Page 243 - Pipeline Pigging Technology
P. 243

Pipeline  Pigging  Technology


        PARAFFIN TREATMENT


         Paraffin  treating compounds are used for three main  reasons:

           (1) to reduce the viscosity of an oil as it cools while traversing a pipeline,
              so  that  if  flow  in  the  line  is  stopped  and  it  cools  to  ambient
              temperature, flow can be re-started within the burst strength of the
              pipe;
           (2) to minimize paraffin  deposition  on the walls of the pipe; and
           (3) to minimize plugging of instrumentation and metering equipment.

        High-viscosity oil is difficult  to pump, and can cause a major problem  if a
      line  is  shut  down  and  cools  off. Deposit  formation  reduces  the  effective
      diameter of the line with an increase in pressure drop  and a  corresponding
      reduction in line capacity.
        Two types of paraffin  treating compounds  are  used  in pipelines:  crystal
      modifiers and dispersants. Crystal modifiers function by distorting the growth
      and shape of paraffin crystals. The result is that when a waxy oil cools below
      its cloud point,  the paraffin  precipitates  as small, rounded, particles rather
      than acicular (needle-like) crystals. Needle-shaped crystals can interlock and
      form gels, greatly increasing the viscosity of the oil. Crystal modifiers change
      the paraffin crystal shape and surface energy, making it less likely to attach to
      the walls of the pipe, and to other wax crystals. Also, the crystal size remains
      so small that the crystals are less prone to sedimentation and agglomeration.
      For this reason, crystal modifiers are known as pour-point depressants or flow
      improvers.
        Dispersants  are surfactant compounds  which  alter the surface energy of
      paraffin  crystals,  making them  less  attractive  to  each  other.  Dispersants
     function by changing the interfacial energy between  the paraffin  crystal and
      the  solvent  oil, which  also make the  crystals less likely to deposit on  solid
      surfaces such as pipe walls. This leaves them dispersed in the oil solvent in a
      non-agglomerated  form.  Both crystal  modification and  dispersion  cause  a
      reduction in the rate of paraffin fouling on the walls of pipes. Typical use rates
     for both paraffin  compounds are in the range of 100 to 200 parts per million.
        Crystal modifiers must be continuously added at a temperature above the
      "cloud point"  of the  oil to  be  effective.  The cloud  point  of the  oil is that
      temperature  at  which  the  oil  becomes  "cloudy"  due  to  precipitation  of
     paraffin  crystals, and as such represents the solubility limit of paraffin  in  the
      oil. It is not the same as the "pour point" of the oil, which is the temperature
      at which  the oil no longer pours out of a beaker under standard conditions.
      Oil below  the pour point  is still pumpable.

                                       224
   238   239   240   241   242   243   244   245   246   247   248