Garuda - Garba Rujukan Digital

All

Reaktor

reaktor
Website

Published by Universitas Diponegoro

ISSN : 08520798 EISSN : 24075973 DOI : https://doi.org/10.14710/reaktor.xx.x.xx-xx

Chemical Engineering, Chemistry & Bioengineering Control & Systems Engineering Energy Materials Science & Nanotechnology

Reaktor invites contributions of original and novel fundamental research. Reaktor publishes scientific study/ research papers, industrial problem solving related to Chemical Engineering field as well as review papers. The journal presents paper dealing with the topic related to Chemical Engineering including: Transport Phenomena and Chemical Engineering Operating Unit Chemical Reaction Technique, Chemical Kinetics, and Catalysis Designing, Modeling, and Process Optimization Energy and Conversion Technology Thermodynamics Process System Engineering and products Particulate and emulsion technologies Membrane Technology Material Development Food Technology and Bioprocess Waste Treatment Technology

Arjuna Subject : Teknik (semua kategori) - Teknik (Lain-Lain)

Articles 530 Documents

24 25 26 27 28

Optimasi Adsorpsi Ion Mg2+ pada Fixed Bed Column dengan Menggunakan Response Surface Methodology Novi Sylvia; Meriatna Meriatna; Fikri Hasfita; Lukman Hakim
Reaktor Volume 17 No. 3 September 2017
Publisher : Dept. of Chemical Engineering, Diponegoro University

Abstract OPTIMIZATION ADSORPTION OF Mg2+ ION ON FIXED BED COLUMN USING RESPONSE SURFACE METHODOLOGY. Modeling of the adsorption process is used to establish the mathematical relationship between the interacting process variables and process optimization. This is important to determine the factor values that produce a maximum response. Adsorption of Mg from groundwater was optimized using response surface methodology based on Box-Behnken design was used to analyze adsorption data. The process was investigated by continuous experiments. Variables included in the process were: bed depths (7.5, 10, and 12.5 cm), time (20, 40, and 60 min), and flow rate (6, 10, and 14 L/min). Regression analysis was used to analyze the developed models. The outcome of this research showed that 72.784% of the variability in removal efficiency is attributed to the three process variables considered, that is, bed depths, time, and flow rate. Optimization tests showed that the optimum operating conditions for the adsorption process occurred at a bed depth of 11.37 cm, time of 55.53 min and flow rate of 6 L/min. Keywords: adsorption; Box-Behnken design; magnesium (Mg2+); optimization AbstrakPemodelan dari proses adsorpsi digunakan untuk menentukan hubungan matematis antara variabel proses interaksi dan proses optimasi. Hal ini penting untuk menentukan nilai faktor yang menghasilkan respon maksimum. Adsorpsi magnesium (Mg2+) dari air tanah dioptimalkan menggunakan metodologi respon permukaan model Desain Box-Behnken yang digunakan untuk menganalisis data adsorpsi. Percobaan dilakukan secara kontinyu. Variabel yang termasuk dalam proses tersebut adalah: tinggi unggun (7,5, 10 dan 12,5 cm), waktu kontak (20, 40, dan 60 menit), dan laju alir (6, 10, dan 14 L/menit). Analisis regresi digunakan untuk menganalisis model yang dikembangkan. Hasil penelitian menunjukkan bahwa 72,784% efisiensi penyisihan Mg2+ ditentukan oleh tiga variabel proses, yaitu tinggi unggun, waktu kontak, dan laju alir. Hasil optimasi menunjukkan bahwa kondisi operasi optimum untuk proses adsorpsi terjadi pada tinggi unggun 11,37 cm, waktu kontak 55,53 menit dan laju alir 6 L/menit. Kata kunci: adsorpsi; Box-Behnken desain; magnesium (Mg2+); optimasi

Synthesis of Matrix Si-K-HAs Gel from Geothermal Sludge and Peat Srie Muljani; Bambang Wahyudi Wahyudi; S Suprihatin; Ketut Sumada
Reaktor Volume 18 No. 2 June 2018
Publisher : Dept. of Chemical Engineering, Diponegoro University

