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"Titania nanotubes (TiO2 NT) and Titania nanowires (TiO2 NW) were fabricated using TiO2 Degussa P25 (TiO2 P25) nanoparticle as precursors via a sonication-hydrothermal combination approach. The prepared catalysts were characterized by means of an X-ray diffraction (XRD), scanning electron microscope (SEM), transmission electron microscope (TEM), ultraviolet-visible diffuse reflectance spectroscopy (DRS) and the Brunauer-Emmett-Teller technique (BET). The photocatalytic activity of prepared catalysts was evaluated for photocatalytic H2 evolution from an aqueous methanol solution. The results showed that activity of the catalyst not only depends on the morphology of its catalysts, but also on the crystalinity and surface area. Hydrogen production of TiO2 NT was about three times higher than TiO2 P25 and TiO2 NW was two times higher than TiO2P25."

"Produksi hidrogen dengan menggunakan metanol atau gliserol sebagai elektron donor pada fotokatalis TiO2, TiNT, Pt/TiO2 dan Pt/TiNT pada suhu reaksi dari 30 oC sampai dengan 70 oC telah diteliti. Metanol dan gliserol efektif sebagai elektron donor untuk produksi hidrogen secara fotokatalisis. Penggunaan metanol lebih unggul 10% dari gliserol pada semua katalis dalam total produksi hidrogen. Produksi hidrogen terbaik ditunjukkan oleh fotokatalis Pt(1%)/TiNT dengan metanol sebagai elektron donor, yaitu sebesar 2306 µmol/gcat, sementara total hidrogen dengan gliserol sebesar 2120 µmol/gcat. Penggunaan dopan Pt pada fotokatalis menghasilkan produksi hidrogen dua kali lebih besar dibandingkan dengan tanpa dopan.

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Hidrogen production with methanol or glycerol as sacrificial agent using TiO2, TiO2 Nanotubes, Pt/TiO2 and Pt/TiO2 Nanotubes photocatalysts at reaction temperature 30 oC to 70 oC have been investigated. Methanol and glycerol were effective for hydrogen production and the best result was methanol with Pt(1%)/TiO2 that have 2306 µmol/gcat, meanwhile with glycerol only produce 2120 µmol/gcat. The other photocatalyst also have the same pattern, which metanol give 10% higher result on total hydrogen production. Catalyst with Pt give twice higher hydrogen production rather than with no Pt."

"ABSTRAKSel QD-CdS-SSC termodifikasi terdiri dari dua zona yaitu zona QD-CdS-SSC dan zona katalitik. Zona QD-CdS-SSC berfungsi sebagai penangkap sinar, sedangkan zona katalitik merupakan tempat terjadinya reaksi katalitik untuk produksi hidrogen. Zona QD-CdS-SSC terdiri dari semikonduktor TiO2 yang disensitasi dengan CdS, larutan elektrolit polisulfida dan counter elektroda platina yang dilapiskan pada permukaan gelas berpenghantar dan transparan yaitu FTO Flour Tin Oxide . Plat titanium digunakan sebagai template untuk TiO2 nanotubes. Pada zona katalitik, untuk kepentingan reduksi H menjadi H2, platina dideposisikan pada permukan titanium. Pengujian produksi hidrogen dilakukan dengan irradiasi sinar visible pada zona QD-CdS-SSC dan counter elektroda BiVO4. Intensias lampu visible yang digunakan adalah 110 mW/cm2 dan 90 mW/cm2. Counter elektroda dengan zona QD-CdS-SSC dihubungkan dengan kawat tembaga. Larutan yang digunakan pada zona katalisis adalah 12,5 metanol dalam air. BiVO4 yang digunakan sebagai counter elektroda dalam sistem QD-CdS-SSC mampu menghasilkan hidrogen pada intensitas 110 mW/cm2 dan 90 mW/cm2 masing-masing sebesar 320,734 mol dan 20,872 mol.

