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method and installation for the homogenization of a single period product quality or to unregelmaessiger homogenisation of a mixture of two or more divided, in particular verhaeltnissen added product
method and installation for the homogenization of a single period product quality or to unregelmaessiger homogenisation of a mixture of two or more divided, in particular verhaeltnissen added product
984,934. Average discharge mixing apparatus. SOC. DES MINES DE FER DE LA MOURIERE. July 10, 1961 [Aug. 13, 1960; Jan. 13, 1961], No. 24950/61. Heading B1C. [Also in Divisions B8 and G1] A -method of rendering a granular product or mixture of such products homogeneous by depositing it in parallel layers to form a heap and reclaiming from the heap in parallel layers oblique to the deposited layers is characterized by causing the depositing and reclaiming operations to proceed simultaneously on a single stationary site in such manner that the heap progressively moves over the site. In Figs. 4 and 5, the heap is formed on an open circular site 12 over which a spreader feeder 15 oscillates in an arc defining the ends 4 and 7 of the heap 2, the limits of this are being displaced in the direction of the arrow F2 at each oscillation. Reclaiming is effected by a device (e.g. a scraper) 19 which removes material from the foot of the slope of fall at the highest end 4 of the heap. In Fig. 7 the site is an annular hopper 21 and the material is laid down in layers parallel to the slope of fall and reclaimed in horizontal layers through a slit 26 in the hopper base, both the feeder 24 and the reclaimer (not shown) moving continuously around the hopper. In Fig. 9 the site is a rectilinear hopper and the operation is similar to the Fig. 7 embodiment, the heap 111 progressing in the direction of arrow F until the leading edge 113 thereof reaches the end 116 of the hopper, when the depositing means 121 is returned to the end 118 and starts to form a new heap while the old one is still being reclaimed. The rates of deposition and reclamation may be controlled by the weighers A and B (see Division G1).
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机译：984,934。平均排放混合设备。 SOC。 DES MINES DE FER DE LA MOURIERE。 1961年7月10日[八月。 1960年13月13日; 1961年1月13日]，第24950/61号。标题B1C。 [也在B8和G1分部中]-通过将颗粒状产品或此类产品的混合物沉积在平行层中以形成堆并从倾斜于沉积层的平行层中从堆中回收而使其均匀的方法，其特征在于：存放和回收操作在单个固定站点上同时进行，以使堆逐渐在该站点上移动。在图。如图4和图5所示，堆形成在开放的圆形位置12上，在该圆形位置上，撒布机进给器15以弧形振荡，该弧限定堆2的端部4和7，其极限在箭头F2的方向上在每次振荡。回收是通过装置（例如刮板）19进行的，该装置从堆的最高端4处的下降坡脚移走材料。在图7中，该位置是一个环形料斗21，物料以平行于下落的坡度的方式分层放置，并通过料斗底部，进料器24和回收器（未显示）中的狭缝26在水平层中回收。在漏斗周围连续移动。在图9中，该位置是直线漏斗，其操作类似于图7的实施例，当沉积装置被放置时，堆111沿箭头F的方向前进直到其前缘113到达漏斗的端部116。 121返回到末端118，并开始形成新的堆，同时仍在回收旧的堆。沉积和回收的速率可以由称重器A和B来控制（参见分区G1）。
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