The synthesis of matrix silica-potassium-humic acid gel (Si-K-HAs) has been performed successfully by gradual extraction and acidification method. The extraction was carried out in two stages: 1) extraction of humic substances from peat prepared by potassium hydroxide to produce potassium humate (K-HAS) solution, 2) extraction silica from geothermal sludge using K-HAs solution to produce Si-K-HAs solution. Acidification of Si-K-HAs solution prepared by citric acid (1-3N) to produce matrix gel of Si-K-HAs. The Si-K-HAs matrix gel products are characterized by Fourier Transform InfraRed (FTIR), X-ray fluroscence (XRF), and Brunauer–Emmett–Teller (BET) analysis. The acidification process was carried out in neutral to acid (pH 3-7) conditions and the results showed that at neutral pH no Si-K-HAs gel formed. IR spectra confirmed the presence of humic acid in the gel product, whereas XRF analysis confirmed the presence of potassium (K) and silica (SiO2) in the gel product. The molar ratio of SiO2:K2O in the product is 0.9 - 0.3 in the pH range of 3-5. Si-K-HAs powder can be used as soil fertilizer especially for soils that lack silica, humic, and potassium nutrients or for future application development. Keywords: gradual extraction; geothermal sludge; matrix gel; humic substance

FORTIFIKASI INORGANIK ZINK PADA TEPUNG UBI JALAR UNGU SEBAGAI BAHAN BAKU BUBUR BAYI INSTAN Noer Abyor Handayani; Herry Santosa; Bunga Profegama; Aditya Yuna
Reaktor Volume 15, No.2, OKTOBER 2014
Publisher : Dept. of Chemical Engineering, Diponegoro University

Fortifikasi zink pada bubur instan bayi berbahan dasar tepung ubi jalar ungu diharapkan mampu memberikan inovasi produk yang dapat mengatasi permasalahan defisiensi zink pada balita. Penelitian ini bertujuan untuk mengkaji pengaruh konsentrasi fortifikan inorganic (ZnO) terhadap sifat fisik (penampilan fisik, densitas kamba, dan daya rehidrasi) dari produk instan. Bubur bayi instan yang dihasilkan melalui tahap pembuatan tepung, fortifikasi zink, dan tahap pembuatan bubur bayi instan. Bubur bayi instan tanpa fortifikan digunakan sebagai variabel kontrol. Hasil penelitian menunjukkan bahwa konsentrasi zink pada bubur bayi instan berhasil meningkat, namun tingkat efektifitas dari fortifikasi sangat rendah. Fortifikasi inorganik zink dapat menurunkan 27,6% nilai densitas kamba dan mampu menaikkan 15% daya rehidrasi dibandingkan dengan bubur bayi instan tanpa fortifikan. Terdapat perubahan warna dari bubur bayi instan setelah mengalami proses fortifikasi zink.

Study Of Solid Planar Source For Phosphorus Diffution Process On Semiconductor Devices Fabrication S. Widodo
Reaktor Volume 6 No. 1 Juni 2002
Publisher : Dept. of Chemical Engineering, Diponegoro University

The sourcing lifetimes, microstructural staility, and diffution performance of a new solid planar phosphorus source for silicon doping were investigated in the temperature range 900-1000 0C. The source wafers were highly porous ceramic wafers containing 25 weight percentage (w/o) SiP2O7 as the “active” component in an inert refractory binder matrix. The microstructural stability and thermografimetric analysis (TGA) result indicated the structural integrity and sourcing ability of this materials at temperatures of at least 1050 0C. Theoretical lifetimesof 260 and 3400 hr at 1000 and 900 0C, respectively, have been predicted from the TGA results. Experimental data relating sheet resistance, junction depth, and diffution coefficient for silicon wafers doped using these source wafers are presented. Special material handling procedure are also described. Keywords : diffution process, solid phosphorus source, SiP2O5, semiconductor devices

KINERJA KATALIS Ag/Al2O3 UNTUK REDUKSI NOx Rakhman Sarwono; Blasius Hangkoso Adi Wicaksono
Reaktor Volume 12, Nomor 4, Desember 2009
Publisher : Dept. of Chemical Engineering, Diponegoro University

