PT Indonesia Ethanol Industry · ENA upgrade
50,000 + 30,000 t/y · Indonesia
Corn-based ENA and medicinal anhydrous alcohol upgrade scope.
CNE project photography
CNE / Related reference entries
| Reference | Customer / contracting entity | Project scope · English source title |
|---|---|---|
| 050 | PT Indonesia Ethanol IndustryIndonesia | Distillation Equipment for Producing 50,000 Tons/Year of Edible Superfine-grade Alcohol & Dehydration Equipment for Producing 30,000 Tons/Year of Absolute AlcoholFood-grade alcohol · Anhydrous ethanol · Cassava |
| 195 | PT. Indonesia Ethanol IndustryIndonesia | Technological Upgrading Project of 50,000 Tons/Year ENA and 30,000 Tons/Year Medical Anhydrous EthanolAnhydrous ethanol · Plant upgrade · Corn |
Project figures describe the recorded scope and capacity basis. Photos show the identified customer’s project archive and may represent different phases.
01 / CNE
Project overview
The Indonesia project moved from a cassava-based production history toward corn-based ENA and medical anhydrous ethanol. That change affects cleaning, milling, mash viscosity, enzyme duty, fermentation and the co-product route. The new fuel distillation/dehydration line was designed for switchable production with the existing line.
We first classify equipment for retention, repair or replacement. Inspection, materials, corrosion allowance, internals and available utility capacity determine what can be reused. Next, the engineering package fixes tie-ins, foundations, piping, controls and shutdown work.
Finally, define commissioning by system and product campaign. Keep host-plant capacity, individual package duty and alternative production modes separate. This makes the investment scope and the acceptance test understandable to both the plant team and the suppliers.
02 / CNE
Engineering scope
Start with saleable output, alcohol concentration and annual operating hours. A tonne of product normalized to 95% v/v is a different basis from a tonne of anhydrous product. Cooling-water circulation is also different from fresh-water consumption.
Then draw the process boundary. The Indonesia design treats the front end through distillation, dehydration and DDGS as separate consumption schedules. Adding figures without checking their denominators can double-count duties or omit important equipment.
Heat integration transfers available vapor or condensate heat to another useful duty. Column pressures, temperature difference, fouling and control stability limit what is practical. For a retrofit, measure the baseline first and compare at equivalent feed, throughput and product quality. Agree meter locations and a stable test period before assigning an energy guarantee.
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