Publications

Browse PTI technical publications

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Find technical publications by the powder behavior, material property, process, or measurement you are working with. You can also browse the latest releases, choose an editorial format, or open the complete publication catalog.

Publications

Browse PTI technical publications

Find content by subject, editorial format, or publication date

Find technical publications by the powder behavior, material property, process, or measurement you are working with. You can also browse the latest releases, choose an editorial format, or open the complete publication catalog.

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Latest from PTI

Recently published

The four newest PTI publications appear here automatically, regardless of subject or editorial format.

  • Granular blend flowing through an inclined chute, with fine particles concentrating near the base and larger particles migrating toward the free surface.
    27 October 2026

    Why Can a Uniform Blend Segregate in a Chute?

    A uniform blend can develop a particle-size gradient while flowing through a [...]

  • Illustrative Dv10 versus obscuration plot showing high variability at low concentration, a stable measurement window, and decreasing apparent Dv10 at high obscuration.
    26 October 2026

    Why Can Higher Obscuration Create False Fines?

    A finer PSD at higher obscuration does not automatically indicate better dispersion [...]

  • Cutaway of a rotary airlock showing partially filled powder pockets, returning gas near the inlet, and discharge into a pneumatic conveying line.
    24 October 2026

    Rotary Valve Failure Modes: How Powder Properties Drive Leakage, Wear, and Jamming

    When a rotary airlock valve leaks, wears, or jams, the cause usually lies in the powder rather than the equipment. This insight maps cohesion, abrasiveness, bulk density, and particle size distribution to distinct failure patterns and explains what each pattern tells you about the powder state.

    Insights

  • Technician checking CMP slurry point-of-use filtration for oversize agglomerates that cause wafer scratch defects
    24 October 2026

    CMP Slurry Abrasive Powders: Why Trace Oversize Agglomerates, Not Median Particle Size, Drive Wafer Scratch Defects

    Median particle size passes QC while wafers still scratch. Here is why a ppm-level population of 1 to 10 micron agglomerates in CMP slurry drives scratch defects, and which measurements actually catch it.

    Feature Article

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Choose the depth and type of content

Feature Articles, Insights, and Know How are editorial formats within PTI publications. They are not separate technical destinations.

Feature Articles

Long-form technical analysis built around a defined engineering question, comparison, mechanism, process, or application.

Technical Briefs

Concise, practical explanations of focused powder and particle technology questions, mechanisms, measurement issues, and process challenges.

Insights

Focused interpretation of a study, method comparison, process result, standard, or emerging technical development.

Know How

Practical technical guides that go deeper into measurement, interpretation, equipment, and powder-behavior decisions.

Feature Articles

Long-form technical analysis

Recent Feature Articles examine a defined engineering question in greater depth, connecting mechanisms, measurements, process context, and interpretation where the subject requires it.

  • Technician checking CMP slurry point-of-use filtration for oversize agglomerates that cause wafer scratch defects
    24 October 2026

    CMP Slurry Abrasive Powders: Why Trace Oversize Agglomerates, Not Median Particle Size, Drive Wafer Scratch Defects

    Median particle size passes QC while wafers still scratch. Here is why a ppm-level population of 1 to 10 micron agglomerates in CMP slurry drives scratch defects, and which measurements actually catch it.

    Feature Article

  • LFP cathode powder sample taken during calcination in a lithium iron phosphate production line
    17 October 2026

    LFP Cathode Powder Production: How Spray-Drying, Calcination, and Pulverization Set Particle Size and Tap Density Targets

    LFP cathode powder quality is built in stages, not inspected at the end. This article follows the precursor-to-powder route and shows why particle size distribution and tap density are the measurements that actually tell you whether the synthesis worked.

    Feature Article

  • Industrial cyclone separator used for cyclone cut size classification of powder fines
    10 October 2026

    Cyclone Separation of Fine Powders: Cut Size, Efficiency Curves, and Agglomeration

    The classical cyclone cut size model assumes discrete, non-agglomerating particles. Cohesive or moisture-sensitive fines can travel through a cyclone as agglomerates instead, which changes what a PSD result actually tells you about classifier performance.

    Feature Article

  • Wood powder bridging above the outlet of a stainless-steel hopper
    3 October 2026

    Wood Powder Feeding Problems: Separating Moisture Effects From Particle Interlocking

    Wood powder can bridge because fibrous particles mechanically interlock, because moisture increases [...]

    Feature Article

Technical Briefs

Concise answers to focused technical questions

Recent Technical Briefs provide concise, practical explanations of focused powder and particle technology questions, covering specific mechanisms, measurement issues, processing challenges, and interpretation problems.

  • Granular blend flowing through an inclined chute, with fine particles concentrating near the base and larger particles migrating toward the free surface.
    27 October 2026

    Why Can a Uniform Blend Segregate in a Chute?