NOx merupakan hasil samping dari suatu reaksi pembakaran. NOx merupakan gas yang beracun sangat berbahaya terhadap kesehatan manusia dan hewan bila terhirup pada waktu bernafas. Untuk mengurangi kadar NOx pada gas buang, banyak penelitian diarahkan pada reduksi NOx dengan katalis secara selektif dengan hidrokarbon dan oksigen berlebihan. Katalis yang digunakan adalah katalis alumina (Al2O3) yang didapat dari katalis komersial (AlO1-7) dan katalis hasil sintesa (ALOA). Katalis Ag/Al2O3 didapat dengan memasukkan logam Ag ke dalam alumina (Al2O3) dengan cara impregnasi dengan larutan perak nitrat. Katalis diuji aktifitasnya pada reaktor fixed bed yang diluarnya terdapat pemanas yang bisa diatur suhunya. Reaktan seperti gas NO, C2H4 dan oksigen dimasukkan kedalam reaktor dengan laju yang ditentukan. Hasil reaksi dianalisa dengan gas chromatography dan dicatat pada recorder, selanjutnya bisa ditentukan kuantitas dan prosentase konversinya. Katalis alumina ALOA mempunyai kemampuan mereduksi NO dengan konversi sekitar 40-45% gas NO menjadi N2. Loading logam perak (Ag) kedalam Al2O3 sebesar 2-3% berat menambah daya reduksi NO menjadi sekitar 45-50% pada suhu 500oC. Pada umpan NO + C2H4 + O2 reaksi reduksi terjadi pada suhu 300oC, sedangkan pada umpan NO + C2H4 (tanpa oksigen) reaksi reduksi baru terjadi pada suhu 450oC, dengan demikian adanya oksigen sangat berperan dalam proses reduksi NOx. Reaksi peruraian C2H4 menjadi COx berkebalikan dengan kinerja katalis pada proses reduksi NOx

Growth Mechanism and Characterization of PbTe0.5Se0.5 Thin Films Used by Closed-Space Vapor Transport in a Vertical Reactor Yanuar Hamzah; Jimmy Copriady; Ariswan Ariswan
Reaktor Volume 19 No. 1 March 2019
Publisher : Dept. of Chemical Engineering, Diponegoro University

A simple method for growing thin film of semiconductor material PbTe0.5Se0.50 has been designed using the vapor transport (CSVT) method in a vertical reactor. The objectivity of this method is to study thin film growth formation due to chemical reactions during the deposition process in the reactor. In this study will describe some formations the vapor transport mechanism of PbTe0.5Se0.50 semiconductor material using iodine gas (I2) to accelerate the etching reaction on the substrate surface. Next, we will describe how the mechanism of the reaction in the reactor zone for growing thin films on the substrate. The thin films were characterized by structural, morphology properties and its composition. The film structure is a cubic structure with the maximum diffraction intensity at peak (222). The surface morphology of the thin film has a microcubes shape with a grain size~10 to 20 mm. Keywords: etching reaction; micro-cube; PbTe0.5Se0.50; close-spaced vapor transport

HIDROLISIS ENZIMATIK KITOSAN DENGAN KOMBINASI ENZIM ENDO-GLUCANASE DAN CELLOBIOHYDROLASE Nur Rokhati; Bambang Pramudono; Titik Istirokhatun; Mohammad Sulchan; Dyah Ayu Kresnianingrum; Luthfi Kurnia Dewi
Reaktor Volume 15 No.4 Oktober 2015
Publisher : Dept. of Chemical Engineering, Diponegoro University

Abstract CHITOSAN ENZYMATIC HYDROLYSIS USING A COMBINATION OF ENDO-GLUCANASE AND CELLOBIOHYDROLASE. Chitosan is very promising in various fields including medicine, pharmacology, and the food industry. However, the application of this polysaccharide is limited by its high molecular weight resulting in its low solubility in aqueous media. In this respect, the chitosan with shorter chain length, display a reduced viscosity and are soluble in aqueous media at pH values close to neutrality. The aim of this study is the hydrolysis of chitosan to obtain a low molecular weight chitosan using enzymes endo-glucanase and cellobiohydrolase. The hydrolysis of chitosan was carried out under a temperature of 40° C and pH 5. Chitosan degradation was monitored by the analysis of reducing sugars and viscosity, whereas the chemical characterization of chitosan is done by using test FTIR (infrared spectroscopy). The results showed that enzyme treatment resulted in a substantial loss in viscosity of the chitosan solution shows depolymerization. Depolymerization using endo-glucanase took place very quickly during the initial 15 minutes. The rate of viscosity decrease on chitosan degradation using cellobiohydrolase is lower than using endo-glucanase. When the reaction time was 4 h, the lowest viscosity is showed by cellobiohydrolase, and the highest solubility is showed by combination of endo-glucanase and cellobiohydrolase. Keywords: endo-glucanase; cellobiohydrolase; chitosan; hydrolysis Abstrak Kitosan dapat dimanfaatkan di berbagai bidang seperti kedokteran, farmasi dan industri makanan. Aplikasi kitosan sering dibatasi oleh berat molekul kitosan yang tinggi sehingga viskositasnya tinggi dan kelarutannya rendah. Kitosan dengan rantai polimer pendek, akan mempunyai viskositas rendah, dan mudah larut pada larutan/air dengan pH mendekati netral. Penelitian ini bertujuan untuk menghidrolisis kitosan secara enzimatis menggunakan enzim endo-glucanase dan cellobiohydrolase. Hidrolisis kitosan dilakukan pada suhu 40 °C dan pH 5. Degradasi kitosan dipantau melalui analisa gula reduksi dan viskositas, sedangkan karakterisasi kimia kitosan dilakukan dengan menggunakan uji FTIR (infra red spectroscopy). Hasil penelitian menunjukkan bahwa hidrolisis enzimatis kitosan dapat menyebabkan terjadinya penurunan berat molekul yang ditandai dengan adanya penurunan viscositas larutan kitosan. Pada 15 menit awal hidrolisis terjadi penurunan viskositas yang sangat besar. Laju penurunan viskositas enzim cellobiohydrolase lebih rendah dibanding dengan enzime endo-glucanase. Setelah waktu reaksi 4 jam, viskositas terendah diperoleh pada enzime cellobiohydrolase, sedangkan kelarutan tertinggi diperoleh pada kombinasi enzime endo-glucanase dan cellobiohydrolase. Kata kunci: endo-glucanase; cellobiohydrolase; kitosan; hidrolisis

