30–35 T/H Pig Feed Manufacturing Plant in Myanmar

RICHI MACHINERY

Myanmar Feed Demand Is Large but the Market Is Not Risk-Free

Myanmar has a substantial commercial feed sector, but current demand is uneven and the livestock industry faces high feed costs, logistics constraints and power risk. That makes a 240,000 T/Y pig feed factory unusually large and increases the importance of captive farm demand plus diversified regional sales.

Local corn, rice bran and broken rice remain important feed ingredients, while soybean meal, amino acids and premix may depend on wider regional supply chains. The plant therefore needs storage and purchasing flexibility rather than assuming every ingredient is consistently available at one price.

A 30–35 T/H pig feed manufacturing plant in Myanmar can work for a large integrated operator, but the commercial case depends on secured raw materials, reliable power, trained operators and enough pig-feed demand to keep three shifts productive. This scale also means a pig feed production line in Myanmar must be planned around real captive demand and working capital rather than nameplate capacity alone.

RICHI MACHINERY

The First Engineering Questions Were Moisture Storage and Product Size

The client understood pig production well, but a three-shift feed mill introduced a different set of operating risks.

The first requirement was a line capable of about 30 T/H from corn, soybean meal and local byproducts while maintaining separate starter, grower and finisher specifications.

The design team therefore worked through the process inputs before freezing the equipment package.

• How high does corn moisture rise during monsoon storage, and what aeration or drying reserve is required?
• Which ingredients need bulk silos and which should remain in bags or smaller bins?
• What pellet sizes are required for piglet crumbles, grower pellets and finisher pellets?
• How much mash feed, if any, should bypass the pelleting section?
• What backup power is needed to protect cooling, controls and safe shutdown during grid interruptions?

The site already included a 2.6-hectare industrial plot and a tall production shell of about 7,808 m². The process had to fit that structure from receiving pit through grinding, batching, pelleting, cooling and packing.

This was a complete pig feed pelletizing line project with three-shift operation, tropical humidity management and enough process redundancy to support a commercial feed program.

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Project Data Close at About 30.3 T/H Average Output

The main equipment package is approximately US$1.28 million for the complete animal feed production line. Completed fixed investment is about US$1.49 million after shipping, local installation, electrical work and retained-building modifications are included.

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Corn and Rice-Milling Byproducts Anchor the Formula System

Myanmar’s feed sector uses corn, rice bran, broken rice and oilseed meals extensively. For this project, the annual purchasing plan is built around corn from central and eastern production areas, soybean meal, fish meal and local milling byproducts, with imported micro-ingredients where necessary.

A separate intake for rice bran and related milling byproducts gives the nutrition team more flexibility on grower and finisher formulas, but inclusion still depends on nutrient specification and storage quality.

The annual ingredient basis is:

Total feed-ingredient intake is approximately 247,500 T/Y, excluding packaging materials and utility fuel.

Monsoon storage is the main quality risk for corn. Aeration, stock rotation and moisture checks are therefore treated as part of feed quality control rather than left to the pelleting section.

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Three Main Pellet Mills Match the 30–35 T/H Plant

This pig livestock feed production line uses a coordinated grinding, batching, mixing and pelleting process. High-fiber ingredients and byproducts are handled according to their actual particle size rather than forcing every ingredient through the same grinding path.

The feed factory machines package includes:

The ring die feed pellet machines are configured as three SZLH420 units, each with a 110 kW main motor and about 10–12 T/H capacity under suitable pig-feed formulas. Combined installed pelleting capacity is roughly 30–36 T/H, matching the 30–35 T/H plant target with limited operating margin for formula variation.

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Six Process Stages Share One Three-Shift Capacity Chain

The process is designed as one continuous capacity chain from truck receiving to finished bags. Each upstream section has to keep enough margin for the three-pellet-mill downstream load.

Stage 1: Intake and Cleaning

Trucks dump corn into a below-floor receiving pit (10m x 8m, with a grate to catch large debris). A scraper conveyor moves it to a bucket elevator, which lifts it to the top of the cleaning tower. Two drum screens remove corn cobs, dirt, and fines. A magnetic separator pulls out any nails or wire pieces – critical for protecting the hammer mill.

Stage 2: Grinding

Clean corn is buffered before four hammer mills. Screen selection is adjusted by formula; the target is a controlled pig-feed particle profile rather than one fixed micron value for every product.

Stage 3: Batching and Mixing

The batching system uses 20 main screws and 8 micro screws. Two double-shaft paddle mixers handle 6-ton batches, giving enough mixing capacity for the 30–35 T/H plant when batch sequencing and discharge timing are coordinated.

