{"id":16724,"date":"2026-04-24T08:14:07","date_gmt":"2026-04-24T08:14:07","guid":{"rendered":"https:\/\/www.jet-mills.com\/?p=16724"},"modified":"2026-04-24T08:16:46","modified_gmt":"2026-04-24T08:16:46","slug":"hard-carbon-anode-ice-powder-morphology-jet-milling-guide","status":"publish","type":"post","link":"https:\/\/www.jet-mills.com\/ko\/hard-carbon-anode-ice-powder-morphology-jet-milling-guide\/","title":{"rendered":"\uacbd\uc9c8 \ud0c4\uc18c \uc591\uadf9 ICE: \ubd84\ub9d0 \ud615\ud0dc \ubc0f \uc81c\ud2b8 \ubc00\ub9c1 \uac00\uc774\ub4dc"},"content":{"rendered":"

Hard carbon is currently the leading commercial anode material for sodium-ion batteries<\/a> (SIBs). It offers a practical sodium storage capacity of 200-350 mAh\/g and operating at a sufficiently low potential to be useful in full-cell configurations. The obstacle to wider adoption is initial Coulombic efficiency<\/a> (ICE): the ratio of first-cycle discharge capacity to first-cycle charge capacity. For many hard carbon materials, ICE falls in the 70-85% range. It means 15-30% of the sodium inserted during the first charge is irreversibly lost and never recovered. In a full cell, this lost sodium must be compensated by extra cathode material. It adds weight, volume, and cost to the cell design.<\/p>\n\n\n\n

Researchers well understand two mechanisms behind low ICE: irreversible sodium consumption during SEI film formation at the anode surface, and irreversible trapping of sodium ions in surface defects and functional groups. But the production context less widely discusses that the powder morphology of the hard carbon material directly influences both mechanisms. Specifically, the powder morphology influences its particle shape (sphericity), specific surface area, and pore structure. These are parameters that the particle processing step, not the synthesis chemistry, primarily determines.<\/p>\n\n\n\n

This article covers the mechanistic connections between powder morphology and ICE, the practical constraints this places on morphology control methods, and why fluidised bed \uc81c\ud2b8 \ubc00\ub9c1<\/a> offers advantages over conventional ball milling for hard carbon processing.<\/p>\n\n\n\n

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\uacbd\uc9c8 \ud0c4\uc18c \uc591\uadf9\uc7ac<\/figcaption><\/figure>\n\n\n\n

The SEI Film Problem: Why Surface Area and Shape Matter<\/mark><\/h2>\n\n\n\n

During the first charge cycle of a sodium-ion battery, the electrolyte is thermodynamically unstable at the potential of the hard carbon anode. It decomposes at the carbon surface, forming the SEI film \u2014 a mixed organic-inorganic passivation layer that is ionically conductive (sodium ions pass through it) but electronically insulating (it stops further electrolyte decomposition once formed). The SEI is essential: without it, electrolyte would continue to decompose throughout the cell’s life. But forming it consumes sodium irreversibly, and that is the core ICE problem.<\/p>\n\n\n\n

Two morphological factors determine how much sodium the SEI formation consumes. First, specific surface area: SEI film formation occurs at the carbon-electrolyte interface. More interface means more SEI, which means more sodium consumed. A hard carbon powder with high specific surface area from abundant open pores, surface roughness, or very small particle size will lose more sodium to SEI than one with lower specific surface area at equivalent capacity. Second, surface defects and functional groups: oxygen-containing surface functional groups (\u2013COOH, \u2013OH) react preferentially with the electrolyte and trap sodium ions irreversibly through adsorption. Surface defects \u2014 edge sites, broken carbon bonds, dangling bonds \u2014 are similarly reactive. Both are present in higher density on irregularly shaped particles with sharp edges and corners than on smooth, rounded particles.<\/p>\n\n\n\n

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Particle Surface<\/figcaption><\/figure>\n\n\n\n

How Particle Shape Affects ICE<\/mark><\/h2>\n\n\n\n

The influence of particle shape on ICE operates through the specific surface area and surface defect density pathways described above. Irregular particles \u2014 elongated fragments, angular shards, flat platelets \u2014 have higher surface area per unit volume than spherical particles of equivalent median size. They also have more edges, corners, and surface discontinuities where defects concentrate.<\/p>\n\n\n\n

