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Design of Dry Cell HHO Generator using NaCl Solution for Hydrogen Production Arif Budiman; Muhammad Yerizam; Yohandri Bow
IJFAC (Indonesian Journal of Fundamental and Applied Chemistry) Vol 7, No 1 (2022): February 2022
Publisher : IJFAC (Indonesian Journal of Fundamental and Applied Chemistry)

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.24845/ijfac.v7.i1.8

Abstract

Excessive use of electricity produces emissions, as well as carbon will have impact on global warming because electricity mostly still using fossil-based energy. Usage of other alternative energy is beneficial to reduce dependence on the use of fossil fuels. Researchers are currently working to reduce the use of fossil energy by using renewable energy. Among the most common alternative energies found is water, so this research focuses on designing dry cell type HHO (Hydrogen Hydrogen Oxygen) Generator technology with hydrogen gas water electrolysis. The HHO generator functions to break water (H2O) into hydrogen atoms and oxygen atoms, known as HHO. Electrolysis testing using NaCl and a storage tube to see the rise and fall of water from the gas produced. NaCl used weighing 20 grams, 50 grams, 75 grams, and 100 grams dissolved in 500 cc of water. The results of the data obtained, many uses of NaCl produce hydrogen gas faster, the data shows 100 grams of NaCl at 180-210 seconds produces a gas volume of 175 CC compared to 20 grams produces a gas volume of 75 CC, 50 grams produces 125 CC, and 75 grams produces 150 CC
Characterization of Fly Ash Catalyst Using XRD Method for Biofuel Production from Used Cooking Oil Dina Eka Pranata; Aida Syarif; Muhammad Yerizam
IJFAC (Indonesian Journal of Fundamental and Applied Chemistry) Vol 6, No 3 (2021): October 2021
Publisher : IJFAC (Indonesian Journal of Fundamental and Applied Chemistry)

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.24845/ijfac.v6.i3.90

Abstract

Fly ash catalyst that has been activated using NaoH 2M was analyzed using XRD at an angle of 2θ = 15 ° - 80 ° with a wavelength (λ) of X rays of 0.15406 nm. From the results of the analysis, the NaO26Si6Y9 compound is obtained with a hexagonal structure. Furthermore, the XRD analysis results obtained in the form of wavelength, intensity, 2θ and FWHM values will be substituted into the Debye Scherrer equation to calculate the size of the crystal structure of the Fly Ash catalyst. From this equation, a graph of the relationship between ln(b) dan ln(1/cos(q ))  will be drawn so that the intercept value is - 4.0688 and the value of K = 0.9 and λ = 0.15406 nm. The value of K and λ can be calculated using the modified Debye Scherrer equation, so that the crystal size (D) is 8,10942 nm.
NOx and CO Emissions Of Rice Straw, Coconut Shell and Biobriket Muhammad Yerizam
Sriwijaya International Seminar on Energy-Environmental Science and Technology Vol 1, No 1 (2014)
Publisher : Sriwijaya International Seminar on Energy-Environmental Science and Technology

Show Abstract | Download Original | Original Source | Check in Google Scholar

Abstract

Biobriquette can be used to anticipate the high fossil fuel needed as alternative fuel, cheap and easily obtained. Biobriquette is solid fuel and derived from organic residues. Generally, coal biobriquette making process used biomass waste such as straws, sawdust or various shell biomasses (coffee, cocoa, hazelnut, corn, cassava and jatropha waste). In this research used biomass waste from rice straw with adding the various coconut shell compositions. The compositions of rice straw: coconut shell are 50% : 50 %, 60%: 40%, 70% : 30%, 80% : 20%, 90% : 10% with 10 % tapioca adhesive addition. One of variables determined the biobriquette quality was pollution level generated in the combustion process which was Nox and CO gas. In this research obtained best quality composition of rice straw : coconut shell was 50% : 50% and had emission level for Nox gas at 3.17 mg/m3 and CO gas at 0.5 mg/m3. The biobriquette product was feasible due to the emission value were below the emission standards set for Nox ≤ 1000 mg/m3 and CO ≤ 500 mg/m3.
Effect of Oxygen Flow Rate on Combustion Time and Temperature of Underground Coal Gasification Apriansyah Zulatama; Aida Syarif; Muhammad Yerizam
International Journal of Research in Vocational Studies (IJRVOCAS) Vol. 1 No. 2 (2021): IJRVOCAS - August
Publisher : Yayasan Ghalih Pelopor Pendidikan (Ghalih Foundation)

