Cómo alcanzar un tamaño de partícula inferior a 5 µm en un molino de tres rodillos

Molino de tres rodillos El tamaño de partícula se refiere a qué tan fina se dispersa una pasta o pintura por los rodillos de la máquina, lo que a menudo se informa como una lectura del calibre de molienda Hegman o un valor de difracción láser D50/D90. Al alcanzar un tamaño de partícula de molino de tres rodillos de menos de 5 micrones, muchos operadores han sido durante mucho tiempo un Santo Grial, por un medio simple: apretar más el espacio. Eso funciona -gnante por un tiempo -ñan hasta que no funciona. Una vez que ya tienes un espacio estrecho y una relación de alta velocidad, la lectura de finura se estabiliza exactamente donde lo hizo en la pasada anterior, y al apretar el espacio, otra muesca no hace nada más que calentar el material y desgastar los rodillos más rápido.

Cómo un molino de tres rodillos crea finura y por qué “apretar la brecha” deja de funcionar por debajo de 10 µm

Un molino de tres rodillos crea una reducción del tamaño de partículas al tirar del material a través de dos puntas que se estrechan entre tres rodillos contrarrotativos que funcionan a velocidades relativas crecientes; el creciente diferencial de velocidad entre rodillos adyacentes genera la fuerza de corte que descompone los aglomerados. Apretar el espacio evita aún más mejorar la finura por debajo de aproximadamente 10 micras porque el cuello de botella cambia del ancho del espacio al desgaste del rodillo, una falta de coincidencia entre la viscosidad y la velocidad de corte o un techo de aglomerado ^ tres modos de falla separados que un espacio más estrecho por sí solo no puede arreglar.

Los molinos de tres rodillos (a veces también escritos molino de tres rodillos) reducen el tamaño de las partículas arrastrando el material a través de dos puntas formadas entre tres rodillos colocados horizontalmente (el rodillo de alimentación, el rodillo central y el rodillo de plataforma). Los rodillos adyacentes giran en direcciones opuestas a diferentes velocidades, y cada paso de laminación es cada vez más rápido que el anterior, y es esta brecha de velocidad relativa entre los rodillos lo que crea fuerza de corte. El material absorbido por el rodillo de alimentación ingresa al primer estrecho (entre los rodillos de alimentación y central) y ya está predisperso. Luego ingresa al segundo estrecho (entre los rodillos del medio y del delantal), moviéndose aún más rápido y donde la fuerza de corte es mayor en la línea. Es esta creciente diferencia en la velocidad relativa la que descompone los aglomerados y dispersa partículas de pigmento, resina o ingrediente activo en el vehículo que los rodea, y es el mismo mecanismo ya sea que el producto final sea una pintura, una tinta, un recubrimiento o una base cosmética.

Una configuración eficiente de molino de tres rodillos utilizada correctamente en las industrias de recubrimiento, tinta, pigmentos y procesos cosméticos utiliza el mismo procedimiento -only el material del rodillo, la relación de velocidad y la secuencia de espacios cambian de acuerdo con el material de alta viscosidad que se utilizará.

En su forma más sencilla, un molino de tres rodillos consta de tres rodillos colocados horizontalmente, creados por tres cilindros dispuestos horizontalmente que funcionan en secuencia, el espacio entre el rodillo de alimentación y el rodillo central maneja la predispersión y el espacio entre el rodillo central y el delantal. El rodillo termina el trabajo. Debido a que el proceso de fresado básico se escala desde una unidad de banco de 50 mm a una línea de producción de más de 400 mm sin cambiar en principio, un molino de tres rodillos es una máquina versátil desde lotes a escala de laboratorio hasta series de producción completas. Tres molinos de rodillos se utilizan ampliamente «y los molinos de rodillos se utilizan más ampliamente “en recubrimientos, cosméticos y productos electrónicos dondequiera que sea importante una dispersión fina; Se utilizan específicamente tres molinos de rodillos cuando un proceso necesita más margen de viscosidad del que puede soportar un molino de cuentas.

