Hasil Pencarian  ::  Simpan CSV :: Kembali

"CPO adalah bahan baku untuk memproduksi biodiesel. Biodiesel adalah energi terbarukan atau alternatif bahan bakar dari mesin diesel dan terbuat dari sumber terbaharui. Dalam proses produksi, CPO dan biodiesel ini memerlukan tempat penyimpanan yang membutuhkan material yang tepat. Material yang digunakan pada penelitian ini adalah baja karbon, SS 304, SS 316 dan monel 400. Pada material tersebut dilakukan uji komposisi kimia, struktur mikro, uji kekerasan mikro Vickers, pengamatan visual dan uji korosi mengacu pada ASTM G31 dengan kondisi tanpa ada aliran, T = ± 25oC selama 112 hari dalam lingkungan CPO dan biodiesel. Sedangkan pada CPO dan biodiesel dilakukan uji TAN dan kadar air. Setelah uji korosi mengacu pada ASTM G31 dilakukan pengamatan visual, pengamatan makro, uji produk korosi, laju korosi, struktur mikro, uji kekerasan mikro Vickers, uji TAN, uji kadar air dan analisa korosi.Hasil penelitian ini adalah nilai laju korosi dilingkungan CPO dengan mengacu pada ASTM G31 untuk sampel baja karbon, SS 304, SS 316 dan monel 400 berturut-turut adalah 0,203 mm/th, 0,019 mm/th, 0,018 mm/th, dan 0,017 mm/th. Nilai laju korosi dilingkungan biodiesel dengan mengacu pada ASTM G31 untuk sampel baja karbon, SS 304, SS 316 dan Monel 400 berturut-turut adalah 0,021 mm/th, 0,018 mm/th, 0,016 mm/th, dan 0,015 mm/th. Material yang memiliki ketahanan korosi yang cukup baik dilingkungan CPO adalah sampel SS 304, SS 316 dan Monel 400. Sedangkan material yang memiliki ketahanan korosi yang cukup baik dilingkungan biodiesel adalah sampel baja karbon, SS 304, SS 316 dan Monel 400. Sampel baja karbon pada CPO mengalami penurunan nilai kekerasan dan pada butiran terjadi korosi yang ditandai dengan terdapatnya lubang pada butiran serta pada batas butir dipermukaan sampel terlihat melebar. Sampel SS 304, SS 316 dan monel 400 pada CPO tidak terjadi penurunan nilai kekerasan dan butiran tidak terkorosi. Sampel baja karbon, SS 304, SS 316 dan monel 400 pada biodiesel tidak terjadi penurunan nilai kekerasan dan butiran tidak terkorosi. Material yang cocok digunakan dilingkungan CPO adalah SS 304, SS 316 dan monel 400. Material yang cocok digunakan dilingkungan biodiesel adalah baja karbon, SS 304, SS 316 dan monel 400.

---

CPO is feed for produce biodiesel. Biodiesel is renewable energy or alternative fuel for diesel mechine and from renewable source. In production process, CPO and biodiesel need storage tank with right material. The material used in this research are Carbon Steel, SS 304, SS 316 and Monel 400. At material to do chemical composition test, microstructure, microhardness Vickers test, visual observation and Corrosion test with ASTM G31 for condition no flow rate, T = ± 25oC until 112 days in CPO and biodiesel environment.For CPO and biodiesel to do TAN test and water contain test. After corrosion test ASTM G31 to do visual observation, makro observation, product corrosion test, corrosion rate, microstructur, microhardness Vickers test, TAN test, water contain test and analysis corrosion.Result this research are corrosion rate in CPO with ASTM G31 for Carbon Steel is 0,203 mm/th, for SS 304 is 0,019 mm/th, for SS 316 is 0,018 mm/th, for Monel 400 is 0,017 mm/th, Corrosion rate in biodiesel with ASTM G31 for Carbon Steel is 0,021 mm/th, for SS 304 is 0,018 mm/th, for SS 316 is 0,016 mm/th and for Monel 400 is 0,015 mm/th. Material have corrosion resistance in CPO are SS 304, SS 316 and Monel 400. Material have corrosion resistance in Biodiesel are Carbon Steel, SS 304, SS 316, and Monel 400. Sample Carbon Steel in CPO have decrease microhardness Vickers value and at boundary have corrosion which is characterized by the presence of hole at boundary and at grain boundary in surface sample Carbon Steel look wider. Sample SS 304, SS 316 dan Monel 400 in CPO no declaine microhardness Vickers value and boundary not corroded. Sample Carbon Steel, SS 304, SS 316 dan Monel 400 in Biodiesel no declaine microhardness Vickers value dan boundary not corroded. Material suitable fot use in CPO are SS 304, SS 316 and Monel 400. Material suitable for use in Biodiesel are Carbon Steel, SS 304, SS 316 and Monel 400."

"[ABSTRAKPenelitian pemanfaatan ekstrak tumbuh-tumbuhan sebagai inhibitor korosibelakangan ini semakin meningkat seiring dengan meningkatnya permintaanpenggunaan bahan-bahan kimia yang ramah lingkungan. Pemanfaatan ekstraktumbuh-tumbuhan sebagai inhibitor korosi menjadi penting mengingatkarakteristiknya ramah lingkungan (green inhibitor), mudah ketersediaannnya,sumberdaya yang melimpah dan dapat diperbaharui, prosedur produksi yangsederhana, dan biaya produksi yang cukup kompetitif. Dalam penelitian inidilakukan pengujian eksperimental efek sinergis jenis inhhibitor baru yaituekstrak ubi ungu (Ipomoea batatas L.) yang memiliki kandungan utamaantosianin dengan inhibitor komersial berbasis amine (aniline) dan denganinhibitor asam askorbat.Penelitian bertujuan untuk menganalisis laju kororsi dan efisiensi inhibisikorosi logam baja (API 5L) di dalam lingkungan air terproduksi menggunakaninhibitor campuran ekstrak ubi ungu dan inhibitor komersial berbasis amine(aniline). Selain itu dilakukan pula analisis laju korosi, efisiensi inhibisi,mekanisme proteksi dan model lapisan inhibisi korosi logam baja (API 5L) didalam lingkungan 3,5% NaCl menggunakan inhibitor campuran ekstrak ubi ungudan asam askorbat.Metode pengukuran laju korosi dan efisiensi inhibisi dilakukanmenggunakan elektrokimia kurva polarisasi. Mekanisme korosi diteliti denganmenggunakan metode Electrochemical Impedance Spectroscopy (EIS). Untukmenganalisis model lapisan inhibisi dilakukan dengan menggunakan metodeFourier Transform Infra Red (FTIR) spectroscopy.Hasil penelitian menunjukan bahwa pencampuran ekstrak ubi ungumemiliki kemampuan sinergis dengan inhibitor komersial berbasis amine (aniline)pada fraksi volume ekstrak ubi ungu sebesar 25% dengan menghasilkan efisiensiinhibisi sebesar 82,14%. Sebagai pembanding, pada sistem yang samapenggunaan esktrak ubi ungu saja menghasilkan efisiensi inhibisi 68,30%,sedangkan penggunaan inhibitor komersial berbasis amine (aniline) sajamenghasilkan efisiensi inhibisi 74,88%.Penambahan volume ekstrak ubi ungu dari 1 mL hingga 4 mL kedalaminhibitor asam askorbat 10-4 M meningkatkan efisiensi inhibisi korosi logam baja(API 5L) dalam larutan 3,5% NaCl dari efisiensi inhibisi sebesar 23,37% menjadi57,52%. Campuran inhibitor korosi tersebut berpengaruh terhadap kurvapolarisasi anodik maupun katodik sehingga dapat berperan sebagai mixedinhibitor. Pengujian EIS menunjukan proses korosi dikontrol oleh mekanismepasivasi yang ditunjukan oleh adanya peningkatan tahanan permukaan korosi.Pada lapisan permukaan terjadi proses adsorpsi dan pembentukan kelatorgano (flavonoid) logam dimana ekstrak ubi ungu dengan kandungan utamaantosianin berperan sebagai pembentuk metal-chelated. Pembentukan kelatekstrak ubi ungu-Fe-asam askorbat terjadi pada gugus hidroksil dan karbonil.Lokasi terjadinya ligan kelat ekstrak ubi ungu dengan kandungan utma antosianinterjadi pada ikatan 3?, 4? Dihydroxy cincin B atau 3-Hydroxy 4-Carbonyl cincin C;

