会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 2. 发明授权
    • Device for continuous filtration and drying of a solid suspension
    • 用于连续过滤和干燥固体悬浮液的装置
    • US5656179A
    • 1997-08-12
    • US550314
    • 1995-10-30
    • Dietrich GehrmannNorbert Schweigler
    • Dietrich GehrmannNorbert Schweigler
    • B01D24/46B01D33/04B01D33/44B01D33/58B01D35/31F26B3/00F26B3/20F26B17/02F26B17/04C02F11/12
    • F26B17/045B01D33/04B01D35/31F26B17/026F26B3/00F26B3/20
    • The device for continuous filtration and drying of a solid suspension comprises a belt filter (1) and downstream a belt drier (2). By means of a porous conveyor belt (3) the filter cake generated in the belt filter (1) is conveyed further into the belt drier (2) in which there are provided heating devices for heating and drying the filter cake (7) which is on the conveyor belt (3). After leaving the belt filter (1), the filter cake (7) is present on the conveyor belt (3) in the form of a gas-permeable bed of solids in layer form having a maximum layer thickness of 50 mm, preferably a maximum of 20 mm. The heating devices in the belt drier comprise, on the one hand, a hot gas chamber (8) disposed above the conveyor belt (3) to generate a hot gas which flows through the bed of solids downwardly from above and, on the other hand, one or more contact heating elements (10, 15, 18, 19, 20, 22) disposed above and/or below the conveyor belt (3).
    • 用于连续过滤和干燥固体悬浮液的装置包括带式过滤器(1)和带式干燥器(2)的下游。 通过多孔输送带(3),带式过滤器(1)中产生的滤饼被进一步输送到带式干燥器(2)中,其中设置有用于加热和干燥滤饼(7)的加热装置,该滤饼 在传送带(3)上。 在离开带式过滤器(1)之后,滤饼(7)以具有最大层厚度为50mm,最好为最大值的层状固体透气床的形式存在于传送带(3)上 20毫米。 一方面,带式干燥器中的加热装置一方面包括设置在传送带(3)上方的热气室(8),以产生从上方向下流过固体床的热气体,另一方面 ,设置在传送带(3)的上方和/或下方的一个或多个接触加热元件(10,15,18,19,20,22)。
    • 3. 发明授权
    • Device for continuous filtration and drying of a solid suspension
    • 用于连续过滤和干燥固体悬浮液的装置
    • US5527458A
    • 1996-06-18
    • US327179
    • 1994-10-21
    • Dietrich GehrmannNorbert Schweigler
    • Dietrich GehrmannNorbert Schweigler
    • B01D24/46B01D33/04B01D33/44B01D33/58B01D35/31F26B3/00F26B3/20F26B17/02F26B17/04F26B23/00C02F11/12
    • F26B17/045B01D33/04B01D35/31F26B17/026F26B3/00F26B3/20
    • The device for continuous filtration and drying of a solid suspension comprises a belt filter (1) and downstream a belt drier (2). By use of a porous conveyor belt (3) the filter cake generated in the belt filter (1) is conveyed further into the belt drier (2) in which there are provided heating devices for heating and drying the filter cake (7) which is on the conveyor belt (3). After leaving the belt filter (1), the filter cake (7) is present on the conveyor belt (3) in the form of a gas-permeable bed of solids in layer form having a maximum layer thickness of 50 mm, preferably a maximum of 20 mm. The heating devices in the belt drier (2) comprise, on the one hand, a hot gas chamber (8) disposed above the conveyor belt (3) to generate a hot gas which flows through the bed of solids downwardly from above and, on the other hand, one or more contact heating elements (10, 15, 18, 19, 20, 22) disposed above and/or below the conveyor belt (3).
    • 用于连续过滤和干燥固体悬浮液的装置包括带式过滤器(1)和带式干燥器(2)的下游。 通过使用多孔输送带(3),带式过滤器(1)中产生的滤饼被进一步输送到带式干燥器(2)中,其中设置有用于加热和干燥滤饼(7)的加热装置, 在传送带(3)上。 在离开带式过滤器(1)之后,滤饼(7)以具有最大层厚度为50mm,最好为最大值的层状固体透气床的形式存在于传送带(3)上 20毫米。 带式干燥器(2)中的加热装置一方面包括设置在传送带(3)上方的热气室(8),以产生从上方向下流过固体床的热气体,并在其上 另一方面,设置在传送带(3)的上方和/或下方的一个或多个接触加热元件(10,15,18,19,20,22)。