The entirety of Mosaic’s mineral reserves and resources exist within sedimentary deposits. Economic phosphorite exists in a matrix of gravels, sands, silts and clays that are readily extractible. These economic deposits overlay a carbonate platform where phosphorite is absent. The bedrock and economic matrix are overlain by sands, clays and silts that are easily removed. Limitations of extraction arc the case of excavation, the capacity of the matrix to slurry, the grade of the phosphorite, gangue minerals, the depth of the matrix, and the overburden to be removed.

Deposition of phosphorite occurred in the Miocene and Pliocene epochs. The depositional environment was shallow marine with sea levels of 300 ft. (100 m) or less. Cold phosphate rich waters were upwelled and mixed with warm surface waters creating vigorous biologic activity. Biological remains settled on the sea floor in regional anoxic zones. Phosphate subsequently substituted into calcium carbonate in the form of the mineral francolite. Accessory- mineralization does occur, but it is of little economic consequence. The deposit underwent transport and rework through marine winnowing. Post-depositional rework is extensive and site factors such as hydrology and groundwater geochemistry influence grade and gangue mineralization.

Gangue minerals are generally limestone, dolomitic limestone, iron concretions of varying sizes and competent clays that resist disaggregation by washing. Limestone, dolomite and iron concretions exist as distinct particles that are inseparable through conventional sizing. There is limited intracrystalline substitution of metals within francolite. Most of the gangue minerals arc distinct particles.

Mosaic's Florida phosphate mining currently consists of three producing facilities and three exploration properties. The geology across all the sites is a consistent sequence of sub- aerial and marine sediments. The upper most sediments are lacking in phosphates. The marine sediments and carbonate system that follow contains an economic concentration phosphate. The lower carbonate system is devoid of phosphate. At a site level, the geology is unique enough to warrant different ore management practices based on gangue clast size, composition and concentration.

The Wingate property geology consists of 35 to 49 ft. (10.7 to 14.9 m) of white to tan-gray poorly graded quartz sand to brown gray to orange iron-ccmentcd clayey sand hardpan to tan-gray to gray clayey sands with varying abundance of reworked phosphate grains. The economic zone is 19 to 37 ft. (5.8 to 11.3 m) thick, ranging in grade from 28 to 31% P2O5and comprised of tan-gray to gray clayey sands with phosphate pellets and grains to gray to gray-blue quartz sands, clays, and phosphate grains and some nodules. The basal units arc gray to gray-blue barren clays to phosphatic limestone rubble to beds of phosphatic limestone.

Wingate is a phosphates production stage mining facility. Phosphate is extracted using surface mining techniques. Mining utilizes dreadges to remove overburden and mine the phosphate ore (matrix). The matrix is hydraulicaly transported to the benefication plants via a series of centrifugal pumping systems.

Wingate has utilized two electric dredges, one to remove overburden and the other to mine phosphate matrix. Both dredges arc equipped with cutter heads and slurry pumping systems to liberate and transport material. Spuds are used to position the dredges and allow a point by which to pivot. Cables extending from the dredges to anchors on the port and starboard sides enable swinging across the cut. Upon each pass, the dredges advance further into the cut. Periodically, the dredges will retreat and perform a "clean up" pass for additional overburden or matrix recovery.

Cut widths are dependent upon dredge geometry and overburden thickness. The water level of the dredge pond is nominally 15 ft. (4.6 m) below the ground surface. The overburden dredge utilizes a centrifugal pumping system with 26 inch (66 cm) steel pipe to transport and discharge spoil into previously mined areas of the pond. As the cutter head feeds the suction underwater, the solids arc diluted with an abundance of surrounding water. Slurry is transported at llows in excess of 20,000 US gpm. On occasion, dense, consolidated sand known as hardpan is encountered. As this material is tough to extract, contractors are used on an as needed basis to remove and haul this material outside the immediate mining area. This is known as pre-stripping.

As with the overburden dredge, the cut width of the matrix dredge is based on dredge geometry and matrix depth. It also utilizes a centrifugal pumping system with 20 inch (51 cm) steel pipe to transport matrix to the beneficiation plant. Ease of material extraction and pumpability are generally determined by the clay content of the matrix. The pumping system is designed to the same specifications as the 20 inch (51 cm) systems used fordragline operations.

Wingate plant has two steps of sizing - primary and secondary. The unsized feed goes to a secondary declay cyclone to remove clay. Cyclone underflow feeds the primary sizer. The overflow of primary sizer reports to the fine flotation feed bin while the underflow is pumped to scalp screen. The overflow of scalp screen is recycled back to trommel screen underflow tank and the underflow goes to the secondary sizer. The overflow of secondary sizer combines with primary sizer overflow and feeds the fine flotation circuits. The underflow of secondary sizer reports to the coarse flotation feed bin. The particle size of Wingate coarse flotation feed and fine flotation feed is 20 to 35 mesh and 35 to 150 mesh, respectively.

The Mosaic processes the ore(matrix) at beneficiation plant. The ore goes through washing, screening, sizing and flotation processes designed to separate the phosphate rock from sands, clays and other foreign materials.

Beneficiation Plant Operations:
Washer
* Removes oversize material.
* Produces “pebble” phosphate.
* Removes clay by scrubbing and rinsing.
* Feeds all undersized phosphate and sand to the sizer.
* Same-sized sand and phosphate is pumped to the flotation plant for separation.

Flotation Plant
* Produces fine-sized “Concentrate” phosphate.
* Uses special additives (mostly biodegradable oils from the pulp and paper industry) to coat the phosphate.
* Phosphate separates from the sand, floats to the top and is skimmed off.
* Pumps sand back to the field for reclamation.

The debris is mineralization rejected due to the high MgO content. The minimum size for the rejected debris is 5/16 inch, % ........