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Rotary condensation drying unit with thermal solid-liquid separation for digestate, liquid manure, sewage sludge and organic sludge

机译:旋转式冷凝干燥单元,具有热固液分离功能,用于消化液,液体肥料,污水污泥和有机污泥

摘要

The method for the production of economic manure, comprises drying fermentation remnants under use of exhaust gas from heat and power cogeneration plant in biogas plant. The drying is carried out in mixing dryers with interior rotating converter in different axle bearing and rotation directions with the help of exhaust gas under mixing of surrounding air or under use of air air heat exchangers. The sequence drying procedure is carried out with the sequence of exhaust gas introduction in the rotation-mixing dryer. The method for the production of economic manure, comprises drying fermentation remnants under use of exhaust gas from heat and power cogeneration plant in biogas plant. The drying is carried out in mixing dryers with interior rotating converter in different axle bearing and rotation directions with the help of exhaust gas under mixing of surrounding air or under use of air air heat exchangers. The sequence drying procedure is carried out with the sequence of exhaust gas introduction in the rotation-mixing dryer. The sequence drying in the later stage is carried out by utilization of condensation warmth with the help of heat exchanger to air drying process for pre-drying of the economic manure. The utilization of chemical and physical characteristics of the exhaust gas is carried out in connection with the chemical valence of the fermentation remnants. The controlling and regulation of the production process and/or its single parameter are carried out for the total drying procedure and its single sequence.
机译:生产经济肥料的方法包括在沼气厂的热电联产厂的废气的作用下干燥发酵残留物。干燥是在带有内部旋转转换器的混合干燥机中,在不同的轴承方向和旋转方向上,借助废气在周围空气混合下或在空气热交换器中进行的。顺序干燥程序是通过将废气引入旋转混合干燥机中的顺序进行的。生产经济肥料的方法包括在沼气厂的热电联产厂的废气的作用下干燥发酵残留物。干燥是在带有内部旋转转换器的混合干燥机中,在不同的轴承方向和旋转方向上,借助废气在周围空气混合下或在空气热交换器中进行的。顺序干燥程序是通过将废气引入旋转混合干燥机中的顺序进行的。后面的顺序干燥是在热交换器的帮助下,利用冷凝热利用热交换器对空气进行干燥,以实现经济肥料的预干燥。结合发酵残余物的化学价来利用废气的化学和物理特性。对整个干燥过程及其单一顺序进行生产过程和/或其单一参数的控制和调节。

著录项

  • 公开/公告号DE102007050058A1

    专利类型

  • 公开/公告日2009-04-23

    原文格式PDF

  • 申请/专利权人 ENTHAL GMBH;

    申请/专利号DE20071050058

  • 发明设计人

    申请日2007-10-19

  • 分类号C02F11/12;C05F3;C05F7;A01C3;

  • 国家 DE

  • 入库时间 2022-08-21 19:09:32

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