Effect of Ultrasonic Treatment on the Physicochemical and Catalytic Properties of Rhodium–Chitosan/HTsVM Catalysts in Dimethyl Ether Conversion to Lower Olefins

2019 ◽  
Vol 59 (9) ◽  
pp. 1017-1022 ◽  
Author(s):  
T. I. Batova ◽  
T. K. Obukhova ◽  
N. V. Kolesnichenko ◽  
S. A. Nikolaev
2020 ◽  
Vol 02 (11) ◽  
pp. 31-39
Author(s):  
Sh.Ch. Aslanov ◽  
◽  
A.Q. Buxorov ◽  
N. I. Fayzullaev ◽  
◽  
...  

Currently, the main source of feedstock for the production of lower olefins is oil. The implementation of the sequential change "CH4 → CH3OH → lower olefins" allows us to consider natural gas as an alternative raw material for the production of expensive raw materials for petrochemicals-ethylene and propylene. The most promising catalysts for converting methanol to olefins are crystalline microporous silicoaluminophosphates (SAPO-34 and SAPO-18) With a chabazite structure and high siliceous zeolites (HSZ) synthesized from kaolin. Despite the existence of industrial processes for converting methanol using HSZ to olefins, the improvement of these catalysts is an urgent task in order to increase the selectivity and stability of the operation of ethylene and propylene. Therefore, we conducted the process of producing ethylene and propylene from methanol by incorporating metals of various nature from natural kaolin to HSZ. The purpose of this work is to study the effect of the nature and amount of the introduced metal on the physicochemical and catalytic properties of the HSZ.


2011 ◽  
Vol 347-353 ◽  
pp. 3681-3684 ◽  
Author(s):  
Young Ho Kim ◽  
Su Gyung Lee ◽  
Byoung Kwan Yoo ◽  
Han Sol Je ◽  
Chu Sik Park

A SAPO-34 catalyst is well known to be one of the best catalysts for DME to olefins (DTO) reaction. Main products of the reaction were light olefins such as ethylene, propylene and butenes. However, the main problem is rapid deactivation of the SAPO-34 catalyst due to coke deposition during DTO reaction. In this study, various SAPO-34/ZrO2 catalysts added with ZrO2 were prepared for improving the lifetime and their physicochemical properties have been characterized by XRD and SEM. The DTO reaction over various SAPO-34/ZrO2 catalysts was carried out using a fixed bed reactor. All SAPO-34/ZrO2 catalysts showed similar activity and selectivity in the DTO reaction. The SAPO-34(9wt%)/ZrO2 catalyst was showed the best performance for the catalyst lifetime.


2020 ◽  
Vol 298 ◽  
pp. 110087 ◽  
Author(s):  
N.V. Kolesnichenko ◽  
Е.N. Khivrich ◽  
T.K. Obukhova ◽  
Т.I. Batova ◽  
G.N. Bondarenko

RSC Advances ◽  
2015 ◽  
Vol 5 (80) ◽  
pp. 65010-65022 ◽  
Author(s):  
Z. Beji ◽  
M. Sun ◽  
L. S. Smiri ◽  
F. Herbst ◽  
C. Mangeney ◽  
...  

The structure and microstructure of polyol-made non-stoichiometric Mn–Zn ferrite nanoparticles were successfully investigated and correlated to their catalytic properties toward dimethyl ether oxidation reaction.


2019 ◽  
Vol 58 (36) ◽  
pp. 16479-16488 ◽  
Author(s):  
Toyin Omojola ◽  
Dmitry B. Lukyanov ◽  
Nikolay Cherkasov ◽  
Vladimir L. Zholobenko ◽  
André C. van Veen

1986 ◽  
Vol 24 (1-2) ◽  
pp. 69-83 ◽  
Author(s):  
Takuo Hibi ◽  
Kazuteru Takahashi ◽  
Toshio Okuhara ◽  
Makoto Misono ◽  
Yukio Yoneda

2012 ◽  
Vol 52 (3) ◽  
pp. 155-160 ◽  
Author(s):  
N. V. Kolesnichenko ◽  
E. E. Kolesnikova ◽  
L. E. Kitaev ◽  
E. N. Biryukova ◽  
N. I. Trukhmanova ◽  
...  

Catalysts ◽  
2020 ◽  
Vol 10 (8) ◽  
pp. 816
Author(s):  
Sabrina Polierer ◽  
David Guse ◽  
Stefan Wild ◽  
Karla Herrera Delgado ◽  
Thomas N. Otto ◽  
...  

The manufacturing of technical catalysts generally involves a sequence of different process steps, of which co-precipitation is one of the most important. In this study, we investigate how continuous co-precipitation influences the properties of Cu/ZnO/ZrO2 (CZZ) catalysts and their application in the direct synthesis of dimethyl ether (DME) from CO2/CO/H2 feeds. We compare material characteristics investigated by means of XRF, XRD, N2 physisorption, H2-TPR, N2O-RFC, TEM and EDXS as well as the catalytic properties to those of CZZ catalysts prepared by a semi-batch co-precipitation method. Ultra-fast mixing in continuous co-precipitation results in high BET and copper surface areas as well as in improved metal dispersion. DME synthesis performed in combination with a ferrierite-type co-catalyst shows correspondingly improved productivity for CZZ catalysts prepared by the continuous co-precipitation method, using CO2-rich as well as CO-rich syngas feeds. Our continuous co-precipitation approach allows for improved material homogeneity due to faster and more homogeneous solid formation. The so-called “chemical memory” stamped during initial co-precipitation is kept through all process steps and is reflected in the final catalytic properties. Furthermore, our continuous co-precipitation approach may be easily scaled-up to industrial production rates by numbering-up. Hence, we believe that our approach represents a promising contribution to improve catalysts for direct DME synthesis.


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