增压器流动炉下水污泥的基础燃烧特性;增压器流动炉下水污泥的基础燃烧特性;Fundamental Combustion Characteristics of Sewage Sludge in Fluidized Bed Incinerator withturbocharger

T. Murakami, Yoshizo Suzuki, Hidekazu Nagasawa, Takafumi Yamamoto, Takami Koseki, Hitoshi Hirose, Shuichi Ochi
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引用次数: 3

摘要

提出了一种具有划时代意义的焚烧装置,该装置配备了增压流化床燃烧室和涡轮增压器,用于回收污水污泥中的能量。这种植物有三个主要优点。(1)最大工作压力为0.3 MPa(绝对压力),无需使用压力容器。可以降低工厂建设的材料成本。(2)由于省略了强制风机(FDF)和诱导风机(IDF),可以减少发电产生的CO2排放。(3)烟气中的蒸汽成为涡轮增压器的工作流体,这样除了燃烧空气外,还产生多余的空气。因此,该电厂既能节约能源,又能发电。本研究的目的是利用实验室规模的加压流化床燃烧器(PFBC)阐明污水污泥的基本燃烧特性。测试的燃料是脱水的污泥和锯末。通过实验澄清了炉内温度分布和烟气中N2O的排放情况。结果表明,对于仅燃烧污泥,通过干燥和热解使砂床温度降低,热解气体在干舷燃烧使温度升高。另一方面,木屑热解后的残炭在砂床中稳定燃烧,用于污泥与木屑共烧。因此共烧的温度比污泥单独燃烧的温度要高得多。N2O排放量随干舷温度的升高而降低,在所有实验条件下均受温度控制。这些数据可用于示范装置的运行。
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過給式流動炉における下水汚泥の基礎燃焼特性;過給式流動炉における下水汚泥の基礎燃焼特性;Fundamental Combustion Characteristics of Sewage Sludge in Fluidized Bed Incinerator with Turbocharger
An epoch-making incineration plant, which is equipped with a pressurized fluidized-bed combustor coupled to a turbocharger, for the recovery of the energy contained in sewage sludge is proposed. This plant has three main advantages. (1) A pressure vessel is unnecessary because the maximum operating pressure is 0.3 MPa (absolute pressure). The material cost for plant construction can be reduced. (2) CO2 emissions originating from power generation can be decreased because the FDF (Forced Draft Fan) and the IDF (Induced Draft Fan) are omitted. (3) Steam in the flue gas becomes a working fluid of the turbocharger, so that in addition to the combustion air, the surplus air is also generable. Therefore, this proposed plant will not only save energy but also the generate energy. The objective of this study is to elucidate the fundamental combustion characteristics of the sewage sludge using a lab-scale pressurized fluidized bed combustor (PFBC). The tested fuels are de-watered sludge and sawdust. The temperature distribution in the furnace and N2O emissions in the flue gas are experimentally clarified. As the results, for sludge only combustion, the temperature in the sand bed decreases by drying and pyrolysis, and the pyrolysis gas burns in the freeboard so that the temperature rises. On the other hand, the residual char of sawdust after pyrolysis burns stably in the sand bed for the co-firing of sludge and sawdust. Thus the temperature of the co-firing is considerably higher than that of the sludge only combustion. N2O emissions decreases with increasing freeboard temperature, and are controlled by the temperature for all experimental conditions. These data can be utilize to operation the demonstration plant.
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