5–6 T/H Cattle Feed Processing Equipment in South Korea

The Pellet Is One Part of the Dairy Ration

The finished product is a 6 mm diameter concentrate pellet with a target length of 10–15 mm. It supplies part of the cow’s energy, protein and mineral requirements. Farms still need suitable forage and a balanced feeding programme; these pellets are not a complete substitute for hay, silage or other effective fibre.

The material supply includes imported maize and soybean meal, alongside wheat bran and quality-controlled rice bran. Minerals, salt and premixes are weighed according to the approved formulation. Ingredient percentages change with nutrient analysis, purchasing conditions and the farms’ forage supply, so one fixed recipe would not represent every order.

For this application, mixed mash entering the feeder is planned at 12–13% moisture, measured on a wet basis. Whole maize passes through the existing grinder. Meal ingredients are checked for lumps, foreign material and consistency before mixing.

Rice Bran Changes the Pressing Conditions

Rice bran brings both fibre and residual oil into the formulation. Changes in oil content can alter die friction and pellet strength, even when the ingredient name on the batch sheet stays the same. Purchasing specifications therefore need to cover ingredient condition as well as price.

The initial grinding target for cereal ingredients is a mean particle size around 2–3 mm, checked by sieve analysis. The animal feed hammer mill’s screen aperture is selected to achieve that distribution; it is not presented as the finished particle size.

Wet brewer’s grain belongs to a different handling route. It cannot simply replace a dry ingredient in this mash without changing moisture control, storage and dosing arrangements. A dried brewing by-product can be evaluated through its own specification.

The 6 mm ring die’s effective working length is chosen through formulation trials. Increasing compression to strengthen one batch can raise resistance on another. The operating recipe therefore records the die, ingredient mix, moisture and feeder setting together.

A 350 mm Ring Die for the Existing Batch Schedule

The SZLH350 cattle feed pellet machine sits between smaller presses rated at 3–4 T/H and larger machines requiring substantially more power and downstream capacity. Its published reference output is 5–7 T/H. The proposed 5–6 T/H dairy-concentrate duty must be confirmed with representative formulas and the specified pellet dimensions.

Seven productive hours within an eight-hour shift would give 35–42 tonnes at the target rate. At 250 operating days, that corresponds to 8,750–10,500 tonnes before rejected product and other losses. These are scheduling calculations, not recorded production results.

Specify the Drive for Korea’s 60 Hz Supply

A machine prepared for a 50 Hz installation cannot be assumed suitable merely because the voltage looks familiar. Motor ratings, transmission ratio, ring die speed, feeder control and conditioner speed all need checking for the Korean supply. The 60 Hz configuration must preserve the intended mechanical operating speeds.

The electrical review also covers starting current, available transformer capacity and protection settings. The listed 59.5 kW is connected motor power for the selected assembly; electricity consumption per tonne requires a loaded production test.

Installation drawings check the mash-bin outlet, conditioner height and hot-pellet discharge into the existing cooler. Foundation loads and space for removing the ring die, motor and roller assembly are confirmed before the replacement shutdown.

Freight planning can start with Qingdao departure and a Korean discharge port suitable for the Gyeonggi truck delivery. Incheon is an option to evaluate with the forwarder. Packing dimensions, lifting points and current cargo service determine the booking.

Steam, Cooling and Bagging Have to Keep Pace

Initial conditioning trials can examine mash temperatures around 75–80°C, adjusted for the formula and additive requirements. Steam quality, mash moisture and actual residence time are checked together. A temperature reading alone cannot confirm suitable conditioning.

The existing boiler must have spare capacity while other steam users are operating. The connection includes appropriate pressure control, drainage and condensate removal. Steam consumption is measured per tonne during trials, allowing the mill to assess utility cost from its own operating conditions.

Downstream, the cooler and screen must handle the proposed output while achieving the agreed discharge conditions. A finished moisture target of no more than 13% is used for initial assessment, then checked against feed specifications and storage conditions.

For 20 kg bags, 5–6 T/H requires 250–300 filled bags per hour before allowances for interruptions. The weighing, closing and pallet-handling arrangements must support that pace. One trained operator can supervise the pelletizing station, while packing labour depends on the existing automation.

Acceptance Should Follow the Feed to Dispatch

A useful acceptance run includes contrasting approved formulas, rather than only the easiest grain-rich batch. Records cover saleable output, motor load, steam use, pellet dimensions, fines and durability after cooling. Samples taken after conveying and bagging show whether handling breaks otherwise satisfactory pellets.

RICHI Machinery’s quotation can include the formula review, die specification, interface drawings, commissioning support and an agreed spare-parts list. Installation responsibilities, documentation language and support coverage are defined in the supply agreement.

When evaluating cattle feed processing equipment in South Korea, send the formulas that cause the most difficulty, current batch times, steam conditions and cooler capacity. Include the electrical supply and available installation drawings. That gives RICHI a practical basis for pricing the replacement pellet mill and identifying any supporting work needed before shutdown.