Mechanism of Catalytic Coke Formation and Some Means to Limit it in Refinery Processes

2008 ◽  
Vol 595-598 ◽  
pp. 681-688 ◽  
Author(s):  
François Ropital ◽  
Frédéric Bonnet

The formation of carbon filaments which occurs at carbon activities ac > 1 in a range of temperatures 450-700°C is a major problem in many chemical, petrochemical and refinery processes where hydrocarbons or other strongly carburizing atmospheres are involved. An excessive carbon deposition causes deterioration of the furnace alloys, such as an important migration of carbon into the alloys. In order to better control and limit this deterioration, this work has been performed to on one side get a more accurate understanding of the mechanisms of formation of catalytic coke and on the other side to find remedies as the injection of selected additives in the feed. Thermogravimetric analyses (TGA) were performed on iron samples in simulated conditions of isobutane dehydrogenation. X ray diffraction (XRD) and scanning electron microscopy examinations were used to identify the different steps during the formation of the catalytic coke. The selection of appropriate remedies to reduce the catalytic coke deposition, requires accurate understanding on both mechanisms of the catalytic particles formation and of the growth of the graphite filaments. We have studied the first steps of the catalytic coke formation on high purity iron that has been previously reduced or oxidised. The comparison of the catalytic coke deposition kinetics indicates that the mass gain is much faster on a pre oxidised state than on a reduced one. In refinery and petrochemical processes, several methods can be selected in order to limit the deposition phenomena of catalytic coke: selection of an appropriate metallurgy, protection of the surfaces by application of coatings, injection of additives with the feed. Steric inhibitors (that block the adsorption sites and slow down the germination and diffusion steps) such as sulfur additives are currently industrially used but special care has to be taken in order to prevent consequential secondary effects such as, for catalytic refinery process, the deactivation of catalysts. Based on TGA experiments, the accurate amount of inhibitor to be injected has been selected regarding the oxidising state of the iron surface.

2020 ◽  
Vol 2 (1) ◽  
pp. 10
Author(s):  
Simona Renda ◽  
Antonio Ricca ◽  
Vincenzo Palma

The depletion of fossil fuels and the growing concerns related to the environmental impact of their processing has progressively switched the interest towards the utilization of biomass-derived materials for a large variety of processes. Among them, biogas, which is a CH4-rich gas deriving from anaerobic digestion of biomass, has acquired a lot of interest as a feedstock for reforming processes. The main issue in employing biogas is related to the carbon deposition and active metal sintering, which are both responsible for the deactivation of the catalyst. In this work, bimetallic and monometallic Rh- and Ni-based formulations were supported on alumina and ceria with the aim of evaluating their activity and stability in biogas oxidative steam reforming. The Rh addition to the monometallic Ni/γ-Al2O3 formulation enhances its catalytic performances; nevertheless, this induces a higher coke deposition, thus suggesting a preferential coke formation on Rh sites. The initial activity of the CeO2-supported catalysts was found to be lower than the Al2O3-supported catalysts, but the 5%Ni/CeO2 sample showed a very good stability during the test and, despite the lower activity, 0.5%Rh-5%Ni/CeO2 did not show coke deposition. The results suggest that the promotion of Ni/CeO2 catalysts with other active metals could lead to the selection of a highly stable and performing formulation for biogas oxidative steam reforming.


Catalysts ◽  
2022 ◽  
Vol 12 (1) ◽  
pp. 95
Author(s):  
Chu-Chin Hsieh ◽  
Jyong-Sian Tsai ◽  
Hwo-Shuenn Sheu ◽  
Jen-Ray Chang

V2O5/NaY-SiO2 adsorbents were prepared by soaking up vanadium oxalate precursors into pellet NaY-SiO2. The NaY-SiO2 supports were prepared from NaY-SiO2 dough followed by extrusion and calcination at 450 °C. Ethanol was used as a model adsorbate to test the performance of the adsorbents. The regeneration efficacy, defined as the ratio of the adsorption capacity of a regenerated adsorbent to that of the fresh adsorbent, was investigated through the dynamics of fixed-bed adsorption (breakthrough curve). TPO, DSC, and FT-IR were used to characterize carbonaceous species on the adsorbents; meanwhile, synchrotron XRPD, XAS, and the N2 isotherm were used to characterize the zeolite, vanadia structure, and surface area, respectively. The results indicated that in low temperature (300 °C) regeneration, adsorption sites covered by alkylated aromatic coke formed during regeneration, causing adsorbent deactivation. In contrast, during regeneration at a high temperature (450 °C), the deactivation was caused by the destruction of the NaY framework concomitant with channel blockage, as suggested by the BET surface area combined with Rietvelt XRPD refinement results. In addition, the appearance of V-O-V contribution in the EXAFS spectra indicated the aggregation of isolated VO4, which led to a decrease in the combustion rate of the carbonaceous species deposited on the adsorbents. For regeneration at 350 and 400 °C, only trace coke formation and minor structural destruction were observed. Long-term life tests indicated that regeneration at 400 °C presents a higher maintenance of stability.


1991 ◽  
Vol 35 (A) ◽  
pp. 607-609
Author(s):  
P. D. Killen ◽  
N. A. Raftery ◽  
D.G. Hay

In this study electrolytic copper powder and atomised high purity iron powders of various size, fractions were consolidated to comparable densities by two very different processes (quasistatic pressing and dynamic, or shook wave, compaction). The resulting pairs of compacts had densities of approximately 0.96 of the theoretical density. These specimens were analysed by X-ray diffraction in order to determine the effect of particle size on the response to compaction.


1987 ◽  
Vol 93 ◽  
Author(s):  
R. J. Arnott ◽  
F. C. Burns ◽  
L. G. Carreiro ◽  
D. R. Chiphan ◽  
W. J. Croft ◽  
...  

ABSTRACTWe report preliminary results from an ongoing study of iron nitride grains formed in high purity iron under nitrogen ion bombardment. Under various implantation conditions, different iron nitride phases grow large enough to produce sharp x-ray diffraction lines. We have used these lines to examine the influence of target temperature during implantation. Between 200°C and 400°C increasing target temperature, which enhances dopant mobility, reduces the retained dose of nitrogen and restricts the formation of nitride phases. Over this temperature range, however, increasing vacancy mobility favors the growth of nitride grains and x-ray line breadth data suggests an optimum temperature for growth of Fe4N grains.


Author(s):  
David S. Wragg ◽  
Georgios N. Kalantzopoulos ◽  
Dimitrios K. Pappas ◽  
Irene Pinilla-Herrero ◽  
Daniel Rojo-Gama ◽  
...  

2005 ◽  
Vol 53 (9) ◽  
pp. 2563-2579 ◽  
Author(s):  
Koji Murakami ◽  
Norihide Nishida ◽  
Kozo Osamura ◽  
Yo Tomota ◽  
Tetsuya Suzuki

Author(s):  
Syed Ejaz Hussain ◽  
Weiguo Wang ◽  
Xinfu Gu ◽  
Yunkai Cui ◽  
Ahua Du ◽  
...  

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