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INDONESIA
Jurnal Bahan Alam Terbarukan
Published by Universitas Negeri Semarang
ISSN : 23030623     EISSN : 24072370     DOI : -
Core Subject : Science,
Materials Science & Nanotechnology
This journal presents articles and information on research, development and applications in biomass conversion processes (thermo-chemical conversion; physico-chemical conversion and bio-chemical conversion) and equipment to produce fuels, power, heat, and value-added chemicals from biomass. A biorefinery takes advantage of the various components in biomass and their intermediates therefore maximizing the value derived from the biomass feedstock. A biorefinery could, for example, produce one or several low-volume, but high-value, chemical or nutraceutical products and a low-value, but high-volume liquid transportation fuel such as biodiesel or bioethanol (see also alcohol fuel). The high-value products increase profitability, the high-volume fuel helps meet energy needs, and the power production helps to lower energy costs and reduce greenhouse gas emissions from traditional power plant facilities. Future biorefineries may play a major role in producing chemicals and materials that are traditionally produced from petroleum.
Arjuna Subject : -
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Search results for , issue " Vol 1, No 2 (2012): December 2012" : 5 Documents clear
PEMUNGUTAN MINYAK ATSIRI MAWAR (Rose Oil) DENGAN METODE MASERASI Damayanti, Astrilia; Fitriana, Endah Ayu
Jurnal Bahan Alam Terbarukan Vol 1, No 2 (2012): December 2012
Publisher : Semarang State University

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.15294/jbat.v1i2.2543

Abstract

Minyak mawar merupakan salah satu produk minyak bunga yang memungkinkan diproduksi di Indonesia dengan kualitas ekspor. Manfaat dari minyak mawar adalah untuk parfum, kosmestik, dan obat-obatan. Minyak mawar dapat diproduksi dengan menggunakan metode diantaranya maserasi. Tujuan penelitian ini adalah mengetahui rendemen minyak atsiri mawar merah (Rosa damascena) dan komponen minyak atsiri yang terambil dengan etanol dan n-heksana. Bahan baku yang digunakan berupa mahkota bunga mawar sebanyak 50 gram yang dipotong kecil-kecil, kemudian direndam dalam pelarut dengan perbandingan 1:3. Pelarut yang digunakan yaitu etanol dan n-heksana. Proses maserasi dilakukan dengan pengadukan selama 1 menit secara manual pada suhu ruang dan didiamkan selama 12 jam di tempat tertutup dan gelap (tanpa terkena cahaya). Hasil maserasi berupa ekstrak mawar dipisahkan dengan cara penyaringan dan pemerasan bunga. Filtrat yang mengandung minyak bunga mawar dievaporasi dengan  rotary vacuum evaporator. Maserasi menggunakan etanol pada suhu 60ºC selama 20 menit, sedangkan maserasi menggunakan n-heksana pada suhu 55 ºC selama 10 menit. Minyak atsiri hasil maserasi bunga mawar merah dilakukan uji GC-MS. Komponen utama minyak atsiri dari bunga mawar dengan pelarut etanol dan pelarut n-heksana secara berurutan adalah phenyl ethyl alcohol (2,73%) dan (31,69%). Rendemen hasil maserasi minyak bunga mawar dengan pelarut etanol adalah 8,76%, sedangkan pelarut n-heksana menghasilkan 0,34 %. Rose oil is one of the flower oil products which is potentially produced in Indonesia with export quality. The uses of rose oils are for perfume, cosmestics, and medicine. Rose oil can be produced using methods such as maceration. The purpose of this reasearch was to determine the yield of essential oil of red roses (Rosa damascena) and the essential oil components taken using ethanol and n-hexane. The raw material used was 50 grams of red roses which subsequently soaked into solvent with ratio of 1:3. The solvent used were ethanol and n-hexane. Maceration process was carried out by manually stirring for 1 minute at room temperature and kept for 12 hours in a closed and dark (without exposure to light) place. Maceration result in the form of rose extract was separated by filtration and extortion of flowers. The filtrate containing rose oil was evaporated using rotary vacuum evaporator. Maceration temperature using ethanol was 60 ºC for 20 minutes, while using n-hexane was 55ºC for 10 minutes. The essential oils produced from maceration process of red roses was analysed using GC-MS. The main components of the essential oil of roses extracted using solvents of ethanol and n-hexane sequentially were phenyl ethyl alcohol (2.73%) and (31.69%). The yield of the rose oil maceration with ethanol was 8.76%, while the solvent of n-hexane yield 0.34%.
SINTESIS BIODISEL DARI MINYAK BIJI KARET DENGAN VARIASI SUHU DAN KONSENTRASI KOH UNTUK TAHAPAN TRANSESTERIFIKASI Kusumaningtyas, Ratna Dewi; Bachtiar, Achmad
Jurnal Bahan Alam Terbarukan Vol 1, No 2 (2012): December 2012
Publisher : Semarang State University

