Skip to main navigation Skip to main content Skip to page footer

How well can unwanted metallic abrasion in the mix be avoided in practice when mixing battery active masses (cathode masses)?

In practice, metallic abrasion during the mixing of battery active masses can be reduced significantly, but it cannot be ruled out entirely through a single measure. A realistic approach is a holistic purity concept that minimises contamination at the source, separates critical particles as early as possible, and monitors the process analytically. Blanket ppb limit values for all cathode masses are not robust, however, because permissible residual contents, critical elements, particle sizes and measurement methods depend on the cell chemistry, the cell manufacturer's specification, the process stage and the specific quality agreement. For cathode active materials, the particularly relevant metallic impurities chromium, iron, copper, zinc and lead are frequently listed in relevant quality standards and analytical applications with target values below 1 mg/kg, i.e. below 1 ppm.

Metallic foreign particles are critical for lithium-ion cells because they can cause local defects, increased self-discharge, unwanted side reactions and, in the worst case, internal short circuits. Individual large or sharp-edged metal particles are particularly problematic, as they can damage separators or increase local current densities. The technical assessment must therefore not be limited to the total chemical metal content in ppm. It must also take into account the number, size, shape, magnetic property and spatial distribution of metallic particles. One industrial technical source classifies metallic particles above 5 µm as critical; other process chains apply different, product-specific size and acceptance limits.

The causes of metallic contamination occur along the entire process chain. They can originate from the raw materials, arise from the wear of milling, classifying, mixing and conveying components, or be introduced through the environment, maintenance activities and human intervention. In mixing and milling in particular, direct product contact with metallic tools, vessel walls or wearing sealing and conveying components can generate metallic particles. A recent review paper explicitly names the wear of metallic components in mixing and milling processes as a source of contamination and recommends, among other things, protective coatings for mixing and milling equipment, magnetic separators or screens, and strict operational cleanliness procedures.

The first and most effective measure is therefore an abrasion-minimised design of all product-contact components. Direct metal-on-metal contact in the product area should be avoided. Mixing tools, vessel wall, discharge elements, conveying bends, flaps, sealing areas and transfer points must be designed so that no grinding, striking or repeated impact of hard particles occurs at critical edges. Depending on the material system, technical ceramics, suitable coatings or high-performance polymers can be useful on selected contact surfaces. However, the specific choice of material must be checked against chemical compatibility, the abrasiveness of the active mass, electrostatic properties, cleanability, thermal load and the possible particle release of the respective lining material. A non-metallic material is not automatically suitable if it itself leads to abrasion, delamination or unwanted organic contamination.

A second important lever is process control. Low but sufficiently effective tool and conveying speeds reduce impact energy and therefore erosive wear. Sharp deflections, tight bends, uncontrolled drop heights, dead zones and repeated recirculation should be avoided. In pneumatic conveying, it is not only air velocity that matters but also solids loading, pipe routing, bend radius, particle hardness, pressure level and start-stop operation. When mixing, the rotational speed must be chosen so that the required homogeneity is achieved with the lowest possible mechanical stress. Unnecessarily long or overly intensive mixing can increase abrasion without further improving product quality.

Magnetic separation is a useful additional protective stage, but it is no substitute for a low-abrasion design. It can capture magnetisable foreign particles such as iron or certain ferritic steel fractions, but it does not reliably act against non-magnetic metals such as aluminium, copper or zinc. Demanding process chains therefore combine several measures: magnetic separators at suitable transfer points, screening or filter stages for coarse particles, controlled raw material release, separation ahead of critical process steps, and a suitable design of material transport. Non-magnetic particles must be controlled primarily by avoiding their entry, suitable filtration or screening, and analytical monitoring. According to the technical literature, non-magnetic foreign particles can be introduced into slurries especially during mixing, transport and storage, and are harder to remove.

An effective concept also requires a systematic maintenance and cleanliness strategy. Wear-critical parts should be monitored via operating hours, torque, vibration, differential pressure, product analytics and visual inspections. Not only the mixer but also charging, dosing, screening, conveying lines, filters, valves, maintenance tools and the ambient air belong in the contamination assessment. Preventive replacement of worn components is significantly more effective than subsequently cleaning already contaminated material. Because metallic particles can also enter the system through open interventions, maintenance or the production environment, closed transfers, defined cleaning zones, tool management, suitable protective clothing and controlled material pathways are important elements of the concept.

Verification should combine several analytical levels. ICP-OES and ICP-MS capture total elemental contents and can quantify metals in the ppm to trace range; ICP-MS offers particularly low detection limits. Both methods are used for analysing critical elements in cathode materials, with standards often specifying ICP-OES and citing limit values below 1 mg/kg for relevant contaminants such as Cr, Fe, Cu, Zn and Pb. Magnetic separation tests, microscopic particle analysis and SEM/EDX are useful in addition, in order to identify individual particles in terms of size, morphology and chemical composition. This particle analysis is indispensable, particularly for assessing process-related abrasion, because a low total metal value can mask individual safety-critical coarse particles.