Research published in ACS Nano has shown that modulating the orbital hybridization state of carbon materials to enrich sp2 hybridised carbon at the interface can reduce electrolyte binding energy and suppress non-uniform SEI growth. Practically, this means that a rounder particle surface with lower defect density is preferable \u2014 and sphericity is the processing parameter that most directly controls whether the particle surface is smooth and sp2-dominated or rough and defect-rich.<\/p>\n\n\n\n

Higher sphericity also improves electrode packing density (tap density), which allows more active material per unit electrode volume and reduces the electrolyte-to-active-material ratio in the electrode, further limiting SEI formation.<\/p>\n\n\n\n

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\uc81c\ud2b8\ubc00 \uc0dd\uc0b0 \ub77c\uc778<\/figcaption><\/figure>\n\n\n\n

How Pore Structure Affects ICE<\/mark><\/h2>\n\n\n\n

Hard carbon contains three distinct pore types, each with a different effect on sodium storage and ICE.<\/p>\n\n\n\n

Open Pores and Specific Surface Area<\/mark><\/h3>\n\n\n\n

Open pores \u2014 mesopores and macropores accessible to electrolyte \u2014 increase specific surface area and provide additional interface for electrolyte decomposition and SEI formation. The BET surface area of hard carbon for SIBs is typically in the range of 2-15 m2\/g; materials at the higher end of this range lose proportionally more sodium to SEI. Open pores are beneficial for electrolyte wetting and sodium ion transport kinetics but are costly in ICE terms. The processing objective is to minimise unnecessary open porosity while preserving closed pores.<\/p>\n\n\n\n

Micropores and Sodium Trapping<\/mark><\/h3>\n\n\n\n

Micropores \u2014 particularly ultramicropores below 0.7 nm \u2014 are a primary site for irreversible sodium trapping. Research published in Nature Communications has shown that the desolvation process of sodium ions in nanopores significantly affects ICE: sodium ions that enter pores below approximately 0.7 nm cannot easily exit once desolvated, and are lost to irreversible capacity. Additionally, micropores increase the contact area between electrolyte and carbon, promoting non-uniform SEI formation.<\/p>\n\n\n\n

The implication for particle processing: any method that creates additional micropores in the hard carbon structure degrades ICE. This is the specific limitation of conventional high-energy ball milling for hard carbon. The mechanical forces break C-C bonds, generating free radicals and surface defects that, during subsequent heat treatment, form abundant micropores. Controlled ball milling can be useful for initial size reduction, but the parameters must be tightly limited to avoid excessive micropore generation.<\/p>\n\n\n\n

Closed Pores and Sodium Storage<\/mark><\/h3>\n\n\n\n

Cavities not accessible to electrolyte are the most complex and most valuable pore type in hard carbon for SIBs. Closed pores in the 2-3 nm range are the primary sites for the ‘pore-filling’ sodium storage mechanism that gives hard carbon its high capacity at low potential (below 0.1 V vs. Na\/Na+). Because electrolyte cannot enter closed pores, sodium stored in them does not contribute to SEI formation. This is ICE-positive sodium storage. Research published in Advanced Functional Materials has shown that tuning closed pore size and distribution improves sodium diffusion kinetics and rate capability.<\/p>\n\n\n\n

Preserving closed pores through particle processing is therefore critical. Prolonged or high-energy mechanical processing \u2014 particularly extended vibratory ball milling \u2014 can collapse closed pores by compressive impact forces, eliminating the very sites that make hard carbon an effective SIB anode. This is the double-edged sword of ball milling for hard carbon. The same mechanical action that achieves size reduction and spheroidisation can destroy the pore structure that determines electrochemical performance.<\/p>\n\n\n\n

