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Feature Article

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  • 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

  • Fertilizer powder and granule handling at a bagging line showing dust extraction at the fill spout
    26 September 2026

    Fertilizer Powder and Granule Handling: Segregation, Caking, and Dust Control

    Bulk-blended fertilizer fails in three recurring ways: segregation between straight materials of different size and density, hygroscopic caking in urea and ammonium nitrate under humidity cycling, and dust release during bagging. Each failure mode maps to a specific diagnostic test rather than a single generic powder check.

    Feature Article

  • Closed vacuum conveying system transferring fine powder through a stainless-steel line into a filter receiver with secondary filtration and vacuum generation.
    19 September 2026

    Vacuum Conveying for Fine and Hazardous Powders: Containment, Velocity, and Filter Design

    Vacuum conveying contains by default: any breach draws air inward rather than pushing powder out. That containment advantage comes with a fixed pressure budget, and filter design competes directly with conveying velocity for every millibar of available driving force.

    Feature Article

  • Co-processed excipient powder sample tested for flow and compaction near a continuous direct compression feed frame
    12 September 2026

    Co-Processed Excipients in Continuous Manufacturing: How Particle Engineering Changes Powder Flow and Compaction Performance

    Co-processing engineers particle morphology, density, and surface structure into a single composite excipient particle. Flow function and compactibility testing show what that buys formulators on continuous direct compression lines, and where it does not.

    Feature Article

  • Copper powder feedstock being loaded into a laser powder bed fusion machine for additive manufacturing
    5 September 2026

    GRCop-42 and the Copper Powder Feedstock Problem in Laser Powder Bed Fusion

    Copper reflects most near-infrared laser light and conducts absorbed heat away faster than almost any other engineering metal. GRCop-42's move into commercial powder catalogs shows how feedstock morphology, oxide content, and particle size distribution are being engineered around that problem rather than worked around it.

    Feature Article

  • Cold spray nozzle depositing metal powder onto a substrate, illustrating cold spray critical velocity and bonding
    29 August 2026

    Cold Spray Powder Deposition: Particle Velocity, Oxide Layers, and Why Some Powders Won’t Bond

    Cold spray coatings form only when particles clear a critical impact velocity, a threshold set by material properties, particle size and morphology, and native oxide condition. This article looks at what powder-side QC can flag before a spray trial, and where it stops short of predicting deposition efficiency.

    Feature Article

  • Triboelectric separation charging tube sorting plastic flakes by contact charge polarity in an industrial free-fall separator
    22 August 2026

    Triboelectric Separation: Using Charge Difference to Sort Plastics and Minerals Instead of Fighting It

    Triboelectric separation turns contact electrification from a handling hazard into a deliberate sorting mechanism. This article covers how material pairs are selected by charge polarity, what feed moisture and particle size do to separation efficiency, and where the technique sits relative to density and optical sorting.

    Feature Article

  • Technician checking blend uniformity data in a pharmaceutical cleanroom relevant to FDA hub-and-spoke distributed manufacturing rule
    15 August 2026

    FDA’s Proposed Hub-and-Spoke Distributed Manufacturing Rule: What It Means for Blend Uniformity and Granulation Consistency

    FDA's proposed hub-and-spoke registration rule treats geographically separate manufacturing units as one establishment. The registration paperwork is new; proving that blend uniformity, granulation endpoints, and moisture behavior actually match between sites is the older, harder problem.

    Feature Article

  • Two stainless steel powder hoppers showing contrasting mass flow and funnel flow behavior.
    8 August 2026

    Powder Spreading in Powder Bed Fusion: What Recoater Interaction Reveals About Layer Defects

    Powder spreading in powder bed fusion is a recoater-powder interaction shaped by cohesion, particle size distribution, and particle shape. This article maps streaking, short-feeding, and layer non-uniformity back to their underlying mechanisms and separates powder-driven causes from blade wear and spreading speed.

    Feature Article

  • Virgin and recovered Ti-6Al-4V powder hoppers connected to a metal PBF-LB system for controlled aerospace powder reuse qualification.
    1 August 2026

    Virgin-to-Reused Powder Blend Ratios in Aerospace PBF-LB Qualification: Where the Decision Actually Sits

    As aerospace metal additive manufacturing capacity expands, more reused powder is going back into qualified builds. The virgin-to-reused blend ratio decision depends on PSD shift, satellite formation, and morphology drift, and cannot be settled by a single powder check disconnected from the part's stress state.

    Feature Article

  • Dense-phase vs dilute-phase pneumatic conveying pipeline with bend and diverter valve in an industrial powder processing plant
    25 July 2026

    Dense-Phase vs Dilute-Phase Pneumatic Conveying: Matching Conveying Mode to Attrition and Segregation Risk

    Dense-phase and dilute-phase pneumatic conveying create different particle contact mechanics, and the resulting attrition and segregation risk depends on velocity, solids loading ratio, and the powder's own attrition sensitivity, not on a fixed assumption about which mode is gentler.

    Feature Article