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"Permintaan air bersih mengalami peningkatan seiring dengan perkembangan suatudaerah. Tersedianya sumber daya menjadi salah satu hal yang perlu diperhatikan.Permasalahan yang dihadapi adalah masih terjadi defisit pemenuhan air bersih dansumber air baku yang masih mengandalkan dari luar DKI Jakarta. Tujuan penelitianadalah mengkaji kualitas pengolahan air limbah supaya dapat digunakan sebagaiair baku untuk air bersih berdasarkan pada proses daur ulang. Metode penelitian iniadalah metode campuran yang terdiri atas metode kualitatif dan kuantitatif. Hasilpenelitian menunjukkan kualitas pengolahan air limbah lebih baik dibandingkandengan kualitas air sungai pada parameter BOD, COD, dan amoniak. Nilai BCRdari teknologi MBBR adalah 2,51 dan teknologi AOP-BMG adalah 1,5. Solusialternatif dari metode AHP untuk meningkatkan pemenuhan air bersih berdasarkanhasil pengolahan air limbah adalah pengembangan teknologi MBBR dengan bobotnilai 0,469. Maka didapatkan potensi pengolahan air limbah berdasarkan baku mutuserta kelayakan teknologi MBBR dari segi ekonomi dan bobot penilaian.

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The demand for clean water continues to increase in line with the development of

an area. Availability of resoruces is one thing that needs to be considered. The

problems faced is that there is still deficit in the fulfillment of clean water and raw

water sources that still rely on from outside DKI Jakarta. The research objective

was to assess the quality of wastewater treatment so that it can be used as raw water

for clean water from reuse process. The research method used is a mixed method

consisting of qualitative and quantitative methods. The results showed that the

quality of wastewater treatment was better than the quality of river water in the

parameters of BOD, COD, and ammonia. The BCR value of MBBR technology is

2,51 and the AOP-BMG technology is 1,5. An alternative solution to the AHP

method to increase the fulfilment of clean water based on the results of wastewater

treatment is the development of the MBBR technology with a weighting value of

0,469. So it can be a potential for wastewater treatment based on quality standards

and the feasibility of MBBR technology from an economic perspective and an

assessment weight."

"Limbah amonia sebagai polutan yang dihasilkan dari berbagai industri kimia seperti industri pupuk, industri petrokimia sangat sulit untuk diolah dengan berbagai metode konvensional yang sudah ada. Metode yang digunakan untuk mendegradasi limbah cair yang mengandung amonia adalah metode plasma ozone nanobubble, karena metode ini tidak mengeluarkan banyak biaya, serta ramah lingkungan. Reaktor plasma yang digunakan merupakan dielectric barrier discharge yang bekerja dengan menerapkan proses oksidasi lanjut dengan mengandalkan spesi aktif yang kuat yaitu radikal hidroksil (·OH), dan ozon (O3). Penelitian ini bertujuan untuk menguji kinerja penggunaan Reaktor Plasma Ozon Nanobubble dalam mendegradasi kandungan senyawa amonia dalam limbah cair dengan variasi pH asam dan basa, variasi tegangan sebesar 5, 15, dan 17 kV, variasi laju alir gas sebesar 1, 3, 5 L/menit, dan variasi jenis gas umpan berupa udara dan oksigen. Berdasarkan penelitian yang telah dilakukan, selama proses degradasi dalam waktu 30 menit, dengan kondisi yang maksimum, reaktor plasma ozon nanobubble dapat mendegradasi limbah amonia dengan persentase degradasi sebesar 55,17% dengan kondisi pH limbah cair sebesar 10, tegangan plasma sebesar 17 kV, dan laju alir oksigen sebesar 5 L/menit.

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Ammonia wastewater as a pollutant, produced from various chemical industries such as fertilizer industry, petrochemical industry, and it is very difficult to be processed using various conventional methods that already exist. In this research, the method used to degrade wastewater containing ammonia is Plasma Ozone Nanobubble method, because this method does not cost much, and is environmentally friendly. The plasma reactor used is dielectric barrier discharge which works by applying an Advanced Oxidation Process by relying on strong active species, hydroxyl radical (·OH), and ozone (O3). This study aims to examine the use of plasma ozone nanobubble in degrading ammonia compounds in wastewater under acidic and alkaline conditions, with concentration of ammonia wastewater are 50, and 200 mg/L, variations in the contact time of ozone nanobubble with wastewater for 1,5,10, 15, and 30 minutes, variation of the plasma reactor voltage are 5, 15, and 17 kV, with gas fluid used for ozone production are air and pure oxygen. Based on the research that has been done, in the process of 30 minutes, with maximum conditions, the nanobubble ozone plasma reactor can degrade with percentage of ammonia removal of 55,17% with pH of 10; plasma reactor voltage is 17 kV; and oxygen flowrate 5 L/minute."