Show Abstract | Download Original | Original Source | Check in Google Scholar | Full PDF (305.651 KB) | DOI: 10.53893/ijrvocas.v1i2.27

Abstract

Underground Coal Gasification (UCG) is a process of converting coal in the ground into synthetic gas that has economic value. In the UCG process which will be carried out in the UCG prototype assisted by the presence of oxygen as a gasification agent, which this gasification agent will help the process of burning coal in the ground. The flow rate of oxygen in the process of UCG affecting the coal combustion temperature and effective flame from burning coal. The highest temperature at a flow rate of 5 l/min is 240oC, at an oxygen flow rate of 3 l/min the highest temperature is 143oC and at an oxygen flow rate of 2 l/min the highest temperature is 135oC and time effective flame at a flow rate of 5 l / min ie 80 minutes, effective burning time on the speed of the flow rate of 3 l / min ie for 120 minutes and time effective flame at a flow rate of 2 l / min ie for 165 minutes. This study proves that the greater the oxygen flow rate is used as the gasification agent at UCG process the lignite coal combustion temperatures will be high and effective flame coal combustion process will be more brief.
Syngas Characteristics from UCG Gasification Process with Lignite and Subbituminous Coal Types Sarmidi; Muhammad Yerizam; Aida Syarif
International Journal of Research in Vocational Studies (IJRVOCAS) Vol. 1 No. 2 (2021): IJRVOCAS - August
Publisher : Yayasan Ghalih Pelopor Pendidikan (Ghalih Foundation)

Show Abstract | Download Original | Original Source | Check in Google Scholar | Full PDF (272.152 KB) | DOI: 10.53893/ijrvocas.v1i2.50

Abstract

Underground Coal Gasification (UCG) is the process of converting the materials used to make synthetic gas in a feasible and economically attractive manner as a method for harnessing energy from underground coal sources. Coal gasification will produce a gas producer in the form of synthetic gas (syngas) with the main components consisting of carbon monoxide (CO), hydrogen (H2), carbon dioxide (CO2) and nitrogen (N2) and low pollutants. The highest temperature produced with MT 47 lignite coal using an oxygen velocity of 5 liters/minute was 2400 C at the 35th minute, while the lowest temperature was 950 C at the 95th minute. For Subbituminous AL 51 coal using an oxygen velocity of 5 liters/minute, the highest temperature is 3540 C at 75 minutes, while the lowest temperature is 1060 C at 130 minutes. At an oxygen velocity of 5 liters/minute the flash point / burn test is on the MT 47 lignite coal type in the 10th minute and at a temperature of 1700 C. Meanwhile, the AL 51 subbituminous coal type is in the 30th minute and at a temperature of 3130 C. Based on the discussion and analysis of data from the gasification test of lignite and subbituminous coal with variations in oxygen velocity of 5 liters/minute, the results obtained are that lignite coal burns faster (burn test) in the 10th minute at a temperature of 1700 C, in the subbituminous type it has higher temperature 3130 C and longer burn test at 30 minutes.
Pengolahan Singkong Karet Menjadi Tepung Mocaf Di Sukabangun Kecamatan Sukarame Kota Palembang Muhammad Yerizam; Ahmad Husaini; Ellina Margaretty; Aliyah Montessa
Aptekmas Jurnal Pengabdian pada Masyarakat Vol 2 No 1 (2019): APTEKMAS Volume 2 Nomor 1 2019
Publisher : Politeknik Negeri Sriwijaya

Show Abstract | Download Original | Original Source | Check in Google Scholar | Full PDF (900.124 KB) | DOI: 10.36257/apts.v2i1.1300

