Page 371 - Academic Press Encyclopedia of Physical Science and Technology 3rd Chemical Engineering
P. 371

P1: GLQ Final Pages
 Encyclopedia of Physical Science and Technology  EN009K-419  July 19, 2001  20:57






               306                                                                         Membranes, Synthetic, Applications


               compound  that  preferentially  and  reversibly  complexes  creases the concentration of carbon dioxide in the natural
               with oxygen. By exposing this liquid membrane (q.v.) to  gas produced and thus reduces its energy value. More-
               air on one side and a vacuum on the other side, the carriers  over, the cost of EOR would be prohibitively high un-
               capture oxygen from the air and release it on the evacu-  less the carbon dioxide is reused. Membranes have been
               ated side. The result is substantial enrichment of oxygen.  used successfully at production wells to separate the car-
               However, many technical problems remain regarding the  bon  dioxide  for  reinjection  while  delivering  a  purified
               useful life of the carrier and of the membrane structure  methane stream.  Figure  18 shows a multistage  process
               itself; commercial realization of this approach is unlikely.  for reducing the carbon dioxide level of natural gas from
               Also,  as  noted  in  the  discussion  of  Fig.  7,  membranes  7 to 2% while achieving almost 95% methane recovery.
               made from inorganic materials, e.g., metals or ceramics,  Using carbon dioxide, permselective membranes such as
               sometimes formed as composites are under active study.  cellulose acetate or various polyimides, the product natu-
               Although not commercially significant, these membranes  ral gas stream remains at high pressure and requires little
               offer the potential of much improved chemical and ther-  recompression for further processing. Such systems have
               mal resistance, and might foster new industrial application  proved to be much more economical to install and operate
               possibilities.                                    thandiethylamineabsorption,theprevailingmethodofgas
                                                                 treating.
                                                                   Depending on source, geographic location, and the ex-
                 3.  Acid Gas Removal
                                                                 tent of extraction, the acid gas content of fuel gases often
               Carbon dioxide, hydrogen sulfide, hydrogen chloride, sul-  exceeds pipeline specifications. Certain natural gases and
               fur dioxide, and some oxides of nitrogen are collectively  landfill gases can contain up to 50% carbon dioxide. Bulk
               referred  to  as  acid  gases.  They  are  responsible  for  the  removal of both carbon dioxide and hydrogen sulfide from
               “sour” nature of fuel gases from various sources. Carbon  such sources, i.e., the process of “sweetening,” not only
               dioxide separation was the first large-scale applications  improves the fuel value of the gas, but also helps reduce
               developed; it remains one of the most important because of  corrosion of pipelines and transmission equipment. Mem-
               the abundance of carbon dioxide in gas mixtures. Another  branesaresuitableforthisapplicationespeciallywherethe
               factor is that membranes exhibiting high permeability to-  scale is relatively small and the economics favor scalable
               ward polar gases were relatively easy to develop based on  membrane systems.
               desalination membrane technology already available.  Sulfurdioxideisacommonpollutantfoundincoal-fired
                 Large quantities of carbon dioxide have been used in  facilities. Various membrane permeation schemes have
               times of high energy costs in conjunction with enhanced  been proposed but few are competitive with wet scrub-
               oil recovery (EOR). This practice of injecting the gas at  bing. More recently, however, bipolar membrane technol-
               high pressure into geological formations to increase oil  ogy (q.v.) has been successfully used to recycle the scrub-
               and natural gas yield, although highly effective, also in-  bing effluent and convert the sulfur into sulfuric acid.




























                           FIGURE 18  Multistage carbon dioxide recovery from natural gas in enhanced oil recovery operation.
   366   367   368   369   370   371   372   373   374   375   376