4.6 Article

Bench-Scale Evaluation of Hydrothermal Processing Technology for Conversion of Wastewater Solids to Fuels

期刊

WATER ENVIRONMENT RESEARCH
卷 90, 期 4, 页码 329-342

出版社

WATER ENVIRONMENT FEDERATION
DOI: 10.2175/106143017X15131012152861

关键词

hydrothermal; liquefaction; biocrude; catalyst; gasification; hydrotreating; upgrading; wastewater solids; sludge

资金

  1. U.S. DOE, Office of Energy Efficiency and Renewable Energy (EERE), Bioenergy Technologies Office (BETO)
  2. DOE [DE-AC06-76RL0 1830]
  3. U.S. EPA [CR-83419201-0]
  4. Melbourne Water Corporation (Australia)
  5. Toho Water Authority (FL)
  6. Metro Vancouver (BC)
  7. City of Orlando, FL
  8. City of Santa Rosa, CA
  9. Silicon Valley Clean Water (CA)
  10. City of Calgary (AB)
  11. Delta Diablo Sanitation District (CA)
  12. Eastman Chemical Company

向作者/读者索取更多资源

Hydrothermal Liquefaction (HTL) and Catalytic Hydrothermal Gasification (CHG) proof-of-concept bench-scale tests were performed to assess the potential of hydrothermal treatment for handling municipal wastewater sludge. HTL tests were conducted at 300 to 350 degrees C and 20 MPa on three different feeds: primary sludge, secondary sludge, and digested solids. Corresponding CHG tests were conducted at 350 degrees C and 20 MPa on the HTL aqueous phase output using a ruthenium-based catalyst. Biocrude yields ranged from 25 to 37%. Biocrude composition and quality were comparable to biocrudes generated from algae feeds. Subsequent hydrotreating of biocrude resulted in a product with comparable physical and chemical properties to crude oil. CHG product gas methane yields on a carbon basis ranged from 47 to 64%. Siloxane concentrations in the CHG product gas were below engine limits. The HTL-CHG process resulted in a chemical oxygen demand (COD) reduction of > 99.9% and a reduction in residual solids for disposal of 94 to 99%.

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