Pore Type<\/strong><\/td>Size Range<\/strong><\/td>ICE Effect<\/strong><\/td>Processing Implication<\/strong><\/td><\/tr>
Open pores (mesopores)<\/td>2-50 nm<\/td>Negative \u2014 increases SEI formation<\/td>Minimise; keep BET surface area below 5 m2\/g where possible<\/td><\/tr>
Ultramicropores<\/td>< 0.7 nm<\/td>Strongly negative \u2014 irreversible Na trapping<\/td>Avoid creating during processing; avoid excessive ball milling<\/td><\/tr>
Closed pores (optimal)<\/td>2-3 nm<\/td>Positive \u2014 high-capacity, ICE-neutral Na storage<\/td>Preserve through processing; avoid high-energy impact<\/td><\/tr><\/tbody><\/table><\/figure>\n\n\n\n

Morphology Control Methods: Plasma Treatment and Ball Milling<\/mark><\/h3>\n\n\n\n

Plasma Treatment: Surface Cleaning Without Pore Damage<\/mark><\/h3>\n\n\n\n

Plasma treatment, particularly dielectric barrier discharge (DBD) in a reducing atmosphere such as H2 or CO \u2014 is a surface engineering approach. It addresses the functional group problem without disturbing the bulk pore structure. High-energy plasma species etch and remove surface oxygen-containing groups (\u2013COOH, \u2013OH) that would otherwise irreversibly trap sodium. The same treatment can repair surface defects and induce partial graphitisation of the outermost surface layer. It can also improve both ICE and interfacial conductivity.<\/p>\n\n\n\n

The practical limitation of plasma treatment is that it operates on the existing surface morphology. It cannot change particle size or sphericity. A hard carbon that exits pyrolysis as irregular angular fragments will remain irregular after plasma treatment, retaining the high-surface-area, high-defect-density morphology that limits ICE. Plasma treatment is most effective as a post-processing step after the particle shape and size have already been optimised by milling.<\/p>\n\n\n\n

Ball Milling: Useful but Requiring Strict Parameter Control<\/mark><\/h3>\n\n\n\n

Ball milling can achieve both size reduction and partial spheroidisation of hard carbon. High-energy ball milling with optimised milling time and media size produces submicron to micron-scale particles with increased roundness compared to the as-pyrolysed irregular fragments. The mechanical forces during milling can also tune the pore structure: pitch-based and phenolic resin-derived hard carbons show increased closed pore content after controlled ball milling followed by heat treatment.<\/p>\n\n\n\n

However, the same mechanical forces that produce these beneficial effects can destroy existing closed pores. It happens if milling parameters are not tightly controlled. Excessively increase specific surface area through micropore generation, and introduce metal contamination from media wear. The acceptable milling energy input is bounded above by the onset of pore collapse and below by insufficient size reduction or spheroidisation. This window is narrower for hard carbon than for most minerals. It depends on the specific precursor and pyrolysis conditions. Controlling milling parameters requires empirical optimisation for each hard carbon formulation.<\/p>\n\n\n\n

Where Jet Milling Fits: Advantages Over Ball Milling for Hard Carbon<\/mark><\/h2>\n\n\n\n
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Fluidised bed jet milling addresses several of the limitations of ball milling that are specific to hard carbon processing for sodium-ion battery anodes.<\/p>\n\n\n\n

No Grinding Media: Zero Metal Contamination<\/mark><\/h3>\n\n\n\n

Jet milling grinds hard carbon entirely through particle-on-particle collision, driven by compressed gas jets. There is no grinding media and no media-particle contact. Metal contamination from wear \u2014 the iron, chromium, and other metals that steel or even ceramic ball mill media introduce into the product \u2014 is eliminated. For sodium-ion battery anode materials where metallic impurities can catalyse SEI decomposition or introduce electrochemically active species, contamination-free processing is a significant advantage.<\/p>\n\n\n\n

Controlled Impact Energy: Preserving Closed Pores<\/mark><\/h3>\n\n\n\n

The critical limitation of ball milling for hard carbon is that excessive impact energy collapses closed pores. In a fluidised bed jet mill, the grinding energy is controlled by gas pressure (typically 4-8 bar) and jet configuration. Importantly, the total energy delivered to each particle is determined by residence time in the grinding zone, which is controlled by the integrated classifier wheel. When a particle reaches the target size, the classifier removes it from the grinding zone immediately. It is not subjected to additional impact events that could damage its pore structure. This prompt removal of on-spec particles is what allows the jet mill to achieve target D50 without the over-processing that destroys closed pores in a ball mill.<\/p>\n\n\n\n

