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de Almeida Batista, Leonard, Claudio Mudadu Silva, Erika Nascimben Santos, Jorge Luiz Colodette, Ana Augusta Passos Rezende, and José Cola Zanuncio. "Partial circuit closure of filtrate in an ECF bleaching plant." Nordic Pulp & Paper Research Journal 35, no. 3 (September 25, 2020): 471–78. http://dx.doi.org/10.1515/npprj-2020-0028.
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AbstractThe bleaching sector of the wood pulp industry is its largest effluent generator. The aim of this study was to reuse the bleaching filtrate in order to reduce water consumption. The experiment was conducted by simulating the D0(EP)D1 bleaching sequence and recirculating different amounts of filtrate from the oxidation stage to control the pulp consistency of the delignification stage (pre-O). Physical, mechanical, chemical and optical properties of the pulp were studied. The accumulation of the non-process elements (NPE) and their effects were evaluated with the Aspen-Plus® computer simulator. The results of the computational modeling were satisfactory. The recirculation of filtrates increased the saturation index of the system by 19 %, but remained at sub-saturation levels. The pulp viscosity and elongation remained statistically stable. Recirculation of up to 50 % of the filtrate did not produce differences in pulp brightness; however, there were slight losses in the pulp resistances. In order to maintain 84 % ISO brightness, there was a higher consumption of the bleaching reagents. Up to 50 % of recirculation of the filtrates was accomplished without jeopardizing the system and the pulp quality and resulted in a savings of 55 m3 h−1 of water – 7 % of the consumption of the entire mill.
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Sereda, T. G., S. N. Kostarev, and E. N. Elancheva. "Study Safety Environmental Protection Landfills Using Models Anaerobic Digesters." Applied Mechanics and Materials 682 (October 2014): 339–45. http://dx.doi.org/10.4028/www.scientific.net/amm.682.339.
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The model of an anaerobic bioreactor in which the basic biochemical reactions under the influence of an acting atmospheric precipitation, technological modes recirculation of a filtrate and participation of alive substance is developed transform a file of waste products in three phase system (gas, a liquid and firm substance).
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Jour, Pia, Karin Lindgren, Katarina Gutke, and Johan Wallinder. "Decreased water usage in a softwood ECF bleaching sequence—full mill simulations." June 2018 17, no. 06 (July 1, 2018): 353–60. http://dx.doi.org/10.32964/tj17.06.353.
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In this study, an elemental chlorine free (ECF) bleach plant with a D0(EOP)D1(EP)D2 sequence was studied with the aim of identifying options for significantly decreasing (fresh) water usage in the bleach plant and decreasing the effluent volume. A base-case simulation model for a softwood kraft market pulp mill was made based on a reference model representing the best available techniques as well as data produced in an extensive laboratory pulp bleaching study. This model was used to evaluate increased closure within the bleach plant and the recirculation of bleach plant effluent to the brownstock system and their effects on both the bleach plant and the recovery cycle. The results indicate that it is possible to reduce the fresh water consumption from 15 metric tons/a.d. metric ton in the base case to about 2 metric tons/a.d. metric ton, without increasing the carryover of chemical oxygen demand (COD) to the pulp machine. Nonprocess elements in wood contribute to the levels of metals found in the bleach plant and thus to the risk of precipitates such as calcium oxalate, barium sulfate, and calcium carbonate. The risk of precipitates forming is a key factor determining the possible degree of closure. In addition, chloride concentration in the black liquor is another important factor that is affected by recirculating bleach plant filtrate to the brownstock washer and by the grade of the sodium hydroxide used in the mill.
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Meunier, N., J. F. Blais, M. Lounès, R. D. Tyagi, and J. L. Sasseville. "Different options for metal recovery after sludge decontamination at the Montreal Urban Community wastewater treatment plant." Water Science and Technology 46, no. 10 (November 1, 2002): 33–41. http://dx.doi.org/10.2166/wst.2002.0282.
