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Busrizal Faisal
Prodi Teknik Kimia, Institut Teknologi Sawit Indonesia, Medan
Chemical Engineering, Chemistry & Bioengineering Materials Science & Nanotechnology Mechanical Engineering

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PENGURANGAN KADAR AIR OPTIMAL (MOISTURE CONTENT) BLANKET SIR 10 MELALUI PROSES MATURASI DI PABRIK PENGOLAHAN KARET Arga Dwi Ananda; Busrizal Faisal; Siti Aisyah
Jurnal Agro Fabrica Vol. 3 No. 2 (2021): Desember 2021
Publisher : Institut Teknologi Sawit Indonesia (ITSI)

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.47199/jaf.v3i2.123

Abstract

Natural rubber processing is one of the potential agro-industrial sectors for Indonesia, whose role is quiteimportant as a foreign exchange earner for the plantation sub-sector. The production rate of 1.6 million tons in2002 or 22% of the world's total natural rubber production has placed Indonesia as the second largest producingcountry after Thailand. This study aims to determine whether the quality of blanket sir 10 is optimal by using amaturation time of 11 days, which is related to: Decreasing Blanket Moisture Content with Maturation Method,Analysis of Blanket Sample Data, Decreasing Water Content, Decreasing Blanket Moisture Content, MaturationProcess. The method of this research was carried out in a crumb rubber processing factory using a researchdesign: Bound variables Rubber sheet / blanket and crumb rubber from a rubber processing factory, theindependent variables in this study were as follows: Maturation treatment: hanging, maturation time: 11 days.The total weight of samples I, II, III, and IV is 975.90 kg, the total water content evaporated is 8.85 kg and theamount of blanket shrinkage is 0.91%. This shrinkage of the blanket amounted to 0.91%, which is the totaldecrease in the blanket moisture content in the eleven (11) days maturation. This process of maturing takes placenaturally. From data analysis and discussion of reducing the blanket moisture content for 11 days and processingmaterial for SIR 10 (Standard Indonesian Rubber) / Low Grade Crumb Rubber, it is concluded, as follows: Using4 (four types of samples with initial blanket weight: 20.15 kg) (sample 1), 20.85 kg (sample 2), 24.90 kg (sample3), and 27.85 kg (sample 4). Decreased moisture content in sample 1 = 1.06%, sample 2 = 0, 85%, sample 3 =0.87%, and sample 4 = 0.88%. The average reduction in water content in the blanket was 0.91% (for 11 days). Inthe reporting of this study, the blanket maturation time was set at 11 (eleven) days, although there are othermaturation times, such as: 6 (six) days, and 8 (eight days). The relatively h
EFEKTIFITAS PEMANASAN KAMAR ASAP MELALUI DISTRIBUSI UDARA MASUK (FORCED DRIVE FAN/FDF) DAN UDARA KELUAR (INDUCED DRIVE FAN/IDF) PADA PENGOLAHAN KARET LEMBARAN (RIBBED SMOKE SHEET) : REVIEW Faisal, Busrizal; Effendi, Zulham
Jurnal Agro Fabrica Vol. 5 No. 1 (2023): Juni 2023
Publisher : Institut Teknologi Sawit Indonesia (ITSI)

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.47199/jaf.v5i1.151

Abstract

The smoke chamber used has a capacity of 3,420 kg with a rubber sheet smoking period of five days. Reducing the water content (moisture content) on the rubber sheet is used by heating it with a smoking system. For smoke chamber operations, the fumigation temperature used on the first day is 40 - 45°C, on the second day 45 - 50°C, on the third day 50 - 55°C, on the fourth day 55 - 60°C, and on the fifth day the smoking temperature was maintained at 60°C. FDF and IDF are two air distribution devices, where the FDF functions to blow the air into the smoke chamber and the IDF draws the air into the smoke chamber. The balance between exhaled air and that drawn out of the smoke chamber must be proportional. Too much airflow will collect in the smoke chamber and too much the air withdrawal will affect heat transfer. After installing the FDF and IDF tools, the smoking time is 4 (four) days, so the use of smoked wood (rubber stem wood) is reduced from 3.19 m3 (for 5 days of smoking) to 2.55 m3 (for 4 days of smoking). There is a saving of one operational day. Reducing the use of smoked wood has an impact on processing efficiency. Heat energy from smoking has also increased. Before the installation of the FDF and IDF devices, the amount of heat energy was 64,074 kcal/day (320,372 kcal in 5 days). After installing the FDF and IDF devices, they increase the amount of air / oxygen (O2) in the combustion process so that there is an additional heat energy of 9,461 kcal/day (47,305 kcal in 5 days). The total amount of heat energy produced is 367,677 kcal for 5 (five) days of smoking. FDF and IDF are two air blowers commonly known as blowers with their respective specifications: The FDF used has an electric power of 3 kilowatts (4 horsepower/hp) with a rotation of 1,420 rpm, while the IDF has an electric power of 7.5 kilowatts (10 horsepower/hp). hp) at 1,440 rpm.
PENGARUH SISTEM DOUBLE PEAK PEREBUSAN TERHADAP OIL LOSSES DARI AIR KONDENSAT PADA PEREBUSAN VERTIKAL DILIHAT DARI PERBEDAAN SUMBER BUAH YANG DIOLAH OLEH PKS HAPESONG PTPN 3 Aisyah, Siti; Mahyunis; Faisal, Busrizal; Firdaus, Khairin
Jurnal Agro Fabrica Vol. 6 No. 1 (2024): Juni 2024
Publisher : Institut Teknologi Sawit Indonesia (ITSI)