"Air limbah dari industri tahu, sebagai salah satu sumber pencemaran air di Indonesia, membutuhkan metode pengolahan yang efektif untuk memenuhi standar peraturan pemerintah. Dalam penelitian ini, pengolahan air limbah dari industri tahu menggunakan kombinasi proses koagulasi-flokulasi dengan teknologi Mikrofiltrasi (MF) dan Osmosis Balik (RO). Tawas digunakan sebagai koagulan dengan variasi dosis antara 100 ppm hingga 800 ppm untuk menentukan dosis optimal. Tekanan trans-membran (TMP) optimal pada membran ditentukan dengan menggunakan variasi 1 bar, 1,5 bar, dan 2 bar pada proses MF, dan 4 bar, 5 bar, 6 bar pada proses RO. Air limbah tahu awal memiliki pH, padatan terlarut total (TDS), padatan tersuspensi total (TSS), kekeruhan, Chemical Oxygen Demand, dan Biological Oxygen Demand (BOD) pada kisaran 3,5-5, 2130-2357 mg / L, 312-780 mg / L, 370-826 FAU, 6135-8879 mg / L, dan 4200-6765. Hasilnya menunjukkan bahwa dosis tawas optimal adalah 300 ppm, TMP optimum MF adalah 1,5 bar, dan 6 bar untuk RO. Hasil akhir telah memenuhi standar peraturan pemerintah. Oleh karena itu, kombinasi ini efektif dalam mengurangi parameter yang sesuai dengan standar air limbah tahu.

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Wastewater from tofu industry, as one of the water pollution sources in Indonesia, needs an effective treatment method in order to meet the government regulation standard. In this research, the treatment for wastewater from tofu industry is using a combination of coagulation-flocculation process with Microfiltration (MF) and Reverse Osmosis (RO) technology. Alum is used as the coagulant with variation of dose between 100 ppm to 800 ppm in order to find the optimum dose. Optimum transmembrane pressure in the membrane technology was determined by using a variation of 1 bar, 1.5 bar, and 2 bar at MF process, and 4 bar, 5 bar, 6 bar at RO process. The initial tofu wastewater has pH, total dissolved solid (TDS), total suspended solids (TSS), turbidity, Chemical Oxygen Demand (COD), and Biological Oxygen Demand (BOD) in the ranges of 3.5-5, 2130-2357 mg /L, 312-780 mg /L, 370-826 FAU, 6135-8879 mg /L, 4200-6765, respectively. The result shows that the optimum alum dose was 300 ppm, the optimum TMP of MF is 1.5 bar, and 6 bar for RO. The final product has meet the government regulation standard; therefore, this combination is effective in reducing all the parameters for tofu wastewater standard."

"The purposes of this research are to identify & characterize the wastewater, discharged from a traditional market and also to evaluate its Sewage Treatment Plant performance. Case study is done in Glodok Traditional Market from November until December 2010. Wastewater identification and characterization took place in wet lot, which consist of fish lot, chicken lot, and meat lot. The source of fish lot wastewater are fish washing and rinsing, shrimp shell and squid cleaning, melting ice cube from fish storage, and hand washing from the seller itself; in chicken lot, wastewater is discharge from chicken slaughter; while in meat lot, the wastewater is released from washing cow stomach wall activities (in the making of tripe).Result of the research in identification showed that the discharge of waste water can be identified using flow rate based on selling volume. Meanwhile, the result of characterization are: Fish lot : pH = 6.153, TSS = 786.667 mg/L, Total N = 123.330, Ammonia = 101.333, Total P = 24.981, BOD = 1109.388, COD = 2037.248, Oil and grease = 1004.5 ; Chicken lot : pH = 5.893, TSS = 666.667 mg/L, Total N = 75.557 mg/L, Ammonia = 54 mg/L, Total P = 16.247 mg/L, BOD = 598.963 mg/L, COD = 1392.304 mg/L, oil and grease = 518 mg/L; Meat lot : pH = 10.553 mg/L, TSS = 460 mg/L, Total N = 32.720 mg/L, Ammonia = 12 mg/L, Total P = 9.43 mg/L, BOD = 100.031 mg/L, COD = 1536.240 mg/L, oil and grease = 668 mg/L.Result of STP evaluation showed that STP plan which is made based on office and hotel biological loading causing the performance of STP is not optimum. It can be displayed from the value of TSS and oil & grease of the effluent, whose not meet by the quality standard of Kepmenlh 112 tahun 2003. The low performance of STP also can be seen from high amount of ammonia in effluent because the process itself only can remove BOD without followed by nitrification."

