首页> 外文会议>Engineering Foundation Conference: Beneficiation of Phosphate III Dec, 2001 St. Pete Beach, Florida >Challenging the Crago Double Float Process III. Beneficiation of Siliceous Phosphate Using the FIPR/SAPR Process
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Challenging the Crago Double Float Process III. Beneficiation of Siliceous Phosphate Using the FIPR/SAPR Process

机译:挑战Crago Double Float Process III。使用FIPR / SAPR工艺对硅质磷酸盐进行选矿

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The FIPR/SAPR process is FIPR's third approach to develop a viable alternative to the Crago "Double Float" process for phosphate flotation. SAPR stands for Single-collector, All-anionic Phosphate Recovery. The FIPR/SAPR process offers a universal flowsheet for any anionic reagent system and flotation feed of varying sizes. For an unsized or fine flotation feed, the FIPR/SAPR process consists of the following steps: 1) high-solids conditioning with an anionic collector; 2) anionic rougher flotation, with the rougher concentrate sized at 48 (or 65) mesh and the +48 mesh recovered as a final product; and 3) cleaning flotation of the -48 mesh fraction from step 2. In a variation of step 2, the rougher concentrate from the first two cells may be collected as a final product, and the rougher concentrate from the last two cells sized at 48 or 65 mesh. The new process was tested with a blend of anionic collectors, achieving single-digit Insol at 85+% recoveries.
机译:FIPR / SAPR流程是FIPR的第三种方法,可开发出替代Crago“ Double Float”流程进行磷酸盐浮选的可行替代方案。 SAPR代表单收集器,全阴离子磷酸盐回收。 FIPR / SAPR工艺为任何阴离子试剂系统和各种尺寸的浮选进料提供了通用流程图。对于不定型或精细浮选的进料,FIPR / SAPR工艺包括以下步骤:1)用阴离子捕收剂进行高固体含量的调理; 2)阴离子粗浮选,粗选精矿的大小为48(或65)目,回收的+48目为最终产品; 3)清洗第2步中的-48目筛分的浮选。在第2步的变体中,可以收集来自前两个单元的粗选精矿作为最终产品,而来自最后两个单元的粗选精矿的粒度定为48或65目。该新工艺经过阴离子收集剂共混物的测试,回收率达到85%以上,达到一位数的Insol。

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