    A uniform blend can develop a particle-size gradient while flowing through a [...]

  • Illustrative Dv10 versus obscuration plot showing high variability at low concentration, a stable measurement window, and decreasing apparent Dv10 at high obscuration.
    26 October 2026

    Why Can Higher Obscuration Create False Fines?

    A finer PSD at higher obscuration does not automatically indicate better dispersion [...]

  • Side-by-side XRF analysis of pressed powder pellets with magnified views comparing coarse and fine mineral grains.
    23 October 2026

    Why Can XRF Results Change With Particle Size?

    A reported XRF concentration depends on the prepared specimen as well as its [...]

  • BET surface area analysis showing a powder degassing station and nitrogen versus krypton adsorption on a magnesium stearate surface.
    22 October 2026

    Why Do BET Results Change With Degassing and Adsorptive Gas?

    A BET surface area reflects how the sample was prepared and which adsorptive [...]

Insights

Focused technical interpretation

Recent Insights examine a study, method, process result, standard, or emerging technical development in a tighter editorial format.

  • Cutaway of a rotary airlock showing partially filled powder pockets, returning gas near the inlet, and discharge into a pneumatic conveying line.
    24 October 2026

    Rotary Valve Failure Modes: How Powder Properties Drive Leakage, Wear, and Jamming

    When a rotary airlock valve leaks, wears, or jams, the cause usually lies in the powder rather than the equipment. This insight maps cohesion, abrasiveness, bulk density, and particle size distribution to distinct failure patterns and explains what each pattern tells you about the powder state.

    Insights

  • Technical illustration of a funnel-flow silo showing localized contamination zones missed by a powder sampling probe.
    17 October 2026

    Why Can a Powder Lot Pass Sampling and Still Be Contaminated?

    September 2026's moringa leaf powder recall, set against a year of Salmonella events touching powdered milk and supergreens blends, shows why bulk powder sampling plans can miss low-prevalence contamination and why low water activity slows but does not eliminate pathogen survival.

    Insights

  • Diagram comparing Hausner ratio, shear cell, and dynamic flow energy methods used in PBF powder flowability testing
    10 October 2026

    PBF Powder Flowability Testing: Why Different Methods Disagree and What the Results Mean

    Hausner ratio, shear cell, and dynamic flow energy results on the same PBF powder lot rarely agree exactly. That disagreement is a decision input, not proof that a method or lab got it wrong.

    Insights

  • DEM comparison of powder flow in two hopper geometries, showing smooth discharge and arching
    3 October 2026

    DEM Calibration: Why a Model That Reproduces One Bulk Test Can Still Fail in a Different Hopper Geometry

    DEM input parameters are fitted to match a bulk observable, not derived from first principles. A parameter set calibrated against an angle of repose test constrains one point in a multi-dimensional parameter space. When the hopper geometry changes, the stress state changes, and unconstrained parameters become the dominant source of prediction error.

    Insights

Know How

Practical technical guidance

Recent Know How publications focus on practical measurement, method selection, interpretation, equipment, and technically useful working guidance.

  • Illustration comparing spiral jet milling with fluidized-bed opposed jet milling and particle classification.
    3 October 2026

    Micronization by Jet Milling: How Classification, Milling Intensity, and Time Change Surface Properties

    Jet milling micronization reduces particle size through particle-particle impact controlled by classifier wheel speed and feed rate. Pushing the cut point lower can raise amorphous surface content and hygroscopicity in ways a passing PSD result will not reveal. This guide covers the mechanism and the tests that actually diagnose a changed lot.

    Know How

  • Jenike shear cell vs ring shear tester comparison diagram for hopper design decisions
    5 September 2026

    Jenike Shear Cell vs Ring Shear Tester: Matching the Method to the Hopper or Silo Decision

    Jenike shear cells and ring shear testers measure the same yield locus through different mechanics. Here is how their sample, stress range, and time differences map onto the mass-flow versus funnel-flow hopper design decision, plus a checklist for choosing between them.

    Know How

  • Technical illustration of dynamic powder testing, showing a rotating blade moving through a powder bed to compare confined flow energy, low-confinement specific energy, and aeration-sensitive behavior.
    1 August 2026

    Dynamic and Aerated Powder Testing: What Flow Energy Adds Beyond the Shear Cell and Hausner Ratio

    Dynamic and aerated powder testing measures basic flow energy and specific energy to fill the gap between shear cell consolidation data and Hausner ratio screening, particularly for fluidized processing and rapid-refill feeding.