"Pengelolaan air limbah di rumah sakit diperlukan untuk mengurangi beban pencemar yang terkandung di dalam air limbah. Pengelolaan air limbah di rumah sakit secara terpadu dilakukan mulai dari reduksi pada sumber, pengolahan, sampai ke pembuangan. Masalah dalam penelitian ini adalah rumah sakit sudah melakukan upaya pemanfaatan air limbah namun dihentikan karena terkendala biaya operasional. Tujuan penelitian ini adalah untuk menganalisis pengaruh penerapan produksi bersih dalam pengelolaan IPAL melalui identifikasi peluang inefisiensi pengelolaan air limbah serta upaya reuse air hasil olahan. Metode yang digunakan menggunakan pendekatan kuantitatif menggunakan mix method. Hasil penelitian menunjukkan bahwa ditemukan adanya inefisiensi pada pengelolaan IPAL dari aspek manusia, metode, material, dan mesin. Pekerja di RS Kanker Dharmais sudah memiliki tingkat keterlibatan yang baik pada upaya penerapan produksi bersih IPAL ditinjau dari tingkat pengetahuan, sikap, dan perilaku karyawan yang baik. Efisiensi biaya operasional yang didapatkan melalui penerapan produksi bersih sebesar Rp.762.375.500/tahun. Kesimpulan penelitian ini adalah Implementasi produksi bersih dapat meningkatkan kinerja IPAL melalui optimasi sistem dan teknologi IPAL.

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Wastewater management in hospitals is needed to reduce the pollutant load contained in wastewater. Integrated management of wastewater in hospitals is carried out starting from reduction at source, processing, to disposal. The problem in this study is that the hospital has made efforts to utilize wastewater but was discontinued due to operational costs. The purpose of this study was to analyze the effect of implementing cleaner production in WWTP management through identifying opportunities for inefficiency in wastewater management and efforts to reuse processed water. The method used is a quantitative approach using a mix method. The results showed that there were inefficiencies in WWTP management from the human, method, material, and machine aspects. Workers at Dharmais Cancer Hospital already have a good level of involvement in efforts to implement cleaner production on WWTP in terms of the level of knowledge, attitudes, and good employee behavior. The operational cost efficiency obtained through the application of cleaner production is Rp.762.375.500/year. The conclusion of this study is that the implementation of cleaner production can improve the performance of WWTPs through system optimization and WWTP technology.."