Pengaruh Loading Metal Dalam Katalis Cu-Zn-Al/γ-Al2O3 Terhadap Konversi Pada Hidrogenasi Karbon Monoksida Menjadi Dimethyl Ether S. Lourentius
Reaktor Volume 09 No.1 Juni 2005
Publisher : Dept. of Chemical Engineering, Diponegoro University

Penelitian ini bertujuan untuk mempelajari unjuk kerja dua katalis Cu-Zn-Al/γ-Al2O3 untuk hidrogenasi karbonmonoksida menjadi DME. Metal-metal dengan “coprecipitating sedimentation method”, dilanjutkan penyaringan. Endapannya dikeringkan pada 120 0C, kemudian dikalsinasi pada 350 0C dan direduksi dengan hydrogen pada 230 0C. Selanjutnya katalis dianalisis dengan instrument X-Ray Diffraction (XRD) dan inductively Coupled Plasma Spectrometer (ICPS). Katalis Cu-Zn-Al/γ-Al2O3 memiliki loading Cu = 8,11%, Zn = 1,98%, dan Al = 0,99%, sementara Cu-Zn-Al/γ-Al2O3 memiliki loading 11% Cu, 1,74% Zn, dan 2,0% Al. Hidrogenasi karbon monoksida dilaksanakan dalam reaktor unggun tetap dengan diameter dalam 10 mm dan panjang 300 mm. kondisi proses : perbandingan mol hydrogen terhadap karbon monoksida (CO) =2/1, kecepatan aliran produk 88-109 ml/menit., suhu 240-300 0C, berat katalis 3 gram dan tekanan 4 MPa. Komposisi umpan dan produk reaksi dianalisis dengan Gas Chromatography. Disimpulakan bahwa kedua katalis mampu mengarahkan reaksi hidrigenasi karbon monoksida menjadi DME dan katalis ( dengan loading lebih besar yaitu) Cu-Zn-Al/γ-Al2O3 dengan loading Cu= 11%, Zn=1,74% dan Al=2% memiliki unjuk kerja yang lebih baik. Kondisi proses yang lebih baik dicapai pada suhu reaktor =260 0C, kecepatan produk 88 ml/menit dan tekanan 40 bar, dengan konversi CO= 0,926 dan selektivitas DME= 0,940.Kata kunci : CO, DME, hidogenasi, katalis, loading

PENGARUH PROSES PENGERINGAN RIMPANG TEMULAWAK (Curcuma xanthorriza ROXB) TERHADAP KANDUNGAN DAN KOMPOSISI KURKUMINOID Bambang Cahyono; Muhammad Diah Khoirul Huda; Leenawaty Limantara
Reaktor Volume 13, Nomor 3, Juni 2011
Publisher : Dept. of Chemical Engineering, Diponegoro University

