Page 435 - Fundamentals of Water Treatment Unit Processes : Physical, Chemical, and Biological
P. 435

390                            Fundamentals of Water Treatment Unit Processes: Physical, Chemical, and Biological



                   management of products, services, and production or  SCADA: An acronym for ‘‘supervisory control and data
                   delivery processes to ensure the attainment of oper-  acquisition.’’ Refers to data acquisition by elec-
                   ational performance, product, or both in keeping   tronic sensors for such quantities as pressure, tem-
                   with quality requirements (Symons et al., 2000,    perature,  specific  electric  conductivity,  pH,
                   p. 384).                                           turbidity, particle counts, dissolved oxygen, specific
            Quality control (QC): A system of functions carried out at a  ions, flow meters, etc. Signals are 4–20 mA and are
                   technical level for the purpose of maintaining and  proportional to the sensor reading and are transmit-
                   documenting quality. It includes such features as  ted to an analog board. The analog board transmits
                   personnel training, standard operating procedures,  the signal to a computer where it is interpreted in
                   and instrument calibrations (Symons et al., 2000,  terms of a calibration to read the actual value, for
                   p. 384).                                           example, 7.5 mg=L dissolved oxygen. Control is by
            Rapid filtration: Rapid filtration is defined here as a technol-  actuated valves that generally have on-off functions
                   ogy that provides the means to implement the ‘‘depth  but may, alternatively, regulate water flow. The
                   filtration’’ process. The technology includes the   computer sends a signal to a micro-dac board
                   under-drain system, the backwash system, the waste-  which contains a micro-relay. For an open valve
                   water system, the instruments, and the control sys-  the signal requires the relay to permit current to be
                   tem to permit the depth filtration process to work;  transmitted to the valve to perform the function
                   coagulation is the most important part of the process.  intended.
            Rate-of-flow controller: A valve in the effluent pipe from a  Single collector: A term that arises often in discussions of
                   filter under-drain system that regulates flow at a   modeling is the ‘‘single collector.’’ The term ‘‘single
                   given set-point by opening or closing the valve,   collector’’ refers to a single constricted cell, Happel’s
                   usually in small increments. The valve has associ-  sphere-in-cell, etc., that by their nature exclude the
                   ated with it a flow meter and that provides the signal  presence of neighboring grains. The effect is that the
                   for valve adjustment. At the start of the filter run,  viscous flow field, for example, as well as other
                   with the water level in the filter box at full depth, the  fields of a complex system, vis-à-vis a single col-
                   valve is near-closed and takes up most of the head-  lector, are not included in the model.
                   loss of the system. As the filter clogs, the valve opens  Slow sand filtration: Slow sand filtration is characterized by
                   further, reducing the valve headloss. As the run   low hydraulic loading rate, with consequent large
                   approaches termination, the valve opens fully, at  filter area and the raw water without coagulation is
                   which point all of the headloss occurs in the media  applied to the filter. Headloss increase is due to a
                   and none in the valve. For a declining rate filter  surface deposit on the top of the filter, called the
                   scheme the rate-of-flow controller valve is not     schmutzdecke. At terminal headloss, the bed is dewa-
                   needed, nor is it needed for a constant flow, rising  tered to just below the bed surface and the schmutz-
                   water level scheme. In every case a flow meter      decke is removed by scraping. Slow sand filtration is
                   should be installed in the pipe from the under-drain  characterized by both straining and depth filtration.
                   system for each individual filter.                  Straining occurs as ambient particles deposit on the
            Regime: A prevailing pattern of behavior or the pattern of a  surface of the filter bed, forming a schmutzdecke.
                   regulated system. Adapted from American Heritage   Depth filtration occurs as a portion of the ambient
                   Dictionary.                                        particles penetrate the filter bed. If the filter has been
            Remnant water: Remnant water is defined as backwash        in operation for some months, the granular particles
                   water that remains in the filter box after backwash  will have developed biofilms which then serve as
                   and includes water in the under-drain system, pore  collectors. At the risk of being simplistic, we might
                   water, and headwater.                              say that in rapid filtration we condition the particles
            Ripening: The first stage of a filtration cycle in which the  (by coagulation) and in slow sand filtration we con-
                   effluent turbidity or particle concentration declines  dition the collectors (by hoping for or promoting
                   with time toward a ‘‘steady state’’ level, say 0.05  growth of biofilms). Slow sand is a distinct technol-
                   NTU or say 10 particles=mL.                        ogy and is the topic of Chapter 13.
            Saturated zone: At the influent end of the filter (the top in  Specific solids deposit: The mass of solids deposit per unit
                   most cases), the influent flux of floc particles is   volume of filter bed, that is, pore volume plus solid
                                                                                                 3
                   received. As these particles adhere to the media   volume; units are kg solids per m filter volume.
                   grains and previously deposited particles, they  Standard temperature pressure: The most common stand-
                   occupy void space causing a higher interstitial vel-  ards for temperature and pressure are 258C and 101
                   ocity with a proportionately increasing rate of    325 kPa (1.00 atm), respectively; this condition is
                   shear. As the rate of shear increases, the rate of  designated STP, meaning standard temperature and
                   detachment of particles at some point equals the   pressure. In U.S. Customary units, the values are
                   rate of attachment. At this point the filter bed is  688F and 1.00 atm. In Europe, the common term
                   ‘‘saturated.’’                                     used is, ‘‘normal’’ temperature and pressure (NTP).
   430   431   432   433   434   435   436   437   438   439   440