After mixing, mash can either follow a dedicated mash-feed route where required or move to steam conditioning and pelleting.

Stage 4: Conditioning and Pelleting

Mash enters the conditioners where steam raises temperature and moisture to the working range for pig-feed pelleting. Conditioning parameters are adjusted by formula rather than fixed at one universal temperature or residence time.

Three SZLH420 pellet mills share the main load. Combined installed capacity is about 30–36 T/H, leaving limited margin for die changes, formula variation and short maintenance events.

Stage 5: Cooling and Crumbling

Three counterflow coolers reduce pellet temperature before screening. Piglet products then pass through the crumbler section to produce smaller particles suitable for starter feeding.

Stage 6: Screening and Bagging

A final rotary screen removes fines (which get recycled back to the mixer). Then the bagging scale fills 50kg woven poly bags – about 700 bags per hour at full capacity. We included a manual bag closer and a conveyor to move bags to the warehouse.

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Monsoon Humidity Changes Storage and Cooling Priorities

Central Myanmar’s wet season raises ambient humidity and increases the risk of moisture pickup in grain, premix and finished feed. The project therefore relies on covered receiving, aerated storage, short finished-feed residence time and controlled cooler airflow.

Three design priorities were added for humid-season operation:

1. Cool against actual ambient humidity so the cooler does not re-wet finished pellets during humid periods.
2. Use corrosion-resistant material selectively where steam, condensate or aggressive cleaning conditions justify it.
3. Size dust aspiration for humid fines and maintain filters before pressure drop begins to limit airflow.

These measures are part of plant reliability, not optional upgrades added after commissioning.

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Utilities Must Support Continuous Operation Not Just Nameplate Output

Water: The pig animal feed production plant uses municipal water for boiler makeup, cleaning and staff facilities. The project basis is about 30 m³/day at peak, with softened boiler-feed water protecting the steam system.

Power: The project uses a 2.5 MVA main transformer with about 1.8 MVA peak plant demand. Backup generation is reserved for controls, cooling and safe shutdown rather than full-load production.

Gas: The steam boiler uses the site’s available gas supply. Annual consumption is metered from actual steam demand rather than fixed to one unverified unit-price assumption.

Wastewater: The plant produces three streams:

• Domestic sewage (toilets, showers) – septic tank + soakaway.
• Boiler blowdown – sent to a cooling pond, then to a municipal drain.
• Vehicle wash water – oil/water separator, then municipal drain.

Wastewater handling follows the site’s approved municipal and industrial-discharge arrangements. The project does not assume that weaker regulation removes the need for proper treatment.

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Seven Dust Collectors Protect Product and Operators

Complete feed mill plants generate dust at receiving, grinding, batching and packing. Dust control reduces product loss and housekeeping load while lowering worker exposure and combustible-dust risk.

The project uses seven pulse-jet baghouse collectors across the main dust points. Captured clean feed dust can be returned to the appropriate process stream where quality control permits.

Bagging dust collection remains necessary even though it does not increase pellet capacity. Clean floors, lower airborne dust and reduced product loss are operating benefits in their own right.

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Noise Control Is Built Into Shift Design

Hammer mills, fans and pellet mills are high-noise equipment. The project therefore combines equipment isolation, enclosed control areas, hearing protection and work-rotation rules rather than presenting the production floor as a quiet workplace.

• All high-noise equipment (mills, fans, pellet mills) on vibration-damping mounts.
• The control room is double-walled with acoustic glass.
• Operators wear earplugs (we supplied reusable ones).
• Shift rotations: no one stays on the mill floor for more than 4 hours.

The objective is controlled exposure and safe work practice, not a claim that the mill operates silently.

The staff layout also includes separate break, changing and sanitation areas so the three-shift workforce does not share production-floor space for basic welfare functions.

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Commissioning Focused on Conveying Wear and Condensation

Startup identified three practical issues that were resolved before the line entered normal operation:

Issue 1: Corn-intake conveying direction and interlocks were checked after an early elevator commissioning fault.

Issue 2: Unexpectedly abrasive local grain increased wear, so screen, die and magnet inspection intervals were shortened.

Issue 3: Cooler exhaust routing was adjusted to prevent warm humid air condensing against the steel roof structure.

The startup team remained on site through product tuning so steam, die loading, cooling and crumbling could be adjusted against actual pig-feed formulas.

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The Product Plan Closes at 240,000 T/Y

The annual product plan is divided across starter, grower and finisher feeds:

At 20,000 tons per month, annual output reaches 240,000 tons when the plant maintains its scheduled operating availability.

The project evaluates manufacturing cost against actual ingredient, utility, labor and maintenance bills. It does not publish a fixed saving versus imported feed because exchange rates and market prices change materially in Myanmar.