EFFECT OF DRYING PROCESSES ON CURCUMINOID CONTENT AND COMPOSITION OF TEMULAWAK (Curcuma xanthorriza ROXB) RHIZOMES. Curcuminoid a yellow coloring agent of turmeric is known to have many benefits in food and medicinal industries. This compound can be isolated by simple extraction from fresh rhizome or symplicia. The research of comparing qualitative and quantitative of curcuminoid in different drying process has not yet been published. Drying methods used in this research were done in an oven at 60°C and under 30-watt electrical lamp at ±30°C. Each method was carried out in time variation of 1, 3, and 5 days. Extraction of curcuminoid was done using ethanol 95% followed by fat reduction process using petroleum ether. Curcuminoid analysis was done by TLC, UV-Visible spectrophotometer and HPLC. The result showed that the water content of all samples was approximately 4.06%-7.76%. TLC analysis identified the presence of two dominant components in the curcuminoid with the Rf values of 0.37 and 0.15. The UV-Visible spectra indicated that simplicia would give more result in curcuminoid than fresh rhizome. There were 4 substances detected in HPLC analysis, they were curcumin 61-67%, demetoxycurcumin 22-26%, bisdemetoxycurcumin 1-3%, and curcuminoid derivative 10-11%. In addition, drying on oven resulted brighter and crispier simplicia than drying under lamp. Kurkuminoid yang merupakan zat utama yang berwarna kuning dalam temulawak telah diketahui memiliki banyak manfaat di bidang kesehatan dan makanan. Bahan ini dapat diisolasi dari bahan segar atau simplisia kering melalui ekstraksi. Riset yang mencoba membandingkan kualitas dan kuantitas kurkuminoid akibat perlakuan panas pada saat pembuatan simplisia hingga sekarang belum pernah dilakukan. Penelitian dimulai dengan pengeringan temulawak segar setelah dirajang pada oven suhu 60°C dan pada pengeringan lampu listrik 30 watt pada suhu ± 30°C. Masing-masing metode dilakukan variasi lama pengeringan 1, 3, 5 hari. Ekstraksi kurkuminoid dilakukan menggunakan etanol 95% dan defatisasi menggunakan petroleum eter, sedangkan analisis kualtatif dan kuantitatif kurkuminoid direalisasikan dengan KLT, spektrofotometer UV-Tampak dan KCKT. Hasil penelitian menunjukkan bahwa kandungan air semua sampel sekitar 4,06%-7,76%. Analisis KLT mengidentifikasi adanya dua komponen dominan dalam kurkuminoid dengan nilai Rf 0,37 dan 0,15. Hasil analisis Spektrofotometri UV-tampak memberikan keenderungan bahwa kurkuminoid dari sampel kering lebih mudah terekstraksi daripada sampel basah. Kromatogram HPLC dapat mendeteksi adanya 4 senyawa yaitu kurkumin 61-67%, demetoksikurkumin 22-26%, bisdemetoksikurkumin 1-3%, dan turunan kurkuminoid 10-11%, urutan prosentase masing-masing komponen tetap sama selama proses pengeringan. Hasil penelitian ini juga telah dapat menunjukkan bahwa perbedaan kondisi operasi pengeringan sangat mempenaruhi penampakan simplisia yang dihasilkan, pengeringan oven memiliki warna lebih cerah dan lebih meremah daripada pengeringan lampu.

APLICATION OF CATALYTIC DIELECTRIC BARRIER DISCHARGE PLASMA REACTOR FOR CO-GENERATION OF SYNTHESIS GAS AND HIGHER HYDROCARBONS istadi istadi; Amin N.A.S. Amin
Reaktor Volume 10 No. 1 Juni 2006
Publisher : Dept. of Chemical Engineering, Diponegoro University

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.14710/reaktor.10.1.17-23

This paper deals with potential application of hybrid catalytic DBD plasma reaktor for the co-generation of C2 hydrocarbons and synthesis gases from methane and carbon dioxide. The synergism of the catalyst, feed ratio and the plasma discharge affect the products, distribution, particularly C2 hydrocarbons selectivity . The CH,CO2 feed ratio total feed flow rate, and the discharge voltage incatalytic BDB plasma reactor systems shoe significant effects on the reactor performances. However increasing the reactor wall temperature has no apparent influence on the selectivity to C2 hydrocarbons and hydrogen within the investigated range. The hybrid catalytic DBD plasma rectorwas more suitable for CO2OCM process than the conventional catalytic reactor over CaO-MnO/CeO2catalyst

