Renewable Fuels Processing Guide
Chapter from the Renewable Fuels Processing Guide.
| Configuration | Description | Feed Blend Limit | Capital Cost | CI Benefit | Advantages | Limitations |
|---|---|---|---|---|---|---|
| Co-processing in existing HDT | Blend renewable feed into existing hydroprocessor | 5-20% (typical limit) | Very low (existing unit) | Proportional to blend | Minimal capital, quick implementation | Limited blend rate, certification challenges |
| Standalone HVO unit | Dedicated unit for 100% renewable feed | 100% | High (new unit) | Full CI credit | Maximum flexibility, full product credit | Higher capital, feedstock logistics |
| Converted refinery unit | Repurpose existing hydrotreater/HCK for renewables | 100% | Medium (modifications) | Full CI credit | Leverages existing equipment | May need metallurgy upgrades, H2 capacity |
| Two-stage (HDT + isomerization) | First stage: HDO/DCO; second stage: isomerization | 100% | Highest | Full CI + better cold flow | Best product quality, SAF capable | Most complex, highest H2 consumption |
Co-processing renewable feedstocks in existing hydroprocessing units is the fastest path to production but has important limitations:
Blend Rate Limits:
• 5-10%: generally no equipment modifications needed
• 10-20%: may need metallurgy review (water formation → corrosion)
• >20%: likely needs dedicated reactor, H2 system modifications
Equipment Impacts:
• WATER: HDO produces ~10-15 wt% water from triglycerides — must be managed
- Sour water system may need expansion
- Reactor internals exposed to acidic water at temperature
- Separator boot capacity may be insufficient
• H2 CONSUMPTION: 2-3× higher than petroleum hydrotreating per barrel
- H2 plant or PSA capacity may limit blend rate
• CO/CO2: decarboxylation produces CO and CO2
- CO inhibits HDS catalyst temporarily
- CO2 can form carbonic acid with water
- Recycle gas purity affected
• HEAT: renewable reactions are more exothermic than petroleum HDS
- Quench capacity may limit feed rate
- Monitor reactor ΔT carefully when increasing blend
Source: Renewable_Fuels_Processing_Guide_v1.xlsx · sheet “Process Configurations”
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