---

ABSTRACTResearch of utilization of plant extracts as a corrosion inhibitor recentlyincreased along with the increasing demand for the use of chemicals that areenvironmentally friendly. Utilization of plant extracts as a corrosion inhibitorbecomes important given the characteristics of environmentally friendly (greeninhibitor), easy availability, resources are abundant and renewable, the productionprocedure is simple, and the production costs are quite competitive. In thisresearch, experimental testing of the synergistic effects of new types inhibitor ieextract purple potato (Ipomoea batatas L.) which has the main content ofanthocyanin with commercial inhibitor-based amine (aniline) and with ascorbicacid inhibitors.The study aims to analyze the rate of corrosion and metal corrosioninhibition efficiency of steel (API 5L) in the produced water environment using amixed inhibitor purple sweet potato extract and commercial-based inhibitors ofamine (aniline). In addition, the corrosion rate analysis was also performed,inhibition efficiency, protection mechanisms and models of metal corrosioninhibition layer steel (API 5L) in the neighborhood of 3.5% NaCl using a mixedinhibitor purple sweet potato extract and ascorbic acid.Method of measuring the rate of corrosion and inhibition efficiency wasperformed using electrochemical polarization curves. Corrosion mechanismsinvestigated by Electrochemical Impedance Spectroscopy (EIS). To analyze themodel layer of inhibition were calculated using Fourier Transform Infra Red(FTIR) spectroscopy.The results showed that mixing purple sweetpotato extract has the abilityto synergistically with commercial inhibitor-based amine (aniline) in purplesweetpotato extract volume fraction of 25% with a yield of 82.14% inhibitionefficiency. For comparison, the same system using purple sweet potato extractonly produce inhibition efficiency of 68.30%, while the use of commercial-basedinhibitors of amine (aniline) alone resulted in inhibition efficiency of 74.88%.The addition of purple sweet potato extract volume of 1 mL to 4 mL intoascorbic acid inhibitors 10-4 M improving steel metal corrosion inhibitionefficiency (API 5L) in a solution of 3.5% NaCl of inhibition efficiency of 23.37%to 57.52%. The corrosion inhibitor mixture affect the anodic and cathodicpolarization curves so that it can act as a mixed inhibitor. Testing EIS shows thecorrosion process is controlled by the passivation mechanism indicated by anincrease in the surface resistance of corrosion.On the surface layer of a process of adsorption and formation of organochelates (flavonoids) in which the metal purple sweet potato extract with the maincontent of anthocyanins act as forming metal-chelated. Location of the chelatingligand purple sweet potato extract with the main content of anthocyanins occur inbond 3 ', 4' dihydroxy ring B or 3-Hydroxy 4-Carbonyl ring C.;Research of utilization of plant extracts as a corrosion inhibitor recentlyincreased along with the increasing demand for the use of chemicals that areenvironmentally friendly. Utilization of plant extracts as a corrosion inhibitorbecomes important given the characteristics of environmentally friendly (greeninhibitor), easy availability, resources are abundant and renewable, the productionprocedure is simple, and the production costs are quite competitive. In thisresearch, experimental testing of the synergistic effects of new types inhibitor ieextract purple potato (Ipomoea batatas L.) which has the main content ofanthocyanin with commercial inhibitor-based amine (aniline) and with ascorbicacid inhibitors.The study aims to analyze the rate of corrosion and metal corrosioninhibition efficiency of steel (API 5L) in the produced water environment using amixed inhibitor purple sweet potato extract and commercial-based inhibitors ofamine (aniline). In addition, the corrosion rate analysis was also performed,inhibition efficiency, protection mechanisms and models of metal corrosioninhibition layer steel (API 5L) in the neighborhood of 3.5% NaCl using a mixedinhibitor purple sweet potato extract and ascorbic acid.Method of measuring the rate of corrosion and inhibition efficiency wasperformed using electrochemical polarization curves. Corrosion mechanismsinvestigated by Electrochemical Impedance Spectroscopy (EIS). To analyze themodel layer of inhibition were calculated using Fourier Transform Infra Red(FTIR) spectroscopy.The results showed that mixing purple sweetpotato extract has the abilityto synergistically with commercial inhibitor-based amine (aniline) in purplesweetpotato extract volume fraction of 25% with a yield of 82.14% inhibitionefficiency. For comparison, the same system using purple sweet potato extractonly produce inhibition efficiency of 68.30%, while the use of commercial-basedinhibitors of amine (aniline) alone resulted in inhibition efficiency of 74.88%.The addition of purple sweet potato extract volume of 1 mL to 4 mL intoascorbic acid inhibitors 10-4 M improving steel metal corrosion inhibitionefficiency (API 5L) in a solution of 3.5% NaCl of inhibition efficiency of 23.37%to 57.52%. The corrosion inhibitor mixture affect the anodic and cathodicpolarization curves so that it can act as a mixed inhibitor. Testing EIS shows thecorrosion process is controlled by the passivation mechanism indicated by anincrease in the surface resistance of corrosion.On the surface layer of a process of adsorption and formation of organochelates (flavonoids) in which the metal purple sweet potato extract with the maincontent of anthocyanins act as forming metal-chelated. Location of the chelatingligand purple sweet potato extract with the main content of anthocyanins occur inbond 3 ', 4' dihydroxy ring B or 3-Hydroxy 4-Carbonyl ring C., Research of utilization of plant extracts as a corrosion inhibitor recentlyincreased along with the increasing demand for the use of chemicals that areenvironmentally friendly. Utilization of plant extracts as a corrosion inhibitorbecomes important given the characteristics of environmentally friendly (greeninhibitor), easy availability, resources are abundant and renewable, the productionprocedure is simple, and the production costs are quite competitive. In thisresearch, experimental testing of the synergistic effects of new types inhibitor ieextract purple potato (Ipomoea batatas L.) which has the main content ofanthocyanin with commercial inhibitor-based amine (aniline) and with ascorbicacid inhibitors.The study aims to analyze the rate of corrosion and metal corrosioninhibition efficiency of steel (API 5L) in the produced water environment using amixed inhibitor purple sweet potato extract and commercial-based inhibitors ofamine (aniline). In addition, the corrosion rate analysis was also performed,inhibition efficiency, protection mechanisms and models of metal corrosioninhibition layer steel (API 5L) in the neighborhood of 3.5% NaCl using a mixedinhibitor purple sweet potato extract and ascorbic acid.Method of measuring the rate of corrosion and inhibition efficiency wasperformed using electrochemical polarization curves. Corrosion mechanismsinvestigated by Electrochemical Impedance Spectroscopy (EIS). To analyze themodel layer of inhibition were calculated using Fourier Transform Infra Red(FTIR) spectroscopy.The results showed that mixing purple sweetpotato extract has the abilityto synergistically with commercial inhibitor-based amine (aniline) in purplesweetpotato extract volume fraction of 25% with a yield of 82.14% inhibitionefficiency. For comparison, the same system using purple sweet potato extractonly produce inhibition efficiency of 68.30%, while the use of commercial-basedinhibitors of amine (aniline) alone resulted in inhibition efficiency of 74.88%.The addition of purple sweet potato extract volume of 1 mL to 4 mL intoascorbic acid inhibitors 10-4 M improving steel metal corrosion inhibitionefficiency (API 5L) in a solution of 3.5% NaCl of inhibition efficiency of 23.37%to 57.52%. The corrosion inhibitor mixture affect the anodic and cathodicpolarization curves so that it can act as a mixed inhibitor. Testing EIS shows thecorrosion process is controlled by the passivation mechanism indicated by anincrease in the surface resistance of corrosion.On the surface layer of a process of adsorption and formation of organochelates (flavonoids) in which the metal purple sweet potato extract with the maincontent of anthocyanins act as forming metal-chelated. Location of the chelatingligand purple sweet potato extract with the main content of anthocyanins occur inbond 3 ', 4' dihydroxy ring B or 3-Hydroxy 4-Carbonyl ring C.]"

