Before a plywood plant adds overtime or a second shift, the quickest way to prevent unplanned downtime is to schedule fuel supply with the same discipline used for production output. For the FBH30-13 Vertical Veneer Dryer, the published operating baseline is straightforward: 2 m³/h drying capacity paired with 200 kg/h fuel consumption, with 15 kW total installed power. If a factory scales hours without matching fuel logistics, the drying line can become the bottleneck—no matter how well upstream peeling and downstream layup are organized.

The FBH30-13 is positioned as a compact Vertical Veneer Dryer solution for continuous drying. Its published parameters define the planning math for shift extensions and fuel purchasing.
| Parameter | FBH30-13 specification |
|---|---|
| Model | FBH30-13 |
| Drying capacity | 2 m³/h |
| Fuel consumption | 200 kg/h |
| Total installed power | 15 kW |
| Machine size (L × W × H) | 13 × 3 × 4 m |
| Moisture content (%) | fresh veneer dried to 0–5% |
| Hot air fan | 9 kW |
| Traction motor | 1.5 kW |
| Induced draft fan | 3 kW |
| Built-in furnace | 1.5 kW |
These figures matter most when the operating schedule changes. Extending hours increases theoretical dried volume, but it also increases the amount of fuel that must be delivered, handled, and fed consistently to keep temperature and airflow stable.
In published product descriptions, the vertical drying line is presented as a four-part Veneer Drying System arranged for continuous operation: Feeding area, Heating area, Cooling area, and Discharging area. Treating these zones as one connected process is useful when planning longer operating windows, because fuel supply stability affects the heating area first—but any disruption shows up as slowdowns or inconsistencies at the discharge end.
A typical vertical configuration is also described with a three-dimensional loading approach and a quick-loading structure, with internal hot air circulation designed to provide uniform airflow and temperature. The drying process is described as using a countercurrent drying cycle to support fast drying and uniform quality.

Cutaway view illustrating loading structure and hot air flow inside the vertical dryer.
For shift planning, the most practical starting point is to compute fuel and output from the hourly published rates. This is not a replacement for measuring real production results, but it is a reliable way to build a first-pass fuel schedule.
Theoretical veneer output (m³) = 2 m³/h × operating hours
Estimated fuel requirement (kg) = 200 kg/h × operating hours
| Operating hours | Theoretical veneer output | Calculated fuel requirement |
|---|---|---|
| 8 | 16 m³ | 1,600 kg |
| 12 | 24 m³ | 2,400 kg |
| 16 | 32 m³ | 3,200 kg |
| 24 | 48 m³ | 4,800 kg |
If a factory plans to move from 8 to 16 hours, the schedule change is easy to interpret: +16 m³ theoretical output requires +1,600 kg fuel at the published rate. This is why fuel delivery, storage, and feeding capacity should be checked before approving extra shifts.
The published moisture target for the FBH30-13 is fresh veneer dried to 0–5%. Hitting a tight moisture target depends on stable drying conditions. In the vertical dryer descriptions, the internal hot air circulation is positioned to deliver large hot air volume, with uniform airflow and uniform temperature, and the countercurrent cycle is described as a way to keep drying fast and consistent.
In practical terms, fuel scheduling affects more than total cost. If fuel supply is irregular, heating conditions can drift, and the mill may find it harder to hold the intended moisture results consistently across a longer operating period. That is why many procurement teams evaluate a dryer as a system—capacity, moisture target, handling rhythm, and fuel supply—rather than focusing on a single headline metric.
To review related product descriptions, buyers often start with the manufacturer’s category pages for a vertical veneer dryer and compare configurations against the factory’s real shift plan.
Vertical drying is frequently evaluated where floor space is limited. In published descriptions, the vertical design is said to cover about two-thirds of the floor area of a roller dryer. The same descriptions also state that vertical plywood loading can increase loading capacity by 30–80% compared with other dryer types.
Those layout points have a scheduling implication: when a dryer fits into a smaller footprint, material staging and operator movement can be tightened around the equipment—provided that feeding and discharge are organized to keep pace with the dryer’s hourly rhythm.
Separately, Shine Machinery’s vertical dryer pages highlight that the equipment needs to be assembled on the customer’s factory site and can be installed according to specific location requirements. For planning, that means shift expansion should be considered alongside workshop constraints—especially around veneer infeed staging, discharge stacking, and safe access for furnace operation.
Equipment choice affects both footprint and daily operating logistics. For reference, a published “Low Cost Veneer Dryer Machine” is described as a roller veneer dryer type with a 3 m working width, veneer thickness range 0.8–8 mm, and a stated drying capacity of 50–60 m³/day.
For buyers comparing a Low Cost Veneer Dryer layout against a vertical configuration, the decision commonly comes down to space, handling rhythm, and the operating schedule the plant wants to run. Vertical dryers are positioned around compact installation and three-dimensional loading; roller dryers are typically evaluated for line-style throughput planning.
In Shine Machinery’s vertical product pages, the drying cost for the vertical dryer is published as less than $8/m³, and described as 30–60% of the drying cost of other dryers. This is presented as a product-range figure rather than a universal operating budget, so buyers usually treat it as a comparative reference while building their own per-shift cost model.
Confirm the fuel schedule from hourly consumption
Use 200 kg/h to compute required fuel for the planned operating hours, then align fuel purchasing and delivery to that target.
Lock in the output expectation tied to the same hours
Use 2 m³/h to estimate dried veneer volume per shift. This prevents overpromising downstream production based on hours alone.
Treat feeding, heating, cooling, and discharge as one rhythm
The dryer is described as a four-area line. A shift extension works best when feeding and discharge can match the same pace as heating.
Confirm the moisture target used for your planning
FBH30-13 is published for fresh veneer dried to 0–5%. Production planning should align the moisture target with the plant’s process requirements.
Record actual results for future scheduling
The published figures are a baseline. Once the plant runs longer hours, recording actual dried volume and fuel used per operating period makes future fuel planning more accurate.
Shift expansion is rarely limited by “dryer capacity” alone. It is limited by whether the plant can sustain the full operating rhythm—especially the fuel supply needed to keep heating stable. Using the FBH30-13 published baseline of 2 m³/h and 200 kg/h, a factory can translate overtime into a clear fuel schedule before extending shifts.
For procurement research, buyers often compare the FBH30-13 product parameters against other options in the broader veneer dryer machine range, and then confirm layout feasibility based on workshop dimensions and handling flow.
The published output is 2 m³/h.
The published fuel consumption is 200 kg/h.
Using the published rate: 200 kg/h × 16 h = 3,200 kg.
The published moisture content specification is fresh veneer dried to 0–5%.
The published machine size is 13 × 3 × 4 m, and the total installed power is 15 kW.
The vertical dryer is described as using about two-thirds of the floor area of a roller dryer and increasing loading capacity by 30–80% through three-dimensional loading.
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