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The MUC (Montreal Urban Community) treatment plant produces approximately 270 tons of dry sludge daily (270 tds/day) during the physico-chemical treatment of wastewater. Recently, this treatment plant endowed a system of drying and granulation of sludge for valorization as an agricultural fertilizer having a capacity of 70 tds/day (25% of the daily sludge production). However, the metal content (mainly Cu and Cd) of the sludge surpasses the norms for biosolids valorization. In order to solve this problem, a demonstration project, from the lab scale to the industrial pilot plant, was carried out to test the Metix-AC technology for the removal of metals. A strongly metal-loaded filtrate was generated during the sludge decontamination. Tests concerned the study of the metal recovery by total precipitation and selective precipitation, as well as the use of alternative products for the metal precipitation. Other works consisted to simulate the acid filtrate recirculation from the decontaminated sludge (25% of the total volume) in the untreated sludge (75% of the total volume) intended for the incineration. The total precipitation with hydrated lime appeared effective for the recovery of metals (87% Cd, 96% Cr, 97% Cu, 98% Fe, 71% Ni, 100% Pb, 98% Zn). However, this option entails the production of an important quantity of metallic residue, which should be disposed of expensively as dangerous material. The selective iron precipitation does not appear to be an interesting option because the iron in solution within the leached sludge was principally present in the form of ferrous iron, which cannot be precipitated at pH lower than five. On the other hand, the use of commercial precipitating agents (TMT-15, CP-33Z, CP-NB and CPX) without pH adjustment of filtrate gave good results for the recovery of Cu and, to a lesser degree for the recovery of Pb. However, the efficiency for the other metals' (Cd, Cr, Fe, Ni and Zn) recovery was weaker (< 25%). Finally, the acid filtrate recirculation containing solubilised metals in untreated sludge destined for incineration appears to be the most interesting option. Metals in solution in the acid filtrate, precipitate or adsorb effectively (97% Cd, 97% Cr, 99% Cu, 82% Ni, 100% Pb and 87% Zn) on the solids of the untreated sludge. Moreover, TCLP tests were done on ashes produced during the incineration of sludge mixed with the acid filtrate produced during sludge decontamination. These tests showed that there were no significant differences, as regards the extractability of metals, between such ashes and those produced during the untreated sludge incineration without addition of filtrate. Therefore, it was predictable that this method can respect the current environmental standards required by the different governmental authorities.
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Sereda, T. G., E. N. Elancheva, S. N. Kostarev, Y. A. Kochinov, and T. V. Kochinova. "Approaches to the selection of measures to ensure the safety of closed landfills for the disposal of solid municipal waste." IOP Conference Series: Earth and Environmental Science 981, no. 3 (February 1, 2022): 032026. http://dx.doi.org/10.1088/1755-1315/981/3/032026.
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Abstract The approaches to the choice of measures to ensure the environmental safety of closed facilities for the disposal of solid municipal waste (MSW) are considered. Laws of the Russian Federation in terms of requirements for ensuring the safety of waste disposal facilities during the operational and reclamation periods have been studied. Scenarios of the conduct of processes at MSW landfills after reclamation are presented. The article presents the results of engineering and geological research: a comprehensive study of engineering and geological and hydrogeological conditions of the site, composition, condition and properties of soils, the activity of geological processes for making design decisions. Field engineering and geological work, soil sampling from wells have been carried out. Laboratory research of soil samples has been carried out in a soil laboratory. The project of reclamation cover of MSW landfill has been completed, including geosynthetic materials and natural soils, a network of pipelines supplying filtrate for recirculation has been calculated, and a set of work and selection of vegetation at the biological stage of reclamation have been justified. Scenarios of the conduct of processes in the course of reclamation of a waste disposal facility are considered in the case of application of the filtrate recirculation technology with preliminary pH-regulation by changing the structure of the landfill in the first year after reclamation and according to the scheme of the section of the reclaimed landfill upon reaching the stage of destruction of the biodegradable part of the waste. The advantages of the developed reclamation pavement are shown: high cultivation capacity, preservation of drainage properties at high loads, reduced costs for excavation and crushed stone laying, high chemical resistance and environmental friendliness of the material.
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LC, Souza, AJV Zanuncio, JL Colodette, AG Carvalho, and VR de Castro. "POST-O2 EUCALYPTUS PULP IN A/D(EP)DP BLEACHING SEQUENCE WASHED WITH RECIRCULATION OF THE ALKALINE FILTRATE." JOURNAL OF TROPICAL FOREST SCIENCE 33, no. 1 (January 19, 2021): 88–94. http://dx.doi.org/10.26525/jtfs2021.33.1.88.
