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    • 3. 发明专利
    • DE112005003618A5
    • 2008-04-03
    • DE112005003618
    • 2005-04-21
    • FAN SEPARATOR GMBH
    • EICHLER DIETRICH
    • B30B9/12
    • The denticulation is used in screw presses before the entrance into the sieve area. In biogas installations, a solids/liquid separation ensues after the digestion of the substrate in the biogas reactor during which such machines are used. Cloggings caused by long-fiber constituents that were not decomposed often occurs. The aim of the invention is to prevent these cloggings. The screw presses work with cylindrical rod sieves (5). The screw starts in the area of the supply, and the housing has a cylindrical transition starting from inlet box and extending up to the beginning of the rod sieve. According to the invention, this cylindrical transition is provided with axial teeth (6) at an angle to the screw rotating thereabove that favors the pushing and shearing action. The teeth form a narrow gap with regard to the screw (4). The 4 6 mm deep slots between the teeth and the teeth have a width of 5 20 mm. The gap between the teeth and the screw is 0.3 to 0.5 mm. The teeth and the screw are armored on the surfaces.
    • 5. 发明专利
    • Arrangement for the concentration of biomass in biogas fermenters using micro-bubbles for flotation purposes, comprises a device control for formation of micro-bubbles, a booster pump and an agitator for mixing the bio-sludge
    • DE102005059723A1
    • 2007-06-21
    • DE102005059723
    • 2005-12-14
    • FAN SEPARATOR GMBH
    • EICHLER DIETRICHWEIGAND FRIEDRICHRABENER MATTHIAS
    • C12M1/107B01F5/20B03D1/20B03D1/24C02F11/04C12M1/09
    • The arrangement for the concentration of biomass in biogas fermenters (9) using micro-bubbles for flotation, comprises a device control (15) for formation of micro-bubbles, a booster pump (5) and an agitator (10) for mixing the bio-sludge. The micro-bubbles are generated by an aerated liquid, which is removed from the system after the separation of floatable components. A negative pressure is produced for suction of the gas by a valve in the inlet of the liquid before the booster pump and the formation of the micro-bubbles takes place through a flow-intensive expansion. The arrangement for the concentration of biomass in biogas fermenters (9) using micro-bubbles for flotation, comprises a device control (15) for formation of micro-bubbles, a booster pump (5) and an agitator (10) for mixing the bio-sludge. The micro-bubbles are generated by an aerated liquid, which is removed from the system after the separation of floatable components. A negative pressure is produced for suction of the gas by a valve in the inlet of the liquid before the booster pump and the formation of the micro-bubbles takes place through a flow-intensive expansion in a cavitation region of the bubbles. The biogas produced in the fermenter is sucked over a line (17) for the device control and a space is enclosed in the fermenter by a wall. The liquid is clarified over the line. The liquid loaded with micro-bubbles is introduced into the space, while the quantity of the liquid phase, which is introduced into the fermenter, is purified against the flow of micro-bubbles, leaves the plant as a purified and an essentially smell-free liquid over a overflow mechanism and over the line of the clarified liquid. From the clarified liquid, the necessary quantity of the micro-bubbles is removed, while the floating bio-sludge is led back into the region of the biogas fermenter and is mixed down by the agitator. The wall terminates 0.5-1 m below the fluid level that adjusts itself through the height of the overflow mechanism. The bio-sludge is sucked in by the agitator with the help of a conduit tube, which is led from the self-forming floating layer and spans beyond the agitator and is mixed with the contents of the fermenter.