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.15294/jbat.v1i2.2544

Abstract

Bahan bakar yang paling banyak digunakan adalah bahan bakar diesel atau fatty acid methyl ester (FAME). Biodiesel berasal dari minyak nabati yang dapat diperbaharui, dapat dihasilkan secara periodik, dan mudah diperoleh. Pada penelitian ini digunakan minyak biji karet untuk sintesis FAME. Proses utama dalam pembuatan FAME adalah transesterifikasi. Penelitian ini mengkaji hasil optimum dari variasi konsentrasi katalis KOH dan suhu reaksi pada reaksi transesterifikasi. Preparasi minyak biji karet dengan menggunakan arang aktif granular diikuti dengan degumming. Reaksi esterifikasi dilaksanakan pada kondisi operasi 500 C selama 1 jam, katalis asam sulfat (98%) sebesar 0,5% volume minyak, dan metanol sebesar 20% volume minyak. Reaksi transesterifikasi dilaksanakan selama 1 jam, serta perbandingan volume minyak dan metanol sebesar 4:1. Analisis kadar metil ester yang terbentuk, jumlah komponen, dan komposisinya yang terdapat pada senyawa hasil dilakukan dengan menggunakan alat GC. Kondisi operasi terbaik pada transesterifikasi minyak biji karet menjadi metil ester adalah pada katalis KOH 1% dan suhu 60 0C. Berdasarkan uji sifat-sifat fisis, metil ester yang dihasilkan belum semua memenuhi mutu sifat fisis biodiesel yang disyaratkan. The most widely used fuel is diesel fuel or fatty acid methyl ester (FAME). Biodiesel is derived from vegetable oil that can be renewed, can be produced periodically, and easy to obtain. In this research, the rubber seed was used for synthesizing the FAME. The main process in the production of FAME is transesterification. This study examined the optimum result from variations of the concentration of KOH catalyst and the reaction temperature on the transesterification reaction. Preparation of the rubber seed oil using granular activated charcoal was followed by degumming. Esterification reaction was carried out at 50 oC for 1 h with the sulfuric acid catalyst of 0.5% by volume of oil and methanol of 20% by the volume of oil. Transesterification reaction was carried out for 1 hour with the oil and methanol volume ratio of 4:1. The concentration of methyl ester, the number of components, and the composition of the contained compounds in the resulted products were analyzed using a GC. The best operating conditions on the transesterification of rubber seed oil into methyl ester was by using 1% KOH catalyst at temperature of 60 0C. Based on the analysis of the physical properties, the resulted methyl esters need to be improved further to meet the quality requirements of the physical properties of biodiesel.
PEMANFAATAN KULIT BUAH NAGA (Dragon Fruit) SEBAGAI PEWARNA ALAMI MAKANAN PENGGANTI PEWARNA SINTETIS Handayani, Prima Astuti; Rahmawati, Asri
Jurnal Bahan Alam Terbarukan Vol 1, No 2 (2012): December 2012
Publisher : Semarang State University

