Page 441 - Industrial Power Engineering and Applications Handbook
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Switchgear and controlgear assemblies  13/41 5
             promptly drying in an oven. Air-drying paint therefore   For level of  biological chemical demand  (BOD)
             must  be  avoided as far as possible.
                                                         BOD is a measure of organic matter present in wastewater
                                                         and can be degraded with the help of biomass. The level
           Wastewater treatment                          of BOD, if it exceeds the permissible limits of 30 mgll,
           Rapid  industrialization  has  created  many  problems  for   will  render the wastewater septic and unsafe for use. A
           the treatment and disposal of industrial wastes which are   higher  level  of BOD.  when  detected, can  be  degraded
           mainly responsible for the pollution of rivers. ponds and   (neutralized) biologically with the help of biomass (micro-
           farmlands,  when  they  are  discharged  directly,  without   organism). The  biomass  consumes  and  degrades  the
           proper treatment.                             organic matter present in the effluent.
             The effluents from a paint  shop are slightly alkaline   Since the discharges  of  effluents from  such  a paint
           with  moderate  to weak  BOD concentration. They may   shop will generally he moderate the required BOD level
           also  contain  traces  of  heavy  metals  such  as  zinc  and   is automatically maintained without any further treatment.
           chromium which, if not trcated. can create environmental   Where required,  a  moderate additional  oxygen  supply,
           and health hazards by  harming crops,  subsoil drinking   for the growth of biomass, can be made available through
           water and aquatic tlora and fauna. These effluents must   aeration of  the  wastewater. This can  be  carried  out  by
           be meticulously treated and neutralized before discharging   passing oil-free compressed air through the effluent. The
           them into the drains. The method of treatment is simple   percolation of effluent dissolves additional oxygen from
           and can be performed along the following lines.   the  atmosphere  and helps  the  growth  of  bacteria.  The
             Figure A 13.1 I  illustrates a flow diagram of a simple   oxygen  requirement  would  be  about 2  kg/kg  of  BOD
           eftluent  treatment  plant.  Chemicals  are  fed  into  the   removed.
           treatment tanks for neutralizing. coagulation, flocculation   In  cases of  still  higher levels of  BOD an additional
           and detoxification. Sufficient air incorporation by means   supply of biomass may become essential. and this can be
           ot surface or diffused aeration is carried out to  replace   easily  obtained  from  cowdung or  municipal  waste. To
           the displaced oxygen in the waste waters. Figure AI 3.12   supplement biomass growth, nutrients such ac urea and
           zhows  the  layout  and  hydraulic  profile  of  a  typical   di-ammonium phosphate may  be added.
           eftluent  treatment  plant  which  can be  installed  for the   The  aeration  system  adopted  should  be  capable  of
           treatment  of  effluents  generated  from  a  medium-siLed   converting the organic waste into more  stable inorganic
           paint  shop. In the figure we have assumed about S MT/   form or to cellular mass. The effluent is aerated at  all
           day of sheet metal work being handled by the shop. The   possible  stages  as  shown  in  Figure A13.12.  The  flow
           actual sizes and numbers of tanks will depend upon the   from reaction  and aeration tank No. S after primary and
           amount  of  discharge  and  type  of  effluents.  In  Figure   chemical treatment is passed through the primary aedimen-
           A 13.12 the sizes given should be adequate for the size of   tation tank No. 6, where most of the soluble and colloidal
           paint  shop we have considered. The process in the flow   organic materials are metabolized by  n diverse group of
           diagram  would  be  capable  of  handling  all  qualities  of   bacteria to carbon dioxide and water. At the same time,
           MS  sheets.  The  brief  treatment  process  is  described   a sizeable fraction ofthe effluents converted into ;I  cellular
           below.                                        mass settle by  gravity sedimentation.

                       Toxic waste (strong waste from
                       electroplating  shop, spray booth
                       and passivation liquor)
                       Wash water from pre-treatment area
                       Wash water from scrubbet

                     Chemical dosing tanks
                    P9 9


                                                                                  Treated water
                    Y      \            ___                                              *

                             Agitator
                  __c
                  _I



                           Reaction tank              Sedimentation tank       Sludge drying beds
                                    Figure A13.11  Flow diagram - effluent-treatment plant
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