"Dalam rangka pengendalian pencemaran lingkungan, Instalasi Pengolahan Air Limbah (IPAL) memegang peranan penting dalam mengolah air limbah agar sesuai dengan baku mutu sebelum di buang ke lingkungan. Akan tetapi tidak semua IPAL telah bekerja secara maksimal sehingga evaluasi secara berkala harus dilakukan untuk mengetahui masalah dan upaya apa yang dapat dilakukan untuk meningkatkan kualitas pengolahan IPAL tersebut. Penelitian ini bertujuan untuk mengevaluasi terhadap IPAL 1 Jababeka yang berfungsi untuk mengolah air limbah pada Kawasan Industri 1 dan Kawasan Industri 7 yang berada di dalam Kawasan Industri Jababeka (KIJ). Evaluasi dilakukan dengan membandingkan efisiensi pengolahan aktual dengan literatur terkait, selain itu evaluasi juga dilakukan terhadap parameter desain dan standar operasional prosedur (SOP). Selain itu, evaluasi juga dilakukan dengan melakukan simulasi proses dan opeasi IPAL dengan menggunakan perangkat lunak STOAT. Hasil pengujian menunjukkan bahwa untuk efisiensi penyisihan IPAL 1 Jababeka pada pengolahan primer diperoleh nilai efisiensi BOD 50%; efisiensi COD 20,5% dan efisensi TSS 18,45%, pada pengolahan sekunder diperoleh nilai efisiensi penyisihan BOD 80%; efisiensi COD 91,22% dan efisiensi TSS 95,24% serta efisiensi IPAL secara keseluruhan adalah sebesar BOD 90%; efisiensi COD 93,02% dan efisiensi TSS 96,12%. Berdasarkan nilai tersebut diketahui bahwa masih perlu dilakukan peningkatan efisiensi dari unit-unit pengolahan IPAL 1 Jababeka. Parameter desain dari unit pengolahan IPAL 1 Jababeka juga belum seluruhnya memenuhi kriteria desain hal ini dikarenakan desain IPAL yang ada saat ini diperuntukan untuk mengolah air limbah dengan debit sebesar 18.000 m3/hari sedangkan rata-rata air limbah yang diolah oleh IPAL 1 Jababeka saat ini adalah sebesar 12.431 m3/hari. Berdasarkan data yang diperoleh selanjutnya juga dilakukan permodelan dengan menggunakan STOAT untuk mengetahui parameter apa saja yang paling signifikan dalam peningkatan efisiensi pengolahan IPAL yang kemudian diketahui bahwa debit air limbah merupakan parameter paling signifikan dalam mempengaruhi efisiensi penyisihan parameter TSS dan BOD.

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In order to control the environmental pollution, wastewater treatment plant (WWTP) plays an important role in treating the wastewater to meet the quality standards before discharged to environment. However, not all WWTP have worked optimally so periodic evaluation must be carried out to find out the problem and effort can be made to improve the quality of WWTP treatments, this study conducted an evaluation of Jababeka’s WWTP 1 that fuctions to treat wastewater of Industrial Zone 1 and Industrial Zone 7 at Jababeka Industrial Estate (KIJ). Evaluation is conducted by comparing the actual process efficiency with related literature, in addition the evaluation is also carried out on design parameters and standard operational procedures (SOP). In addition, the evaluation was also conducted by simulating the process and operation of WWTP using STOAT software.The test results show that the removal efficiency for BOD, COD and TSS at primary treatment are 50%, 20.5% and 18.45% respectively, at secondary treatment are 80%, 91.22% and 95.24% respectively and WWTP’s overall efficiency are 90%, 93.02% and 96.12% respectively. Based on this result, it can be inferred that is still necessary to increase the removal efficiency of these unit. The design parameters of Jababeka’s 1 WWTP treatment units also do not fully meet the design criteria because the existing WWTP design is intended to treat wastewater with a discharge of 18,000 m3/day while the average wastewater treated by Jababeka’s 1 WWTP currently is amounting 12,431 m3/day. Based on the data obtained thereafter also carried out modeling using STOAT to find out which parameters are the most significant in increasing the efficiency of WWTP treatment which later found that the discharge of wastewater is the most significant in order to remove the TSS and BOD parameter."

"Peningkatan perkembangan industri minyak dan gas di Indonesia berbanding lurus dengan semakin banyaknya limbah air berminyak yang dihasilkan. Limbah air berminyak mengandung kadar kontaminan seperti COD, TDS, TSS, pH, dan kekeruhan yang tinggi serta cenderung memiliki warna yang pekat. Pada penelitian ini, dilakukan proses pemisahan limbah air berminyak menggunakan proses ultrafiltrasi (UF) membran poliviniliden fluorida (PVDF). Namun, sifat hidrofobik pada polimer PVDF dapat meningkatkan fouling yang terjadi pada saat proses UF. Sehingga, pada penilitian ini dilakukan modifikasi dengan zat aditif polivinilpirolidon (PVP) serta pelarut dimetilasetamida (DMAc) yang membantu pembentukan struktur morfologi pada membran. Sintesis membran dilakukan dengan metode presitipasi imersi dengan variasi massa PVP 0,1 ; 0,2 dan 0,3 gram. Karakterisasi pada membran dilakukan untuk mengetahui sifat pada membran menggunakan uji SEM, FTIR, sudut kontak, uji tarik, dan uji porositas. Digunakan proses perlakuan terdahulu sebelum UF untuk meningkatkan rejeksi pada permeat. Kemudian dilakukan variasi tekanan pada membran dengan variasi massa PVP optimal yakni 0,1 gram pada 1 dan 2 bar. Nilai fluks yang dihasilkan meningkat seiring dengan meningkatnya massa PVP pada membran. Pada variasi membran optimal didaptkan rejeksi untuk COD, TDS, TSS, kekeruhan dan pH secara berturut-turut adalah 82,05% ; 44,46% ; 90,38% ; 85,42% ; 7,1.

