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1. 发明授权

US5881475A Non-draining type human waste disposal method by pulse combustion drying 失效
标题翻译：不排水型人体废物处理方法采用脉冲燃烧干燥法
公开(公告)号：US5881475A
公开(公告)日：1999-03-16
申请号：US945605
申请日：1997-10-28
申请人： Ken Kishimoto , Atsuyoshi Kubotani , Takashi Enkawa , Tateo Asatsu , Toshiaki Kikuchi , Shunji Kishima , Hitoshi Touji
发明人： Ken Kishimoto , Atsuyoshi Kubotani , Takashi Enkawa , Tateo Asatsu , Toshiaki Kikuchi , Shunji Kishima , Hitoshi Touji
IPC分类号： A47K11/02 , C02F1/04 , F26B3/12 , F26B23/02 , F26B7/00
CPC分类号： F26B23/026 , C02F1/048 , F26B3/12 , Y02W10/40
摘要： This method relates to a non-draining type human waste disposal by pulse combustion drying. In the method, a pulsating combustion gas is discharged downward into a vertically cylindrical dryer from a pulse combustor disposed at the top of the dryer, and making contact the pulsating combustion gas with residue-removed human waste, digester chamber sludges or their mixtures charged therein, turning the charged matters to dried powder and steam under the dryer conditions of 120.degree.-150.degree. C., withdrawing the dried powder from the bottom of the dryer and the combustion gas containing steam from a lower side of the dryer, dust-removing the combustion gas containing steam maintained at 120.degree.-150.degree. C., deodorizing the dust-removed combustion gas, and exhausting the deodorized gas into the air. As an alternative method, the dried powder and the combustion gas containing steam are withdrawn from the bottom of the dryer, the withdrawn material maintained at 120.degree.-150.degree. C. is charged to a incinerator, odorous components and the dried powder entrained in the combustion gas containing steam are incinerated under supply of a fuel and combustion air, dust-removing the incinerated matters, and exhausting the dust-removed gas into the air.
摘要翻译： PCT No.PCT / JP97 / 00621 Sec。 371日期1997年10月28日第 102（e）1997年10月28日PCT PCT 1997年2月28日PCT公布。公开号WO97 / 31862 日期1997年9月4日该方法涉及通过脉冲燃烧干燥的非排水型人造废物处理。在该方法中，脉动燃烧气体从设置在干燥器顶部的脉冲燃烧器向下排放到垂直圆柱形干燥器中，并使脉动燃烧气体与残留物去除的人类废物，消化器室污泥或其混合物接触，在120〜150℃的干燥条件下将带电物料转移到干燥粉末和蒸汽上，从干燥器底部取出干燥粉末，从烘干机的下侧取出含有蒸汽的燃烧气体，除尘含有蒸汽的燃烧气体保持在120°-150℃，除尘除尘燃烧气体，并将除臭气体排放到空气中。作为替代方法，将干燥的粉末和含有蒸汽的燃烧气体从干燥器的底部排出，将保持在120-150℃的抽出的材料装入焚化炉中，将气味成分和干燥的粉末夹在含有蒸汽的燃烧气体在燃料和燃烧空气的供给下被焚烧，除去焚烧的物质，并将除尘气体排出到空气中。

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