent flow rate (m3/s),AS = surface area of flotation chamber (m2)
33Basic Design Concept The D/W ratio is usually between 0.3 and 0.5 D = effective depth (m)W = effective width (m)L = effective length (m)The D/W ratio is usually between 0.3 and 0.5F′= factor for short circuiting and turbulence, assumed as 1.4.