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Souza, Luciana Cerqueira, Antonio Jose Vinha Zanuncio, and Jorge Luiz Colodette. "THE EFFECTS OF ALKALINE FILTRATE RECIRCULATION TOWARDS THE PROPERTIES OF LONG FIBER PULPS WITH OD(EPO)DED BLEACHING SEQUENCE." CERNE 24, no. 3 (September 2018): 233–39. http://dx.doi.org/10.1590/01047760201824032528.
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Yanuhar, Uun, Dyah Kinasih Wuragil, Heru Suryanto, Rhobithotus Mufidah, Tifa Fauliza, Nezya Pramudya Wardani, Reval Pahlefi, Dewa Sukma Trinanda Adhitya, and Nico Rahman Caesar. "PKM PENERAPAN RECIRCULATING AQUACULTURE SYSTEM UNTUK PENGELOLAAN AIR DAN KESEHATAN IKAN BERKELANJUTAN DI POKDAKAN ROI LELE KABUPATEN MALANG." Jurnal Pengabdian Pendidikan dan Teknologi (JP2T) 3, no. 2 (November 1, 2022): 159. http://dx.doi.org/10.17977/um080v3i22022p159-165.
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Pemeliharaan ikan lele yang dilakukan pembudidaya di Pokdakan ROI Lele sebagian besar tidak melakukan upaya pengelolaan kualitas air seperti, filtrasi, sirkulasi maupun penggantian air (water exchange). Hal ini menyebabkan penurunan mutu air sebagai akibat dari penumpukan sisa pakan maupun feses ikan serta sisa hasil metabolisme lainnya. Lingkungan perairan merupakan suatu hal yang sangat berperan penting dalam pertumbuhan ikan lele (Clarias sp.). Oleh karena itu, perlu adanya manajemen lingkungan dan kesehatan pada pemeliharaan ikan lele (Clarias sp.). Keberhasilan suatu usaha budidaya sangat erat kaitannya dengan kondisi lingkungan yang optimum untuk kelangsungan hidup dan pertumbuhan ikan yang dipelihara. Setelah Tim PKM Mengidentifikasi pemecahan masalah yang ada, maka kegiatan pemecahan atau pengembangan yang dilakukan harus sesuai dengan kebutuhan yakni dengan menerapkan teknologi Recirculating Aquaculture System (RAS) pada kolam budidaya ikan di Pokdakan ROI Lele. Dalam penerapan sistem RAS, penggunaan filtrasi air sangat menentukan keberhasilan sirkulasi air. Pada progam PKM ini akan menggunakan Filtrasi air terdiri dari filter mekanis, filter biologi dan filter kimia. Hasil dari kegiatan pengabdian masyarakat PKM terhadap mitra adalah Pengetahuannya meningkat, keterampilannya meningkat, kapasitas produksi meningkat dan keuntungannya meningkat.
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Golper, T. A., A. A. Kaplan, N. Narasimhan, and M. Leone. "Transmembrane pressures generated by filtrate line suction maneuvers and predilution fluid replacement during in vitro continuous arteriovenous hemofiltration." International Journal of Artificial Organs 10, no. 1 (January 1987): 41–46. http://dx.doi.org/10.1177/039139888701000110.
