Biochar pellet production equipment in Mexico for agave-bagasse biochar. RICHI MZLH420 provides 1–1.2 t/h for commercial carbon-product densification.

Agave bagasse has more than one possible destination. That was the premise behind this biochar pellet production equipment in Mexico project.
The customer operated within the tequila-processing supply chain in Jalisco, where fibrous agave bagasse was generated after sugar extraction. Some residues already had established outlets, so the company was not looking for a machine that would consume every tonne leaving the tequila process. Instead, it planned a separate carbon-product business: divert a controlled share of bagasse to pyrolysis, prepare the resulting biochar, and manufacture pellets only when the carbon product specification required a densified form.
RICHI Machinery configured one MZLH420 ring die pellet machine for that stage. With a 90 kW main motor and 1–1.2 t/h capacity, it provided commercial output without forcing the tequila plant to reorganize its entire residue-management system around pellet production.
Name:
Biochar Pelletizer
Country:
Mexico
Date:
2025
Capacity:
1–1.2 t/h
Model:
MZLH420
Main Motor Power:
90 kW
Raw Materials:
Agave bagasse
Pellet diameter:
6 mm
Understanding where the residue comes from matters.
Agave bagasse is not harvested as a dedicated pellet feedstock. It remains after the agave-processing operation has extracted the sugars required for beverage production.
Research using material from a tequila producer in Jalisco describes the residue as the torn and exhausted agave fibre remaining after sugar extraction. Other Mexican studies likewise identify Agave tequilana bagasse as a significant lignocellulosic by-product of tequila production.
That fibrous residue was the beginning of the customer's carbon route.
It was not the material entering the MZLH420.
Between those two points came thermal conversion.
Agave bagasse can be considered for several utilization routes.
Composting, thermochemical conversion and other forms of material or energy recovery have all been studied in Mexico.
The customer therefore avoided designing the factory around the assumption that pelletized biochar was automatically the highest-value destination for every batch.
Instead, residue allocation could change.
Bagasse suitable for the carbon route was prepared for pyrolysis. Other material could remain available for existing uses. After carbonization, the company again decided what proportion of biochar should be pelletized.
There were two decision points, not one.
That flexibility reduced the risk of installing equipment whose capacity depended on capturing the entire bagasse stream.
The tequila plant could generate considerably more than 1–1.2 t/h of wet or dry bagasse under suitable production conditions.
That number was irrelevant to the final pellet-machine selection unless all of that material could eventually become prepared biochar for pelletizing.
It could not.
Pyrolysis changes material mass. Some bagasse followed other utilization routes. Some biochar could also remain in loose form.
RICHI therefore worked backward from the prepared-char stream.
| Project Item | Configuration |
|---|---|
| Equipment | Biochar pellet production equipment |
| Model | MZLH420 |
| Quantity | 1 unit |
| Main Motor | 90 kW |
| Capacity | 1–1.2 t/h |
| Original Residue | Agave bagasse |
| Pelletizer Feed | Prepared agave-bagasse biochar |
| Customer Sector | Tequila-industry residue utilization |
| Project Role | New carbon-product module |
The result was a machine that could be supplied realistically without being sized from an impressive but misleading raw-bagasse figure.
Raw agave bagasse is fibrous and lignocellulosic.
Biochar is not simply black bagasse.
Thermal conversion alters its structure and composition, which means pelletizing conditions have to be developed around the carbonized product rather than borrowed from an untreated biomass-pellet project.
Recent Mexican research has directly produced biochar from agave bagasse through pyrolysis, including work using bagasse sourced from tequila-producing areas in Jalisco.
For the customer, the char was cooled before entering downstream preparation.
Oversized carbonized material could then be reduced where necessary. Particle consistency was checked, and mixing provided an opportunity to adjust the material before ring-die compression.
Only at that point did the MZLH420 become relevant.
A tequila plant generates another major residue besides bagasse: vinasse.
The two should not be casually merged in an equipment description.
Bagasse is the fibrous solid residue used as the biochar precursor in this project. Vinasse is a liquid effluent arising from tequila production and presents a very different handling problem.
Mexican research has investigated both waste streams, including strategies that combine agave-bagasse biochar with tequila vinasse for soil-amendment research.
That does not mean raw vinasse should be fed into the MZLH420.
