Page 162 - Pipeline Rules of Thumb Handbook
P. 162

Pipeline Drying  149

           being internally sand blasted by using air or nitrogen to propel  clay, rust, and mill scale. Caution must be taken to ensure that
           the sand. This procedure, if properly executed, will leave the  short sections are cleaned each time so that high velocities
           pipeline dry upon completion.                         may be maintained; that large quantities of dry air or gas are
             After the pipeline has been dewatered, clay is blown into  available to sustain the high velocities; that the pipeline is dust
           short sections of the pipeline with a dry gas to absorb the  dry; that all sand has been removed from the pipeline after
           remaining water. The correct type of sand is then blown  the sand blasting is complete; and, that the pipeline facilities
           through the dust dry section at a high velocity to remove the  will not be damaged by the high velocity sand.







           Chemical cleaning


             Cleaning with chemicals is typically used for smaller diam-  Typically, chemical cleaning is more involved than other
           eter lines. A properly planned chemical cleaning operation  cleaning processes in that some special equipment will be
           can produce a very clean pipeline. Chemical cleaning will  required to safely handle the chemicals. Disposing of the
           remove rust from any internal pits. Chemical cleaning is  spent material will also present a problem. Care must be exer-
           accomplished by pushing a batch of hydrochloric acid and  cised in the selection of pigs to be sure they will not be con-
           water for rust removal, a neutralizer, and a passivator, all   sumed by the cleaning solution. Personnel safety must be
           separated by pigs, through the pipeline. This method will  carefully considered when choosing this method of pipeline
           leave a bright metal finish on the interior of the pipeline. If   cleaning.
           a pipeline is being converted for a different service, such as
           a crude oil line being converted to chemical service, a batch  Purging with gas. This method is seldom used for
           of detergent can be added behind the cleaning process to  pipeline cleaning since the amount of debris that will be
           remove any traces of the crude oil or other product.  removed is small. A high gas velocity is required.







           Pipeline drying


             Pipelines used to transport petrochemicals such as pro-  Air at +70°F with a humidity of 100% has a dew point of
           pylene and ethylene must be dried in order for the delivered  +70°F and holds approximately 1,253 pounds of water (150
           product to meet moisture specifications. Natural gas pipelines  gallons) per million standard cubic feet.
           are usually dried to a lesser extent to prevent the formation  The most common methods for drying pipelines are as
           of hydrates. It is not unusual for a petrochemical line to be  follows:
           dried to a dew point of -80°F. A typical dew point for a pro-
           pylene pipeline will be  -70°F. A carbon dioxide pipeline  • Drying with super dry air
           might be typically dried to a -40°F dew point. The natural  • Drying with methanol
           gas industry specifies dryness in pounds of water per million  • Drying with inert gas such as nitrogen
           standard cubic feet of gas. The table at the end of this section  • Internal sand blasting
           will enable you to convert from one method to the other.  • Drying with the medium to be transported
             Dew point, by definition, is the temperature at which water  • Vacuum drying
           vapor begins to condense out of a gas at atmospheric pres-
           sure. For example, at atmospheric pressure, water vapor  All of these methods may be applied to pipeline drying
           begins to condense out of a gas that has a moisture content  depending on the particular line and amount of dryness
           of seven pounds of water per million standard cubic feet at   required. No single method can be considered ideal for
           -39°F. Therefore, a gas that has a moisture content of seven  all situations. Many times, a combination of two or more
           pounds of water per million standard cubic feet has a dew  methods will be used to achieve a dry pipeline at the least
           point of -39°F.                                       cost. The first three methods are probably the most eco-
   157   158   159   160   161   162   163   164   165   166   167