1 Ocak 2024 Dergi makalesi Açık Erişim

Altinsoy, N. Semih; Avci, Ahmet K.

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        "affiliation": "Bogazici Univ, Dept Chem Engn, TR-34342 Istanbul, Turkiye", 
        "name": "Altinsoy, N. Semih"
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        "affiliation": "Bogazici Univ, Dept Chem Engn, TR-34342 Istanbul, Turkiye", 
        "name": "Avci, Ahmet K."
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    "description": "<p>DME synthesis by direct CO2 hydrogenation was studied on physical mixture of commercial Cu-ZnO/Al2O3 (CZA) and in-house synthesized PTA (phosphotungstic acid)/gamma-Al2O3 catalysts. Effects of PTA loading (0-50 % by mass) and relative amounts of the catalysts on CO2 conversion and DME yield were investigated. The process was intensified through integration of in-situ steam separation by Zeolite 3A (Z3A) adsorbent mixed with the catalysts. Experiments were run at 498 K, 30 bar, H2:CO2=3:1 and GHSV=1750 h-1 (based on CZA catalyst). Optimum PTA loading and CZA:PTA/gamma-Al2O3 mass ratio were 30 % and 1:2, respectively, that gave -21 % CO2 conversion and 6.3 % DME yield. These values remained below the respective thermodynamic limits (28.5 % and 21 %), which were exceeded upon adsorbent integration. Catalytic performance depended strongly on adsorbent quantity studied at the catalyst (CZA+PTA/gamma-Al2O3):adsorbent mass ratio range of 1:0.33-4. Catalysts and the adsorbent remained stable during the pressure swing driven adsorption-regeneration cycles. Sorption assistance at catalyst:adsorbent ratio=1:4 increased catalyst productivity from 5.5x10- 3 to 2x10- 2 kgDME h-1 kgcat - 1. The latter value was comparable to those of the sorption enhanced CO2+CO hydrogenation systems due to the PTAbased dehydration catalyst with strong acidic features and was promising when the strong thermodynamic limitations of CO2-DME conversion was considered.</p>", 
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      "title": "CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION", 
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    "publication_date": "2024-01-01", 
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    "title": "Sorption enhanced DME synthesis by one-step CO2 hydrogenation"
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