"Sebagai instalasi yang sangat vital untuk mentransportasikan gas dari suatu lapangan untuk sampai kepada pengguna (End User) maka kehandalan sisstem pipa transmisi gas harus terus dijaga. Hal tersebut dilakukan dengan beberapa cara antara lain pelaksanaan inspeksi, program perawatan (maintenance) secara berkala atas sistem pipa transmisi gas tersebut. Metode inspeksi dirasakan masih memiliki beberapa kelemahan antara lain biaya tinggi, pelaksanaan inspeksi lebih ditekankan pada waktu inspeksi dan tidak mempertimbangkan risiko yang mungkin timbul serta dampaknya bila terjadi kegagalan operasinya. Dalam rangka meningkatkan efisiensi dalam hal keinspeksian, di industri migas telah dikenal suatu metode inspeksi yang didasari kepada pertimbangan risiko yang dikenal dengan istilah inspeksi berbasis risiko (Risk Based Inspection/RBI). American Petroleum Institute telah mengembangkan metodologi RBI tersebut yang pada awalnya masih dikhususkan pada instalasi dan peralatan yang berada pada suatu area tertentu dan memiliki tekanan (pressurize) RBI memfokuskan pelaksanaan inspeksi pada peralatan dan instalasi yang memiliki risiko kegagalan operasi sangat tinggi dengan dampak terhadap manusia sangat berbahaya. RBI dasar dikenal dengan perkalian antara Pof x CoF, dimana PoF itu adalah faktor penyebab kegagalan dan Cof itu adalah dampak yang ditimbulkan. Perkalian Pof dengan CoF menghasilan risiko yang ada pada instalasi dan peralatan. Mengingat parameter-parameter yang digunakan untuk menghitung PoF dan CoF pada peralatan dan instalasi bersifat tetap, maka menghitung risiko yang ada mudah dilaksanakan. Sebaliknya untuk sistem pipa transmisi gas dengan material baja API 5L X52 yang digelar melintasi berbagai area dimana memiliki sifat dan karakteristik yang berbeda sehingga menjadikan banyak factor ketidakpastian (uncertainity), maka RBI sulit untuk diaplikasikan. Penelitiaan ini bertujuan untuk mengembangkan dan mengaplikasikan model inspeksi berbasis risiko pada sistem pipa transmisi gas baja API 5L X52 di daratan dengan melakukan analisa permodelan terhadap faktor uncertainity sebagaimana disebutkan di atas. Hasil penelitian ini menunjukkan bahwa korosi eksternal menjadi faktor utama penyebab terjadinya kegagalan operasi dengan catatan gas yang mengalir adalah dry gas. Seluruh faktor kondisi tanah sekitar pipa digelar dan ditanam termasuk coating dan proteksi katodik menjadi faktor uncertainity. Untuk mengetahui tingkat risiko pada sistem pipa transmisi gas, maka dilakukan permodelan kuantifikasi dengan penghitungan melalui analisa distribusi weibull, dengan demikian risiko pada setiap segmen dapat diperhitungkan. Pada sistem pipa transmisi gas yang diproteksi dengan pelindung maka coating breakdown factordan penurunan proteksi katodik menjadi parameter yang penting dalam menghitung laju korosinya. Metode pengukuran laju korosi dilakukan dengan menggunakan polarisasi dengan parameter resistivitas tanah dan pH. Hasil pengukuran resistivitasdan pH sepanjang jalur pipa dengan sampel tanah yang diambil dianalisis di laboratorium dengan prinsip mengaplikasikan arus sinyal/AC dalam sel elektrokimia dengan menggunakan sirkuit tiga elektroda. Hasil penelitian menunjukkan bahwa laju korosi material baja API 5L X 52 meningkat dengan semakin kecilnya resistivitas tanah dan sebaliknya akan menurun dengan semakin tingginya resistivitas tanah. Laju korosi yang dihasilkan berdasarkan hasil analisis yaitu 0.7409 e –0.002(r) (pH) (CB) (CP). Besaran laju korosi untuk tiap segmen dapat diperhitungkan sehingga PoF dapat ditentukan. Permodelan kedua adalah penghitungan dampak yang diakibatkan bila pipa tersebut mengalami kegagalan operasi dan mengakibatkan kebocoran pipa maka dampak terhadap manusia menjadi hal yang harus diperhitungkan atau dikenal dengan istilah Number Of Death (NOD). Secara spesifik Jo dan Ann telah menemukan bahwa NOD dapat dihitung dan sangat tergantung pada densitas penduduk yang berada pada jarak tertentu dengan jalur pipa itu. CoF dalam hal ini diambil dari hasil perhitungan NOD dan diperhitungan untuk setiap segmen pipa. Pada tingkat fatality 90 % dengan densitas penduduk 0.00769 maka NOD adalah 1.Permodelan inspeksi sebagai bagian dari mitigasi risiko merupakan tahapan akhir dari proses penelitian ini sebagai respon dari analisis risiko yang dibuat agar pipa transmisi gas dapat dioperasikan dengan handal dan aman.. Skema inspeksi diperoleh melalui perhitungan laju korosi dengan mengetahui tingkat kritikaliti (kekritisan) per tahun atau per segmen. Penurunan risiko secara signifikan mampu mengurangi frekuensi inspeksi dimana meningkatkan efisiensi dan menghemat biaya. Penurunan risiko adalah implementasi metode ALARP yang implementasinya dilaksanakan melalui strategi IMR sebagai keluaran dari proses permodelan inspeksi berbasis risiko pada penelitian ini.

---

For installations that are vital for transporting gas from a field to get to the user (End User) the reliability system gas transmission pipeline must be maintained. This is done in several ways, among others, the implementation of the inspection, maintenance program (maintenance) periodically over the gas transmission pipeline system. Perceived inspection method still has some drawbacks include high cost, the implementation of the inspection more emphasis on inspection time and do not consider the possible risks and impacts in the event of failure of the operation. In order to improve efficiency in terms of inspection, in the oil and gas industry has known an inspection method that is based on the consideration of risk is known as risk-based inspection ( Risk Based Inspection / RBI ).

