ֲý

150,000+

9.8M+

94%+

150,000+

9.8M+

94%+

FEATURED PRODUCT

Lithium Carbonate

Lithium carbonate is a foundational material for lithium-ion batteries and industrial manufacturing, serving as the primary precursor for lithium iron phosphate (LFP) cathode production. Its versatility, stability, and cost efficiency make it a critical input for electric vehicles, grid energy storage, ceramics, and specialty glass applications. Unlike conventional lithium production methods that require multiple downstream impurity removal and softening stages, ֲý’s Direct Lithium Extraction technology removes nearly all impurities including boron during the initial extraction process, polishing off the rest downstream and concentrating the lithium at high purity. Battery grade lithium carbonate is then directly precipitated from this–eliminating several of the complex and expensive refinery steps. Lithium hydroxide can also be directly produced from this using a membrane process that skips the lithium carbonate precipitation step. By producing high-purity battery grade lithium carbonate and hydroxide from lithium brines using advanced separation and refining technologies, ֲý reduces chemical consumption, achieves high recoveries and simplifies the process resulting in one of the lowest capital as well as operating costs in the industry, streamlining the path to scalable lithium production for the rapidly growing electrification market.

The Next Chapter of
Global Critical Materials

DLE Plant Process Overview

The DLE processing plant includes Brine Pre-Treatment, Adsorption, RO, Ca-Mg Removal, Ca-Mg and Boron IX, and Brine Evaporation units. The facility also consists of reagent storage and preparation areas, utility systems (power, water, and air distribution), a laboratory, and a centralized control station.

The raw brine from the storage pond contains suspended solids and other contaminants that could affect adsorption column operations.

Therefore, the brine is pretreated using candle filters. The treated brine then gravitates to the nearby adsorption feed pond. The brine goes through 5-micron strainers before entering adsorption columns.

The eluate and the spent brine coming from adsorption is also filtered before going to the respective storage ponds.

The filtration system is designed for a capacity of 2,712 m³/hr, providing a 30% margin above the required brine flow rate.

The adsorption system consists of 18 columns arranged in six rows, with three columns per row. Each column measures 21 ft in diameter and 9 ft in height. Each column is designed for a flow rate of 520 m³/hr.

The eluate (product brine) from each row of columns gravitates to the eluate pond for further processing. The overall system features a high degree of process automation, minimizing labor requirements.

Each row of three columns is capable of producing 7,500 up to 15,000 tpa LCE with adsorption improvements, depending on feed grade and productivity.

The RO system has a design capacity of 2,880 m³/hr, with each RO unit processing 480 m³/hr. The system includes six operating units, housed within a total of thirty-six 40-ft containers. Six of the 40-ft containers operate as one unit.

Eluate from the AX process is concentrated through a series of RO membrane stages to achieve a final brine total dissolved solids (TDS) of 8%. The feed eluate has a TDS of 0.58%. The RO skids are provided as a full turnkey solution, designed for plug-and-play operation.

The calcium and magnesium purification stage consists of three reactors, each with a capacity of 82.5 m³.

The system provides a total active residence time of ~45 minutes. The first two reactors are equipped for dosing NaOH and Na₂CO₃, which are used for the precipitation of calcium carbonate (CaCO₃) and magnesium hydroxide (Mg(OH)₂).

The precipitated calcium and magnesium cake from the reaction tanks is pumped to the filtration stage.
The filtration stage consists of two membrane filters – one in operation and one on standby.

Each filter press is equipped with a total of 155 polypropylene (PP) filter plates.
The mass flow rate of each filter press is 203 t/h, with a solid concentration of 0.6%.

The filtration area per chamber is 3.66 m², giving a total filtration area of 564 m² per filter press. The target cake thickness before squeezing is 35 mm The total wet cake volume per filter press is 8.9 m³.

The polishing step consists of a two-stage ion exchange (IX) system. The first stage removes residual calcium and magnesium from the brine solution. The second stage performs boron ion exchange for further purification.

Each IX stage consists of three columns operating in a lead– lag and regeneration configuration. The columns are constructed from fiberglass reinforced plastic (FRP).

The IX stages are provided as a full turnkey solution, designed for plug-and-play operation. Each stage is supplied with online regeneration support system.

The brine evaporation stage consists of two falling-film evaporators and a sodium chloride crystallizer. The system includes two standalone brine evaporator stages, each capable of handling a feed flow rate of ~190 m³/hr with output capacity of 22,500 tpa of LCE.

The stage also includes two pusher centrifuge systems for the separation and removal of sodium chloride crystals. Centrifuges are designed for a total solids throughput (dry basis) of 9.18 t/h.