Dos operadores de palancas buscan primero, con justificación: reducir el espacio conduce a una mayor tensión de corte que el material ve en cada línea de contacto, y una mayor diferencia de velocidad entre los rodillos proporciona una mayor velocidad de corte. Muchos manuales de operación de la industria especifican un espacio de 0,001 pulgadas (aproximadamente 25 µm) como estándar en uso, y para mayor finura se agrega y repite un tensor hasta obtener el tamaño deseado en pasadas sucesivas. Esa es la física, lo que muestra por qué reducir el espacio tiene un efecto bastante consistente hasta que se reducen las primeras micras de tamaño.

Lo que no nos dice es por qué la finura a veces se detiene muy por encima de nuestro objetivo, mientras que la brecha hace tiempo que alcanzó la precisión nominal del molino. Cuando ese es el techo que los operadores encontramos golpeando, la brecha casi nunca es la fuente del problema; el culpable suele ser uno de estos otros tres problemas: el desgaste del rodillo altera la brecha en efecto si no se indica, hay un desajuste entre la viscosidad y la velocidad de corte de ese material, o estamos en el “techo aglomerado” donde las partículas restantes han alcanzado su tamaño de partícula primaria y los pases posteriores no sirven para romperlos más. Elección del material del rodillo también influye en con cuál de estos tres es más probable que te encuentres. La siguiente sección nos lleva a través de una secuencia de diagnóstico en lugar de un enfoque con una sola respuesta.

Troubleshooting a lack of fineness: first, get to understand how the two common test methods actually measure the fineness – because the D90 from a laser diffraction analysis isn’t equivalent to the reading on a grind-gauge, and misinterpreting one as the other is perhaps one of the most frequent ways in which operators convince themselves that they’ve produced a failing batch (or that they’ve produced a passing batch when it should be failing).

Leyendo su medidor de molienda, escala Hegman a micrones

The grind gauge (sometimes known as a Hegman gauge or grindometer) provides a quick, on-the-floor measure of three roll mill particle size between applications. ASTM D1210-05(2022), the Standard Test Method for Fineness of dispersion of pigment-Vehicle Systems by Hegman-Type Gage, was most recently revised in 2005 and reapproved in 2022 without technical changes, and remains the currently approved document to reference. This apparatus consists of a precisely milled steel plate, which has a wedge shaped channel of varying depth (0 – approx 100μm).

A small amount of the product is spread across the length of the channel and read against the inscribed calibrated scale where visible specks or streaks first become visible – the position of this reading on the 0-8 Hegman (or corresponding NS scale) is the grind fineness value.

grind gauges are quick – reading one batch takes less than a minute – which is why they’re ideal for monitoring three roll mill particle size between passes through the shop equipment. Here’s exactly what the gauge is actually measuring, though: ASTM D1210 gauges whether pigment agglomerates have been adequately reduced in size so they won’t mar the coating-film, not whether the whole particle size population has the correct distribution. Two batches may have identical Hegman ratings because both have the same coarse tail, but their median particle sizes – and their complete distributions – could be vastly different. Academic literature on particle-size measurement makes the same point about single-point metrics generally: if you need a full understanding of the batch contents, especially with stringent specifications such as for electronic paste or pharmaceutical suspensions, laser diffraction is a necessary complementary method.

Difracción láser PSD, lo que realmente le dicen D10/D50/D90 y Span

Laser diffraction particle size analysis is controlled by ISO 13320:2020, Particle size analysis – Laser diffraction methods, and a related USGS laboratory laser-diffraction study follows the same method family. It’s worth highlighting the edition in full, because many documents on this topic, including several popular guides currently at the top of the search rankings, continue to refer to the canceled 2009 version, ISO 13320:2009, which was technically replaced in 2020. If a supplier’s data sheet or a competitor’s blog post refers to the 2009 version of the standard, consider it a sign that the content has not been updated in some time.