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The rapid growth of Indonesia's oil and gas industry has a linear effect on the growth of wastewater produced by the industry. A high level of COD, TDS, TSS, color, turbidity, and pH usually characterizes oily wastewater. In this study, the process of separating oily wastewater will be conducted using a polyvinylidene fluoride (PVDF) membrane ultrafiltration (UF) process. However, the hydrophobic nature of the PVDF polymer can increase the fouling that occurs during the UF process. Therefore, in this study PVDF membrane is modified with the additive polyvinylpyrrolidone (PVP) with dimethylacetamide (DMAc) as a solvent which helps the formation of the morphological structure of the membrane. Membrane synthesis was conducted by immersion precipitation with a mass variation of PVP 0.1; 0.2; and 0.3 grams. Characterization of the membrane was carried out to determine the properties of the membrane using the SEM test, FTIR, contact angle, tensile test, and porosity test. The pre-treatment process is used before UF to increase the rejection of the permeate. Then the pressure variation on the membrane will be carried out with the optimal PVP mass variation of 0,1 gram at 1 and 2 bar. The resulting flux value increases with increasing PVP mass on the membrane. The rejection obtained at optimal membrane variations for COD, TDS, TSS,turbidity, and pH were 82.05%; 44.46%; 90.38%; 85.42%; 7.1."

"IPAL Rumah Sakit Universitas Indonesia sudah lama mengalami tantangan dalam menyisihkan kandungan fenol yang sering melebihi baku mutu. Anomali nilai COD pada penelitian sebelumnya dan kecenderungan efluen yang lebih tinggi dibandingkan influen mengharuskan COD sebagai parameter yang juga membutuhkan perhatian. Penelitian ini bertujuan (1) menganalisis teknologi pengolahan air limbah potensial berdasarkan kajian literatur dan kondisi eksisting IPAL; (2) Menganalisis konsentrasi fenol dan COD di sump pit, netralisasi, sterilisasi, grease trap, inlet, dan outlet IPAL; dan (3) mengevaluasi efektivitas penyisihan fenol dan COD teknologi terpilih dengan simulasi laboratorium. Penelitian ini menggunakan decision matrix untuk memilih lima teknologi potensial (adsorpsi, fotokatalisis, fitoremediasi, ion exchange, dan chemical precipitation). Hasil menunjukkan teknologi yang terpilih adalah adsorpsi dan chemical precipitation. Kemudian, hasil sampling menyatakan bahwa sumber konsentrasi fenol tertinggi adalah toilet (sump pit) sebesar 0.258 mg/L. Eksperimen jar test dilakukan dengan dosis yang berbeda, baik untuk FeCl3 (40, 80, 120, 160, dan 200 mg/L), maupun PAC (0.09, 0.18, 0.45, 0.90, dan 1.80 g/L). Pengadukan cepat (40 rpm) dan lambat (120 rpm) masing - masing dilakukan selama 1 menit dan 20 menit untuk chemical precipitation, sedangkan pengadukan sebesar 150 rpm selama 3 jam untuk adsorpsi. Sampel dianalisis, ketika waktu pengendapan mencapai 15 menit (chemical precipitation) dan 30 menit (adsorpsi). Simulasi menunjukkan dosis optimum (160 mg/L) FeCl3 mampu menyisihkan 68% fenol dan 43.6% COD. Sedangkan adsorpsi mengungkapkan bahwa PAC pada dosis optimum 1.8 g/L mengeradikasi fenol (92%) dan COD (70%). Secara keseluruhan dapat disimpulkan bahwa adsorpsi merupakan teknologi potensial terbaik untuk IPAL Rumah Sakit Universitas Indonesia.

