Hasil Pencarian  ::  Simpan CSV :: Kembali

"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.

---

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."

"Poliviniliden fluorida (PVDF) merupakan bahan polimer yang lazim digunakan untuk membran ultrafiltrasi. Namun, sifat hidrofobik yang dimiliki oleh PVDF menghasilkan membran dengan sifat anti-fouling yang buruk dalam proses filtrasi. Sehingga, pada penelitian ini, membran yang berbahan dasar PVDF akan dimodifikasi dengan aditif polivinilpirolidon (PVP). Membran flat sheet dipreparasi menggunakan metode presipitasi imersi dengan variasi massa PVP sebanyak 0,1; 0,15 dan 0,2 gram. Membran yang telah dipreparasi kemudian dikarakterisasi menggunakan SEM, FTIR, serta sudut kontak. Membran kemudian digunakan untuk mengolah limbah cair batik. Sebelum digunakan sebagai umpan ultrafiltrasi, metode koagulasi-flokulasi dengan koagulan PAC digunakan sebagai pre-treatment limbah. Limbah cair batik kemudian difiltrasi menggunakan membran PVDF/PVP dengan variasi tekanan umpan yaitu 4, 5, 6, dan 7 bar. Nilai fluks air bersih dan fluks permeat yang dihasilkan pada penelitian ini meningkat dengan bertambahnya penambahan massa PVP pada larutan cetak. Rejeksi warna dan COD yang dihasilkan pada penelitian ini memiliki rentang besaran dari 32,45% hingga 58,11% dan 8,91% hingga 14,95% berturut-turut; sedangkan rejeksi TDS dan konduktivitas yang dihasilkan memiliki rentang besaran dari 4,83% hingga 6,95%.

---

Polyvinylidene fluoride (PVDF) is commonly used polymeric material for the fabrication of ultrafiltration (UF) membranes. However, the hydrophobic nature of PVDF leads to poor membrane performance with low anti-fouling properites during filtration process. Hence, the PVDF-based flat sheet membrane was modified with polyvinylpyrrolidone (PVP) as additive. PVDF/PVP flat sheet membrane preparation was carried out by the immersion precipitation method with a variation of PVP mass 0.1; 0.15 and 0.2 grams. The membrane produced is then characterised using SEM, FTIR and contact angle. Prior to membrane application on treating batik wastewater, pre-treatment is carried out on Batik wastewater using coagulation and flocculation methods using PAC as coagulant. Batik wastewater from the pre-treatment is then filtered with PVDF/PVP membrane with pressure variations of 4, 5, 6, and 7 bars. In this application, the water and permeate fluxes are increased in accordance with the increase in the addition of PVP. The colour and COD rejections achieved in this research are in value of 32.45% until 58.11% and 8.91% until 14.95% respectively. The TDS and conductivity rejections achieved in this research are in value of 4.83% until 6.95%."

"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."

"processes of Biological treatment intend to reduce the organic matter content by using microorganisms. Problems, which often occur in the treatment process, include the Wastewater Treatment Plant (WWTP) being planned for treating domestic wastewater only, but in fact the WWTP often receives non-domestic wastewater particularly direct or indirect faecal deposits. There are 13 simultaneous systems of nonlinear differential equations using the method of Runge-Kutta-Fehlberg (RKF45). Data validation is measured in a facultative stabilization pond at a distance of 0 m, 25 m, 50 m and 75 m respectively. Samples are taken at the inlet and outlet of the pond covering the concentration of Bacteria (B), Algae (A), Zooplankton (Z), Organic Matter (OM), Detritus (D), Organic Nitrogen (ON), Ammonia (NH3), Organic Phosphorus (OP), Soluble Phosphorus (SP), Dissolved Oxygen (DO), Total Coliform (TC), Faecal Coliform (FC), and Biochemical Oxygen Demand (BOD). The research comparing observation and count data results in 11 kinds of concentration that have a relative error <20% and 2 concentrations > 20%, namely Chemical Oxygen Demand (COD) and Faecal Coliform.(FC). Wastewater quality is predicted with 45o angle charts and tolerance ± 20%, respectively for BOD (76.8%), COD (57.7%) and DO (81.9%). The model, as a means for performance evaluation of the WWTP, is appropriate for Class II water quality standards."

"This present study is aimed at removing phenol compounds in wastewater by using a Contact Glow Discharge Electrolysis (CGDE) reactor. To start with, the effect of voltage to direct current connections in a CGDE reactor was investigated in order to estimate several possibilities for optimum voltage for phenol degradation. Several parameters were studied for phenol treatment including the effects of voltage, electrolyte concentration, anode depth, and the presence of Fe2+ ions. Production of hydrogen peroxide, the percentage of phenol degradation, and energy consumption were used as main research indicators. The optimum condition was found at 700 V, in 0.03 M Na2SO4, and an anode depth of 5mm. The phenol degradation was valued at 40.83% after the first 15 minutes in the process, with an energy consumption of 278 kJ/mmol of phenol. Under the same conditions, with an addition of 20 mg/L of Fe2+ ions, the phenol degradation shot up to 92.57% and energy consumption significantly decreased to 127 kJ/mmol. The largest phenol degradation was obtained at 99.6% after 90 minutes during the experiment. The results pointed out a promising path for phenol treatment in wastewater by utilizing a CDGE reactor with recommended operating conditions which were obtained during this study."

"This paper presents the efficiency improvement in aerobic wastewater treatment technology through the application of a microbubble generator (MBG) for aeration. Aeration using an MBG is accomplished through water circulation and does not need air compressors, making it more energy efficient than conventional aerators. The MBG aerobic system with the variations on liquid flow rate (Q1) and airflow rate (Qg) combination was tested using artificial wastewater with a typical composition of organic waste. Experimental data were evaluated by means of a simplified mathematical model to systematically compare different MBG schemes. The study confirmed that the soluble chemical oxygen demand (SCOD) removal efficiency was significantly affected by the Qg values. Lower Qg values were preferable because they tended to have higher soluble chemical oxygen demand (SCOD) removal efficiency. However, the microbubbles were less stable at lower Qg due to the high incidence of bubble collisions. The study concluded that for applications in an actual aerobic waste treatment pond, the positioning of the MBG in the pond had to be carefully designed to minimize the collision tendency."