Inflection Point Engineering Renewable Fuels Processing Guide

Process Configurations

Chapter from the Renewable Fuels Processing Guide.

PROCESS CONFIGURATIONS

Configuration Comparison

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 Considerations

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”