The American Petroleum Institute has developed the RBI methodology which initially was devoted to the installation and equipment located in a particular area and have the pressure ( pressurize ) RBI to focus inspections on equipment and installations that have a very high risk of failure with extremely harmful effects on humans. RBI base known as the multiplication between POF x CoF, which PoF it is a factor that is a failure and Cof impact. Multiplication POF with CoF produce risk of the installation and equipment. Given the parameters used to calculate the PoF and CoF on equipment and installations are fixed, then calculate the risks that exist easily implemented. In contrast to the gas transmission pipeline system with API 5L X52 steel materials are held across a range of areas which have different properties and characteristics that make a lot of uncertainty factors ( uncertainity ), the RBI is difficult to apply. The aim of this research to develop and apply models of risk -based inspection system of gas transmission pipeline API 5L X52 steel in the mainland by analyzing uncertainity modeling of the factors mentioned above.

The results of this study indicate that external corrosion becomes a major factor causing the failure of the operation to record the flowing gas is gas cleaning. All factors of soil around the pipe was held and planted including coatings and cathodic protection uncertainity factor. To determine the level of risk in the gas transmission pipeline system, it is done by calculating the quantification modeling through analysis of weibull distribution, thus the risks on each segment can be calculated. In the gas transmission pipeline systems protected with the protective coating breakdown factordan decrease in cathodic protection becomes an important parameter in calculating the corrosion rate. The method of corrosion rate measurements done using polarization with soil resistivity and pH parameters. Results ressitivity dan pH measurements along a pipeline with soil samples taken were analyzed in the laboratory by applying the principle of signal flow / air in an electrochemical cell using a three- electrode circuit.

The results showed that the corrosion rate of the steel material API 5L X- 52 increased with the size of the soil resistivity and vice versa to decrease with increasing soil resistivity. The resulting corrosion rate based on the results of the analysis are 0.7409 e -0002 ( r ) ( pH ) ( CB ) ( CP ). The amount of corrosion rate can be calculated for each segment so that PoF can be determined. The second is the calculation modeling the impact caused when the pipe failure resulting in leakage of pipeline operations and the impact of humans into things that must be considered or known as Number Of Death ( NOD ). Specifically Jo and Ann have found that NOD can be calculated and is highly dependent on the density of the population who are at a certain distance with the pipeline. CoF in this case are taken from the calculation of NOD and reckoned for each pipe segment. At the fatality rate of 90 % with a population density of 0.00769 then NOD is 1.

Modeling inspection as part of risk mitigation is the final stages of the research process in response to the risk analysis made to the gas transmission pipeline can be operated reliably and safely. Inspection scheme is obtained by calculating the corrosion rate by knowing the level kritikaliti ( criticality ) per year or per segment. Decreased risk significantly reduced the frequency of inspections which improve efficiency and save costs. The reduction in risk is ALARP method implementation are implementation strategies implemented through IMR as the output of a risk -based inspection process modeling in this study."

"Secara umum penelitian ini bertujuan untuk mengeksplorasi kemungkinan penggunaan limbah biomassa dalam proses reduction roasting bijih besi nikel laterite Indonesia. Adapun motif di balik penelitian ini adalah untuk meningkatkan nilai tambah dari bijih besi kadar rendah dan mendapatkan bio-reduktor baru yang akan menjadi alternatif pengganti batu bara di masa depan. Dalam penelitian ini diteliti tiga limbah biomassa sebagai agen pereduksi bijih besi nikel laterite dari Sorowako, yaitu: ampas tebu dari kabupaten Cirebon, cangkang sawit dari Palangkaraya - Kalimantan Tengah, dan sekam padi dari Kerawang - Jawa Barat. Adapun metode yang digunakan adalah reduction roasting dengan variasi parameter temperatur, rasio massa, dan waktu reduksi. Selanjutnya dilakukan analisis berdasarkan pola difraksi hasil X-Ray Diffraction (XRD), X-Ray Fluorescence (XRF), dan Induced Couple Plasma Mass Spectroscopy (ICP-MS).Hasil yang diperoleh dalam penelitian ini menunjukkan bahwa ampas tebu, cangkang sawit, dan sekam padi terbukti mampu digunakan sebagai agen pereduksi alternatif pengganti batu bara. Pada penelitian ini, ampas tebu hanya mampu menghasilkan fasa wustite dalam reduction roasting bijih besi nikel laterite, di mana hasil reduksi tertinggi diperoleh pada sampel dengan rasio massa 1:4 yang direduksi pada temperatur 1000°C selama 30 menit. Sementara itu, cangkang sawit mampu mereduksi bijih besi nikel laterite menjadi Fe metal, dimana parameter optimalnya adalah: rasio massa = 1:3, durasi waktu reduksi = 30 menit, dan temperatur reduksi 1000°C. Di samping itu, meskipun sekam padi hanya mampu mereduksi bijih besi sampai fasa magnetite (dimana hasil optimal diperoleh pada penambahan padi sebesar 20%), tetapi dari sekam padi berhasil diperoleh bio-silika amorf dengan tingkat kemurnian 99,99% dan specific surface area (luas permukaan spesifik) 192 m2/g.

---

In general, this study aims to explore the utilization of local biomass as renewable reducing agents in the reduction roasting of Indonesian nickel laterite iron ore. The motive behind this research is to increase the added value of low grade iron ore and to obtain reducing agents to substitute coal in the reduction process. In this study, the three of biomass which have potential to be used as reducing agents for coal substitutes in reducing nickel laterite iron ore from Sorowako, are: bagasse from Cirebon, palm shells from Palangkaraya - Central Kalimantan, and rice husk from Kerawang - Jawa Barat. The reduction method used is reduction roasting with various temperature, mass ratio, and reduction time. And the analysis is based on the diffraction pattern of X-Ray Diffraction (XRD), X-Ray Fluorescence (XRF), and Induced Couple Plasma Mass Spectroscopy (ICP-MS).The results obtained in this study indicate that bagasse, palm kernel shells, and rice husks have been proven to be able to be used as an alternative reducing agent for coal substitution. In this study, bagasse was only able to produce the wustite phase in the reduction roasting of nickel laterite iron ore, where the highest reduction results were obtained in samples with a mass ratio of 1: 4 which was reduced at a temperature of 1000°C for 30 minutes. Meanwhile, palm kernel shells could reduce nickel laterite iron ore to Fe metal, where the optimal parameters were: mass ratio = 1: 3, reduction time duration = 30 minutes, and reduction temperature = 1000°C. In addition, although rice husk was only able to reduce iron ore to magnetite phase (where optimal results are obtained by adding rice by 20%), but from rice husk it was successfully obtained amorphous bio-silica with a purity level of 99.99% and specific surface area 192 m2/g."