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.47199/jaf.v6i1.228

Abstract

In the last 10 years, the Palm Oil Mill (PKS) in Indonesia has grown very rapidly. Most of the large names of oil palm plantations have gradually changed throughout Indonesia to oil palm plantations. One of the processes to achieve efficiency in the Palm Oil Mill can be determined in the fruit ripening process. Where the perfection of the ripening process is influenced by the condition of the fruit and the ripening system. One of the problems that need to be faced in the vertical boiling process is the occurrence of losses or also called oil loss in the condensate air. Oil losses can occur due to various factors, including differences in fruit sources processed in the PKS. In this study, a factorial complete randomized planning method will be used which has two factors. The highest losses are in third party fruit/community fruit with a total of 11.04%, and the lowest total losses are in core plantation fruit with a total of 4.8%. The highest oil losses are in third party fruit or community fruit, this is due to the length of time the fruit has been sorted overnight which can cause the fruit to be overripe and also in fruit that is injured by the loader. The results of this analysis show that the double peak system has a significant impact on oil losses to third parties/community members.
PENGARUH SUHU PEMANASAN PADA STASIUN KERNEL SILO DRYER TERHADAP MUTU KERNEL DI PABRIK KELAPA SAWIT PT. XYZ Zakwan; Mahyunis; Faisal, Busrizal; Sembiring, Arifa Sura; Noor, Faiz
Jurnal Agro Fabrica Vol. 6 No. 1 (2024): Juni 2024
Publisher : Institut Teknologi Sawit Indonesia (ITSI)

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.47199/jaf.v6i1.246

Abstract

Oil palm plantations are widespread in Indonesia, triggering the birth of many palm oil processing industries, so that this plant becomes a commodity for the country. Palm oil factories process fresh fruit bunches (FFB) which will later produce crude palm oil (CPO) and palm kernel oil (PKO) as derivative products. Based on my experience and information, kernel processing in PKS cannot be fully maximized. Because many kernels are heated for a very long time so that the cost of production is high, and also many kernels are abandoned, moldy and smell rancid because the quality of the kernel is not fully achieved. In this case, the best processing of the kernel is needed. So that the quality of the kernel can be achieved. In this final assignment, it will be analyzed how the quality of the kernel is if heated with time and temperature below previous research. So that the kernel quality will be obtained according to SNI 01-000201- 1987 with lower energy consumption. This study will use a non-factorial random design method because it only has 1 factor, namely temperature variation (70 OC, 80 OC, and 100 OC).
EFEKTIFITAS PEMANASAN KAMAR ASAP MELALUI DISTRIBUSI UDARA MASUK (FORCED DRIVE FAN/FDF) DAN UDARA KELUAR (INDUCED DRIVE FAN/IDF) PADA PENGOLAHAN KARET LEMBARAN (RIBBED SMOKE SHEET) : REVIEW Faisal, Busrizal; Effendi, Zulham
Jurnal Agro Fabrica Vol. 5 No. 1 (2023): Juni 2023
Publisher : Institut Teknologi Sawit Indonesia (ITSI)