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Universitas Indonesia Hospital WWTP has long experienced challenges in removing phenol content which often exceeds quality standards. The anomaly in the COD value in previous studies, as well as the tendency for the effluent to be higher than the influent which requires COD to be a parameter that also needed attention. For this reason, research was carried out on optimizing phenol and COD levels in WWTP RSUI. This study aims to (1) analyze the potential wastewater treatment technology based on a review of the literature and the existing WWTP conditions; (2) Analyze the concentration of phenol and COD in the sump pit, neutralization, sterilization, grease trap, inlet and outlet of WWTP; and (3) evaluating the phenol and COD removal effectiveness of the selected technology with laboratory simulations. This study uses a decision matrix to select five potential technologies (adsorption, photocatalysis, phytoremediation, ion exchange, and chemical precipitation). The results show that the technology that has been selected through a decision matrix are adsorption and chemical precipitation. Jar test experiments were carried out with different doses, both for FeCl3 (40, 80, 120, 160, and 200 mg/L), and PAC (0.09, 0.18, 0.45, 0.90, and 1.80 g/L). Rapid (40 rpm) and slow (120 rpm) mixing were carried out for 1 minute and 20 minutes respectively for chemical precipitation, while mixing at 150 rpm for 3 hours for adsorption. Samples were analyzed, when the settling time reached 15 minutes (chemical precipitation) and 30 minutes (adsorption). Simulation of the optimum dose (160 mg/L) of FeCl3 was able to remove 68% phenol and 43.6% COD. While adsorption revealed that PAC at the optimum dose of 1.8 g/L eradicated phenol (92%) and COD (70%). Overall, it can be said that adsorption is the best potential technology for Universitas Indonesia Hospital WWTP."

"Rencana Pengembangan Lapangan Migas Terbatas di Blok Tonga oleh PT. Energi Mega Persada Tonga menyebabkan penambahan produksi minyak bumi menjadi1.700 barel minyak per hari. Meningkatnya produksi minyak bumi akan diikuti oleh jumlah produced water yang semakin besar pula mencapai 4.000 barel air per hari. Oleh karena itu, muncul pilihan untuk mendaur ulang produced water menjadi air bersih yang dapat dimanfaatkan untuk kebutuhan nonpotable operasional lapangan seperti flushing toilet, pengairan taman, pencucian alat dan kendaraan. Berdasarkan uji laboratorium dan analisis data sekunder (untuk parameter BOD) didapatkan kualitas produced water dari unit pengolahan eksisting sebagai berikut : BOD 39,46 mg/L ; COD 48 mg/L ; TSS 15 mg/L; TDS 84,1 mg/L; Ammonia 0,06 mg/L ; Phenol < 0,001 mg/L; Sulfida 0,01 mg/L; Pb < 0,023 mg/L; Zn < 0,006 mg/L; Cu < 0,006 mg/L; serta minyak dan lemak sebesar < 1,13 mg/L. Alternatif teknologi daur ulang yang dianalisis meliputi pengolahan dengan chemical precipitation, pengolahan membran dengan reverse osmosis, dan pengolahan biologis dengan fitoremediasi wetland menggunakan tanaman akar wangi. Target kualitas air daur ulang mengacu pada Peraturan Pemerintah No.82 tahun 2001 peruntukkan air kelas 2. Pemilihan teknologi pengolahan lanjutan produced water dilakukan dengan metode pembobotan yang memperhitungkan parameter removal kontaminan dan biaya, serta mempertimbangkan luasan lahan yang diperlukan dan dampak lingkungan. Dari perhitungan yang dilakukan, unit pengolahan lanjutan yang terpilih adalah fitoremediasi wetland menggunakan tanaman akar wangi. Melalui pengolahan tersebut, didapatkan kualitas efluen berupa BOD 2,34 mg/L ; COD 4,8 mg/L ; TSS 1,5 mg/L; TDS 84,1 mg/L; Ammonia 0,06 mg/L ; Phenol 0,0007 mg/L; Sulfida 0,002 mg/L; Pb 0,0067 mg/L;Zn 0,0006 mg/L; Cu 0,0006 mg/L; serta minyak dan lemak sebesar 0,098 mg/L.Total biaya investasi awal yang diperlukan sebesar Rp 1.320.855.290,00.