"Penelitian yang akan dikembangkan adalah material pelat bipolar polimer komposit berbasis karbon, terdiri dari epoksi resin dan hardener sebagai binder, sedangkan grafit, carbon black (CB) dan tabung nano berdinding banyak (multiwall carbon nanotube-MWCNT) sebagai penguat (reinforcement) dan pengisi (filler). Berbagai komposisi material serta variasi proses kompresi dilakukan untuk mendapatkan optimasi pelat bipolar yang memenuhi persyaratan, oleh karena itu penelitian ini dilakukan dalam beberapa tahapan. Pada tahapan awal penelitian, bertujuan untuk mengetahui apakah grafit limbah elektroda electric arc furnace (grafit EAF) dapat digunakan untuk menggantikan grafit sintetis sebagai reinforcement material dalam polimer karbon komposit. Pelat bipolar berbasis grafit EAF yang berukuran partikel < 44 µm dan pelat bipolar berbasis grafit sintetis berukuran partikel < 55 µm dicampur dengan carbon black (CB) pada interval komposisi dari (0; 2.5; 5; 7.5; 10; 12.5; 15; 17.5 dan 20) wt%. Proses kompresi dilakukan pada tekanan 30 MPa dan temperatur 70 0C. Sifat pelat bipolar dengan penguat (reinforcement) yang berasal dari grafit sintetis atau grafit EAF menunjukkan hasil yang relatif sama untuk ke empat jenis pengujian yaitu pengujian densitas, porositas, kekuatan fleksural dan konduktivitas listrik pada penambahan CB (5 dan 10) wt%. Hasil pengujian dengan penambahan polimer konduktif polianilin (PANI) pada rentang konsentrasi dari (0.027; 0.054; 0.081 dan 0.108) %wt memberikan konfirmasi dan justifikasi bahwa grafit EAF dapat digunakan sebagai reinforcement untuk menggantikan grafit sintetis. Penelitian pada tahapan lanjut hanya menggunakan grafit EAF dan CB yang berasal dari serabut kelapa hasil proses pirolisis pada temperatur 600 0C dalam lingkungan nitrogen. Variabel penelitian mencakup variasi tekanan dan temperatur kompresi, variasi ukuran partikel baik untuk grafit maupun CB. Kekuatan fleksural optimum dicapai pada tekanan kompresi 55 MPa dan temperatur kompresi 100 0C sebesar (48 ? 48.24) MPa, telah memenuhi persyaratan pelat bipolar DOE yaitu > 25 MPa. Nilai densitas seluruh hasil pengujian (1.69 ? 1.78) gr/cm3lebih kecil dari 5 gr/cm3, hal ini juga telah memenuhi persyaratan sebuah pelat bipolar yang ringan. Hasil pengujian untuk porositas berkisar antara (0.36-0.70) %. Pelat bipolar dengan komposisi CB 5 wt%, temperatur kompresi pada 100 0C serta tekanan kompresi pada 55 MPa memberikan hasil yang relatif lebih baik dibandingkan dengan komposisi CB 10 wt%. Penambahan MWCNT bertujuan untuk meningkatkan sifat mekanik dan listrik pada pelat bipolar yang dihasilkan dari penelitian sebelumnya. Nilai densitas terendah dan kekuatan fleksural tertinggi dihasilkan pada komposisi 90grafit EAF/5CB/5MWCNT yaitu sebesar 1.52 gr/cm3 untuk densitas dan 63.71 MPa untuk kekuatan fleksural. Nilai konduktivitas tertinggi dari seluruh tahapan penelitian diperoleh dari pelat bipolar dengan komposisi 95grafit EAF/2CB/3MWCNT yaitu sebesar 8.94 S/cm.

---

This research will examine the utilization of an alternative material to obtain bipolar plates that are light, affordable, and can be mass produced. The research that will be developed is to create carbon-based composite bipolar plate material consisting of epoxy resin and hardener as a binder, graphite, carbon black (CB) and multiwall carbon nano-tube (MWCNT) as a reinforcement or filler material. Various material compositions and variations made to get the compression molding process optimization of bipolar plates that meet requirements that can be obtained by several stages. We investigated whether graphite electrode waste from electric arc furnace (EAF) can subtitute graphite synthetic as a reinforcement material for polymer carbon composite. Bipolar plate based on graphite EAF has particle size < 44 micron, and bipolar plate based on graphite synthetic with particle size of < 55 micron mixing with carbon black (CB) from 0-20% w/w at intervals of 2.5% w/w. The materials are molded using compression hot press machine (30 MPa, 70oC). Samples are tested for: density, porosity, flexural, and electric conductivity, indicated the bipolar plate characteristics with graphite synthetic or graphite EAF showed the same results relatively. Further research showed that the characteristics of synthetic graphite-based bipolar plates and graphite EAF were influenced by the addition of conductive polymers such as polyaniline at interval concentration from 0,027 w/w; 0,054w/w; 0,081 w/w and 0,108 w/w. These results provide confirmation and justification that graphite is used subsequently derived from EAF graphite as reinforcement and the CB additions at (5 and 10) w/w used as a filler material bipolar plates. We then used graphite EAF and CB resulting from pyrolysis process of coconut husk at 600 0C for 10 hours in nitrogen environment. Research variable covered of variety of pressure and temperature compression, variety of particle sizes of graphite EAF or CB. Flexural strength was recorded to be optimum at 48.24 MPa (at 45 MPa, 100 0C), which fulfilled the requirement of bipolar plate > 25 MPa. Density test for all EAF graphite based bipolar plates less than 5 g/cm3. In addition, the porosity for all samples were under 2% (0.36 %-1.92%). Properties of bipolar plates with CB 5 w/w (at 55 MPa, 100 0C and pyrolysis temperature at 900 0C) showed relatively better results compared with CB 10 w/w. The effect of MWCNT improved mechanical and electrical properties. The lowest density value and the highest flexural strength achieved at composition of 90graphite EAF/5CB/5MWCNT of 1.53 g/cm3 for density and 63.71 MPa for flexural strength. The highest conductiviy value from of all research stages achieved from composition of 95graphite EAF/2CB/3MWCNT of 8.94 S.cm-1."

"Peningkatan keselamatan dan efisiensi dalam industri minyak dan gas bumi di Indonesia masih memerlukan pendekatan yang canggih untuk memelihara sistem perpipaan yang ada. Disertasi ini membahas penerapan metode Risk Based Inspection (RBI) dengan dukungan teknologi machine learning (ML) dan deep learning (DL) untuk mengembangkan model yang mampu mengidentifikasi akar permasalahan dan solusi untuk menanggulangi kegagalan tersebut. Penelitian dilakukan pada sampel ex-spool berdiameter 16’’ melalui pengujian metalografi dan penggunaan algoritma AdaBoost, Random Forests, dan Gradient Boosting. Metode klasifikasi masalah dilakukan berdasarkan prinsip K-Means Clustering dan Gaussian Mixture Model dan penelitian divalidasi menggunakan metode k-fold cross-validation. Model yang dihasilkan mampu mengidentifikasi dan mengklasifikasikan jenis kegagalan ke dalam 3 kelompok sesuai jenis risikonya masing-masing serta memberikan beragam metode pemeliharaan material yang lebih ekonomis. Program artificial intelligence ini diharapkan mampu meningkatkan keselamatan dan keandalan operasi perpipaan minyak dan gas di Indonesia melalui penerapan berbagai metode pemeliharaan pipa di masa depan.

---

Improving safety and efficiency in the oil and gas industry in Indonesia still requires a sophisticated approach to maintain the existing piping systems. This dissertation discusses the application of the risk-based inspection (RBI) method with the support of machine learning (ML) and deep learning (DL) technology to develop a model that is able to identify the potential root-cause and its solutions to overcome these failures. The research was carried out on a 16'' diameter ex-spool sample through metallographic testing and the use of AdaBoost, Random Forests, and Gradient Boosting algorithms. The problem classification method was carried out based on the principles of K-means clustering and the Gaussian Mixture Model, while the research was validated using the k-fold cross-validation method. The resulting model is able to identify and classify types of failure into three groups according to each type of risk and provides a variety of more economical material maintenance solutions. It is hoped that this artificial intelligence program can support efforts to increase the safety and reliability of oil and gas pipeline operations in Indonesia through the application of various pipeline maintenance methods in the future."

