Page 446 -
P. 446

MEMBRANE PROCESSES                   13.43

        Membrane Cleaning System

        With few exceptions, all membrane systems are subject to fouling by one or more source
        water components and therefore require periodic cleaning. Membrane cleaning is usually
        performed  without removing membranes  from  the  pressure  vessels  or  the  system  (i.e.,
        cleaned in place).  A  cleaning system is designed to prepare  and recirculate chemical so-
        lutions through some of or all membrane modules at low pressure.
           The cleaning system can also be used to feed special membrane posttreatment chem-
        icals (not to be confused with membrane system posttreatment) that  sometimes are used
        to improve membrane performance. The cleaning system also serves to prepare and trans-
        fer membrane storage  solutions, or preservatives,  used  to prevent microbial growth  and
        in some cases to prevent freezing when the membrane system is shut down for extended
        periods, typically more than a week.
           The cleaning system for an RO or NF system should be designed to accommodate all
        cleaning and membrane storage  solutions expected to be used at the plant. Cleaning sys-
        tems typically consist of the following basic components:
        •  Tanks with mixers for holding cleaning solutions.
        •  A  pump providing sufficient head  to  circulate the  solution from the  tank through  the
          membrane system and back to the tank.
        •  A  cartridge filter to intercept any suspended solids present in the cleaning solution and
          prevent them from clogging the module flow passages.
        •  Piping and valves to transfer the solution to and from the train feed, permeate, and con-
          centrate  headers.  The  design  should  consider the  use  of removable piping  spools  or
          hoses  to  provide positive  air  break  in the  cleaning system  connection points.  An  air
          break prevents chemical  solutions from  entering the product header piping and being
          transported  to  downstream  product  facilities  when  the  membrane  system  is  being
          put back into service or when one train is being cleaned while other trains remain in
          operation.
        •  Instrumentation and control for proper system operation, including tank level, temper-
          ature  switches,  and a pH monitor.
        •  A  cleaning solution heating device (not always required), such as an immersion heater,
          to  increase  solution temperature  and  improve  the  efficiency of cleaning, particularly
          when cleaning with detergents.
        •  A  cleaning solution cooling device (usually not required), such as a heat exchanger ex-
          ternal to the cleaning solution tank or cooling coils inside the tank, if it is determined
          that  the  maximum solution temperature  needs to  be controlled.  The  need for  cooling
          increases when the cleaning solution makeup water is at relatively high temperature or
          the heat  energy expected  to  be  transferred  to  the  cleaning solution from the  cleaning
          pump while recirculating is too great.
          Typical design allows for  separate  cleaning of each  stage of a  multistage train. With
        large-capacity trains, individual sections of a stage can be designed to allow separate clean-
        ing, minimizing cleaning tank volume and pumping requirements.

        Residuals Disposal

        The designer must consider the least expensive, acceptable method of disposing of wastes
        generated  in both  pretreatment processes  and  residuals  resulting from  membrane treat-
        ment processes.
   441   442   443   444   445   446   447   448   449   450   451