Abstract

Sukabangun is one of the Sukarami sub-districts in the city of Palembang, South Sumatra, which can be reached approximately 20 minutes from the Sriwijaya State Polytechnic.The targets and outcomes expected from this dedication are the emergence of awareness to utilize Manihot Glaviozii which is rarely used by the society for daily needs, increase business opportunities and create workforce for the local and surrounding society which are still unemployed and teenagers who are no longer attending school and make a mocaf flour as an alternative to wheat flour.The implementation methods of this dedication that is applied includes Presentations and interactive discussions conducted for the targets, namely the residents of Sukarame sub-district, presentation material namely knowledge of processing mocaf flour from Manihot Glaviozii, displaying and giving banners for example mocaf flour, showing a mocaf flour has been processed, digging up the absorption of participants in interactive discussions through question and answer. From the result of this dedication is the residents get the knowledge about the processing of Manihot Glaviozii becomes mocaf flour as an alternative wheat flour so that, it will impact for the economic society in Sukabangun, Sukarame sub-district, Palembang city.
Rancang Bangun Digester Untuk Proses Pulping dari Campuran Tandan Kosong Kelapa Sawit dan Pelepah Pisang dengan Pelarut NaOH Nyayu Fia Atindu; Muhammad Yerizam; Erwana Dewi
Jurnal Pendidikan dan Teknologi Indonesia Vol 1 No 9 (2021): JPTI - September 2021
Publisher : CV Infinite Corporation

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.52436/1.jpti.88

Abstract

Kebutuhan pulp dan kertas di dunia semakin meningkat. Menurut Asosiasi Pulp dan Kertas Indonesia (APKI) permintaan global maupun domestik masih terus meningkat setiap tahunnya sebesar 2 %. Hal ini mengakibatkan ketersediaan bahan baku industri kertas menipis. Maka dari itu bahan baku lain yang dapat dijadikan suatu alternatif dari dampak tersebut yaitu tandan kosong kelapa sawit dan pelepah pisang. Digester merupakan suatu bejana pemasak yang digunakan sebagai suatu tempat proses delignifikasi bahan baku pada pembuatan pulp. Pada perancangan alat digester ini mempunyai dimensi meliputi : diameter tangki : 15 cm, tinggi tangki : 30 cm, tebal plate : 0,3 mm, tinggi impeler : 33 cm, kecepatan pengaduk : 95 rpm dan kapasitas 5,5 liter. Penelitian ini menggunakan metode rancang bangun dan eksperimen. Metode rancang bangun dilakukan untuk perancangan dan pembuatan digester Metode eksperimen dilakukan dengan tujuan yaitu mengetahui kinerja digester agar mendapatkan kondisi optimum alat digester dalam pulping dari campuran tandan kosong kelapa sawit dan pelepah pisang. Tahapan proses pulping ini yaitu : (1) tandan kosong kelapa sawit dan pelepah pisang di potong-potong lalu di cuci dengan air kemudian dikeringkan, (2) pemasakan di dalam digester , (3) pulp disaring, (4) pulp di analisa. Parameter yang diukur yaitu temperatur pemasakan dengan variasi 90, 100,110,120 oC, Parameter yang terjaga konstan yaitu konsentrasi larutan, waktu pemasakan, dan putaran pengaduk. Pada hasil pengamatan dan analisis didapatkan kondisi optimum pada temperature 110oC denganhasil yang di dapat yaitu kadar air 15,50 %, kadar lignin 10,07 % , kadar hemiselulosa16,03 % dan kadar selulosa 58,41 %.
Analisis Karakteristik Pulp Campuran Tandan Kosong Kelapa Sawit dan Pelepah Pisang dengan Pelarut NaOH Sari Rizky Amelia; Muhammad Yerizam; Erwana Dewi
Jurnal Pendidikan dan Teknologi Indonesia Vol 1 No 10 (2021): JPTI - Oktober 2021
Publisher : CV Infinite Corporation

