Page 2 - Packed bed columns for absorption, desorption, rectification and direct heat transfer
P. 2

Preface


                             Separation processes in gas (vapour) - liquid systems, like absorption, des-
                         orption and rectification, are estimated to account for 40%-70% of both capital
                         and operating costs in process industry [1]. A significant part of the costs are
                         connected with the packed bed columns used for these processes. The employ-
                         ment of these apparatuses also for direct heat transfer between gas and liquid,
                         including utilization of waste heat from flue gases, enlarges their importance.
                             Packed bed columns are the best type of apparatuses, from thermodynamical
                         point of view, for carrying out of mass and heat transfer processes between gas and
                         liquid phase. It is because of all types of highly effective apparatuses, they operate
                         as near as possible to the conditions of countercurrent flow, i.e., at maximum
                         driving force for given initial and end concentrations of the two phases and a given
                         ratio between their flow rates.
                             The history of packed bed columns has begun with absorption and desorption
                         processes. The first apparatus of this type was proposed by Gay-Lussac in 1827
                         who at this time was a consulting chemist of Saint Gobain Company [2]. The
                         column, called by his name, was designed to absorb NO X after the nitrosyl method
                         for production of sulphuric acid. 10 years later, filled up with coke, it was
                         implement in industry.
                             After 1980 a gradual displacement of the tray-type contactors by packet
                         columns began in the distillation plants, and until 1990 it was considered the
                         greatest novelty in the area of distillation [42].
                             Because of high efficiency, low pressure drop, and high admissible flow rates,
                         packed bed columns are now largely used in chemical and food industry,
                         environmental protection and also for carrying out of some processes in thermal
                         power stations such as water purification, flue gas heat utilization and SO 2
                         removal.
                             This book is intended for chemical and heat engineers working in these
                         industries and also especially for chemical engineers and scientists working on
                         development of new technologies which include absorption, desorption,
                         distillation, and direct heat transfer processes in gas-liquid systems. It is especially
                         proper for designers of such types of apparatuses.


                                                                                        N. Kolev
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