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.15294/jbat.v1i2.2545

Abstract

Kulit buah naga merupakan limbah hasil pertanian yang mengandung zat warna alami antosianin cukup tinggi. Antosianin merupakan zat warna yang berperan memberikan warna merah yang berpotensi menjadi pewarna alami untuk pangan dan dapat dijadikan alternatif pengganti pewarna sintetis yang lebih aman bagi kesehatan. Pengambilan zat warna antosianin dilakukan dengan metode ekstraksi. Pelarut yang digunakan adalah aquades. Variabel penelitian antara lain varietas buah naga, konsentrasi asam sitrat dalam pelarut, suhu ekstraksi, dan waktu ekstraksi. Potongan kulit buah naga diekstraksi dengan pelarut aquades dan asam sitrat dengan perbandingan tertentu, pada suhu ekstraksi 25-800C dan waktu ekstraksi 0,5-3 jam. Analisis kadar antosianin dilakukan dengan analisa antosianin metode Glusti dan Wrolstad. Hasil percobaan diperoleh bahwa varietas buah naga daging merah menghasilkan kadar antosianin terbesar 22,59335 ppm. Selain itu kadar antosianin terbesar diperoleh pada variasi pelarut aquades:asam sitrat (5:1) 26,4587 ppm, variasi pada suhu kamar menghasilkan 21,5028 ppm dan waktu pengadukan  3 jam menghasilkan 23,3027 ppm. Pewarna alami ini telah diaplikasikan pada makanan dan diujikan pada tikus putih, hasil uji coba menunjukkan pewarna buah naga dapat dipakai sebagai pewarna alami makanan. Dragon fruit peel is agricultural waste which contains quite high natural pigments of anthocyanins. Anthocyanin is a dye that potentially provides a red natural colorant for food and alternatively used as synthetic dye which is safe for health. In this study, the process of taking anthocyanin was conducted using extraction method. The solvent used was distilled water. The variables observed in the research include dragon fruit varieties, the concentration of citric acid in the solvent, extraction temperature, and extraction time. The dragon fruit peel was extracted using solvents of distilled water and citric acid at a certain ratio, at extraction temperature varies from 25-80oC with the extraction time varies from 0.5 to 3 hours. The analysis of anthocyanin concentration was conducted by using Glusti and Wrolstad method. The experimental result shows the red dragon fruit varieties produced the greatest concentration of anthocyanin (22.59335 ppm). Moreover, the result shows the greatest concentration of anthocyanin obtained from the following variations, i.e. the 5:1 solvent ratio of distilled water : citric acid produces 26.4587ppm,  the extraction at room temperature produced 21.5028 ppm, and the extraction for 3 hours stirring produced 23.3027 ppm. The extracted dragon fruit dye has been applied for food and tested on white mice; the test result shows the dye can be used as a natural food dye.
PENGAMBILAN MINYAK ATSIRI BUNGA CENGKEH (Clove Oil) MENGGUNAKAN PELARUT n-HEKSANA DAN BENZENA Hadi, Saiful
Jurnal Bahan Alam Terbarukan Vol 1, No 2 (2012): December 2012
Publisher : Semarang State University

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.15294/jbat.v1i2.2546

Abstract

Minyak cengkeh merupakan salah satu jenis minyak atsiri yang dapat diperoleh dari bunga, tangkai atau gagang bunga dan daun cengkeh. Kandungan minyak atsiri bunga cengkeh mencapai 21,3% dengan kadar eugenol antara 78-95%, dari tangkai atau gagang bunga mencapai 6% dengan kadar eugenol antara 89-95%, dan dari daun cengkeh mencapai 2-3% dengan kadar eugenol antara 80-85%. Kandungan terbesar minyak cengkeh adalah eugenol, yang bermanfaat dalam pembuatan vanilin, eugenil metil eter, eugenil asetat, dll. Ektraksi dengan pelarut adalah salah satu metode yang digunakan untuk ekstraksi minyak atsiri bunga cengkeh. Pelarut yang digunakan dalam proses ekstraksi adalah n-heksana dan benzena. Penelitian ini bertujuan untuk mengetahui rendemen yang diperoleh dengan menggunakan pelarut n-heksana dan benzene serta mengetahui komponen-komponen minyak cengkeh yang terambil dengan pelarut n-heksana dan benzena. Tahapan penelitian diawali dengan mengeringkan bunga cengkeh dengan dijemur di bawah sinar matahari selama 1 minggu. Setelah itu, bu-nga cengkeh kering ditumbuk sampai halus. Bunga cengkeh diekstraksi menggunakan soxhlet dengan 100 mL pelarut pada suhu didihnya selama 15 siklus (+ 80 menit). Dari percobaan yang telah dilakukan dihasilkan rendemen ekstrak bunga cengkeh dengan pelarut n-heksana sebesar 17,61% dan kadar eugenol 65,02%. Sedangkan dengan pelarut benzene, rendemen ekstraks bunga cengkeh sebesar 18,90% dan kadar eugenol 8,81%. Oleh karena itu, ekstraksi minyak atsiri bunga cengkeh dengan menggunakan pelarut n-heksana relatif lebih baik karena memberikan kadar eugenol lebih besar daripada pelarut benzena. Clove oil is one of the essential oils obtained from the cloves, stalks or clove steam and clove leaf. The clove contains 21.3% of the essential oils with the eugenol content of 78-95%, the clove stalk contains 6% of the essential oils with the eugenol content of 89-95%, and the clove leaf contains 2-3% of the essential oils with the eugenol content of 80-85%. The clove oil is mostly composed of eugenol, which is useful in the production of vanillin, eugenil methyl ether, eugenil acetate, etc. The extraction using solvent is one of the methods used for the extraction of essential oils of clove flower. The solvents used for the extraction process were n-hexane and benzene. This study aimed to determine the yield of the essential oil obtained from the extraction using n-hexane and benzene as well as to know its components. The first step of the process was initiated by drying the cloves in the sun for a week. Then the dried cloves were finely ground. Clove was extracted using a Soxhlet with 100 mL of solvent at its boiling temperature for 15 cycles (+ 80 minutes). The obtained yield of the extraction process using n-hexane was 17.61% with the eugenol content of 65.02%. While the obtained yield from the extraction process using benzene solvent was 18.90% with the eugenol content of 8.81%. Therefore, the clove essential oil extraction using n-hexane solvent is relatively better than using benzene because it produces greater eugenol content.
OPTIMASI YIELD ETIL P METOKSISINAMAT PADA EKSTRAKSI OLEORESIN KENCUR (Kaempferia galanga) MENGGUNAKAN PELARUT ETANOL Setyawan, Eko; Putratama, Pandhu; Ajeng, Asriningtyas; Pita Rengga, Wara Dyah
Jurnal Bahan Alam Terbarukan Vol 1, No 2 (2012): December 2012
Publisher : Semarang State University