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ABSTRACTModified QD CdS SSC has been successfully applied for hydrogen production. Modified QD CdS SSC cell consists of two zones there are QD CdS SSC and catalytic zone. QD CdS SSC zone serves to absorb light, while the catalytic zone is operate as the catalytic reaction site for hydrogen production. QD CdS SSC zone consists of TiO2 nanotubes sensitized by CdS immobilized on Ti plate, polysulfide electrolyte solution and platinum as counter electrode that is coated on the surface of FTO glass. Reduction of H to H2 occur on the platinum coated titanium at catalytic zone. Hydrogen production was performed by visible light irradiation on the QD CdS SSC zone and the counter electrode BiVO4 as well. The intensity of the visible light used was 110 mW cm2 and 90 mW cm2. Counter electrode and QD CdS SSC zone were connected by copper wire. The solution used in the catalytic zone in this study was 12.5 methanol in water. QD CdS SSC is able to produce hydrogen at an intensity of 110 mW cm2 and 90 mW cm2. Total hydrogen production at an intensity of 110 W cm2 and 90 mW cm2 were 320.734 mol and 20.872 mol respectively."

"Produksi hidrogen dan degradasi 2,4,6-Triklorofenol secara simultan sudah dilakukan pada berbagai fotokatalis yaitu P25-TiO2, Titania Nanotube Arrays (TNTAs), dan variasi TNTAs-CdS selama 240 menit. VariasiTNTAs-CdS menggunakanperbandingan mol dari prekursor CdS yaitu CdCl2:CH3CSNH2dengan 0,2:0,12; 0,1:0,06; dan 0,05:0,03 mol/L. Hasil karakterisasi UV-Vis DRS menunjukkanenergy band gap berkisar antara 2,71- 2,89 eV.Fotokatalis terbaik didapat pada perbandingan 0,1:0,06 (TNTAs-CdS-2) karena menghasilkan hidrogen (3,17𝜇𝜇mol/g.s) dan degradasi 2,4,6-Triklorofenol (mencapai 80%) yang paling baik dibandingkan dengan katalis lainnya. Fotokatalis tersebut menghasilkan hidrogen 1,5 kali dibandingkan TNTAs dan 7 kali dibandingkan dengan P25-TiO2. Produksi hidrogen berjalan simultan dengan pendegradasian 2,4,6-Triklorofenol, dimana kinerja keduanya bergantung pada katalis yang digunakan. Disamping itu, pengaruh konsentrasi 2,4,6-Triklorofenol (10, 20, dan 40 ppm) dipelajari dengan menggunakan fotokatalis TNTAs-CdS-2 dan menghasilkan total produksi hidrogen berturut-turut 1,008; 1,061; dan 1,197𝜇𝜇mol/g.s. Semakin besar konsentrasi 2,4,6-Triklorofenol, semakin besar pula hidrogen yang dihasilkan.

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Hydrogen production and 2,4,6-Trichlorophenoldegradationhave been investigated simultanously usingP25-TiO2, TNTAs, and variation of TNTAs-CdS for 240 minutes. TNTAs-CdS variations use mol ratio of CdS precursor that isCdCl2:CH3CSNH2 with ratio 0.2:0.12, 0.1:0.06, and 0.05:0.003.Rever to UVVis analysis, the TNTAs-CdS prepared have the band gap energy in the range of 2.71-2.89 eV. Among them, the optimum composition is0.1:0.06 (TNTAs-CdS- 2) which results in the highest total hydrogen production (3,17𝜇𝜇mol/g.s) and 2,4,6-Trichlorophenol degradation(achieve 80%) compared toothers. TNTAs- CdS-2 produces total hydrogen 1.5 and 7 times compared with TNTAs and P25- TiO2, respectively.Hydrogen production and 2,4,6-Trichlorophenol degradation could be perormed simultaneously and it depands on the catalyst employed. Furthermore, the effect of2,4,6-Trichlorophenol initial concentrations (10, 20, and 40 ppm) was also studied using TNTAs-CdS-2 and produced1.008,1.061, and1.197 𝜇𝜇 mol/g.s respectively.The higherthe 2,4,6-Trichlorofenol initial concentration, the more hydrogen produced."