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A recirculating in vitro CAVH system was designed which generated pulsatile blood and filtrate flows. Monitors recorded hydrostatic pressures simultaneously in the arterial, venous and filtrate lines during varying plasma or blood flow rates and predilution (vs postdilution) replacement fluid flow rates. Similar hydrostatic pressure monitoring was carried out during multiple maneuvers to generate suction on the filtrate side of the hemofilter (Amicon® D-20's and Renaflo®‘s). With a plasma flow (Qp) of 100 cc/min and predilution replacement fluid infusion rate of 500 cc/hr, the arterial pressure was 5% greater than during postdilution (p < 0.05). With a blood flow (Qb) of 50 cc/min, predilution fluid replacement rates of 500 and 1000 cc/hr, and vacuum suction applied to the filtrate compartment, the arterial pressure was 33% lower than during postdilution fluid replacement (p < 0.03). Nonetheless, the ultrafiltration rate (UFR) was 10 to 30% higher (p < 0.03). At many other combinations of Qp, Qb and replacement rates and modes, there were no significant changes in arterial pressure. Despite these arterial pressure changes, > 70% of the transmembrane hydrostatic pressure (TMP) was due to the negative pressure induced by filtrate suction (gravity, Gomco®, wall suction, IMED®). The actual pressure in the filtrate compartment measured during Gomco® or wall suction was 3/4 of that stated by their gauges, presumably due to leakage. Maximum wall suction never generated TMP's > 150 mmHg. Using an IMED® 960 as the suction device (bypassing the air alarm), for a Qp of 50, IMED® settings of 300, 600 and 900 cc/hr generated TMP's of 67 ± 3, 77 ± 3, and 97 ± 3 mmHg, respectively. When Qp was 20 cc/min, an IMED® setting of 999 cc/hr generated TMP's consistently < 136 mmHg but UFR was only 668 ± 246 cc/hr. With the IMED® set at 999 cc/hr and Qp of 30 cc/min, the TMP was < 132 mmHg and the UFR was 944 ± 10 cc/hr. No filters ruptured. These suction maneuvers do not generate enough pressure to rupture filters. When Qp is low the IMED® may not generate the UFR one expects. Predilution will probably alleviate this concern.
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Busnach, G., A. Dal Col, M. L. Perrino, B. Brando, C. Brunati, and L. Minetti. "Performance Evaluation of Cascade Filtration with High Flow Rate Recirculating Plasma on the Secondary Filter." International Journal of Artificial Organs 10, no. 2 (March 1987): 121–28. http://dx.doi.org/10.1177/039139888701000212.
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Cascade filtration (CF) has been performed in 67 on-line procedures in 9 normolipidemic patients with paraproteinemic disorders. A modified dead-end technique has been employed, with high flow rate recirculating plasma on the plasma fractionation filter (QD recycled CF), and an albumin-rich, globulin-poor filtrate was reinfused into the patient. Postprocedure recoveries were 81 ± 15% for albumin, 55 ± 23% for IgM and 48% for cryocrit, with an increase in A/G ratio from 1.8 to 2.1. An improvement was observed also in antiatherogenic/atherogenic lipoproteins ratio, suggesting a possible use of this technique in the treatment of familial hypercholesterolemia. Plasma primary separation was obtained by centrifugation or by filtration, and no significant differences were observed on subsequent protein fractionation process. An albumin priming of the plasmafractionation circuit accounted for an additional 13% saving in postprocedure level. Different surface area secondary filters have been employed: with larger surfaces, larger volumes were processed without any increase in the waste volume and with reduced need for washouts, but with an additional loss of small molecules possibly due to entrapping onto the membrane.
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Huang, J. Y., S. Takizawa, and K. Fujita. "Pilot-plant study of a high recovery membrane filtration process for drinking water treatment." Water Science and Technology 41, no. 10-11 (May 1, 2000): 77–84. http://dx.doi.org/10.2166/wst.2000.0613.
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Successful application of energy efficient dead-end micro-filtration (MF), which does not require recirculation like cross-flow filtration, depends on achieving high recovery rates. In this study, two different types of pilot scale membrane systems (horizontally and vertically stretched membrane filters) were evaluated based on the effects of pre-chlorination, intermittent chlorination and circulation flow by air-scrubbing. Additionally, the effects of operating factors including physical cleaning and chemical cleaning on membrane fouling were examined. The vertically stretched membranes showed better performance than horizontally stretched membranes at filtration fluxes of either 0.55 m/day or 0.78 m/day even under 2.6 to 27.5°C and raw water turbidity higher than 300 units, as long as intermittent chlorination (10 mg/l once a week) along with the circulation flow by air-scrubbing (once in 30 minutes) in the housing were employed. It was demonstrated that the vertically stretched membranes have been operated for one year without chemical cleaning of the membranes, wherein the recovery of raw water as a filtrate was 97.0% or 98.9%.
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Janning, K. F., K. Mesterton, and P. Harremoës. "Hydrolysis and degradation of filtrated organic particulates in a biofilm reactor under anoxic and aerobic conditions." Water Science and Technology 36, no. 1 (July 1, 1997): 279–86. http://dx.doi.org/10.2166/wst.1997.0065.
