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Solar Power And Chemical Energy Systems

An Implementing Agreement of the International Energy Agency

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SOLHYCARB - High Temperature Solar Chemical Reactor for Co-production of Hydrogen and Carbon Black from Natural Gas Cracking


Participants:

  • CNRS-PROMES (F)

  • ETH (CH)

  • PSI (CH)

  • WIS (IL)

  • CERTH/CPERI (GR)

  • DLR (D)

  • TIMCAL (B)

  • SOLUCAR R&D (E)

  • CREED (F)

  • N-GHY (F)

 

Achievements in 2006

At CNRS-PROMES, a high-temperature lab-scale solar chemical reactor (1 kWth) has been successfully modeled and tested. The solar receiver consists of a tubular graphite cavity which absorbs the solar power and transfers the heat to the reactant flow. Several parameters such as receiver geometry, temperature, gas flow rates and CH4 composition in the feed were studied. Maximum chemical conversion of methane was higher than 95%. Conversion increased with temperature or gas residence time. Reactor simulations showed that the reaction occurred near the hot wall where the gas velocity is minimal and the temperature is maximal, since the coldest gas temperatures were found at the center of the laminar flow profile.

 

Contour plots of (a) temperature and (b) H2 molar concentration in the small-scale solar reactor.

 

In addition, work at CNRS has focused on the design and development of a medium-scale solar reactor (10 kWth) based on the indirect heating concept without the need for an optical window. For the purpose of predicting the temperature and species concentration profiles in the reactor, a reactor model has been developed, taking into account the hydrodynamics of the two-phase flow as well as the heat and mass transfer coupled to the chemical reaction. Solar reactor experimental testing is scheduled for 2007.

At WIS, a directly heated solar reactor (10 kWth) for solar thermal methane splitting (STMS) is being developed. The reactor window is protected from contact with incandescent CB particles by maintaining a confined cyclonic flow inside the reaction chamber. The reactor is designed for operation at temperatures of up to 2300 K since valuable CB nanotubes are expected to be produced by STMS at such high temperatures. The reactor development is based on previous experience with solar reactors using volumetric gas heating by seeding the reaction chamber with radiation-absorbing particles.

At ETH, a numerical model of a CH4-flow laden with carbon particles is being developed for simulating its behavior under direct exposure to concentrated solar radiation.  A joint PSI-ETH experimental campaign with a small-scale 5 kWth solar reactor was performed in the High-Flux Solar Simulator to experimentally validate simulation results. The solar reactor concept proven for thermal decomposition of methane features a vortex-flow laden with carbon particles. In previous solar experiments, the best chemical conversion was 67%. Nano-filamentary carbon was produced. Some experimental results were evaluated to find the kinetic parameters. A mixed flow (MFR) and a plug flow (PFR) reactor model were distinguished, and the influence of temperature, CH4 concentration and residence time on the chemical conversion was examined. Finally, a model was developed using the Monte Carlo method to understand and predict the heat transfer phenomena in a vortex-flow laden with particles flowing through a cylindrical cavity.

Publications  

 

Contact:

Funding:  
  • EC funded project, cost shared: 2,000 k€

Duration:  
  • March 1, 2006 – February 28, 2010

Background:  

The SOLHYCARB project addresses the development of an unconventional route for potentially cost-effective hydrogen production from solar energy without emitting carbon dioxide. The process thermally decomposes natural gas in a high temperature solar chemical reactor. Two products are obtained: H2-rich gas and a marketable high-value nano-material, Carbon Black (CB).

 

Objectives

The project aims at designing, constructing, and testing innovative solar reactors at different scales (10 kWth and 50 kWth) for operating conditions at 1500-2300 K and 1 bar. Methane conversion over 80% and CB properties equivalent to industrial products are targeted. At the 50 kWth scale, production of 3 sm3/h H2 and 1 kg/h CB is expected. Three main scientific and technical challenges are faced: 1) design and operation of high temperature solar chemical reactors containing nano-size particulates; 2) production of two valuable products (H2 and CB) in the same reactor; 3) solar reactor scale-up based on modeling and experimental validation.

 

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