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.52436/1.jpti.91

Abstract

Tandan kosong kelapa sawit (TKKS) merupakan limbah padatan yang dihasilkan dari proses pembuatan minyak kelapa sawit yang selulosa (45,95%), kadar abu (1,23%), hemiselulosa (22,84%), kadar air (3,74%) dan lignin (16,49%). Pelepah pisang mempunyai kandungan selulosa yang tinggi akan tetapi belum dimanfaatkan secara optimal yang memiliki kandungan densitas ( 1,35 gr/cm3), selulosa (63 -64 %), hemiselulosa (20 %), lignin (5%), kekuatan Tarik rata-rata (600 Mpa), modulus tarik rata-rata (17,85 Gpa), pertambahan panjang (3,36 %), diameter serat (5,8 µm), serta panjang serat (30,9240 cm). Namun bahan-bahan ini mempunyai karakteristik dan sifat fisika kimia yang berbeda-beda. Karakteristik menjadikan perlunya analisa agar menghasilkan pulp yang diinginkan berada pada kondisi optimal. Beberapa parameter yang diukur di antaranya, konsentrasi larutan NaOH dengan variasi 7% dan 9%, dengan variasi bahan baku 40-60% serta waktu pemasakan dengan variasi waktu 75, 90, 105, 120 dan 135 menit. Sehingga pada penelitian ini didapatkan kondisi optimumnya yakni pada rasio 40:60, dengan konsentrasi 9% dan waktu pemasakan selama 120 menit didapatkan nilai kadar lignin 11,21% dan kadar selulosa 68,94%. Oil palm empty fruit bunches or TKKS are solid wastes produced from the process of making palm oil which are cellulose (45.95%), ash content (1.23%), hemicellulose (22.84%), water content (3.74 %) and lignin (16.49%). Banana midrib has a high cellulose content but has not been used optimally which contains density (1.35 g/cm3), cellulose (63 -64 %), hemicellulose (20 %), lignin (5%), average tensile strength. average (600 Mpa), average tensile modulus (17.85 Gpa), increase in length (3.36%), fiber diameter (5.8 m), and fiber length (30,9240 cm). However, these materials have different physicochemical characteristics and properties. The characteristics make the need for analysis in order to produce the desired pulp in optimal conditions. Several parameters were measured including the concentration of NaOH solution with variations of 7% and 9%, with variations of raw materials 40-60% and cooking time with variations of 75, 90, 105, 120 and 135 minutes. So that in this study the optimum conditions were obtained, namely at a ratio of 40:60, with a concentration of 9% and cooking time for 120 minutes, the lignin content was 11.21% and the cellulose content was 68.94%.
RANCANG BANGUN ALAT DRYER UNTUK PENGERINGAN PULP BERBASIS CAMPURAN TANDAN KOSONG KELAPA SAWIT DAN PELEPAH PISANG M. Ridho Triadi; Muhammad Yerizam; Selastia Yulianti
Jurnal Pendidikan dan Teknologi Indonesia Vol 1 No 12 (2021): JPTI - Desember 2021
Publisher : CV Infinite Corporation

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.52436/1.jpti.113

Abstract

Penggunaan campuran TKKS dan pelepah pisang sebagai bahan pengganti kayu dalam pembuatan pulp menjadi solusi atas kerusakan lingkungan akibat meluasnya penebangan hutan secara liar guna memenuhi bahan baku pembuatan kertas. Dalam pembuatan pulp pada UKM masih ditemukan permasalahan dimana proses pengeringan pulp masih mengunakan cara konfensional sehingga memakan waktu yang lama, pengeringan tidak merata, dan bergantung pada cuaca. Hal tersebut yang melatar belakangi penulis melakukan sebuah penelitian dengan tujuan memperoleh satu unit alat dryer tipe tray pada proses pembuatan pulp dari campuran TKKS dan pelepah pisang, serta mendapatkan kondisi optimum dari dryer berdasarkan waktu dan laju pengeringan pulp yang diharapkan memenuhi standar SNI kadar air pulp. Penelitian ini menggunakan metode rancang bangun dan eksperimen. Metode rancang bangun dilakukan untuk perancangan alat pengering tipe tray pada pengeringan pulp. Metode eksperimen dilakukan untuk mendapatkan data kinerja dryer yang ditinjau dari waktu dan laju pengeringan. Hasil dari penelitian ini yaitu didapat sebuah alat Dryer tipe Tray dengan panjang 34,5 cm, lebar 35 cm dan tinggi 39,5 cm dengan kapasitas maksimal 42 kg. didapatkan pulp dengan kadar air yang sesuai SNI kadar air pulp yaitu sebesar 9,1% pada waktu pengeringan selama 420 menit dengan laju pengeringan total sebesar 0,012656 kg/jam m2
Kinetika Reaksi Delignifikasi Campuran Tandan Kosong Kelapa Sawit dan Pelepah Pisang sebagai Bahan Baku Pembuatan Pulp Menggunakan Alat Digester Azaria Hikmah Fajrianti; Indah Purnamasari; Muhammad Yerizam
Jurnal Pendidikan dan Teknologi Indonesia Vol 2 No 2 (2022): JPTI - Februari 2022
Publisher : CV Infinite Corporation

