4803 Development of a high-efficiency Hydrogen generator for Fuel cells for Distributed Power Generation

Monday, May 3, 2010
Long Beach Convention Center
Kandaswamy DuraiSwamy, Ph.D., P.E. , Intelligent Energy Ltd., Long Beach, CA
Joshua L. Mauzey , Intelligent Energy Ltd., Long Beach, CA
Diane Aagesen , Intelligent Energy Ltd., Long Beach, CA
Lei Wang , Intelligent Energy Ltd., Long Beach, CA
Mingheng Li, Ph.D. , Chemical and Materials Engineering, California State Polytechnic University, Pomona, Pomona, CA
Gregory Smith , Chemical and Materials Engineering, California State Polytechnic University, Pomona, Pomona, CA
Yi Liu , Chemical and Materials Engineering, California State Polytechnic University, Pomona, Pomona, CA
Development of a high-efficiency Hydrogen generator for Fuel cells for Distributed Power Generation

Authors: K. Durai-Swamy, Ph.D., Joshua Mauzey, Lei Wang, Ph.D., & Diane Aagesen, Intelligent Energy, Gregory Smith, Ph.D.,  Yi Liu, Ph.D., & Mingheng Li, Ph.D., California Polytechnic University, Pomona, CA

Correspondence: durai.swamy@intelligent-energy.com

Conventional hydrogen generation by steam methane reforming (SMR), employing a high temperature reformer (~800C), a water gas shift reactor (~300C) and  multiple pressure swing adsorbers, operates at an efficiency of around 65 to 67% based on lower heating value (LHV) of feed and product. This conventional SMR system is not very easy to scale down cost-effectively for supplying 35 to 150 slpm H2 (to produce 3 to 13 kW electricity).  Intelligent Energy has developed an adsorption enhanced reformer (AER) for the H2 generation for use in conjunction with fuel cells in the small sizes (3 to 13 kW). This AER has an efficiency of around 80% on LHV basis and operates at lower temperature (~500C) than the SMR.

The AER employs a carbon dioxide (CO2) capturing material with the reforming catalyst which removes the CO2 from the products to effect the reactions to go forward such that H2is produced in one step with little CO and CO2 impurities. H2 content in the product is over 98%, the balance being unconverted methane. This paper presents the results from an AER unit with four beds and overall process simulation. The AER unit has been operated with ethanol, natural gas and LPG as feeds. This project is partially supported by US. DOE (contract # DE-FC36-07GO17013).References:

  1. K. DuraiSwamy, J. L. Mauzey, D. A. Pena, and A. S. Chellappa. Low-cost high-efficiency distributed hydrogen production. In AIChE Spring National Meeting, paper 168b, New Orleans, LA, 2008.
  2. Y. Ding and E. Alpay. Adsorption-enhanced steam-methane reforming. Chem. Eng. Sci., 55:3929–3940, 2000. 
  3. Y. Ding and E. Alpay. Equilibria and kinetics of CO2 adsorption on hydrotalcite adsorbent. Chem. Eng. Sci., 55:3461–3474, 2000.
  4. K. B. Lee, M. G. Beaver, H. S. Caram, and S. Sircar. Novel thermal-swing sorption-enhanced reaction process concept for hydrogen production by low-temperature steam-methane reforming. Ind. Eng. Chem. Res., 46:5003–5014, 2007.
  5. K. B. Lee, A. Verdooren, H. S. Caram, and S. Sircar. Chemisorption of carbon dioxide on potassium-carbonate-promoted hydrotalcite. J. Colloid Interf. Sci., 308:30–39, 2007.
  6. Mingheng Li, Equilibrium Calculation of Gaseous Reactive Systems with Simultaneous Species Adsorption, Ind. Eng. Chem. Res. 2008, 47, 9263–9271
  7. Mingheng Li, Equilibrium, Thermodynamic Analysis of Adsorption Enhanced Reforming of Ethanol, under review by International J of Hydrogen Energy, 2009.