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US$1.49 Million Fixed Investment Is the Relevant Project Number

The completed investment is separated from operating cost and financing:

The project financing mix belongs to the customer’s capital structure and is not used as a universal benchmark for other Myanmar feed mills.

Commercial evaluation should focus on:

• Actual ingredient cost versus purchased complete feed
• Labor, utilities, maintenance and working-capital requirements
• Finance cost and foreign-exchange exposure on imported ingredients and equipment
• Feed consumed internally versus feed sold to outside farms

The article does not use a two-month payback claim. A 240,000 T/Y feed factory should be evaluated with a full cash-flow model, not a simple imported-feed price difference.

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Operator Training Was Split by Mechanical Process and PLC Control

Training covered wear parts, moisture and temperature readings, safe pellet-mill response, PLC recipes and interlocks before the plant moved into three-shift production.

• How to change dies and rollers (they practiced on a spare mill)
• How to read moisture and temperature readings
• Basic troubleshooting (what to do when the pellet mill stalls)
• PLC adjustments (batch sizes, mixing times)

On-site support covered mechanical completion, cold testing, hot commissioning, product tuning and operator handover. The sequence matters more than the exact number of training days.

Remote support continues through normal service channels for fault codes, wear-part identification and maintenance planning.

RICHI MACHINERY

Myanmar’s Feed Market Supports Demand but Also Raises Utilization Risk

A 30–35 T/H pig feed manufacturing plant in Myanmar is a large project relative to the current swine-feed segment. Commercial feed production exists at scale, but poultry remains the dominant compound-feed user and the livestock sector faces significant cost and logistics pressure. A pig feed mill in Myanmar at this scale therefore needs a stronger utilization plan than a small regional mill.

That means the strongest case for this project is the customer’s own pig operations plus verified regional sales—not an assumption that national swine-feed demand alone will absorb 240,000 tons every year.

Government policy, import conditions and currency rules can change, so the project should not be justified with a fixed future tariff assumption.

Industrial zones around major cities provide access to roads, labor and utilities, but reliability still has to be checked at the actual site before a three-shift factory is designed.

The major risks are ingredient-price volatility, power interruption, logistics constraints, exchange-rate movement and the need for strong local operating management.

For an integrated livestock business that already consumes large feed volumes, those risks can be managed more effectively than for a speculative merchant mill with no captive demand.

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RICHI Scope Centers on Capacity Balance and Commissioning

Large commercial feed mills need coordinated process engineering across receiving, grinding, batching, mixing, steam, pelleting, cooling and packing. One oversized machine cannot compensate for a smaller upstream or downstream bottleneck.

The project scope therefore starts with process design, ingredient behavior, building constraints and operating hours before individual equipment is finalized.

Process design before equipment selection. Capacity commitments should be tied to the actual formula, pellet diameter and operating conditions used for acceptance testing.

Capacity based on the full line. Grinding, batching, steam, pelleting, cooling and packing are checked together instead of promising output from one machine in isolation.

Regional support planning. Service response depends on travel, visas, logistics and parts stock, so the support plan is agreed project by project.

Training for repeatable operation. Operators are trained on safe die service, moisture control, alarms and preventive maintenance rather than arbitrary speed targets.

Fair equipment specification. Our feed mill equipment is selected by process duty and total project value instead of a blanket claim that one country’s machines are a fixed percentage cheaper than another’s.

RICHI MACHINERY

A 30–35 T/H Pig Feed Plant Only Makes Sense at High Utilization

Not every pig producer needs this scale. The right capacity depends on annual captive feed demand, outside sales, operating shifts and the amount of production that will be pellets versus mash or crumbles.

The Myanmar project is justified by a 240,000 T/Y product plan and around-the-clock operation, not by a claim that feed savings repay the equipment in a few weeks.

If you’re considering a pig feed pellet production line in Southeast Asia, send annual tonnage by starter, grower and finisher feed, the raw-material list, pellet sizes, shift schedule and site dimensions. Those inputs determine the right grinding, batching and pelleting configuration. The same information is needed before sizing a pig feed pellet production line in Myanmar for a different customer.

For a commercial pig feed factory in Myanmar, power reliability, corn storage, micro-ingredient logistics and working capital should be checked before the final equipment contract is signed.

RICHI MACHINERY

Qingdao to Thilawa Then North to Naypyidaw

Main equipment ships from Qingdao Port to the Yangon/Thilawa port area before inland trucking to Naypyidaw. Container count, transit time and customs cost should be confirmed against the final packing list and current shipping schedule rather than treated as fixed for every project.