Laser diffraction analysis results don’t yield a single number, but rather a complete particle size distribution that’s often reported as three percentile values: D10 (the particle size at which 90% of particles are larger than this size), D50 (the median – at which half the particles are larger and half smaller), and D90 (the particle size at which only 10% of particles are larger than this size). Also, a derived metric, span, provides a measure of the breadth of the distribution:

Why this distinction can matter practically is evident from IDA’s testing on an application involving PV silver-paste: one customer was producing 8.2μm D50 (with high variation) using a standard ball-mill method, which fell short of a target paste-supplier specification of <3μm D50 and had an approximate 12% reject rate at the coarser distribution. That same paste ran through a 2-stage grind approach – the first pass was with smaller production three roll mills and the second, a finishing pass, was with hydraulic mill with a gap-servo-adjusted to 2μm – yielding a final D50 of 2.1μm, tighter distribution, and ~2% rejection rate (from 12%). Worth noting is that not only was the mean particle size reduced, but also its variance – which a span calculation could have highlighted prior to looking at rejection data.

Reporting D10/D50/D90 values is standard on nearly all modern particle-characterization equipment, from sophisticated research-level laser diffraction units down to online process quality-control devices. This standardization is helpful; a D90 specification you negotiate with your customer or a raw-material supplier should, in theory, be testable on any laser diffraction unit from any maker.

One caution when treating D90 data as truth: Laser diffraction produces an equivalent spherical diameter – a calculation that determines particle sizes from light-scattering patterns based on a model assuming spherical particles, rather than by direct measurement of particle shape. For roundish pigments or filler materials, the approximation can be quite good, but for flat, needle-like or heavily agglomerated particles, D-values may differ significantly from the actual measured shape viewed under a microscope. Always maintain consistent optical models and refractive indices between instruments when performing comparative analyses, otherwise, changing settings mid-study can result in reported D-values appearing to change without any real shift in the actual process.

Step back from the instrument-specific caveats and the goal is simple: three roll mills remain the standard tool for particle size reduction and for preparing very fine particle dispersions precisely because gap and speed together give you precise control over the particle size distribution — not just an average reading. That precise control lets you reduce the particle size step by step until you reach a uniform particle size and a consistent particle size distribution batch after batch, which is the whole point of running a controlled multi-pass process instead of a single aggressive one.

Secuenciación de brechas paso a paso, un ejemplo práctico

The concept behind gap sequencing is running the largest gap setting first, then successively decreasing it over several passes, as opposed to attempting to achieve a sub-5μm specification in a single pass. Operating with an overly tight gap against a coarse, unprepared feedstock causes two problems: it increases heat and torque, and it may not result in greater fineness significantly more quickly than a carefully designed multiple pass process would. Fracturing larger agglomerate particles is the initial objective, not necessarily achieving the final fineness. A three-roller grinding mill patent covering automatic gap drawback describes the same progressive-tightening logic from the equipment-design side.

“La mayoría de los operadores realizan de 3 a 5 pasadas. El paso uno rompe grandes aglomerados. Cada paso posterior refina la distribución. Verifique la calidad con un medidor de molienda después de cada paso para alcanzar su objetivo exactamente.”

In practical terms, that means don’t assess a mill’s performance by number of passes alone without considering roller diameter and speed ratio. A 5-pass result on a 50mm lab roller can represent the exact same finished fineness as a 3-pass result on an 80mm production roller – the difference in passes is due to roller geometry, not performance.

Best practices for keeping a 3 roll mill running well start with the basics: never let the mill dry between batches, since three adjacent rolls rotating in opposite directions will glaze and score if run without material for more than a few seconds. The take-off knife needs regular sharpening too — a dull edge leaves a thick film of processed material on the apron roll instead of collecting it cleanly. This holds whether the mill is used on one of the smaller bench and floor models in a lab or on a full production line.