Page 26 of 53 | Total Record : 530

24 25 26 27 28

Filter by Year

1999 2025

Filter By Issues

All Issue Volume 25 No.2 August 2025 Volume 25 No.1 April 2025 Volume 24 No.3 December 2024 Volume 24 No.2 August 2024 Volume 24 No.1 April 2024 Volume 23 No.3 December 2023 Volume 23 No.2 August 2023 Volume 23 No.1 April 2023 Volume 22 No. 3 December 2022 Volume 22 No.2 August 2022 Volume 22 No. 1 April 2022 Volume 21 No.4 December 2021 Volume 21 No. 3 September 2021 Volume 21 No. 2 June 2021 Volume 21 No. 1 March 2021 Volume 20 No.4 December 2020 Volume 20 No.3 September 2020 Volume 20 No.2 June 2020 Volume 20 No.1 March 2020 Volume 19 No. 4 December 2019 Volume 19 No. 3 September 2019 Volume 19 No. 2 June 2019 Volume 19 No. 1 March 2019 Volume 18 No. 4 December 2018 Volume 18 No. 3 September 2018 Volume 18 No. 2 June 2018 Volume 18 No. 1 March 2018 Volume 17 No. 4 Desember 2017 Volume 17 No. 3 September 2017 Volume 17 No. 2 Juni 2017 Volume 17 No.1 Maret 2017 Volume 16 No.4 Desember 2016 Volume 16 No.3 September 2016 Volume 16 No. 2 Juni 2016 Volume 16 No.1 Maret 2016 Volume 15 No.4 Oktober 2015 Volume 15 No.3 April 2015 Volume 15, No.2, OKTOBER 2014 Volume 15, No.1, APRIL 2014 Volume 14, No. 4, OKTOBER 2013 Volume 14, No. 3, APRIL 2013 Volume 14, Nomor 2, Oktober 2012 Volume 14, Nomor 1, April 2012 Volume 13, Nomor 4, Desember 2011 Volume 13, Nomor 3, Juni 2011 Volume 13, Nomor 2, Desember 2010 Volume 13, Nomor 1, Juni 2010 Volume 12, Nomor 4, Desember 2009 Volume 12, Nomor 3, Juni 2009 Volume 12, Nomor 2, Desember 2008 Volume 12, Nomor 1, Juni 2008 Volume 11, Nomor 2, Desember 2007 Volume 11, Nomor 1, Juni 2007 Volume 10, Nomor 2, Desember 2006 Volume 10 No. 1 Juni 2006 Volume 09 No. 02 Desember 2005 Volume 09 No.1 Juni 2005 Volume 08 No.2 Desember 2004 Volume 08 No.1 Juni 2004 Volume 07 No.2 Desember 2003 Volume 07 No. 1 Juni 2003 Volume 6 No. 2 Desember 2002 Volume 6 No. 1 Juni 2002 Volume 5 No.2 Desember 2001 Volume 5 No. 1 Juni 2001 Volume 3 No.1 Desember 1999 More Issue

Home Page

OAI Link

Editorial Team

Contact

Reviewer

Google Scholar

Contact Name
Dessy Ariyanti

Contact Email
dessy.ariyanti@che.undip.ac.id

Phone
+62247460058

Journal Mail Official
j.reaktor@che.undip.ac.id

Editorial Address
Department of Chemical Engineering, Diponegoro University Jl. Prof. Soedarto SH Tembalang Semarang 50275

Location
Kota semarang,

Jawa tengah

INDONESIA

Abstract

Abstract

Abstract

Abstract

Abstract

Abstract

Abstract

Abstract

Abstract

Abstract

Home Page

OAI Link

Editorial Team

Contact

Reviewer

Google Scholar

Contact Name Dessy Ariyanti

Contact Email dessy.ariyanti@che.undip.ac.id

Phone +62247460058

Journal Mail Official j.reaktor@che.undip.ac.id

Editorial Address Department of Chemical Engineering, Diponegoro University Jl. Prof. Soedarto SH Tembalang Semarang 50275

Location Kota semarang, Jawa tengah INDONESIA

Abstract

Abstract

Abstract

Abstract

Abstract

Abstract

Abstract

Abstract

Abstract

Abstract

Contact Name
Dessy Ariyanti

Contact Email
dessy.ariyanti@che.undip.ac.id

Phone
+62247460058

Journal Mail Official
j.reaktor@che.undip.ac.id

Editorial Address
Department of Chemical Engineering, Diponegoro University Jl. Prof. Soedarto SH Tembalang Semarang 50275

Location
Kota semarang,

Jawa tengah

INDONESIA