CHARACTERIZATION OF A POTASSIUM-PROMOTED COBALT MOLYBDENUM ALUMINA WATER-GAS SHIFT CATALYST

A series of potassium-promoted CoMo/Al2O3 has been investigated by means of X-ray diffraction (XRD), X-ray photoelectron spectroscopy (XPS), and temperature-programmed reduction (TPR). CoMoO4 was found in the CoMo/Al2O3 catalyst by XRD and is destroyed by the presence of potassium. The reducibility of molybdenum is enhanced by potassium in the CoMoK/Al2O3 catalyst and is easier to reduce to Mo(IV) during sulfidation. In the oxidic state catalyst cobalt is increased on the surface by the addition of potassium. After sulfidation this phenomena disappeared, the distribution of cobalt remains at a constant level and is unaffected by the potassium content. The addition of potassium leads to a monotonical decrease of the molybdenum dispersion with the impregnating amount of potassium in the oxidic state catalyst but is more complicated after sulfidation. Potassium is well dispersed on the surface in both the oxidic and sulfided state. The activity in the water-gas shift reaction was correlated with the potassium content of CoMoK/Al2O3.

乙苯脱氢与水煤气变换耦合反应催化剂的研究

中国科学院山西煤炭化学研究所

COMPARISON OF THE SULFURIZATION OF COMOK/AL2O3 CATALYST WITH H2S AND CS2

Only H2S consumption and H2O formation was found in the sulfurization of CoMoK/Al2O3 water gas shift catalyst with H2S/H-2. but CO2 was formed first, then CH4, H2O and H2S appeared in the later part of TPS with CS2/H-2. Carbon deposition on the catalyst during the sulfurization with CS2/H-2 caused a lower activity than the catalyst sulfurized with H2S but could be removed in the run of WGS reaction.

Autothermal reforming of n-octane on Ru-based catalysts

In an attempt to effectively integrate catalytic partial oxidation (CPO) and steam reforming (SR) reactions on the same catalyst, autothermal reforming (ATR) of n-octane was addressed based on thermodynamic analysis and carried out on a non-pyrophoric catalyst 0.3 wt.% Ru/K2O-CeO2/gamma-Al2O3. The ATR of n-octane was more efficient at the molar ratio Of O-2/C 0.35-0.45 and H2O/C 1.6-2.2 (independent parameters), respectively, and reforming temperature of 750-800 degrees C (dependent parameter). Among the sophisticated reaction network, the main reaction thread was deducted as: long-chain hydrocarbon -> CH4, short-chain hydrocarbon -> CO2, CO and H-2 formation by steam reforming, although the parallel CPO, decomposition and reverse water gas shift reaction took place on the same catalyst. Low temperature and high steam partial pressure had more positive effect on CH4 SR to produce CO2 other than CO. This was verified by the tendency of the outlet reformate to the equilibrium at different operation conditions. Furthermore, the loss of active components and the formation of stable but less active components in the catalyst in the harsh ATR atmosphere firstly make the CO inhibition capability suffer, then eventually aggravated the ATR performance, which was verified by the characterizations of X-ray fluorescence, BET specific surface areas and temperature programmed reduction. (c) 2005 Elsevier B.V. All rights reserved.

煤层气储层工程的地下水行为研究

The practice of coalbed methane development from home and abroad demonstrated Hydrogeological factor is one of the important geological factors influencing the coalbed methane productivity. The grasp of groundwater behavior feature is the prerequisite to success development of coalbed methane. Through researching the mechanism by which hydrodynamics factors control the storage and transportation of coalfen methane, the ground- water behavior reflecting the feature of coalbed, and mathematics model describing the production process of coalbed methane, this paper devoted to finding the law of groundwater behavior during the course of storage and production and gave hydrogeology theoretical support to the development of coalbed methane. This paper firstly studied hydrodynamic factors influencing the productivity of coalbed methane, based on the analysis of the relative feature of coalbed methane and that of it's reservoir. The productivity of coalbed methane is controlled by reservoir pressure、permeability and recharge conditions. Reservoir pressure, the key factor controlling gas content of coalbed, is ruled by the history of hydrodynamic and current hydrogeological conditions. It indirectly controls the poductivity through influencing the permeability. The permeability of coalbed is the direct factor controlling the productivity. The recharge conditions controls the productivity through influencing initial reservoir pressure and the descend of reservoir pressure during development of coalbed methane. The field of hydrodynamic and the field of hydrochemistry can be used to identified the flow model of groundwater and the coalbed feature can be deducted by the hydraulic gradient、pressure compartment and hydrochemistry. The production of coalbed methane is a complex physical process which including the mutual action between water、solid and gas. This paper studied the mechanism of water-solid action and that of water-gas action, conducted the controlling equation describing the complex process and gave the corresponding mathematics model with its solution by finite-Element method. Finally, this paper analysised the prospective of coalbed methane development of the south section of Hongguo area in Yizikong basin and put emphasis on the analysis of productivity of liangshan and jingzhuping blocks.

Combined single-pass conversion of methane via oxidative coupling and dehydro-aromatization

A single-pass process with the combination of oxidative coupling (OCM) and dehydro-aromatization (MDA) for the direct conversion of methane is carried out. With the assistance of the OCM reaction over the SrO-La2O3/CaO catalyst loaded on top of the catalyst bed, the duration of the dehydro-aromatization reaction catalyzed by a 6Mo/HMCM-49 catalyst shows a significant improvement, and. the initial deactivation rate constant of the overall process revealed about 1.5 x 10(-6) s(-1). Up to 72 h on stream, the yield of aromatics was still maintained at 5.0% with a methane conversion of 9.6%, which is obviously higher than that reported for the conventional MDA process with single catalyst. Upon the TPR results, this wonderful enhancement would be attributed to an in-situ formation of CO2 and H2O through the OCM reaction, which serves as a scavenger for actively removing the coke formed during the MDA reaction via a reverse Boudouard reaction and the water gas reaction as well.