"Disertasi ini membahas pengaruh batubara pada bijih besi tipe lateritik dalam bentuk pelet komposit. Tiga sampel R, C dan CTR digunakan dalam penelitian ini. R merupakan sampel yang berasal dari lokasi tambang, C merupakan bijih besi R yang telah dicuci dengan classifyer, dan CTR merupakan sampel C yang telah dilewatkan pada pemisah magnetik. Ketiganya berbeda dalam jumlah goethit, hematit dan magnetit. Sampel C hanya digunakan untuk reduksi diatas 1000 °C. Batubara yang digunakan sebagai reduktor merupakan batubara dengan kadar karbon rendah. Ketiga sampel digunakan berukuran lebih kecil dari 140 mesh. Sampel ditambahkan batubara dengan jumlah yang bervariasi, dibuat pelet dan dikeringkan. Pelet komposit kemudian direduksi. Reduksi diatas 1000 °C dilakukan dengan tungku tabung. Kecepatan pemanasan tungku 10 °C/menit hingga temperatur yang diinginkan, temperatur ditahan selama 10 menit dan kemudian diturunkan hingga temperatur kamar. Variasi jumlah batubara adalah 20 % berat dan 29 % untuk R dan C serta 31 % untuk CTR. Jumlah batubara yang terakhir tersebut berhubungan dengan komposisi stoekiometri Fet dan C. Variasi temperatur adalah 1100 °C, 1200 °C, 1300 °C dan 1350 °C. Analisis dilakukan dengan XRD untuk mengetahui fasa-fasa yang terbentuk dan diikuti dengan kuantifikasi fasa dengan metode Rietvield. Densitas pelet diukur untuk mengetahui perubahannya terhadap perubahan fasa. Mikrostruktur pelet diamati dengan SEM untuk mengetahui perbedaan dari pelet R dan CTR. Reduksi dibawah 1000 °C dilakukan dengan alat Simultaneous Thermal Analysis dan tungku tabung. Reduksi dengan alat STA dilakukan dengan kecepatan 10.

---

The dissertation discusses the reduction process of lateritic iron ore-coal composite pellet. Three samples have been used, called R, C and CTR. R is lateritic iron ore from mining, C is washed lateritic iron ore and CTR is lateritic iron ore which has been washed folllowed by magnetic separation. The three samples have different quantity of goethite, hematite and magnetite phases. C has been used only for direct reduction above 1000 °C. The used coal has low fixed carbon. The R, C and CTR are smaller than 140 mesh. The composite pellets are made of mixture of coal and ore.

Reduction above 1000 °C is carried out in tube furnace. Heating rate is 10 °C/minute. The temperature is fixed and maintained for 10 minutes. Then, temperature is decreased by turning off the electricity to room temperature. The composite of R and C are made of 20 % and 29 % of total weight whereas the composite of CTR are made of 20 % and 31 % of total weight. The temperatures are fixed at 1100 °C, 1200 °C, 1300 °C and 1350 °C.

X-Ray Diffraction is used for analysing the phases present after heating and followed by quantification using Rietveld Method. Density of composite pellet are measured. Microstructure of pellets are also investigated using SEM. Reduction below 1000 °C is carried out using Simoultaneous Thermal Analysis and tube furnace. Heating rate is 10 °C/minute. Nitrogen is flowed 20 mL/minute. Obtained thermal graphs are analysed. Reduced samples are analysed using X-Ray Diffraction. During reduction, released gases are analysed using gas analyser."

"Laju korosi material baja API 5L X52 di dalam larutan 3,5 % NaCl teraerasi pada kondisi aliran turbulen berlangsung relatif tinggi yang dapat mencapai lebih dari 80 mpy (2 mm/tahun). Upaya menurunkan laju korosi tersebut umumnya dilakukan secara konvensional dengan penambahan zat inhibitor seperti oxygen scavenger atau senyawa organik jenis adsorpsi. Bilamana efektifitas kinerja inhibitor tersebut relatif rendah maka diperlukan jenis inhibitor altematif dengan kinerja yang lebih baik. Dalam penelitian ini dilakukan pengujian eksperimental terhadap suatu jenis inhibitor barn yaitu ekstrak campuran antara green tea (teh hijau) dengan kandungan utama epiga/lo cacethin gallate dan piper betle (daun sirih) dengan kandungan utama hydroxychavicol yang bersifat ramah lingkungan (green corrosion inhibitor).Penelitian bertujuan untuk menganalisis penurunan besaran laju korosi material baja (API 5L X52) di dalam lingkungan larutan 3,5 % NaCI teraerasi, pada kondisi aliran turbulen (0-5000 rpm) dengan penambahan inhibitor campuran ekstrak piper betle dengan green tea sehingga dapat dievaluasi effisiensinya. Selain itu dilakukan pula analisis serta sintesis terhadap mekanisme inhibisi elektrokimia ekstrak campuran inhibitor tersebut.Metoda pengukuran laju korosi dilakukan dengan menggunakan simulasi Rotating Cylinder Electrode (RCE) serta pengukuran elektrokimia kurva polarisasi. Mekanisme korosi diteliti dengan metoda Electrochemical Impedance Spectroscopy (EIS). Sedangkan karakterisasi ekstrak green inhibitor dilakukan dengan menggunakan metoda Fourier Transform Infra Red (FTIR).Hasil penelitian menunjukkan bahwa laju korosi material baja API 5L X52 di dalam larutan 3,5 % NaCl meningkat secara tajam hingga 195 mpy atau 5 mm/tahun pada 5000 rpm tanpa penambahan inhibitor. Sebagai pembanding, penggunaan inhibitor oxygen scavenger yang berupa senyawa sodium sulfit dapat menurunkan laju korosi dengan effisiensi inhibitor > 90 %. Pada konsentrasi campuran green inhibitor I 000 ppm piper betle + 4000 ppm green tea, effisiensi inhibitor dapat mencapai ±90 %. Inhibitor korosi tersebut berpengaruh terhadap kurva polarisasi anodik mapun katodik sehingga dapat berperan sebagai mixed inhibitor. Pengujian EIS menunjukkan pada kondisi turbulen dengan penambahan inhibitor, proses korosi dikontrol oleh mekanisme aktivasi yang ditunjukkan oleh adanya impedansi kapasitif. Pengujian FTIR menunjukkan adanya gugus-gugus fungsi ikatan kimia yaitu: hydroxyl phenolic, C=O dan alkena =CH2 yang berkombinasi sebagai pembentuk lapisan (film- forming).Pada kondisi 3,5% NaCI dengan tekanan gas C02 sebesar I atmosfir dan keadaan stagnan, dengan penambahan konsentrasi ekstrak campuran inhibitor I 000 ppm piper betle + 4000 ppm green tea, effisiensi inhibitor yang diperoleh adalah sebesar ± 74 %. Sintesis lapisan inhibisi campuran ekstrak green tea dengan piper betle ditunjukkan dengan usulan model lapisan yang bekerja secara sinergis antara karakteristik sifat-sifat: adsorpsi, antioxidant dan hydrophobic.

