BibTex Citation Data :
@article{Reaktor6092, author = {Deddy Irawan and Zainal Arifin}, title = {SINTESA GULA DARI SAMPAH ORGANIK DENGAN PROSES HIDROLISIS MENGGUNAKAN KATALIS ASAM}, journal = {Reaktor}, volume = {14}, number = {2}, year = {2012}, keywords = {asam klorida; hidrolisis; sampah organik; kadar gula; yield}, abstract = { SYNTHESIS OF SUGAR FROM ORGANIC WASTES VIA ACID CATALYST HYDROLYSIS. Hydrolysis process is an important step from every process to produce biofuel with organic wastes as raw material. Hydrolysis process with chemical uses hydrochloride acid as catalyst in which will transform holocellulose to glucose. Raw material of 100 grams is put into hydrolysis reactor with batch system equipped with pressure control and ratio hydrochloride of 1 : 6 w/v. The variables studied were temperature of 110-140oC, HCl concentration of 0.5-1%, time of hydrolysis of 15-60 minutes. The sugar concentration was taken and then be analyzed by Nelson-Somogy method. The hydrolysis, which was carried out with the temperature of 120oC, time of 30 minutes, HCl concentration of 0.75%, and the pressure of 6 bar, produced sugar reduction of 27.3 mg/mL and yield of 15.07%. Proses hidrolisis merupakan satu tahap penting dari rangkaian tahapan proses produksi bahan bakar nabati menggunakan bahan baku sampah organik. Proses hidrolisis secara kimiawi menggunakan HCl sebagai katalis akan mengubah holoselulosa yang terdapat pada sampah organik menjadi gula. Gula yang dihasilkan inilah yang dapat difermentasi menjadi bahan bakar nabati. Bahan baku sebanyak 100 g dimasukkan dalam reaktor hidrolisis sistem batch yang dilengkapi dengan pengukur tekanan dan ditambahkan larutan HCl pada perbandingan 1:6 b/v. Hidrolisis dilakukan dengan memvariasikan suhu operasi 100-140oC, waktu proses 15-60 menit, serta konsentrasi HCl 0,5- 1%. Hidrolisat yang dihasilkan dianalisis kadar gula menggunakan metode Nelson-somogy. Hasil hidrolisis yang dilakukan pada suhu 120oC selama 30 menit serta konsentrasi HCl 0,75% dan tekanan terukur 6 bar menghasilkan gula 27,30 mg/mL dan yield gula sebesar 15,07%. }, issn = {2407-5973}, pages = {118--122} doi = {10.14710/reaktor.14.2.118-122}, url = {https://ejournal.undip.ac.id/index.php/reaktor/article/view/6092} }
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SYNTHESIS OF SUGAR FROM ORGANIC WASTES VIA ACID CATALYSTHYDROLYSIS. Hydrolysis process is an important step from every process to produce biofuel withorganic wastes as raw material. Hydrolysis process with chemical uses hydrochloride acid as catalystin which will transform holocellulose to glucose. Raw material of 100 grams is put into hydrolysisreactor with batch system equipped with pressure control and ratio hydrochloride of 1 : 6 w/v. Thevariables studied were temperature of 110-140oC, HCl concentration of 0.5-1%, time of hydrolysis of15-60 minutes. The sugar concentration was taken and then be analyzed by Nelson-Somogy method.The hydrolysis, which was carried out with the temperature of 120oC, time of 30 minutes, HClconcentration of 0.75%, and the pressure of 6 bar, produced sugar reduction of 27.3 mg/mL and yieldof 15.07%.
Proses hidrolisis merupakan satu tahap penting dari rangkaian tahapan proses produksi bahan bakarnabati menggunakan bahan baku sampah organik. Proses hidrolisis secara kimiawi menggunakanHCl sebagai katalis akan mengubah holoselulosa yang terdapat pada sampah organik menjadi gula.Gula yang dihasilkan inilah yang dapat difermentasi menjadi bahan bakar nabati. Bahanbaku sebanyak 100 g dimasukkan dalam reaktor hidrolisis sistem batch yang dilengkapi denganpengukur tekanan dan ditambahkan larutan HCl pada perbandingan 1:6 b/v. Hidrolisis dilakukandengan memvariasikan suhu operasi 100-140oC, waktu proses 15-60 menit, serta konsentrasi HCl 0,5-1%. Hidrolisat yang dihasilkan dianalisis kadar gula menggunakan metode Nelson-somogy. Hasilhidrolisis yang dilakukan pada suhu 120oC selama 30 menit serta konsentrasi HCl 0,75% dan tekananterukur 6 bar menghasilkan gula 27,30 mg/mL dan yield gula sebesar 15,07%.
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JURNAL REAKTOR (p-ISSN: 0852-0798; e-ISSN: 2407-5973)
Published by Departement of Chemical Engineering, Diponegoro University