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P. 201

188    Gas Purification

                               Thermal Reclaiming, 255
                                Ion Exchange for Amine Solution Purification, 264
                                Electrodialysis for Amine Solution Purification, 264

                           NONACIDIC-GAS ENTRAINMENT IN SOLUTION, 265


                           REFERENCES, 269





                                              INTRODUCTION

                     One of the reasons that alkanolamine processes have become the predominant choice for
                   both refinery gas treating and natural gas purification is their comparative freedom from
                    operating difficulties. Nevertheless, several factors can result in undue expense and cause
                    difficulty in the operation of  alkanolamine units. Chief among these, from an economic
                    standpoint, are corrosion and amine loss. Other operating difficulties which occasionally
                    limit the capacity of a plant for gas purification include foaming and plugging of equipment.
                    In many cases, operation can be  significantly improved by daily monitoring of key plant
                    operating variables and by proper control and design of the treating plant.
                                         AMINE PLANT CORROSION


                    Background
                     The most serious operating problem encountered with alkanolamine gas purification
                    plants is corrosion, and, as would be expected, this problem has been given the widest atten-
                    tion. Several theories have been advanced to explain corrosion mechanisms, patents describ-
                    ing measures to eliminate or deviate corrosion have been issued, and numerous papers have
                    been published. Based on this appreciable amount of information and experience, the corro-
                    sion phenomena observed in a large number of plants operating under a wide variety of con-
                    ditions can be reasonably explained, and certain guidelines can be established to minimize
                    corrosion.
                     Amine systems are subject to corrosion by carbon dioxide and hydrogen sulfide in the
                    vapor phase, in the amine solution, and in the regenerator reflux, and by amine degradation
                    products in the amine solution. In refineries, amine systems often suffer from corrosion by
                    several agents not generally found in natural and synthesis gases, namely ammonia, hydro-
                    gen cyanide, oxygen, and organic acids, some of which tend to accumulate in certain parts of
                    the refinery amine system.
                     Amine units must be designed to overcome these special problems. This chapter reviews
                    both the causes of corrosion problems and possible solutions. It describes the locations with-
                    in amine units where the various agents cause corrosion, discusses the corrosion mechanisms
                    in these places, and reviews the design practices and preventive measures required to miti-
                    gate corrosion. These measures include control of velocities and impingement, process con-
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