A robust practical strategy begins with a contamination risk analysis. First, the critical elements and particle sizes are derived from the cell manufacturer's specification. All potential sources of contamination along the process chain are then mapped and assessed in terms of probability, quantity introduced and detectability. On this basis follow the choice of materials and construction, the definition of permissible process windows, the positioning of magnets and screens, and a test plan with raw material, intermediate product and final product analytics. It must then be demonstrated with representative active material that the plant meets the agreed limit values even after a defined operating period, after cleaning and after maintenance.

Minimising abrasion and metal contamination

When mixing abrasive battery active masses, particularly cathode active materials, metallic abrasion can be greatly reduced through a coordinated combination of low relative speed, suitable mixing kinematics, wear-optimised materials and a low-contamination design. A universally valid ppm or ppb commitment would not be credible, however. The metal content actually achievable depends on product hardness, particle size distribution, particle shape, moisture, mixing duration, fill level, tool geometry, circumferential speed, material pairing and the analytics chosen. For cathode materials, besides the total quantity, the size, shape, number and elemental composition of individual foreign particles are especially decisive. Metallic particles can be safety-critical because they can promote local defects, internal short circuits and, in extreme cases, thermal runaway.

amixon® first reduces the possible generation of abrasion through the mixing kinematics. The mixing tools operate at comparatively low circumferential speeds starting at about 0.8 m/s and, depending on the task and apparatus design, can be run at up to about 3.5 m/s. SinConvex® total flow-through produces continuous, three-dimensional product circulation. The mix is restratified in a controlled manner instead of being moved through energetic throwing motion, pronounced impact zones or unnecessarily high shear forces. This allows relative speed and contact pressure at critical product-contact surfaces to be reduced. This is particularly important with abrasive, hard particles, because wear typically increases with rising relative speed, repeated particle impact and high local contact pressures.

The choice of materials is matched to the abrasiveness, chemical resistance and contamination target of the respective product. For abrasive powders such as ceramic powders, metal powders, battery materials or mineral mixtures, wear-resistant materials and surface protection systems can be used. These include, for example, Hardox® wear-resistant steel, hardened mixing tools, carbide-tipped designs, duplex stainless steels and ceramic plasma coatings on particularly stressed surfaces. The right choice must always be made on a project-specific basis: a material with high abrasion resistance is not automatically suitable for a battery process chain if it can itself release critical elements, is not chemically resistant, or if its coating is damaged under the actual process conditions.

Constructional avoidance of foreign particle ingress supplements the wear protection. Mixing chambers welded free of crevices and ground smooth, without bolted connections in the product area, reduce possible gaps, loose fastening elements and residue-prone areas. Mixing tools supported only at the top avoid a lower shaft passage in the product space; this avoids product-contact bearing points in the vessel base. Mechanical seals on optional rotors can be designed so that seal and bearing wear remain separated from the product area. Closed, dust-tight systems with OmgaSeal® seals additionally limit the entry of dust and foreign particles from the production environment.

The purity actually achievable must be measured in practice. amixon® can carry out trials with the original product in the pilot plant for this purpose and combine the evaluation with the analytics specified by the operator. ICP-OES or ICP-MS, for example, are suitable for determining elemental metal traces. ICP-MS enables particularly low detection limits and is used for analysing metal contamination in lithium-ion battery materials. In addition, SEM/EDX examinations, magnetic separation tests or imaging particle analyses may be necessary, because the total chemical metal content alone does not reliably capture individual critical coarse particles.

On the basis of such trials, the material pairing, mixing tool, rotational speed, mixing time, fill level and, where applicable, the design of charging, discharge and conveying are matched to the agreed purity value. This does not consider the mixer alone. Raw material feed, containers, dosing units, screens, magnetic separators, conveying lines, filters, transfer points and maintenance procedures can also introduce metal particles. A robust concept for battery materials therefore combines abrasion-minimised mixing design with a comprehensive contamination protection concept covering source materials, plant periphery, separation, preventive maintenance and cleaning processes. Abrasion from processing equipment and ingress via machine components are demonstrably among the relevant sources of contamination in battery production.

amixon® covers a wide batch spectrum with various apparatus designs. Vertical and conical mixers such as VM, HM and AM, as well as mixer-dryer reactors such as VMT and AMT, can be built in project-specific sizes up to about 50,000 litres. The Gyraton® GM is intended for large batches in the range of approximately 10 to 100 m³. For smaller batches, the EM in the range of approximately 5 to 200 litres and the container mixer COM in the range of approximately 100 to 4,000 litres are available. Depending on the product and design, fill levels of approximately 10 to 100 per cent of the usable volume can be possible. However, the actually usable range and the achievable mixing quality must be confirmed for the specific abrasive product through trials.

Pilot plant and validation

At the amixon® pilot plant at its Paderborn headquarters, more than 30 test units in various sizes are available. Trials can additionally be carried out at pilot plants in Japan, India, Thailand, China, South Korea and the USA. The tests are conducted with the original product, realistic fill levels and batch sizes, and under the intended temperature and pressure conditions. Mixing quality, product protection, energy input, cleanability, reproducibility and – particularly relevant for battery active materials – abrasion and metallic contamination are assessed. The results are documented together with amixon® experts and serve as the technical and economic basis for designing the plant before the investment.