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Two experiments were performed in order to investigate the anoxic and the aerobic degradation of filtrated organic matter in a biofilter. In submerged lab. scale reactors with Biocarbone media as filter material, accumulated particulate organic matter from pre-settled wastewater served as the only carbon source for anoxic and aerobic degradation respectively. In order to utilise the accumulated organic matter, the bacteria in the biofilm had to produce extracellular hydrolytic enzymes for the hydrolysis process. In the first experiment with anoxic degradation, a significant denitrification occurred. The maximum nitrate removal rate, with particulate organic matter as carbon source, was found to 1 g NO3-N/ (m2d), declining exponentially as rA.NO3-N = 1.04 e −4t g NO3-N/(m2d) (t = days). A significant release of soluble organic matter (< 0.45 μm) and production of inorganic carbon to the bulk liquid was observed as an indication of hydrolysis taking place. The second experiment was designed as a series of on-line OUR batch experiments in a biofilm reactor with recirculation, in order to investigate further the degradation of particulate organic matter. After the biofilm had been starved in order to remove the original organic matter, particulate organic matter was added and the degradation kinetics recorded. The initial removal rate was high, rA.02 = 2.1 g O2/(m2d) though fast declining towards endogenous respiration. The respiration ratio between removed oxygen and produced carbon dioxide was declining from 1.3 to 1.0 g O2/g CO2 during the degradation of organic particulates. The respiration ratio during endogenous respiration was determined to be 0.7 g O2/g CO2 indicating a thorough mineralisation of biomass.
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Zhang, Stephanie Y., and Gretchen J. Mahler. "Modelling Renal Filtration and Reabsorption Processes in a Human Glomerulus and Proximal Tubule Microphysiological System." Micromachines 12, no. 8 (August 19, 2021): 983. http://dx.doi.org/10.3390/mi12080983.
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Kidney microphysiological systems (MPS) serve as potentially valuable preclinical instruments in probing mechanisms of renal clearance and osmoregulation. Current kidney MPS models target regions of the nephron, such as the glomerulus and proximal tubule (PCT), but fail to incorporate multiple filtration and absorption interfaces. Here, we describe a novel, partially open glomerulus and PCT microdevice that integrates filtration and absorption in a single MPS. The system equalizes pressure on each side of the PCT that operates with one side “closed” by recirculating into the bloodstream, and the other “opened” by exiting as primary filtrate. This design precisely controls the internal fluid dynamics and prevents loss of all fluid to the open side. Through this feature, an in vitro human glomerulus and proximal tubule MPS was constructed to filter human serum albumin and reabsorb glucose for seven days of operation. For proof-of-concept experiments, three human-derived cell types—conditionally immortalized human podocytes (CIHP-1), human umbilical vein endothelial cells (HUVECs), and human proximal tubule cells (HK-2)—were adapted into a common serum-free medium prior to being seeded into the three-component MPS (T-junction splitter, glomerular housing unit, and parallel proximal tubule barrier model). This system was optimized geometrically (tubing length, tubing internal diameter, and inlet flow rate) using in silico computational modeling. The prototype tri-culture MPS successfully filtered blood serum protein and generated albumin filtration in a physiologically realistic manner, while the device cultured only with proximal tubule cells did not. This glomerulus and proximal convoluted tubule MPS is a potential prototype for the human kidney used in both human-relevant testing and examining pharmacokinetic interactions.
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Kistriyani, Lilis, Zainus Salimin, and Achmad Chafidz. "Utilization of extracellular polymeric substances (EPS) immobilized in epoxy polymer as double ion exchanger biosorbent for removal of chromium from aqueous solution." Communications in Science and Technology 5, no. 1 (July 2, 2020): 40–44. http://dx.doi.org/10.21924/cst.5.1.2020.179.