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Development Plan of Oil & gas Limited Block in Tonga by PT Energy Mega Persada Tonga will cause the additional of petroleum production up to 1.700 barrels of oil per day. The increased petroleum production will be followed by the number of produced water which are getting bigger too until reached 4.000 barrels of water per day. Therefore, it appears the option to recycle produced water into clean water that can be used for the needs of the operational field as nonpotable needs, as flushing toilets, watering the garden, and also washing equipment and vehicles. Based on laboratory tests and analysis of secondary data (for parameters BOD), the quality of produced water from the existing processing units as follows: BOD 39,46 mg/L; COD 48 mg/L; TSS 15 mg/L; TDS 84,1 mg/L; Ammonia 0.06 mg/L; Phenols < 0,001 mg/L; Sulfide 0,01 mg/L; Pb < 0,023 mg/L;Zn < 0,006 mg/L; Cu < 0,006 mg/L; and oil and grase < 1,13 mg/L. Alternative recycling technology which is analyzed covers chemical precipitation, reverse osmosis, and wetland plant use V. zizanioides. The target of the quality of water recycling are referenced to PP No.82/2001 designated class 2 water. Selection of advanced processing technology produced water is done by weighting method that takes into account parameters of contaminant removal and costs, as well as considering the land area required and the environmental impact. From the calculation, the advanced processing unit selected is phytoremediation wetland by plants Vetiver. Through the treatment, effluent quality is obtained in the form of BOD 2,34 mg/L ; COD 4,8 mg/L ; TSS 1,5 mg/L; TDS 84,1 mg/L; Ammonia 0,06 mg/L ; Phenol 0,0007 mg/L; Sulfida 0,002 mg/L; Pb 0,0067 mg/L;Zn 0,0006 mg/L; Cu 0,0006 mg/L; also oil and grase 0,098 mg/L. The total cost of the initial investment required of Rp 1.320.855.290.00."

"Pabrik pengolahan air limbah ini berada di 594 km timur dari Perth di kota Kalgoorlie. Region ini dikenal dengan industri pertambangan emas, yang diketahui mengggunakan jumlah air yang besar dan jejak lingkungan yang ditinggalkan. Hasil riset dari CSIRO mengatakan bahwa operasional tambang emas membutuhkan lebih dari 250ML air untuk memproduksi 1 ton emas. Selain itu, situasi pertambangan emas saat ini di Kalgoorlie meninggalkan efek yang cukup drastic pada lingkungan sekitar. Di Kalgoorlie terdapat 26 sumber air yang dipergunakan untuk industri pertambangan. Selain itu, bendungan yang dipergunakan untuk menyimpan air hasil proses berbahaya bagi lingkungan sekitar. Tujuan utama dari pabrik ini merupakan untuk mendapatkan air proses pertambangan dari industri pertambangan emas untuk diolah kembali agar dapat dipergunakan kembali. Air yang dihasilkan akan menjadi 80% kelas C dan 20% kelas B.

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The wastewater treatment plant (WWTP) is located 594km east of Perth in the town of Kalgoorlie. This region has a prolific gold mining industry, an industry well known for its large water consumption and large environmental footprint. Research from CSIRO found that a gold mine operation requires over 250ML of water to produce a single tonne of gold. Moreover, current gold mining operations over the last few decades have devastated the natural landscape and quality of local waterways through the excessive sourcing of water from ground water reserves. There are a total of twenty-six operational bore fields in Kalgoorlie to supply water to all mining operations. Furthermore, tailing dams used to store processed mine water have caused further damage to waterways through the continual seepage back into underground reserve which has affected drinking water supplies. The sum of this reported damage over many years, further exacerbated by the call for more sustainable mining operations has allowed Gold Wastewater to see the benefits and longevity of investing in the area. Ultimately, the main purpose of the plant is to receive mine tailings from local gold mining operations, to process the tailings water up to re-use quality, and to return this water to the same mine operations in large quantities thus reducing the load on local water supplies. The water to be returned to mining operations will fall under Class C and will make up 80% of the water produced. The remaining 20% of water will undergo further processing to Class B, available for watering of parks, gardens and sports facilities, supporting the green vision of Kalgoorlie’s community."