When selecting a pelletizer, buyers usually focus on moisture content, capacity, power, and price, but they most easily overlook a more fundamental parameter — the particle size distribution (PSD) of the raw material. PSD is more insidious than moisture: high moisture content is visible to the naked eye and can be felt by hand, while uneven particle size distribution often only becomes apparent when the pelletizer is running and the pelleting rate is low. Uneven PSD directly inhibits pelleting; large particles must be pre-crushed or screened, otherwise even the most expensive pelletizer will not perform as expected.

I. Quantitative Impact of PSD on Pelletizing Rate

The essence of pelleting is the mutual bonding and layering growth of powder particles under the action of moisture and mechanical force. This process relies on a reasonable gradation of “fine powder as the binder phase and medium-sized particles as the skeleton.” When PSD is concentrated in a narrow range, the contact area between powder particles is insufficient or the skeleton is lacking, resulting in decreased pelleting efficiency.

Industry practice shows that when the proportion of coarse particles larger than 2 mm in the raw material exceeds 10%, the granulation efficiency decreases by 20%–30%. Coarse particles have a small specific surface area and absorb water slowly, making it difficult to form strong liquid bridges with fine powder. They simply “roll without sticking” in the pan or drum, significantly reducing the pelleting rate. Conversely, if the proportion of fine powder (less than 0.1 mm) is too high and there is a lack of skeleton particles, the material easily forms overly wet clumps, resulting in a polarization of particle size. The ideal PSD should be a “coarse–fine mix”: fine powder acts as the binding core, medium-sized particles (0.1–1 mm) act as the skeleton, and coarse particles are controlled within 10%. Roller extrusion granulation is more sensitive to PSD, typically requiring the material to pass through an 80–120 mesh sieve with a residue ratio not exceeding 5%. Insufficient fineness results in insufficient particle strength, while excessive fineness easily leads to moisture absorption and pore blockage.

II. Matching the Mesh Size of the Grinding Section with the Granulation Section

The PSD problem cannot be solved solely in the granulation section; it must be traced back to the grinding section. The screen mesh size of the pulverizer determines the upper limit of the output PSD (Particle Size Distribution), while the granulator has specific requirements for the feed PSD; the two stages must be matched.

The recommended feed fineness for disc granulators and rotary drum granulators is generally 80–120 mesh, corresponding to a particle size of approximately 0.125–0.18 mm. If the screen aperture in the pulverizing section is too large (e.g., below 60 mesh), a large number of coarse particles will enter the granulator, reducing the pelleting rate and increasing the amount of returned material. If the screen is too fine (e.g., above 150 mesh), the proportion of fine powder will be too high, resulting in poor material flowability and easy agglomeration, which is also detrimental to pelleting. Roller extrusion granulation requires even finer particles; typically, the residue on an 80–120 mesh screen should not exceed 5%. Therefore, when selecting a granulator, the recommended feed PSD should be confirmed first, and then the pulverizer screen mesh size should be selected accordingly. A vibrating screen should be installed between the pulverizing and granulating sections to screen out oversized coarse particles and return them to the pulverizer, forming a closed-loop particle size distribution system. Modifying only the granulator parameters without adjusting the pulverizing section is a common cause of uncontrolled PSD.

 

Grinding Stage Setting Recommended Value Consequence If Wrong
Coarse screen (< 60 mesh) Avoid for fertilizer granulation Many coarse particles enter the granulator; pelleting rate drops, return load rises
Balanced screen (80–120 mesh) 0.125–0.18 mm; residue < 5% on 80–120 mesh Matched feed for disc, drum and roller extrusion granulators
Over-fine screen (> 150 mesh) Avoid for most fertilizer applications Excess fine powder; poor flowability, wet clumps, die pore blockage
Vibrating screen between stages Installed as closed-loop reject Without it, oversized particles recycle uncontrolled through the granulator

III. PSD Thresholds for Different Raw Materials

The tolerance for PSD varies significantly among different raw materials. Livestock and poultry manure compost has a high fiber content; the proportion of coarse particles (greater than 2 mm) should ideally be controlled below 10%. If this proportion exceeds 10%, secondary crushing is necessary; otherwise, fibers will entangle the granulator shaft. For straw-like materials, if the proportion of fibers longer than 5 mm is too high after crushing, pelletizing will be difficult; it is recommended to crush to below 3 mm. Inorganic raw materials such as urea, DAP, and MOP have relatively uniform particles, but particle size matching must still be confirmed before blending or granulation to avoid large particle crystals clogging the die pores. Urban sludge has high viscosity; if the PSD is too fine, it will easily stick to the wall, requiring adjustment with a certain proportion of dry skeleton materials. Regardless of the raw material, the PSD threshold can be summarized as follows: coarse particle proportions should not exceed 10%, fine powder should not be excessively concentrated, and the gradation should be reasonable.

Raw Material PSD Threshold Required Action
Livestock / poultry manure compost Coarse (> 2 mm) < 10% If exceeded, perform secondary crushing to prevent fiber entanglement on the granulator shaft
Straw-like materials Fibers < 3 mm Re-crush if fibers longer than 5 mm are still present
Urea, DAP, MOP (inorganic) Uniform crystals; confirm before blending Screen out large crystals to prevent die pore blockage
Urban sludge Avoid overly fine PSD Blend in dry skeleton material to reduce wall sticking

IV. FAQ: How to Quickly Determine PSD Without a Particle Size Analyzer

I don’t have a laser particle size analyzer. How can I quickly check whether my raw material PSD is acceptable?

A simple sieving method can be used: take a representative 500 g sample and sieve it manually or with vibration for 5–10 minutes using standard sieves of 2 mm, 1 mm, 0.5 mm, and 0.15 mm, and weigh each layer separately. If the proportion of particles larger than 2 mm exceeds 10%, or the proportion of fine powder smaller than 0.15 mm exceeds 50%, the PSD needs adjustment. The “clumping and gently rubbing” test can also be used to aid judgment: if coarse particles feel noticeably rough to the touch after rubbing, it indicates an excess of coarse particles; if it is all fine powder with no structural feel, it indicates an excessive amount of fine powder. While these simple methods are not as precise as instruments, they are sufficient to identify obvious PSD issues before selection.

In summary, granulator selection should not only consider moisture content and capacity; the raw material particle size distribution (PSD) is a more hidden but fundamental decision variable. Measuring the PSD first, then determining the grinding mesh size, and finally matching the granulator model are essential steps to ensuring the equipment’s performance is truly realized.
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