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Cation and industrial pollutant anions are removed from wastewater using organic cation and anion exchange resin. "Extracellular Polymeric Substance" (EPS) from bacterial extraction can accumulate cation and anion elements through biosorption by adsorption mechanism, ion exchange, formation of complex compounds and hydrogen bonds. EPS can be used as an biosorbent and ion exchange bioresin replacing organic resins, because EPS contains organic functional groups that are negatively charged (RCOOH, ROPO3H, ROPO3Na, ROSO3H, ROSO3Na, etc.) cation absorbers and positively charged (ROH, RCNH2HCOOH, etc.) anion absorber. EPS consists of 40-95% polysaccharide compounds, protein 1-60%, nucleic acids 1-10%, lipids 1-10% and the remaining amino acid polymers and other compounds. The tannery industry produces trivalent (Cr+3) chromium pollutants at levels of 15.2 ppm and hexavalent (CrO4-2 or Cr2O7-2) levels of 0.77 ppm which exceeds the standard quality for a total Cr of 0.6 ppm. Cr pollutants are very dangerous for human health. Research had been done on the use of immobilized EPS bioresin in epoxy polymers for chromium binding. EPS was extracted from bacterial activated sludge by centrifugation at 9000 rpm for 20 minutes at 4°C, the filtrate was EPS. The analysis showed EPS content were 16% fat, 12% carbohydrate, and 16% protein. The functional group analysis results with infrared ray spectroscopy (FTIR) showed EPS containing chemical bonds such as -CH, -OH, -NH, and -C=O which proved that EPS extraction contained RCOOH, ROH, and RCNH2HCOOH functional components which were exchanging components cations and anions. Epoxy polymers were prepared by mixing bisphenol A monomers and 1: 1 ratio epichlorohydrin. Immobilized EPS double ion exchange biorecin in epoxy polymers was prepared by mixing 200 mg EPS and 1800 mg epoxy. The binding of chromium ions in the resin was carried out by recirculating the chromium solution through a burette column filled with 2 rams of bioresin at pH 5, 6 and 7. The optimum results gave chromium ion absorption efficiency of 89.20% at pH 5. Column operations could be optimized by varied the amount of bioresin used.
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Wen, Qianqian, Yuan Liu, Wenbo Yu, Qian Zhu, Yuwei Zhu, Shijie Bian, Xintai Su, et al. "Evaluation of Sludge Deep-Dewatering Filtrate Recirculation to Wastewater Treatment Plant by Toxicity Detection with Microbial Fuel Cells." ACS ES&T Water, January 17, 2023. http://dx.doi.org/10.1021/acsestwater.2c00571.
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Yeole, T. Y., N. S. Deshmukh, K. L. Lapsiya, and D. R. Ranade. "Production of biogas from cattle waste at low temperature." Linnaeus Eco-Tech, October 23, 2019, 639–44. http://dx.doi.org/10.15626/eco-tech.2005.062.
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Production of Bio gas from cattle waste and other biomass is now considered as one of the majorroutes to obtain gaseous fuel for sustainable development. In tropical countries like Indiathousands of rural families in villages are using 3 to 5 M3 biogas plants to suffice their dailycooking fuel need. All these plants are run on cattle waste. Since these plants are operated atambient temperatures, effect of temperature variation affects daily gas yield. The effect becomesvery prominent during winter season. In general about 50-60% reduction in daily biogas yield isobserved when ambient temperature is around l 5°C as compared to that produced at around 30-350C. A low cost and simple to operate technique to enhance biogas yield from the biogas plantduring winter season shall help to get optimum biogas yield from these plants during the winterseason. We thought of a simple technique of filtering the digested effluent slurry of biogas plantthrough a triple layer muslin cloth to obtain a filtrate, hence-forth called as clarified digestedslurry (CDS), rich in cell mass and then adding it back to the biogas plant along with the influentslurry. Experiments were carried out on 25 L capacity cattle dung biogas plant operated at 15°Cto see effect of recirculation of CDS. Addition of 25 and 40% v/v CDS in daily influent resultedin 15% and 37% increase in daily biogas yield. Recirculation of 40% v/v CDS supplementedwith Diammonium phosphate(DAP) increased the biogas yield by 75% v/v. In anotherexperiment use of clarified rumen fluid (CRF) to prepare influent slurry and added exclusivelyfor one day enhanced the daily biogas yield by 70% v/v for a period of two months. Popular dailywears in India called cotton dhoti or cotton sari can be used for the filtration of the slurry.