首页> 外国专利> Drying pasty materials such as sludge from treatment plants, comprises subjecting sludge exiting from electrode hydration to laying operation that is moderated to preserve structure of sludge present in outlet of electro dehydration

Drying pasty materials such as sludge from treatment plants, comprises subjecting sludge exiting from electrode hydration to laying operation that is moderated to preserve structure of sludge present in outlet of electro dehydration

机译:干燥糊状物料(例如来自处理厂的污泥)包括使从电极水化过程中排出的污泥经受铺设操作,该工序要适度保持电脱水出口中存在的污泥结构

摘要

The process comprises subjecting sludge exiting from electro dehydration (3) to laying operation (4) that is moderated to preserve a structure of the sludge present in an outlet of electro dehydration. A temperature of air in contact to the sludge in thermal drying step (5) is 75[deg] C. The laying operation comprises an operation of fragmentation of the sludge on a slab of installation of solar drying, and a transfer of fragmented sludge towards thermal drying in a solar drying installation, where the fragmentation step takes placed before heat drying step. The process comprises subjecting sludge exiting from electro dehydration (3) to laying operation (4) that is moderated to preserve a structure of the sludge present in an outlet of electro dehydration. A temperature of air in contact to the sludge in thermal drying step (5) is 75[deg] C. The laying operation comprises an operation of fragmentation of the sludge on a slab of installation of solar drying, and a transfer of fragmented sludge towards thermal drying in a solar drying installation, where the fragmentation step takes placed before heat drying step. The heat obtained from the water evaporated by electro dehydration is collected in a heat exchanger (6) for thermal drying. The steam heat is recovered with condensation of evaporated water. The dryness of sludge in outlet of the electro dehydration step is 30 mass.% while the dryness of sludge from the drying step is 60-95 mass.%. The thermal drying is performed under a partial vacuum to lower the evaporation temperature of the water. An independent claim is included for an installation for drying pasty materials.
机译:该方法包括使从电脱水(3)出来的污泥经受铺设操作(4),该铺设操作被调节以保持电脱水出口中存在的污泥的结构。在热干燥步骤(5)中与污泥接触的空气的温度为75℃。铺设操作包括将污泥破碎在安装有太阳能干燥装置的板上的操作,以及将破碎的污泥向在太阳能干燥设备中进行热干燥,其中破碎步骤先于热干燥步骤进行。该方法包括使从电脱水(3)出来的污泥经受铺设操作(4),该铺设操作被调节以保持电脱水出口中存在的污泥的结构。在热干燥步骤(5)中与污泥接触的空气的温度为75℃。铺设操作包括将污泥破碎在安装有太阳能干燥装置的板上的操作,以及将破碎的污泥向在太阳能干燥设备中进行热干燥,其中破碎步骤先于热干燥步骤进行。从通过电脱水蒸发的水中获得的热量被收集在热交换器(6)中以进行热干燥。蒸汽热通过蒸发水的冷凝而回收。电脱水步骤的出口处的污泥的干燥度为30质量%,而来自干燥步骤的污泥的干燥度为60-95质量%。在部分真空下进行热干燥以降低水的蒸发温度。干燥膏状物料的安装包括独立索赔。

著录项

  • 公开/公告号FR2960870A1

    专利类型

  • 公开/公告日2011-12-09

    原文格式PDF

  • 申请/专利权人 DEGREMONT;

    申请/专利号FR20100054470

  • 申请日2010-06-08

  • 分类号C02F11/12;B01D61/56;

  • 国家 FR

  • 入库时间 2022-08-21 17:04:14

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