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Method for management of impregnated wood wastes, preferably railway sleepers, by means of gasification method, with production of electric and heat energy

机译:用气化方法处理浸渍的木材废物,最好是铁路轨枕的方法,并产生电能和热能

摘要

The way in which impregnated wood waste is disposed of, in particular the rolling stock, the method of reconciling it with the production of electricity and heat, is characterised by the fact that prepared, granulated 5-80 mm wood waste impregnated from a reservoir (1) shall be fed to a known sintering reactor (3) through at least one sludge reservoir (2),where the low-calorific process gas 4-6 MJ/nm3 with temperature 650-750-C is produced, directed to the repellent cyclone (5),and then cooled air from the fan (8) in the heat exchanger (7) to the temperature 400-500-C. Heated in the heat exchanger (7) to the temperature 100-200-C hot air is fed to the condensation reactor (3). The process gas cooled in the heat exchanger (7) is then discharged into the ceramic filter set (9),then the 350-450-C process gas is transferred to the cooling unit (10),equipped with at least two heavy fraction condensation coolers and a light fraction condensation cooler, from which the heavy condensation fraction is directed to the condensation reactor (3),and the fraction of the light process gas at temperature 30-50oC is directed to the demister (11). Subsequently, the diluted, cooled and purified process gas (13) by an additional sludge separator (14) is directed to the exhaust engine (16.1) of the electrical generating unit (16). The exhaust engine cooling system (16.1) of the electrical generating unit (16) cooperates with the heat exchanger (15). Combustion burns from the exhaust engine (16.1) of the electrical generating unit (16) through the exhaust ignition and exhaust aftertreatment system (17) shall reach the heat exchanger (18),from which, after passing through the exhaust monitoring system (19) are directed to the chimney (20).
机译:处理浸渍过的木屑的方法,特别是机车车辆的处理方法,将其与电力和热量的生产相协调的方法,其特征在于以下事实:从储罐中浸渍的制备好的,颗粒化的5-80毫米木屑( 1)应通过至少一个污泥池(2)送入已知的烧结反应器(3),在这里产生温度为650-750-C的低热值工艺气体4-6 MJ / nm3,并直接导向驱虫剂旋风除尘器(5),然后将来自风扇(8)的空气在热交换器(7)中冷却至温度400-500-C。在热交换器(7)中加热到100-200-C的温度的热空气被送入冷凝反应器(3)。然后,将在热交换器(7)中冷却的过程气体排放到陶瓷过滤器组(9)中,然后将350-450-C过程气体转移到冷却装置(10),该装置至少装有两次重馏分冷凝冷却器和轻馏分冷凝冷却器,其中重的冷凝馏分被引导至冷凝反应器(3),温度为30-50oC的轻质工艺气体的馏分被引导至除雾器(11)。随后,通过附加的污泥分离器(14)将稀释,冷却和纯化的处理气体(13)引导至发电单元(16)的排气发动机(16.1)。发电单元(16)的排气冷却系统(16.1)与热交换器(15)协作。发电机(16)的排气发动机(16.1)的燃烧燃烧物通过排气点火和排气后处理系统(17)到达热交换器(18),在经过排气监控系统(19)之后从热交换器(18)燃烧。被导向烟囱(20)。

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