The engine reformer: Syngas production in an engine for compact gas‐to‐liquids synthesis

Canadian Journal of Chemical Engineering - Tập 94 Số 4 - Trang 623-635 - 2016
Emmanuel Lim1, Enoch Dames2, Kevin Cedrone3, Angela J. Acocella4, Thomas R. Needham1, Andrea Arce1, D.R. Cohn5, L. Bromberg3, Wai K. Cheng1, William H. Green2
1Department of Mechanical Engineering, Massachusetts Institute of Technology, Cambridge, MA 02139, USA.
2Department of Chemical Engineering, Massachusetts Institute of Technology, Cambridge, MA, 02142, USA
3MIT Plasma Science and Fusion Center, Cambridge, MA 02139, USA
4Engineering Systems Division Massachusetts Institute of Technology Cambridge MA 02142 USA
5MIT Energy Initiative Cambridge MA 02139 USA

Tóm tắt

Methane (CH4) reforming was carried out in an internal combustion engine (an “engine reformer”). We successfully produced syngas from the partial oxidation of natural gas in the cylinder of a diesel engine that was reconfigured to perform spark ignition. Performing the reaction in an engine cylinder allows some of the exothermicity to be captured as useful work. Intake conditions of 110 kPa and up to 480 °C allowed low cycle‐to‐cycle variability (COVnimep < 20 %) at methane‐air equivalence ratios (ϕM) of 2.0, producing syngas with an H2‐to‐CO ratio of 1.4. Spark ignition timing was varied between 45–30° before top‐dead‐center (BTDC) piston position, showing significant improvement with delayed timing. Hydrogen (H2) and ethane (C2H6) were added to simulate recycle from a downstream synthesis reactor and realistic natural gas compositions, respectively. Adding these gases yielded a stable combustion up to hydrocarbon‐air equivalence ratios (ϕHC) of 2.8 with COVnimep < 5 %. Ethane concentrations (with respect to methane) of up to 0.2 L/L (20 vol%) (with and without H2) produced robust and stable combustions, demonstrating that the engine can be operated across a range of natural gas compositions. Engine exhaust soot concentrations demonstrated elevated values at ϕHC > 2.4, but < 1 mg/L below these equivalence ratios. These results demonstrate that the engine reformer could be a key component of a compact gas‐to‐liquids synthesis plant by highlighting the operating conditions under which high gas conversion, high H2‐to‐CO ratios close to 2.0, and low soot production are possible.

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