---

The corrosion rate of type API 5L X52 steel in 3.5% NaCl aerated solution under turbulent flow condition is relatively high (can reach more than 2 mrnlyear). Method to reduce the rate of corrosion is generally done conventionally by the addition of corrosion inhibitor substance such as oxygen scavenger or adsorption of organic compounds. In case of the effectiveness of inhibitor performance is low then types of alternative inhibitors with better performance are required. This study was carried out dealing with experimental testing of a new inhibitor type i.e. a mixture extracts of green tea with the main content epiga/lo cacethin gallate (EGCG) and piper betle with the main content hydroxychavicol which were classified as environmentally friendly inhibitor (green corrosion inhibitor).The purpose of this study was to analyze the decreasing of corrosion rate of type API 5L X52 steel in aerated 3.5% NaCl solution under turbulent flow conditions (0-5000 rpm). The effect of green inhibitor addition in the solution was observed and its inhibitor efficiency was evaluated. Moreover, analysis as well as synthesis of the electrochemical inhibition mechanism of the extract mixture of these inhibitors was performed.Corrosion rate measurement method was conducted by using a simulation of the Rotating Cylinder Electrode (RCE) and by electrochemical measurements of polarization curves. Corrosion mechanism was examined by Electrochemical Impedance Spectroscopy (EIS) while the characterization of green inhibitor material was carried out using the method of Fourier Transform Infra-Red (FTIR).The results showed that the corrosion rate of type API 5L X52 steel in 3.5% NaCl aerated solution increased sharply up to 195 mpy (5 mm/year) at 5000 rpm without the addition of corrosion inhibitor. As a comparison, the use of inhibitor of type oxygen scavenger using sodium sulfite compound decreased the corrosion rate with inhibitor efficiency > 90%. The addition of green inhibitor concentration of 1000 ppm piper betle + 4000 ppm green tea resulted in approximately 90% inhibitor efficiency. The green inhibitor affected the cathodic as well as the anodic polarization curves which were known as mixed corrosion inhibitor type. EIS testing showed that under turbulent conditions with the addition of corrosion inhibitor, the processes were controlled by an activation mechanism which indicated by the presence of capacitive impedance. The type of chemical bonds on the steel surface layer was analyzed by FTIR method which indicated the presence of function groups : phenolic hydroxyl, C=O and alkene C=CH2 which combined as film forming.In a solution containing 3,5 % NaCl with I atm C02 gas pressure and stagnant condition, the addition of 1000 ppm piper betle + 4000 ppm green tea extracts resulted in approximately 74% inhibitor efficiency. Synthesis of inhibition layer created by a mixture of extracts of green tea and piper betle was proposed which had several characteristics : adsorption, antioxidant and hydrophobic which were believed to have a synergistic effect."

"Proses anodisasi pada aluminium menghasilkan struktur fenomenal berupa oksida logam yang terkenal dengan istilah Anodic Aluminum Oxide (AAO). AAO sangat diperlukan untuk meningkatkan daya adhesi pada proses pelapisan selanjutnya baik pada aluminium dan paduannya maupun komposit aluminium. Hal tersebut terjadi akibat adanya ikatan saling kunci antara lapisan oksida hasil anodisasi (AAO) dengan pelapis berikutnya. Morfologi pori pada AAO dapat dengan mudah dimodifikasi melalui perubahan parameter anodisasi. Namun, sayangnya penelitian-penelitian sebelumnya belum menyediakan informasi apapun mengenai pengontrolan diameter pori. Sedangkan seperti yang kita ketahui bahwa perbedaan aplikasi yang diinginkan membutuhkan diameter pori yang berbeda pula. Oleh karena itu guna mendapatkan diameter pori dengan ukuran tertentu maka pemilihan parameter proses anodisasi yang tepat sangatlah penting. Untuk memenuhi kebutuhan tersebut, dalam penelitian ini akan dihasilkan persamaan empiris yang dapat memprediksi ukuran diameter dan densitas pori AAO yang terbentuk hasil anodisasi dengan berbagai parameter tertentu agar dapat digunakan dalam aplikasi yang sesuai. Tujuan utama penelitian ini adalah pengembangan persamaan empiris yang menggambarkan hubungan konsentrasi oksalat, tegangan dan waktu anodisasi terhadap diameter pori. Namun penelitian ini juga menganalisis mekanisme pembentukan, karakteristik, dan ketahanan korosi lapisan terintegrasi pada Al7075/SiC. Serta menganalisis pengaruh konsentrasi, temperatur, dan resistivitas larutan elektrolit, dan tegangan anodisasi terhadap diameter dan densitas pori AAO pada aluminium foil. Proses anodisasi Al7075/SiC dilakukan dalam larutan asam sulfat 16% H2SO4 dengan rapat arus 15, 20, 25 mA/cm2 pada 25, 0, -25oC selama 30 menit. Selanjutnya dilakukan proses sealing dalam larutan CeCl3.6H2O + H2O2 pada temperatur ruang dengan pH 9 selama 30 menit. Proses anodisasi pada aluminium foil dilakukan dalam larutan 3 M H2SO4 + 0,5 M; 0,7 M; dan 0,9 M H2C2O4, dan 0,3; 0,5; 0,7 M H2C2O4 selama 40-60 menit. Proses anodisasi dilakukan pada tegangan konstan 35, 40, dan 45 V untuk larutan asam oksalat dan 15 V untuk larutan campuran. Pengamatan dan evaluasi morfologi lapisan pori hasil anodisasi dilakukan menggunakan alat FE-SEM (Field Emission Scanning Electron Microscope), ketahanan korosi material diinvestigasi menggunakan pengujian polarisasi dan EIS, sedangkan analisa kualitatif terhadap morfologi pori (diameter dan densitas) pada AAO menggunakan perangkat lunak ImagePro. Pengembangan persamaan empiris menggunakan metode derajat terkecil dan permukaan respon. Proses terintegrasi yang diaplikasikan pada komposit Al7075/SiC pada temperatur anodisasi 0 oC menghasilkan terbentuknya deposit bulat kaya cerium dengan diameter 64 nm ( 3 nm) yang menutupi seluruh permukaan lapisan oksida dan rongga secara efektif. Proteksi terintegrasi anodisasi dan pelapisan cerium meningkatkan ketahanan korosi hingga 4 order perbesaran dibandingkan tanpa perlindungan akibat terjadinya ikatan saling kunci antara kedua lapisan tersebut. Peningkatan konsentrasi larutan elektrolit asam oksalat, temperatur, tegangan dan waktu celup anodisasi dalam larutan 0,3; 0,5; dan 0,7 M mengakibatkan peningkatan diameter pori permukaan pada AAO. Sedangkan, penambahan asam sulfat dalam asam oksalat menghasilkan pori dengan morfologi diameter pori yang jauh lebih halus dan densitas pori yang jauh lebih besar. Secara umum, densitas pori hanya tergantung pada diameter pori hasil anodisasi, dimana peningkatan diameter pori menghasilkan densitas pori yang semakin menurun. Persamaan empiris hubungan antara tiga faktor anodisasi (konsentrasi asam oksalat, tegangan, dan waktu anodisasi) dengan diameter pori hasil dari penelitian ini adalah : Dp = 0,140625 MVt + 0,33125 MV ? 523542 Mt + 35,64583 M ? 0,04006 Vt + 0,685764 V +1,792431 t ? 42,5053 (derajat terkecil) dan Dp = 33,3 ? 236,3 M ? 1,453 V + 0,3942 t + 7,60 MV (metode derajat satu)

---

Anodizing process in aluminum produces a phenomenal structure in form of metal oxide which is known as Anodic Aluminum Oxide (AAO). AAOis a very useful morfology to improve the adhesion properties for further coating in aluminum alloy and composite aluminum. This phenomenon is related to the presence of interlock bond between AAO and the next layer. The AAO morphology can be modified simply by varying anodizing parameters.

Therefore, selecting appropriate parameters plays an important role in order to obtain the desired pore size. Unfortunately, the preliminary studies did not provide any information on controlling the pore size and density (through increasing/decreasing the concentration of sulfuric acids, voltage, and duration of anodizing to determine pore diameter and density).