The grinding pressure can also be tuned. Lower pressure produces less intense collisions, which is appropriate for hard carbon where pore preservation is the priority. Higher pressure is used when particle size reduction is the primary objective. This tunability allows the process engineer to optimise the balance between size reduction, spheroidisation, and pore preservation for a specific hard carbon formulation.<\/p>\n\n\n\n

Nitrogen Atmosphere: Preventing Surface Oxidation<\/mark><\/h3>\n\n\n\n

Hard carbon surfaces, particularly those that have been freshly processed to smaller particle size with exposed fresh surfaces, are susceptible to oxidation in air. Surface oxidation introduces oxygen-containing functional groups \u2014 the same groups that plasma treatment removes \u2014 which increases SEI formation and reduces ICE. Jet mills can be operated in a closed nitrogen atmosphere, with nitrogen as the grinding gas rather than compressed air. It prevents any oxidation of freshly generated surfaces during the milling step. This is particularly important for hard carbon from oxygen-sensitive precursors or for materials where the surface chemistry is tightly specified.<\/p>\n\n\n\n

Particle Size and Sphericity for SIB Anode Applications<\/mark><\/h3>\n\n\n\n

Typical particle size targets for hard carbon anode powders in sodium-ion batteries are D50 in the 5-12 micron range. Its D97 below 20-25 microns. This range balances electrode packing density, electrolyte accessibility, and the sodium diffusion path length within the particle. A fluidised bed jet mill with integrated dynamic classifier can consistently produce hard carbon in this range with a controlled D97 upper limit. The classifier prevents oversize particles from reporting to the product stream. It is particularly important for electrode coating processes that are sensitive to particle size outliers.<\/p>\n\n\n\n

\uc694\uc778<\/strong><\/td>Ball Milling<\/strong><\/td>Fluidised Bed Jet Milling<\/strong><\/td><\/tr>
Metal contamination<\/td>Yes \u2014 media and liner wear<\/td>None \u2014 no media<\/td><\/tr>
Closed pore preservation<\/td>Risk at high energy input or long milling<\/td>Better \u2014 classifier removes particles before over-processing<\/td><\/tr>
Micropore generation<\/td>High risk with excessive milling<\/td>Lower \u2014 controlled impact energy<\/td><\/tr>
D97 \uc81c\uc5b4<\/td>Requires external classifier; less precise<\/td>Integrated classifier \u2014 hard upper cut<\/td><\/tr>
\uc9c8\uc18c \ubd84\uc704\uae30 \uc635\uc158<\/td>Complex and costly for wet\/dry ball mill<\/td>\uc81c\ud2b8 \ubc00\uc758 \ud45c\uc900 \uc635\uc158<\/td><\/tr>
Surface oxidation risk<\/td>Moderate \u2014 media contact generates heat<\/td>Lower \u2014 cooling effect from gas expansion; N2 option<\/td><\/tr>
Spheroidisation mechanism<\/td>Mechanical abrasion (effective but requires optimisation)<\/td>Repeated low-energy particle collisions (gentler)<\/td><\/tr><\/tbody><\/table><\/figure>\n\n\n\n
Processing Hard Carbon for Sodium-Ion Battery Anodes?<\/mark><\/strong>
\uc5d0\ud53d \ud30c\uc6b0\ub354<\/a> Machinery’s fluidised bed jet mills are configured for hard carbon and other sodium-ion battery anode materials \u2014 delivering morphology-controlled, contamination-free particle processing in closed nitrogen atmosphere. We offer free test grinds on your hard carbon material and return PSD data, SEM images confirming sphericity, BET surface area measurements, and a recommended process configuration.Tell us your precursor type, target D50, required sphericity, and whether nitrogen atmosphere is needed for your application.  <\/strong>
Request a Free Hard Carbon Test Grind: www.jet-mills.com\/contact-us<\/a><\/mark><\/strong>
Explore Our Sodium-Ion Battery Material Solutions: www.jet-mills.com<\/a><\/mark><\/strong><\/td><\/tr><\/tbody><\/table><\/figure>\n\n\n\n
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