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Muhammad Faizal

    Muhammad Faizal

    Oil palm empty fruit bunch (OPEFB) is one of the enormous waste expected to become a renewable energy source. This study aimed to convert OPEFB into syngas through a gasification process using bentonite as a catalyst. The effects of... more
    Oil palm empty fruit bunch (OPEFB) is one of the enormous waste expected to become a renewable energy source. This study aimed to convert OPEFB into syngas through a gasification process using bentonite as a catalyst. The effects of temperature and product gas catalysts were investigated, and the efficiency of the gasification process was summarized. The process has used an updraft gasifier at 350-550°C and air as the gasification medium (ER 0.2). The results indicate that syngas can be produced by updraft gasifier. When the temperature increase, the H2 and CO rising. The highest H2 and CO content of 27.74% and 20.43% are obtained at 550°C when bentonite applied. HHV and LHV range of 3.38~12.79 MJ/Nm3 and 3.03~11.58 MJ/Nm3 , respectively. The maximum carbon conversion efficiency (CCE) and cold gas efficiency (CGE) reach 85.49% and 82.34%. Bentonite has been able to increase the concentration of the gas composition especially H2 and CO and the heating value of syngas.
    Fine coal waste from the coal mining process has not been used as clean energy even though the amount is very abundant in the world. The conversion of fine coal to syngas is a new way to increase the value of fine coal. Syngas... more
    Fine coal waste from the coal mining process has not been used as clean energy even though the amount is very abundant in the world. The conversion of fine coal to syngas is a new way to increase the value of fine coal. Syngas composition, gas ratio, gasification efficiency, and heating value of syngas have been determined under various conditions of temperature (550-750 °C) and bentonite catalyst ratio (0-0.25). The results indicate that fine coal is the suitable raw material for the gasification process. At the highest temperature (750 °C), the gas composition consists of 42.6 vol% H2, 19.1vol% CO, 19.5 vol% CH4, and 7.9vol% CO2. The best performance was achieved when the catalyst/feed ratio is 0.25 with the gas composition of 54.3vol% H2, 26.2vol% CO, 23.8 vol% CH4, and 3.5vol% CO2, heating value and gasification efficiency were 19.72 MJ/Nm3 and 72.27% at 750 °C.
    The presence of CO2 in the syngas is attracting more attention in terms of reducing the greenhouse gas emissions in its utilisation. The aim of this study was to purify syngas from the CO2 content of fine coal gasification. Fine coal is... more
    The presence of CO2 in the syngas is attracting more attention in terms of reducing the greenhouse gas emissions in its utilisation. The aim of this study was to purify syngas from the CO2 content of fine coal gasification. Fine coal is gasified with and without absorption using CaO, which is hydrated to Ca(OH)2 in the modified updraft gasifier at 450–700 °C. Apart from investigating the CO2 absorption process, the gasification process also evaluates the influence of temperature in terms of its synergy with Ca(OH)2. The best conditions for the gasification process are achieved at 700 °C. The content of CO2 was proven to be well absorbed, which is characterised by a decrease in the CO2 content and an increase in H2 in syngas. After the absorption process, the H2 content obtained increased from 42.6 mole% to 48.8 mole% of H2 at 700°C. The H2 ratio also increased after absorption to 2.57 from the previous value of 2.23. The highest absorption efficiency of CO2 by Ca(OH)2 occurred at 70...
    Kromium diketahui sebagai salah satu polutan beracun yang menyebabkan masalah lingkungan dan kesehatan masyarakat. Kromium Heksavalen Cr(VI) merupakan logam berat, dimana dalam konsentrasi yang kecil dapat menghasilkan tingkat keracunan... more
    Kromium diketahui sebagai salah satu polutan beracun yang menyebabkan masalah lingkungan dan kesehatan masyarakat. Kromium Heksavalen Cr(VI) merupakan logam berat, dimana dalam konsentrasi yang kecil dapat menghasilkan tingkat keracunan yang tinggi pada makhluk hidup. Jika senyawa kromium (VI) terbuang ke lingkungan dan masuk ke dalam tubuh makhluk hidup maka akan sangat berbahaya, sehingga penting untuk mengolah limbah tersebut. Penelitian ini difokuskan pada proses pengolahan Cr(VI) dengan metode kombinasi yaitu secara kimia dan secara fisika. Penelitian ini bertujuan untuk mengolah air limbah yang mengandung Cr(VI) menggunakan reagen Fenton yang dilanjutkan adsorpsi menggunakan adsorben berbahan dasar zeolit dan tanah liat yang dibentuk menjadi keramik. Air limbah yang mengandung Cr(VI) dikontakkan dalam reaktor berpengaduk sehingga terjadi reaksi reduksi oksidasi, selanjutnya air limbah ini dilewatkan ke dalam kolom adsorpsi yang berisi adsorben keramik zeolit. Kondisi terbaik d...
    NAMA : MUHAMMAD FAIZAL
    NIM : 21102015
    TUGAS TEORI PEMBANGUNAN
    Tugas teori pembangunan_tulisan singkat tentang resellience city, network governance, urban development
    Tugas teori pembangunan
    The number of laundry industry has been increasing rapidly which influences the amount of detergent usage in the washing process. Generally the laundry industries dump their wastewater directly to environment without any treatment.... more
    The number of laundry industry has been increasing rapidly which influences the amount of detergent usage in the washing process. Generally the laundry industries dump their wastewater directly to environment without any treatment. Phosphate contained in detergent shall accumulate in the environment then finally would cause eutrofication where the water body becomes rich of dissolved nutrient which effects the dissolved oxygen contained in water body. One of wastewater treatment methods is adsorption. Two different kinds of adsorbents were applied in this investigation namely activated carbon and natural zeolite. Synthetic laundry wastewater was used in order to control the phosphate concentration. The objective of this experiment was to study the removal of phosphate concentration of each adsorbent filled in adsorption column by using circulation method. The column has 1 inch of diameter, 50 cm of height, and 50 ml/minute of flowrate. The concentration of phosphate was varied betwe...
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