"ABSTRAKHidrogen banyak diproduksi oleh teknologi modern seperti steam reforming, oksidasi parsial dan metode gasifikasi batubara. Namun, proses ini memanfaatkan bahan bakar fosil sebagai bahan baku mereka, yang dapat menyebabkan penipisan pada bahan bakar fosil secara global. Dari situasi ini, permintaan untuk menciptakan metode alternatif dalam memproduksi hidrogen menjadi meningkat. Siklus termokimia sulfur-iodin S-I adalah salah satu metode alternatif untuk memproduksi hidrogen. Ini adalah metode yang menarik untuk menghasilkan hidrogen tanpa menggunakan bahan bakar fosil sebagai bahan baku dan memproduksi emisi gas rumah kaca. Pada siklus termokimia S-I, bagian dekomposisi HI memiliki sistem dinamis yang kompleks karena suhu proses yang tinggi yang terlibat dan adanya molekul azeotrop homogen dalam fase Hix. Dalam penelitian ini, simulasi dinamika melalui strategi Model Predictive Control diimplementasikan untuk mengontrol proses siklus termokimia S-I. Kemudian, kinerja Model Predictive Control diperiksa dan dibandingkan dengan strategi Proportional Integral Derivative dalam hal set point tracking dan disturbance rejection. Berdasarkan hasil, strategi Model Predictive Control menunjukkan kinerja yang lebih baik dibandingkan dengan strategi kontrol Proportional Integral Derivative.

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ABSTRACTHydrogen is widely produced by advanced technologies such as steam reforming, partial oxidation and coal gasification method. However, these processes utilize fossil fuels as their feedstock, which can cause the depletion on fossil fuels globally. From this situation, the demand for creating alternative methods of producing hydrogen has been emphasized. The sulfur iodine S I thermochemical cycle is one of the alternative methods for producing hydrogen. It is an attractive method to produce hydrogen without using fossil fuels as the feedstock and producing emission of any greenhouse gas. In the S I thermochemical cycle, HI decomposition section has complex dynamic systems due to the high process temperature involved and the presence of a homogenous azeotrope in the HIx phase. In this research, the dynamic simulation through the design of Model Predictive Control strategy were implemented to control the process of S I thermochemical cycle. Then, the performance of the Model Predictive Control was examined and compared with the Proportional Integral Derivative control strategy in terms of set point tracking and disturbance rejections. Based on the results, Model Predictive Control strategy has presented better performance as compared to the Proportional Integral Derivative control strategy."

"Upaya untuk memproduksi hidrogen masih sedikit dari sumber yang terbarukan. TiO2 dalam bentuk nanotube arrays dengan dopan Boron yang disintesis dengan metode anodisasi untuk produksi hidrogen telah diinvestigasi. Perlakuan termal katalis B-TiO2 nanotube arrays (B-TNTAs) dilakukan dengan kalsinasi reduksi dengan gas hidrogen pada suhu 500oC selama 2 jam. Analisis SEM menunjukkan morfologi nanotube arrays tiap konsentrasi boron seragam. Analisis UV-Vis DRS menunjukkan B-TNTAs memiliki absorbansi yang besar pada jangkauan panjang gelombang sinar tampak dengan band gap energy yang relatif rendah yaitu menjadi 2,9 eV. Analisis XRD menunjukkan hasil 100% kristal anatase murni. Melalui proses fotokatalisis, hidrogen mampu dihasilkan hingga 48959 μmol/m2 setelah 4 jam pengujian dengan katalis 7,5 mM B-TNTAs.

