YTC PROJECT REFERENCE
KMG Myanmar: 20,000 t/y ethanol CO₂ recovery
The KMG Myanmar ethanol project appears in our current master register as a 2019 reference with a nominal CO₂ recovery capacity of 20,000 tonnes per year.
| Reference element | Recorded basis |
|---|---|
| Source / application | Ethanol & distillery |
| Product specification | Food-grade, purity ≥99.998% |
| Record IDs | 74 |
Fermentation recovery for an overseas ethanol project
The KMG Myanmar ethanol project appears in our current master register as a 2019 reference with a nominal CO₂ recovery capacity of 20,000 tonnes per year. The recorded feed is ethanol or alcohol fermentation CO₂. Our scope is equipment supply with installation guidance, and the current worksheet specifies food-grade product with a design purity of at least 99.998%.
The portfolio also contains a separately identified Myanmar Phase II reference in 2025. Because the source does not explicitly connect that later entry to KMG, it remains a separate project record. The KMG case is described on the basis of its own documented capacity, application and supply boundary.
Planning a second product stream
An ethanol plant considering CO₂ recovery needs to evaluate both technical availability and customer demand. The starting point is a measured flow and composition profile from the fermentation process. The commercial assessment then considers the quantity of saleable liquid that can be produced during the plant’s actual operating calendar.
Storage and distribution should be part of the feasibility study. If deliveries leave the site intermittently, working liquid inventory must bridge the gap between production and collection. A proposed annual recovery capacity should therefore be tested against fermentation availability, maintenance periods and the planned sales route before it becomes a procurement target.
Treatment selected for the incoming gas
For an ethanol-derived stream, the recovery route normally considers gas collection, washing or other conditioning, compression, moisture removal, purification and liquefaction. The gas analysis determines which contaminants need specific treatment and how much duty each stage must handle. Fermentation-derived gas should not be assumed suitable for food applications without this assessment.
A comparable project brief should describe feedstock, fermentation process, expected liquid carryover, volatile compounds and the conditions at the collection point. Sampling during more than one representative operating state helps distinguish normal variation from a problem that requires additional upstream control.
Making international delivery practical
Equipment supply with installation guidance is a clearly defined delivery model. For an overseas buyer, it works best when the local and supplier responsibilities are agreed before manufacture. Foundation preparation, utilities, lifting, local pipework and electrical installation all need a named owner and a compatible schedule.
The technical package should identify equipment interfaces and the information required for local execution. Installation guidance, commissioning assistance and operator training should be described as actual deliverables within the agreed scope. Spare-parts planning and access to operating documentation help the customer prepare for service after startup.
What buyers can learn from this reference
KMG Myanmar gives prospective customers a documented example of our overseas ethanol recovery experience at 20,000 t/y. Its value as a reference comes from the defined feed sector, capacity and equipment-supply model. It provides a practical starting point for discussing a plant that combines specialist recovery equipment with locally executed installation work.
For a similar enquiry, send your gas analysis, hourly flow profile, annual operating hours, local utility conditions and required product specification. Add the intended storage and loading arrangement and identify which installation tasks your local team can perform. We can use this information to develop a process proposal and responsibility schedule that fit both the source gas and the realities of delivering the project overseas.
Reference & evidence notes
- Current master worksheet contains more detailed and conflicting quality/location/scope values compared with Website Highlights. Master values are preserved; conflicting legacy highlight values are not silently substituted.
Recorded capacity and quality values are source specifications, not independently verified operating output. Engineering discussion explains the application; it is not a reconstruction of unrecorded project details.
START WITH YOUR SOURCE
Discuss a project with a comparable source and scale.
Send your gas analysis, flow profile, product target and project location. We will help connect the technical questions with a practical supply scope.