It was not part of this pellet-machine feed.
The distinction keeps the project technically clear: prepared solid agave-bagasse biochar entered the pelletizing stage.
Untreated biomass can retain natural components that contribute to binding during densification.
Pyrolysis changes that situation.
For agave-bagasse biochar, the customer needed to establish whether additional binder was necessary and, if so, what type and quantity suited the intended carbon product.
RICHI did not assign a standard percentage.
The answer depends on the actual char, particle preparation, moisture condition, compression behavior and required pellet integrity.
The final application matters as well.
A pellet designed as an agricultural carbon product may place different restrictions on additives from a carbon pellet developed for an industrial use.
Testing therefore preceded recipe standardization.
There was no expectation that the pellet machine would solve every problem created upstream.
If the char contained oversized pieces, preparation handled them.
If material moisture was unsuitable, conditioning addressed it.
If feeding became irregular because of poor bulk flow, the cause was investigated before operators tried to compensate indefinitely with machine settings.
Once acceptable material reached the pelletizer, the job became much clearer: feed consistently, compress through the ring die and produce a stable pellet form.
This division of responsibility made troubleshooting easier.
The MZLH420 was a forming machine, not a substitute for raw-material control.
The carbon section could not interfere with the customer's primary business.
That changed the integration discussion.
Bagasse movement had to be organized without obstructing normal tequila-production logistics. Carbonized material and fine char required their own appropriate handling area. The pelletizer also needed electrical supply, operating clearance and maintenance access without competing unnecessarily with the main processing equipment.
RICHI therefore treated the MZLH420 as an independent downstream module.
This approach allowed the customer to expand residue utilization without making the biochar section the center of the entire factory.
The tequila operation remained the tequila operation.
The carbon business was added around it.
Initial extrusion confirmed whether the prepared char could form.
It did not confirm commercial quality.
The customer also needed to observe what happened during stabilization, screening, packaging and subsequent transfer.
A pellet that looked acceptable immediately after extrusion but broke heavily during these later stages would simply recreate the fine-carbon handling problem in another location.
Production trials therefore considered downstream fines alongside machine output.
When breakage increased, operators could review particle preparation, moisture, binder distribution, feeding and die condition rather than making one arbitrary adjustment.
That gave the plant a repeatable way to improve the product.
The finished material in this project remained predominantly agave-derived biochar.
It was not a fertilizer pellet composed mainly of compost, manure or other nutrient-bearing organic ingredients.
RICHI therefore selected the MZLH biomass densification series.
Mexico offers a useful example of why that distinction matters. Agave bagasse can be composted, carbonized or incorporated into other residue-management strategies. A future customer could deliberately combine agave biochar with composted organic materials and manufacture a true biochar-based organic fertilizer.
That would be another product.
RICHI Machinery would reassess its physical characteristics and could select an FZLH fertilizer pellet machine instead.
The original feedstock name would remain "agave." The correct equipment could still change.
The MZLH420 was manufactured and inspected in China before sea shipment from Qingdao Port to Manzanillo, Mexico.
From the Pacific port, the machine could continue inland toward the customer's operation in Jalisco.
Site preparation took place before arrival. RICHI supplied machine dimensions and requirements for the foundation, electrical connection, material inlet, discharge arrangement and maintenance space.
Commissioning then moved from mechanical checks to actual agave-bagasse biochar.
Operators received guidance on feeding, load observation, lubrication, ring die and roller inspection, normal wear and troubleshooting when material behavior changed.
That description would have skipped most of the project.
Agave bagasse first had to be separated from the tequila-production process. The customer then decided which fraction justified thermal conversion. Pyrolysis transformed that fibrous residue into biochar. Another commercial decision determined how much of the char should remain loose and how much should become pellets.
Only after all of those decisions did the MZLH420 enter the picture.
Mexico already has a strong technical basis for converting tequila-industry agave bagasse into carbon materials. Recent research has produced agave-bagasse biochar from material sourced directly in Jalisco and examined it for applications ranging from soil amendment to adsorption.
For this customer, RICHI's role was narrower and more practical.
One MZLH420 at 1–1.2 t/h gave the company a commercial densification module without forcing every kilogram of agave bagasse into the same route.
That flexibility was the point of the investment.
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