Selección de relación de velocidad, 1:2:4 vs 1:3:9 y cuándo se aplica cada uno

The speed ratio refers to the increasing relative rotational speed between the successive rollers and the feed roll – for example, a 1:3:9 ratio means the center roll runs three times the speed of the feed roll and the apron roll runs nine times the speed. High ratios result in higher stress to the shear in each nip, which in turn allows for smaller particle size targets to be reached, but also creates greater friction heat and more wear on the rollers and bearings. Numerous manufacturers provide a specification sheet for their equipment listing a 9/3/1 speed ratio (equivalent phrasing of 1:3:9), for instance, as their high-shear option alongside a gentler 1:2:4 ratio option for softer applications or less stringent requirements.

In the lab or the production line, the choice really comes down to hardness and heat generation during the processing phase. A 2,000,000 mPas viscosity pigment paste having a high hardness value would be a suitable candidate for a 1:3:9 ratio in order to achieve less than 5μm in few passes, assuming the mill is water-cooled and uses ceramic or hardened rollers to mitigate wear. On the other hand, a less hard cosmetic base with a D90 in the less than 10μm range may reach target specs more readily with a 1:2:4 ratio, while generating less heat, and also increasing roller lifespan between maintenance cycles.

We see that this same fundamental concept of manipulating speed relative to volumetric throughput applies in published patent literature in other applications. A patent on an improved particle size distribution for mineral dispersion uses changes in volumetric feed and speed to hit a target particle size; it’s a different packaging of the same relationship between speed ratio selection for a three roll mill.

Since the three rollers rotate at different speeds by design, matching that speed ratio to material hardness is the core decision covered above. When you’re trying to choose the right three roll mill for a new line, it helps to see how established manufacturers handle the same trade-offs — Charles Ross & Son, whose engineering bulletins are cited in the references below, is one well-known Ross three roll mill maker, and comparing a few vendors’ approaches to gap and speed control is a useful way to judge whether a given spec sheet number represents genuine performance.

El techo de finura: diagnóstico de tres causas

Here’s the scenario the gap-tightening argument misses: the mill has its factory-set precision already built in, the speed ratio selected matches the material’s hardness and fineness target, and yet the D90 is still too high. In such a situation, the solution is rarely, if ever, “tighten the gap.” If the mill is running correctly, it’s already operating at the mechanical limits of what that unit can do, and there’s almost certainly one of three specific problems with the setup.

Wear on one of the rollers is the most frequent cause because wear is often invisible in daily operations. Even a severely worn roller can report an accurate reading for the digital gauge (because that number refers to a mechanical position), while the actual spacing between the rollers themselves has increased significantly. Using a micrometer to check against the roller’s original diameter spec can prevent the issue from being caught only after fineness is affected. roller material plays a role in how fast wear happens. The material selection for a ceramic roller will influence its lifespan relative to an alloy-steel one.

As grinding equipment goes, roller material is where a lot of the cost-versus-durability trade-off lives. Hardened steel rolls (often just called steel rolls) are the economical default for general industrial use, and they handle medium to high viscosity viscous materials without issue as long as metal contamination isn’t a concern. Ceramic rolls cost more but remove that risk entirely (see the roller materials guide for the full contamination-risk and cost-per-hour breakdown). Either way, best practices call for inspecting the roller surface regularly for scoring or pitting — that’s the fastest way to catch wear before it shows up as a fineness complaint down the line.

Most frequently, operators mistakenly identify the viscosity-shear mismatch to be a matter of “machine is too weak,” when the actual fix requires only a process parameter adjustment instead of equipment. And the agglomerate ceiling is precisely the one you should be checking last — because it’s the only of the three for which milling adjustment of any kind will no longer do — now the fineness has been kicked upstream to the raw material.