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.47199/jaf.v5i1.151

Abstract

The smoke chamber used has a capacity of 3,420 kg with a rubber sheet smoking period of five days. Reducing the water content (moisture content) on the rubber sheet is used by heating it with a smoking system. For smoke chamber operations, the fumigation temperature used on the first day is 40 - 45°C, on the second day 45 - 50°C, on the third day 50 - 55°C, on the fourth day 55 - 60°C, and on the fifth day the smoking temperature was maintained at 60°C. FDF and IDF are two air distribution devices, where the FDF functions to blow the air into the smoke chamber and the IDF draws the air into the smoke chamber. The balance between exhaled air and that drawn out of the smoke chamber must be proportional. Too much airflow will collect in the smoke chamber and too much the air withdrawal will affect heat transfer. After installing the FDF and IDF tools, the smoking time is 4 (four) days, so the use of smoked wood (rubber stem wood) is reduced from 3.19 m3 (for 5 days of smoking) to 2.55 m3 (for 4 days of smoking). There is a saving of one operational day. Reducing the use of smoked wood has an impact on processing efficiency. Heat energy from smoking has also increased. Before the installation of the FDF and IDF devices, the amount of heat energy was 64,074 kcal/day (320,372 kcal in 5 days). After installing the FDF and IDF devices, they increase the amount of air / oxygen (O2) in the combustion process so that there is an additional heat energy of 9,461 kcal/day (47,305 kcal in 5 days). The total amount of heat energy produced is 367,677 kcal for 5 (five) days of smoking. FDF and IDF are two air blowers commonly known as blowers with their respective specifications: The FDF used has an electric power of 3 kilowatts (4 horsepower/hp) with a rotation of 1,420 rpm, while the IDF has an electric power of 7.5 kilowatts (10 horsepower/hp). hp) at 1,440 rpm.
PENGARUH SISTEM DOUBLE PEAK PEREBUSAN TERHADAP OIL LOSSES DARI AIR KONDENSAT PADA PEREBUSAN VERTIKAL DILIHAT DARI PERBEDAAN SUMBER BUAH YANG DIOLAH OLEH PKS HAPESONG PTPN 3 Aisyah, Siti; Mahyunis; Faisal, Busrizal; Nasution, Khairin Firdaus Marajoki
Jurnal Agro Fabrica Vol. 6 No. 1 (2024): Juni 2024
Publisher : Institut Teknologi Sawit Indonesia (ITSI)

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.47199/jaf.v6i1.228

Abstract

In the last 10 years, the Palm Oil Mill (PKS) in Indonesia has grown very rapidly. Most of the large names of oil palm plantations have gradually changed throughout Indonesia to oil palm plantations. One of the processes to achieve efficiency in the Palm Oil Mill can be determined in the fruit ripening process. Where the perfection of the ripening process is influenced by the condition of the fruit and the ripening system. One of the problems that need to be faced in the vertical boiling process is the occurrence of losses or also called oil loss in the condensate air. Oil losses can occur due to various factors, including differences in fruit sources processed in the PKS. In this study, a factorial complete randomized planning method will be used which has two factors. The highest losses are in third party fruit/community fruit with a total of 11.04%, and the lowest total losses are in core plantation fruit with a total of 4.8%. The highest oil losses are in third party fruit or community fruit, this is due to the length of time the fruit has been sorted overnight which can cause the fruit to be overripe and also in fruit that is injured by the loader. The results of this analysis show that the double peak system has a significant impact on oil losses to third parties/community members.
PENGARUH SUHU PEMANASAN PADA STASIUN KERNEL SILO DRYER TERHADAP MUTU KERNEL DI PABRIK KELAPA SAWIT PT. XYZ Zakwan; Mahyunis; Faisal, Busrizal; Sembiring, Arifa Sura; Noor, Faiz
Jurnal Agro Fabrica Vol. 6 No. 1 (2024): Juni 2024
Publisher : Institut Teknologi Sawit Indonesia (ITSI)

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.47199/jaf.v6i1.246

Abstract

Oil palm plantations are widespread in Indonesia, triggering the birth of many palm oil processing industries, so that this plant becomes a commodity for the country. Palm oil factories process fresh fruit bunches (FFB) which will later produce crude palm oil (CPO) and palm kernel oil (PKO) as derivative products. Based on my experience and information, kernel processing in PKS cannot be fully maximized. Because many kernels are heated for a very long time so that the cost of production is high, and also many kernels are abandoned, moldy and smell rancid because the quality of the kernel is not fully achieved. In this case, the best processing of the kernel is needed. So that the quality of the kernel can be achieved. In this final assignment, it will be analyzed how the quality of the kernel is if heated with time and temperature below previous research. So that the kernel quality will be obtained according to SNI 01-000201- 1987 with lower energy consumption. This study will use a non-factorial random design method because it only has 1 factor, namely temperature variation (70 OC, 80 OC, and 100 OC).
Co-Authors Arga Dwi Ananda Firdaus, Khairin Mahyunis Nasution, Khairin Firdaus Marajoki Noor, Faiz Sembiring, Arifa Sura Siti Aisyah Siti Aisyah Zakwan Zulham Effendi Zulham Effendi