Magnetic filters, consisting of fine ferromagnetic wires to provide sharp local field gradients in a uniform magnetic field, can separate fine, even weakly magnetic particles from fluid streams. This technique is called high gradient magnetic separation (HGMS) and has been applied to operations; mineral beneficiation, magnetic desulfurization of coal and water pollution control. If economically feasible, this technique appears useful for the separation of steel, magnetite or like air-borne magnetic particles from exhaust gases in steel, bearing and various other industries. In this paper, we make clear the performance of the magnetic filter in which the wire axis and the fluid flow are mutually parallel and the magnetic field perpendicular to them (Parallel stream type magnetic filter). The parallel stream type magnetic filter has been investigated by Uchiyama et al. and the collecting efficiency of the filter was calculated based on the particle trajectory model. In their model the fluid stream was uniform and had no velocity gradient. The laminar flow, however, in a narrow slit of the parallel stream type filter has the parabolic velocity distribution. Then we derive the equations for the magnetic, drag and inertia forces acting on a particle in the parabolic fluid stream. By solving these equations numerically, we can obtain the single-wire efficiency rather different from Uchiyama's. For practical estimation of the collecting efficiency of air-borne particles by weight, it is required to consider the effect of neighbouring wires and the particle size distribution on the single-wire efficiency. Nukiyama's formula is applied to represent the particle size distribution and we can obtain the equation of the collecting performance. The experimental results for ferromagnetic or paramagnetic air-borne particles show the good agreement with our theoretical solutions. With the theoretical and experimental analysis on the parallel stream type magnetic filter, it is found that high collecting efficiencies for fine magnetic particles can be achieved. Let us consider a concrete example. Suppose the stainless-steel wire is of 100μ diameter, and has a saturation magnetization 2000G. The background field is 3kOe and the air flows in the filter at a velocity of 2m/s. Let us suppose that the particles, say Fe_3O_4, have a diameter 0.8μ. The saturation magnetization of the particles is then 470G. We make clear that with the parallel stream type filter of 5% in packing density, 10cm in thickness and 1mm in width of the slits, the collecting efficiency is higher than 99% and the pressure drop is lower than 20mmAq. Throughout of the preceding experiment, the efficiency and the pressure drop are determined for clean filters. For practical purpose, however, the effect of particles build-up onto the wire, in other words, the performance after the filter has been operated for a certain length of time, is one of the most important properties to be examined. The authors are making an examination of the magnetic filter in which the wire axis, the fluid flow and the magnetic field are mutually perpendicular. A report on the details will follow.
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