As one piece of illustrative patent evidence for this class of equipment, a published three-roller grinding mill utility patent describes a machine expressly designed to discriminate abrasive particles by size and handle automatic roller drawback — a mechanical solution to the exact problem of wear and clearance discussed above. This shows that roller wear compensation is already known as an issue for this type of equipment, one significant enough to warrant a dedicated patent application.

There’s one other consideration to check before accepting the mill is at a true fineness limit: over-compression itself. Particle characterization studies published about roll crushing have demonstrated that with reduced spacing you achieve both breaking and agglomeration simultaneously, and this means that the D90 that’s reading “stuck” or even ticks upward during passes isn’t always a signal to increase the amount of shear that you’ve applied-instead it’s a signal that the current pass has the effect of re-agglomerating material that has already reached fineness. If you’re reducing the space and the D90 value is getting worse and not better then this suggests backing off one increment of closing and repeating with the same space on the next pass.

Apunte a la finura mediante la aplicación, ¿a qué debería aspirar realmente?

“Sub-5μm” isn’t an absolute – what’s ‘fine’ will depend in large part upon the end use of the dispersion and how much of the milled material ends up in that end product. Specifying more fine material than the application requires simply results in more passes and more roller wear with no benefit. On the other hand, underspecifying will result in a rejection and the loss of production capacity that can’t be compensated for by simply adjusting the amount of shear.

Note how that “finer is better” isn’t necessarily the guiding principle for any mill system – the acceptable particle size distributions for architectural pigment and adhesives are significantly more coarse than for cosmetics or for electronic paste, because their functional properties such as gloss or bond-line thickness aren’t dictated by very fine particle size control, but in contrast, for example, because strict adherence to very low contamination levels is a requirement of a cosmetics product line — and for the pharmaceutical row above, regulatory literature on particle-size analysis ties the target directly to dosing uniformity, not just texture. When considering particle size specifications for the product and then selecting a grind and mill system the final goal is to select and use those equipment pieces which satisfy those product requirements in an economically justifiable way; one doesn’t default to the most restrictive specification which one may have encountered, or the least expensive.

¿qué está cambiando en la verificación de la finura

Fineness verification is shifting from single-point checks toward paired measurement: more manufacturers now confirm a grind-gauge reading with a full laser-diffraction particle size distribution rather than relying on either method alone. Tightening scrutiny from regulators and end-users is driving the shift, not a change in how three roll mills grind — buyers increasingly expect documented D10/D50/D90/span data alongside a Hegman number, especially for cosmetics, pharmaceutical, and export-grade specifications.

Clearly the driving factor behind the way the fineness is being checked now isn’t a change in the way we perform the mill step, but the increase in the scrutiny by end-users and regulatory bodies of product quality leading to more and more users utilizing two, not just one measurement methods. This is demonstrated by the IDA cosmetics product application, where for example a European customer’s launch of a new liquid foundation formulation necessitated confirmation of zero heavy metal contamination by ICP-MS due to stringent EU regulations – that’s in addition to checking particle size distribution to confirm a grind reading and ensure no roller contributed metals were present from the roller material (ceramic vs. alloy steel).

One more point made by the particle-size measurement literature is useful for anyone contemplating the design of a QC process around the topic: “full distribution analysis” (as is produced by laser diffraction) is generally considered a more justifiable basis for quality-system/regulatory sign-off than is either a standalone, single-point measurement, such as a grind gauge reading or just a number-based D50 without span. If you’re setting up a QC protocol in 2026 to address a tight-specification process-e.g., for electronic paste, pharmaceutical, or export cosmetics-then budgeting for both a grind gauge (quick in-line check between passes) and periodic laser-diffraction confirmation (full-distribution QC sign-off) is more defensible than betting on a single measurement device to provide all the information needed to assess product quality.

Market researchers expect the particle-size analysis market to continue expanding through the end of the decade, based on market research forecasts; that data offer only a directional signal of expanding investment throughout the industry, however-it tells you neither what nor how to measure, so regulatory/full-distribution considerations are more significant in practice than raw market growth numbers.

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