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.15294/jbat.v1i2.2547

Abstract

Kencur (Kaempferia galanga L.) banyak digunakan sebagai bahan baku obat tradisional (jamu), fitofarmaka, industri kosmetika, industri makanan, dan industri insektisida. Minyak atsiri rimpang kencur mengandung etil sinnamat dan metil p-metoksi sinamat (EPMS). Ekstraksi oleoresin kencur dilakukan dengan etanol sebagai pelarut. Optimasi yield EPMS diteliti terhadap perbandingan massa serbuk kering kencur dan etanol dan waktu ekstraksi. Perbandingan kencur : etanol yang digunakan adalah 1 : 2, 1 : 3, dan 1 : 4. Waktu operasi yang digunakan adalah 2 s.d 5 jam. Tahapan proses ekstraksi oleoresin kencur adalah preparasi bahan, ekstraksi, evaporasi dan pemurnian. Oleoresin hasil ekstraksi dianalisis dengan uji GC-MS untuk mengetahui kandungan EPMS dan kandungan minyak atsiri lain dalam oleoresin kencur. Oleoresin hasil ekstraksi berwarna coklat tua dengan yield antara 6-8%. Kandungan EPMS dalam oleoresin bervariasi antara 67,77 hingga 87,57%. Massa oleoresin optimal hasil ekstraksi adalah 6,09 gram pada perbandingan kencur dan etanol 1:4 selama 4 jam. Pendekatan persamaan hasil ekperimen ekstraksi kencur dan etanol menghasilkan titik optimal EPMS pada waktu ekstraksi 3,62 dengan massa EPMS 6,04 gram Lesser galangal (Kaempferia galanga L.) is widely used as a traditional medicine (herbal medicine), fitofarmaka, cosmetics industry, food industry, and insecticide industry. The essential oils in the Lesser galangal contain ethyl sinnamat and methyl p-methoxy cinnamic (EPMS). The oleoresin extraction of Lesser galangal was performed using ethanol as a solvent. Optimization of the EPMS yield was investigated to dry powder mass ratio of Lesser galangal and ethanol as well as the extraction time. The ratio of Lesser galangal : ethanol was  varied from 1: 2, 1: 3 and 1: 4. The chosen operating time were 2 to 5 hours. The procedure of the oleoresin extraction process of Lesser galangal includes the preparation of materials, extraction, evaporation and purification. The extracted oleoresin was analyzed by GC-MS to determine the content of Ethyl P-methoxycinnamate (EPMS) and other volatile oil content in the oleoresin of Lesser galangal. The extracted oleoresin color was light brown to dark brown with the yield of between 6.31 to 8.3%. The EPMS content of the oleoresin varies between 67.77 to 87.57%. The optimum mass of the extracted oleoresin was 6.09 gram for 1:4 ratio of Lesser galangal : ethanol and 4 hours of the extraction time. The equation approach of the experimental results of Lesser galangal and ethanol produced the EPMS optimum point at the extraction time of 3.62 hours and EPMS mass of 6.04 grams.

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