UTILIZATION OF ZIRCON FROM THE BY-PRODUCT OF TIN MINING AS CATALYSTS SUPPORT FOR STEAM REFORMING OF METHANOL
Abstract: <br /> <br /> <br /> <br /> <br /> ZrSiO4 (zircon) is one of the by product of tin mining. ZrSiO4 potency as a catalyst support was never been studied before. In this research, zircon is used as support for Cu based catalysts, and their activities in stea...
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id-itb.:64592017-09-27T11:42:32ZUTILIZATION OF ZIRCON FROM THE BY-PRODUCT OF TIN MINING AS CATALYSTS SUPPORT FOR STEAM REFORMING OF METHANOL Widiastri (NIM:105 03 015), Meta Indonesia Final Project INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/6459 Abstract: <br /> <br /> <br /> <br /> <br /> ZrSiO4 (zircon) is one of the by product of tin mining. ZrSiO4 potency as a catalyst support was never been studied before. In this research, zircon is used as support for Cu based catalysts, and their activities in steam reforming of methanol are tested. Cu/ZrSiO4 and Cu/ZnO/ZrSiO4 catalysts were synthesized by incipient wetness impregnation method. Catalysts that have been synthesized were Cu/ZrSiO4 with 9% and 15% Cu-mole (9%Cu/ZrSiO4 and 15%Cu/ZrSiO4); Cu/ZrSiO4 catalysts with different calcination temperature (300oC and 500oC); and 15%Cu/15%ZnO/ZrSiO4 catalyst. Characteristic and activity of the catalysts were compared to LTSC (Low Temperature Shift Conversion) commercial catalyst (Cu/ZnO/Al2O3). Steam reforming of methanol catalyzed by those catalyst at 300oC showed methanol conversion of 15% for 9%Cu/ZrSiO4, 28% for 15%Cu/ZrSiO4, 4% for 15%Cu/ZrSiO4 (Tcalcination = 300oC), and 21% for 15%Cu/15%ZnO/ZrSiO4. XRD diffractograms show that the catalysts are crystalline. The BET measurement results shows that specific surface area are 4.94 m2/g for ZrSiO4, 5.58 m2/g for 15%Cu/ZrSiO4, and 2.74 m2/g for 15%Cu/15%ZnO/ZrSiO4. text |
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Abstract: <br />
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ZrSiO4 (zircon) is one of the by product of tin mining. ZrSiO4 potency as a catalyst support was never been studied before. In this research, zircon is used as support for Cu based catalysts, and their activities in steam reforming of methanol are tested. Cu/ZrSiO4 and Cu/ZnO/ZrSiO4 catalysts were synthesized by incipient wetness impregnation method. Catalysts that have been synthesized were Cu/ZrSiO4 with 9% and 15% Cu-mole (9%Cu/ZrSiO4 and 15%Cu/ZrSiO4); Cu/ZrSiO4 catalysts with different calcination temperature (300oC and 500oC); and 15%Cu/15%ZnO/ZrSiO4 catalyst. Characteristic and activity of the catalysts were compared to LTSC (Low Temperature Shift Conversion) commercial catalyst (Cu/ZnO/Al2O3). Steam reforming of methanol catalyzed by those catalyst at 300oC showed methanol conversion of 15% for 9%Cu/ZrSiO4, 28% for 15%Cu/ZrSiO4, 4% for 15%Cu/ZrSiO4 (Tcalcination = 300oC), and 21% for 15%Cu/15%ZnO/ZrSiO4. XRD diffractograms show that the catalysts are crystalline. The BET measurement results shows that specific surface area are 4.94 m2/g for ZrSiO4, 5.58 m2/g for 15%Cu/ZrSiO4, and 2.74 m2/g for 15%Cu/15%ZnO/ZrSiO4. |
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Final Project |
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Widiastri (NIM:105 03 015), Meta |
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Widiastri (NIM:105 03 015), Meta UTILIZATION OF ZIRCON FROM THE BY-PRODUCT OF TIN MINING AS CATALYSTS SUPPORT FOR STEAM REFORMING OF METHANOL |
author_facet |
Widiastri (NIM:105 03 015), Meta |
author_sort |
Widiastri (NIM:105 03 015), Meta |
title |
UTILIZATION OF ZIRCON FROM THE BY-PRODUCT OF TIN MINING AS CATALYSTS SUPPORT FOR STEAM REFORMING OF METHANOL |
title_short |
UTILIZATION OF ZIRCON FROM THE BY-PRODUCT OF TIN MINING AS CATALYSTS SUPPORT FOR STEAM REFORMING OF METHANOL |
title_full |
UTILIZATION OF ZIRCON FROM THE BY-PRODUCT OF TIN MINING AS CATALYSTS SUPPORT FOR STEAM REFORMING OF METHANOL |
title_fullStr |
UTILIZATION OF ZIRCON FROM THE BY-PRODUCT OF TIN MINING AS CATALYSTS SUPPORT FOR STEAM REFORMING OF METHANOL |
title_full_unstemmed |
UTILIZATION OF ZIRCON FROM THE BY-PRODUCT OF TIN MINING AS CATALYSTS SUPPORT FOR STEAM REFORMING OF METHANOL |
title_sort |
utilization of zircon from the by-product of tin mining as catalysts support for steam reforming of methanol |
url |
https://digilib.itb.ac.id/gdl/view/6459 |
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