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Attempts to produce hydrogen is still slightly from renewable sources. TiO2 nanotube arrays in the form of boron dopants synthesized by anodizing method for hydrogen production has been investigated. Catalyst-thermal treatment of TiO2 nanotube arrays B (B-TNTAs) performed by calcination reduction with hydrogen gas at a temperature of 500oC for 2 hours. SEM analysis showed the morphology of nanotube arrays by uniform boron concentration. UV-Vis DRS analysis showed B-TNTAs has a large absorbance in the visible wavelength range with a band gap energy is relatively low, to 2.9 eV. XRD analysis produces 100% anatase crystals. Through a photocatalytic process, hydrogen is able to produce up to 48959 μmol/m2 after 4 hours of testing with catalyst 7.5 mM B-TNTAs."

"Telah diteliti pengaruh modifikasi fotokatalis TiO2 Degussa P-25 dalam memproduksi hidrogen dari gliserol dan air. Modifikasi yang dilakukan berupa perubahan morfologi menjadi nanotubes, pemberian dopan Pt, dopan N, dan penumbuhan fasa kristalin masing-masing melalui perlakuan hidrothermal (130oC, 12 jam), photo-assisted deposition, impregnasi dan kalsinasi 500oC selama 1 jam. Analisa SEM-EDS dan XRD menunjukkan bahwa katalis Pt-N-TiO2 nanotubes dengan tingkat kristalinitas dengan fasa anatase menyerupai TiO2 Degussa P-25. Berdasarkan uji kinerja fotokatalis di bawah sinar tampak, konsentrasi gliserol yang paling optimal adalah 50%. Morfologi nanotubes, dopan N, dopan Pt, dan dopan Pt dan N masing-masing memberikan kenaikan total produksi hidrogen sebanyak 2; 3; 11; dan 13,5 kali secara berurutan dibandingkan TiO2 Degussa P25.

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The effects of modified TiO2 Degussa P-25 in hydrogen generation from water and glycerol have been observed. The photocatalyst was formed to nanotubes, doped with Pt, doped with N and crystallized each by hydrothermal treatment (130oC, 12 hours), photo-assisted deposition, impregnation, and calcination (500oC) respectively. Result of SEM-EDS and XRD show that Pt-N-TiO2 nanotubes composite crystallinity with anatase phase similar to TiO2 Degussa P-25 was successfully obtained. The effects of glycerol and water composition have also been observed under visible light resulting 50% of glycerol as the optimum concentration. Nanotubes morfology, N doped, Pt doped, and Pt-N doped catalyst increase the hydrogen production each by 2, 3, 11, and 13.5 times respectively compare to TiO2 Degussa P-25. "

"Objectives of this research are mainly to study impacts of acidity strength (by varying amount of precipitant and loading Al-Si) and the effect of nickel particle size (by varying calcinations temperature) on decomposition reaction performances. In this research, high-nickel-loaded catalyst is prepared with two methods. Ni-Cu/Al catalysts were prepared with co-precipitation method. While the Ni-Cu/Al-Si catalyst were prepared by combined co-precipitation and sol-gel method. The direct cracking of methane was performed in 8mm quartz fixed bed reactor at atmospheric pressure and 500-700°C. The main results showed that the Al content of catalyst increases with the increasing amount of precipitant. The activity of catalyst increases with the increasing of catalyst?s acidity to the best possible point, and then increasing of acidity will reduce the activity of catalyst. Ni-Cu/4Al and Ni-Cu/11Al deactivated in a very short time hence produced fewer amount of nanocarbon, while Ni-Cu/15Al was active in a very long period. The most effective catalyst is Ni-Cu/22Al, which produced the biggest amount of nanocarbon (4.15 g C/g catalyst). Ni catalyst diameter has significant effect on reaction performances mainly methane conversion and product yield. A small Ni crystal size gave a high methane conversion, a fast deactivation and a low carbon yield. Large Ni particle diameter yielded a slow decomposition and low methane conversion. The highest methane conversion was produced by catalyst diameter of 4 nm and maximum yield of carbon of 4.08 g C/ g catalyst was achieved by 15.5 nm diameter of Ni catalyst."