For that purpose, in this research some empirical models were built to predict the pore size produced by anodizing process in various parameters. The grand design if this research aims to develop empirical equations which predict the relationship between oxalic acid concentration, anodizing voltage and time to the pore diameter. However, this research also aims to analyze the formation mechanism and of the integrated layer on Al7075/SiC, as well as the enhancement of corrosion resistance resulted from the integrated layer. Moreover, the influence of various anodizing parameters, i.e. resistivity, concentration, temperature, and type of electrolyte on pore characteristics of AAOis also conducted in this study.

Anodizing process of Al7075/SiC was conducted in 16% H2SO4 solution in current densities 15, 20, 25 mA/cm2 at25, 0, -25oC for 30 minutes. Subsequently, cerium sealing process was carried out in CeCl3.6H2O+H2O2 at room temperature and pH 9 for 30 minutes. Anodizing of aluminum foil were carried out in 0,3; 0,5; 0,7M H2C2O4 solution and a mixture solution of 0.5M, 0.7M, and 0.9M H2C2O4 and 3M H2SO4 for 40-60 minutes. Anodizing processes were performed under potentiostatic conditions with constant potentials of 35, 40, and 45V for oxalic solution and 15 V for a mixture solution.

Morphology of AAO layer observations were performed using field emission scanning electron microscopy (FE-SEM) FEI Inspect F50, while the corrosion resistance of materials were investigated by means of polarization and EIS, and qualitative analysis of pore characteristics (pore diameters and densities) accomplised by ImagePro software.

The development of empirical equations using least square and response surface methods Integrated protection by conducting anodization at 0oC prior to cerium sealing in Al7075/SiC leads tothe formation of cerium spherical deposit in the diameter of 64 nm ( 3nm) which effectively covered most of the surface of oxide film as well as cavity. Moreover, this integrated protection enhanced four orders magnification of corrosion resistance than that of bare composite due to interlock bonding between the layers.

The increasing of electrolyte concentration and temperature, as well as voltage and duration of anodizing in 0.3; 0.5; dan 0.7 M oxalic acid leads to the increasing of pore diameter in AAO surface. While, the addition of sulfuric acid in oxalic acid provides much smaller pore diameters and higher pore densities at lower voltages than single electrolyte of oxalic acid. In general, pore density is only dependent on pore diameter, which decreases with the increases of pore diameter. The empirical equations built in this research are : Dp = 0,140625 MVt + 0,33125 MV ? 523542 Mt + 35,64583 M ? 0,04006 Vt + 0,685764 V +1,792431 t ? 42,5053 (least square) and Dp = 33,3 ? 236,3 M ? 1,453 V + 0,3942 t + 7,60 MV (first order model) "

"Memompa larutan hidroklorik ke dalam sumur lapangan migas dikenal sebagai stimulasi pengasaman sumur. Pengasaman dilakukan untuk menghilangkan kerak, karat, puing-puing atau partikulat larut asam lainnya pada permukaan internal pipa guna membersihkan jalan bagi minyak dan gas untuk mengalir dari dalam sumur ke permukaan. Untuk menghindari masalah seperti kebocoran pipa karena korosi, selama pengasaman biasanya diterapkan perlakuan penghambatan oleh inhibitor korosi anorganik yang sebagian besar senyawa ini tidak hanya mahal tetapi juga beracun bagi lingkungan. Sudah banyak riset inhibitor ramah lingkungan dari bahan ekstrak tumbuhan yang telah dilakukan, namun hampir semua riset tersebut tidak pernah di uji secara laboratorium industri maupun uji langsung di lapangan migas sehingga tidak cocok untuk sepenuhnya mengkarakterisasi potensi kemanjuran inhibitor,baik dari sifat ramah lingkungannya maupun sifat teknis di lapangan. Oleh karena itu, tantangan dalam penelitian ini adalah menghasilkan terobosan inhibitor ramah lingkungan yang aplikatif di lapangan migas.

Kandidat ekstrak tanaman yang dipilih untuk pengembangan inhibitor ramah lingkungan adalah Bunga Pinang. Teknik pengujian meliputi uji kehilangan berat, Uji Wheel Test, Polarisasi, Spektroskopi Impedansi Elektrokimia (EIS), Spektroskopi Infra-merah Fourier Transform (FTIR), Uji Toksisitas akut dan Uji di lapangan migas. Hasil pengujian wheel test selama 72 jam pada dosis 20 ml untuk kayu secang didapatkan persentase perlindungan 82.27% dan  bunga pinang 90.07%. Nilai toksisitas akut (LD₅₀₎ untuk bunga pinang adalah 5728 mg/kgbb termasuk dalam kategori “praktis tidak toksik”. Adsorpsi terjadi secara spontan sesuai dengan adsorpsi isotermal Langmuir. Efisiensi hambatan optimal terjadi dengan penambahan pada konsentrasi 20 ml yaitu 96.6% pada pengujian Electrochemical Impedance Spectroscopy (EIS). Hasil polarisasi menunjukkan bahwa ekstrak bunga pinang bekerja melalui inhibisi tipe campuran. Nilai energi bebas adsorpsi –7.026 kJ / mol menunjukkan bahwa adsorpsi molekul inhibitor adalah khas dari adsorpsi fisik.

Hasil uji di lapangan di dapatkan laju korosi 0.134 mm/tahun dengan nilai persentase perlindungan 78% pada dosis 20 ml, sehingga mengkonfirmasi bahwa Bunga Pinang sudah teruji sebagai inhibitor ramah lingkungan di sektor minyak dan gas bumi.

---

Pumping the hydrochloric solution into oil and gas field wells is known as well acid stimulation. Acidification is used to remove scale, rust, debris or other acid-soluble particulates on the internal surface of the pipe to clear a way for oil and gas to flow from the well to the surface. To avoid problems such as pipe leakage due to corrosion, during acidification it is usually applied an inhibitory treatment by inorganic corrosion inhibitors most of which these compounds are not only expensive but also toxic to the environment. There has been a lot of research on environmentally friendly inhibitors from plant extract ingredients that have been carried out, but almost all of this research has never been tested in industrial laboratories or directly in the oil and gas field so it is not suitable to fully characterize the potential efficacy of the inhibitor, both from its environmentally friendly nature and technical properties in the field. Therefore, the challenge in this research is to produce a breakthrough environmentally friendly inhibitor that is applicable in the oil and gas field.

The plant extract candidates selected for the development of environmentally friendly inhibitors are Pinang Flower. Testing techniques include weight loss test, Wheel Test, Polarization, Electrochemical Impedance Spectroscopy (EIS), Fourier Transform Infra-red Spectroscopy (FTIR), Acute Toxicity Test and Oil and Gas Field Testing. The results of wheel test for 72 hours at a dose of 20 ml for secang wood obtained a protection percentage of 82.27% and 90.07% for areca flowers. The acute toxicity value (LD₅₀) for areca flowers is 5728 mg / kg, which is included in the category of "practically non-toxic". Adsorption occurs spontaneously in accordance with Langmuir adsorption isotherm. Optimal inhibition efficiency occurs with the addition of a concentration of 20 ml, namely 96.6% in the Electrochemical Impedance Spectroscopy (EIS) test. The polarization results showed that the betel nut extract worked through a mixture type inhibition. The adsorption free energy value of –7,026 kJ / mol indicates that the adsorption of the inhibitor molecule is typical of physical adsorption.

The field test results obtained a corrosion rate of 0.134 mm / year and a protection percentage value of 78% at a dose of 20 ml, thus confirming that Bunga Pinang has been tested as an environmentally friendly inhibitor in the oil and gas sector."