Upgrading Methane Using Ultra-Fast Thermal Swing Adsorption

The purpose of this project is to design and demonstrate an approach to upgrade low-BTU methane streams from coal mines to pipeline-quality natural gas. The objective of Phase I of the project was to assess the feasibility of upgrading low-Btu methane streams using ultra-fast thermal swing adsorption (TSA) using Velocys' modular microchannel process technology. The project is on schedule and under budget. For Task 1.1, the open literature, patent information, and vendor contacts were surveyed to identify adsorbent candidates for experimental validation and subsequent demonstration in an MPT-based ultra-fast TSA separation for methane upgrading. The leading candidates for preferential adsorption of methane over nitrogen are highly microporous carbons. A Molecular Gate{trademark} zeolite from Engelhard Corporation has emerged as a candidate. For Task 1.2, experimental evaluation of adsorbents was initiated, and data were collected on carbon (MGN-101) from PICA, Inc. This carbon demonstrated a preferential capacity for methane over nitrogen, as well as a reasonable thermal swing differential capacity for a 90% methane and 10% nitrogen mixture. A similar methane swing capacity at 2 psig was measured. The mixture composition is relevant because gob gas contains nearly 85% methane and must be purified to 97% methane for pipeline quality.

[1]  K. Warmuziński,et al.  Effect of adsorption pressure on methane purity during PSA separations of CH4/N2 mixtures , 1999 .

[2]  Christopher R. Clarkson,et al.  The effect of pore structure and gas pressure upon the transport properties of coal: a laboratory and modeling study. 1. Isotherms and pore volume distributions , 1999 .

[3]  Beat Müller,et al.  Determination of methane and other small hydrocarbons with a platinum–Nafion electrode by stripping voltammetry , 2001 .

[4]  J. Pires Chapter 12 – TEXTURAL AND SURFACE CHEMISTRY CHARACTERIZATION OF ZEOLITES VIA ADSORPTION PHENOMENA , 2001 .

[5]  Y. Takeuchi,et al.  Control of Adsorption Rate on Zeolite by Chemical Vapor Deposition , 1996 .

[6]  P. Kluson,et al.  The design of microporous graphitic adsorbents for selective separation of gases , 2000 .

[7]  F. Rodríguez-Reinoso,et al.  Phosphoric acid activated carbon discs for methane adsorption , 2003 .

[8]  José Sánchez,et al.  Gas diffusion and sorption properties of polysiloxane membranes prepared by PECVD , 2002 .

[9]  Soon-Haeng Cho,et al.  Numerical Analysis on the Power Consumption of the PSA Process for Recovering CO2 from Flue Gas , 2002 .

[10]  R. T. Yang,et al.  Adsorber dynamics and optimal design of layered beds for multicomponent gas adsorption , 1998 .

[11]  G. Zgrablich,et al.  High-Pressure Methane Adsorption on NaX and NaY Zeolites with Different Si/Al Ratios , 1994 .

[12]  A. Olajossy,et al.  Methane separation from coal mine methane gas by vacuum pressure swing adsorption , 2003 .

[13]  S. Farooq,et al.  Revisiting Transport of Gases in the Micropores of Carbon Molecular Sieves , 2003 .

[14]  S. H. Kim,et al.  Adsorption equilibria of methane, ethane, ethylene, nitrogen, and hydrogen onto activated carbon , 2003 .

[15]  Vincent G. Gomes,et al.  Coalseam methane recovery by vacuum swing adsorption , 2001 .

[16]  F. Keil,et al.  Adsorption of Methane, Ethane, and Their Binary Mixtures on MCM-41: Experimental Evaluation of Methods for the Prediction of Adsorption Equilibrium , 2002 .

[17]  Phillip C. Wankat,et al.  Intensification of pressure swing adsorption processes , 1990 .

[18]  M. Jaroniec,et al.  Thermodynamics of High-Pressure Adsorption of Argon, Nitrogen, and Methane on Microporous Adsorbents , 1998 .

[19]  R. L. Robinson,et al.  Adsorption of Methane, Nitrogen, Carbon Dioxide, and Their Binary Mixtures on Dry Activated Carbon at 318.2 K and Pressures up to 13.6 MPa , 2003 .

[20]  D. Do,et al.  Modeling of gas adsorption equilibrium over a wide range of pressure: a thermodynamic approach based on equation of state. , 2002, Journal of colloid and interface science.

[21]  Alexander M Puziy,et al.  Heterogeneity of synthetic carbons obtained from polyimides , 2002 .

[22]  Alexander M Puziy,et al.  Modeling of High-Pressure Adsorption Using the Bender Equation of State , 2003 .

[23]  F. Rittig,et al.  Pure- and mixed-gas sorption measurements on zeolitic adsorbents via gas-phase nuclear magnetic resonance , 2002 .

[24]  Manohar Kulkarni,et al.  Enrichment of Methane concentration via separation of gases using vortex tubes , 2002 .

[25]  N. Seaton,et al.  Development and Validation of Pore Structure Models for Adsorption in Activated Carbons , 1999 .

[26]  C. Volzone,et al.  Selective gas adsorption by metal exchanged amorphous kaolinite derivatives , 2000 .

[27]  I. Karimi,et al.  Binary and ternary adsorption kinetics of gases in carbon molecular sieves , 2003 .

[28]  M. Rood,et al.  Correlating N2 and CH4 Adsorption on Microporous Carbon Using a New Analytical Model , 1998 .

[29]  D. R. Paul,et al.  Gas sorption and transport in side-chain crystalline and molten poly(octadecyl acrylate) , 2001 .

[30]  A. B. Fuertes Preparation and Characterization of Adsorption-Selective Carbon Membranes for Gas Separation , 2001 .

[31]  R. Cracknell,et al.  Adsorption and selectivity of carbon dioxide with methane and nitrogen in slit-shaped carbonaceous micropores: Simulation and experiment , 1996 .

[32]  Y. Uraki,et al.  Activated carbon sheet prepared from softwood acetic acid lignin , 2000, Journal of Wood Science.

[33]  Calculation of single adsorption isotherms from gravimetrically measured binary gas mixture adsorption isotherms on activated carbon at high pressures , 1997 .

[34]  A. Sakoda,et al.  Adsorption of Methane onto Activated Carbon by a Graphite Crystal Aggregate Model , 1996 .

[35]  N. Quirke,et al.  Characterization of Porous Materials by Gas Adsorption at Ambient Temperatures and High Pressure , 2001 .

[36]  Ambalavanan Jayaraman,et al.  Kinetic separation of methane/carbon dioxide by molecular sieve carbons , 2002 .

[37]  P. Harlick,et al.  Adsorption of carbon dioxide, methane, and nitrogen: pure and binary mixture adsorption by ZSM-5 with SiO2/Al2O3 ratio of 30 , 2002 .

[38]  F. Tezel,et al.  Adsorption of nitrogen, methane, carbon monoxide, and their binary mixtures on aluminophosphate molecular sieves , 1997 .

[39]  K. Loughlin,et al.  Separation of methane—nitrogen mixtures by pressure swing adsorption using a carbon molecular sieve , 1995 .

[40]  N. Seaton,et al.  Adsorption of Carbon Dioxide and Methane and Their Mixtures on an Activated Carbon: Simulation and Experiment , 1999 .

[41]  Benjamin R. Mattes,et al.  Gas transport and sorption in polyaniline thin film , 1999 .

[42]  M. Goto,et al.  A New Concept in the Design of Pressure-Swing Adsorption Processes for Multicomponent Gas Mixtures , 1999 .