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.52436/1.jpti.138

Abstract

Pulp adalah hasil pemisahan selulosa dari bahan baku berserat (kayu maupun non kayu) melalui berbagai proses pembuatan baik secara mekanis, semi-kimia dan kimia. Campuran bahan dalam pembuatan pulp yaitu Tandan Kosong Kelapa Sawit (TKKS) dengan kandungan selulosa sebesar 42,7 – 65% dan pelepah pisang dengan kandungan selulosa sebesar 63 – 64%. Penelitian ini menggunakan variasi temperatur pemasakan 90°C, 100°C, 110°C dan 120°C serta variasi waktu pemasakan selama 60, 75, 90, 105 dan 120 menit. Selain itu juga menggunakan larutan pemasak NaOH konsentrasi 9% dengan komposisi sample (TKKS:pelepah pisang) yakni 2:1. Berdasarkan hasil penelitian yang telah dilakukan titik optimum kadar lignin pulp didapatkan sebesar 7,75% pada waktu pemasakan 90 menit dan temperatur pemasakan 110°C.
Co-Authors Abu Hasan Abu Hasan Abu Hasan Achmad Reza Aditya Amin Agum Try Wardhana Agus Manggala Agustin Pratiwi, Ines Ahmad Zamheri AIDA SYARIF Aida Syarif Akbar Ismi Aziz Pramito Aliyah Montessa Amin, Achmad Reza Aditya Anerasari Meidinariasty Anerasari Meidinariasty Anggi Dwi Chandrika Apriansyah Zulatama Aprilia, Luraselly Arda Aria Yopianita Arif Budiman Asyeni Miftahul Jannah Asyeni Miftahul Jannah Ayuni Lestari Azaria Hikmah Fajrianti Az’zahrah, Nandyta Rizqi Cindi Ramayanti Dilia Puspa Dina Eka Pranata Dwi Nugroho, Afrian Eka Mulyana, Eka Ellina Margaretty Endang Sri Rahadianti Erwana Dewi Erwin Erwin Fatahul Arifin, Fatahul Febri Liani Br Simanjuntak Fenoldi, Nova Feri Hafidz, Abdurrahman Helen Chairunisa Ihtifazhuddin, Farhan INDAH PURNAMASARI Indah Purnamasari Indah Purnamasari Indrayani Indrayani Jabborov, Behzod Kalsum, Leila Khairunnisa, Annisa Septia Kusuma, Mutmainnah Ningtyas M, Anerasari M. Ridho Triadi M. Zaman Manggala, Agus Martha Aznury Martha Martha Muhammad Yori Pratama Muhammad Zaman Mustain Zamhari Nabila, Rizky Ayu Ningsih, Anis Wahyu Nyayu Fia Atindu Nyayu Zubaidah Nyayu Zubaidah Pratama, Andrian Putra Pratama, Muhammad Yori Putra, Rizkika Raysha Amelya Renny Citra Ramadhani Riansyah, Epan Robert Junaidi Robert Junaidi Rusdianasari Rusdianasari Rusdianasari Sabrina, Delanisa Salsha Ardiani Saqila Putri Aulia Sari Rizky Amelia Sarmidi Sarmidi Selastia Yulianti Selastia Yuliati Selastia Yuliati Silmi Tsabita Sirait, Agnes Tasya Pintauly Tamara, Ade Wan Qori Sri Maulani Winnugroho Wiratman, Manfaluthy Hakim, Tiara Aninditha, Aru W. Sudoyo, Joedo Prihartono Yahya, Muhammad Habib Yohandri Bow Zain, Raina Khoirunisa