    Know How

  • Technical hero image for a PowderTechnology.info Monthly Know-How on Hausner Ratio and Carr Index, showing two graduated cylinders with loose and tapped powder, three different powder mechanism backgrounds, the Hausner Ratio and Carr Index formulas, a workflow from result to next test, and a reference to an included practical interpretation guide.
    4 July 2026

    Hausner Ratio and Carr Index: What the Numbers Tell You and Where They Break Down

    Both the Hausner Ratio and Carr Index reduce bulk and tapped density to a single number. The mechanism behind that number, whether aeration, particle shape, or surface cohesion, determines whether it supports a process decision or actively misleads one.

    Know How

All Publications

The complete PTI publication catalog

Browse all published PTI content, newest first. Use the subject index above when you know the technical topic, or the structured PTI hubs when you want a guided route through a problem, property, measurement, process area, or industry.

  • Granular blend flowing through an inclined chute, with fine particles concentrating near the base and larger particles migrating toward the free surface.
    27 October 2026

    Why Can a Uniform Blend Segregate in a Chute?

    A uniform blend can develop a particle-size gradient while flowing through a [...]

  • Illustrative Dv10 versus obscuration plot showing high variability at low concentration, a stable measurement window, and decreasing apparent Dv10 at high obscuration.
    26 October 2026

    Why Can Higher Obscuration Create False Fines?

    A finer PSD at higher obscuration does not automatically indicate better dispersion [...]

  • Cutaway of a rotary airlock showing partially filled powder pockets, returning gas near the inlet, and discharge into a pneumatic conveying line.
    24 October 2026

    Rotary Valve Failure Modes: How Powder Properties Drive Leakage, Wear, and Jamming

    When a rotary airlock valve leaks, wears, or jams, the cause usually lies in the powder rather than the equipment. This insight maps cohesion, abrasiveness, bulk density, and particle size distribution to distinct failure patterns and explains what each pattern tells you about the powder state.

    Insights

  • Technician checking CMP slurry point-of-use filtration for oversize agglomerates that cause wafer scratch defects
    24 October 2026

    CMP Slurry Abrasive Powders: Why Trace Oversize Agglomerates, Not Median Particle Size, Drive Wafer Scratch Defects

    Median particle size passes QC while wafers still scratch. Here is why a ppm-level population of 1 to 10 micron agglomerates in CMP slurry drives scratch defects, and which measurements actually catch it.

    Feature Article

  • Side-by-side XRF analysis of pressed powder pellets with magnified views comparing coarse and fine mineral grains.
    23 October 2026

    Why Can XRF Results Change With Particle Size?

    A reported XRF concentration depends on the prepared specimen as well as its [...]

  • BET surface area analysis showing a powder degassing station and nitrogen versus krypton adsorption on a magnesium stearate surface.
    22 October 2026

    Why Do BET Results Change With Degassing and Adsorptive Gas?

    A BET surface area reflects how the sample was prepared and which adsorptive [...]

  • Side-by-side NIR moisture measurement of coarse and fine powders, illustrating how particle size changes diffuse light scattering.
    21 October 2026

    Why Does an NIR Moisture Reading Shift When Particle Size Changes?

    NIR moisture predictions depend on both water absorption and light scattering. Changing [...]

  • Comparison of untreated and silica-treated powder discharge, showing increased airborne dust and magnified silica particle detachment.
    20 October 2026

    Why Can Anti-Caking Agents Increase Dustiness?

    An additive that improves powder flow or caking resistance can also increase [...]

  • Comparison of funnel and scoop filling methods showing different powder bed heights and particle packing arrangements in identical measuring cylinders.
    19 October 2026

    Why Does Pouring Method Change Bulk Density?

    Loose bulk density depends on how powder enters the measuring container. Funnel [...]

  • Technical illustration of a funnel-flow silo showing localized contamination zones missed by a powder sampling probe.
    17 October 2026

    Why Can a Powder Lot Pass Sampling and Still Be Contaminated?

    September 2026's moringa leaf powder recall, set against a year of Salmonella events touching powdered milk and supergreens blends, shows why bulk powder sampling plans can miss low-prevalence contamination and why low water activity slows but does not eliminate pathogen survival.

    Insights

  • LFP cathode powder sample taken during calcination in a lithium iron phosphate production line
    17 October 2026

    LFP Cathode Powder Production: How Spray-Drying, Calcination, and Pulverization Set Particle Size and Tap Density Targets

    LFP cathode powder quality is built in stages, not inspected at the end. This article follows the precursor-to-powder route and shows why particle size distribution and tap density are the measurements that actually tell you whether the synthesis worked.

    Feature Article

  • Laser diffraction illustration showing identical scattering data producing different particle size distributions, with a greater shift in D10 than D50 after changing optical settings.
    16 October 2026

    Refractive Index in Laser Diffraction: D10 vs D50

    Laser diffraction calculates particle size from measured scattering using an optical model [...]

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