Slaughterhouse Wastewater Treatment Research Articles

High-performance internal circulation anaerobic granular sludge reactor for cattle slaughterhouse wastewater treatment and simultaneous biogas production

This research investigates the efficacy of a high-performance pilot-scale Internal Circulation Anaerobic Reactor inoculated with Granular Sludge (ICAGSR) for treating cattle slaughterhouse wastewater while concurrently generating biogas. The primary objective is to assess the efficiency and performance of ICAGSR in terms of organic pollutant removal and biogas production using granular anaerobic sludge. The research methodology entails operating the ICAGSR system under ambient conditions and systematically varying key parameters, including different Hydraulic Retention Times (HRTs) (24, 12, and 8 h) and Organic Loading Rates (OLRs) (3.3, 6.14, and 12.83 kg COD/m³. d). The study focuses on evaluating pollutants’ removal and biogas production rates. Results reveal that the ICAGSR system achieves exceptional removal efficiency for organic pollutants, with Chemical Oxygen Demand (COD) removal exceeding 74%, 67%, and 68% at HRTs of 24, 12, and 8 h, respectively. Furthermore, the system demonstrates stable and sustainable biogas production, maintaining average methane contents of 80%, 76%, and 72% throughout the experimental period. The successful operation of the ICAGSR system underscores its potential as a viable technology for treating cattle slaughterhouse wastewater and generating renewable biogas. In conclusion, this study contributes to wastewater treatment and renewable energy production by providing a comprehensive analysis of the ICAGSR system’s hydrodynamic properties. The research enhances our understanding of the system’s performance optimization under varying conditions, emphasizing the benefits of utilizing ICAGSR reactors with granular sludge as an effective and sustainable approach. Identifying current gaps, future research directions aim to further refine and broaden the application of ICAGSR technology in wastewater treatment and renewable energy initiatives.

Modeling of Biofoam Destabilization by Biodefoamers in Poultry Slaughterhouse Wastewater Treatment Activated Sludge

Biofoam formation in wastewater treatment is a challenge globally. Previously, we successfully proposed the use of biodefoamers instead of synthetic defoamers for environmental protection. In this study, we report on biodefoamation modeling using activated sludge organisms. Overall, the rate law model was determined to adequately describe foam drainage including collapse while applying biodefoamers. The target industry is the poultry processing industry whereby foam formation during wastewater treatment is an ongoing challenge.

The use of Iron Sand as Filtration Media for Slaughterhouse Wastewater Treatment

An increase in slaughtering animals will have an impact on increasing the liquid waste produced. The resulting RPH liquid waste can damage the environment if it is not treated, so it is necessary to conduct research to reduce pollutant levels so that it is suitable for disposal into the environment. The technique used in processing RPH wastewater is iron sand filtration method. Iron sand filtration is a filtering process using renewable media, namely iron sand. Iron sand is known to contain the mineral magnetite (Fe3O4) which has the ability to absorb colloidal solids, so it has the potential to be used to remove pollutant content of RPH liquid waste. This research objective to determine the effect of variations in the thickness of the filtration media (cm) and grain size (mesh) on pollutant parameters. The thickness variations used were 20, 25, and 30 cm, with grain sizes of iron sand 40, 60 and 100 mesh. The experimental results showed that the iron sand filtration method was able to reduce Chemical Oxygen Demand (COD) and Total Suspended Solid (TSS) levels, increase the Dissolve Oxygen Meter (DO) value, and change the pH value. The highest reduction in COD was in the thickness variation of 30 cm with 100 mesh. the percentage of decrease in the value of Chemical Oxygen Demand (COD) was 95.05%, the highest decrease in Total Suspended Solid (TSS) value was in the media thickness variation of 30 cm with 100 mesh, the percentage of TSS value reduction was 97.11%, the pH value increased in the thickness variation media 30 cm with a mesh number of 100 from 5.8 to 7.4, and the value of Dissolve Oxygen Meter (DO) increased with variations in thickness of 30 cm with 100 mesh, increased from 1.2 to 15.2. Based on the parameter test results, it was concluded that iron sand filtration is effective in reducing pollutant levels below the quality standard, so that it is expected to be applied directly on a larger scale.

Optimizing electrocoagulation for poultry slaughterhouse wastewater treatment: a fuzzy axiomatic design approach

White meat consumption is increasing day by day, and accordingly, there is an increase in the amount of wastewater resulting from the processes. Today, the reuse of wastewater has become a goal within the scope of the Green Deal. For this reason, wastewater treatment with high pollution and volume has gained importance. In this study, the fuzzy axiomatic design (FAD) method, one of the multi-criteria decision-making methods, has been used. With this method, coagulation, electrocoagulation (EC), dissolved air flotation (DAF), and anaerobic treatment alternatives preferred in poultry slaughterhouse wastewater (PSW) treatment were compared with each other and their information contents were calculated. The information content from the smallest to the largest is EC, DAF, coagulation, and anaerobic treatment, respectively. This treatment method was chosen because the smallest information content is in electrocoagulation. EC was applied to bloody PSW containing 1% blood by volume. The effectiveness of Fe and Al electrodes for PSW treatment in the batch EC reactor has been compared. The effective surface areas of 2 anodes and 2 cathodes connected bipolarly in the processes are 288 cm2. The electrolyte, pH, time, and current density effects on energy consumption were also investigated. The optimum conditions for Al and Fe electrodes were found to be 0.5 g·L−1 NaCl concentration, pH 5, 0.639 mA·cm−2 current density, and 5 min time. Under optimum conditions for the Fe electrode, COD, TOC, TN, and oil-grease removal efficiencies were determined as 76.3%, 71.8%, 70%, and 74%, respectively. Moreover, the highest COD, TOC, TN, and oil-grease removal efficiencies were achieved with an Al electrode (82.2%, 82.3%, 82.7%, and 78.9%, respectively). The experimental data were fit to a variety of isotherms and kinetic models to determine the characteristics of the EC. The results indicated that the pseudo-second-order equation provided the best fit for COD removal. Under optimum conditions, the operating cost was calculated as $3.39 and $3.09 for Al and Fe electrodes, respectively. In this study, the fuzzy axiomatic design method was used for the first time to select the most appropriate treatment method for PSW. In addition, blood, a major problem for the poultry slaughterhouse industry, was mixed with PSW at a ratio of 1% (v/v) and treated with EC for the first time with high removal efficiency. By treating PSW, which has a high pollution load, with electrocoagulation, the pollution load of the water to be given to secondary treatment has been greatly reduced.

Effective removal of organic and inorganic pollutants from abattoir wastewater using magnesium oxide/activated carbon nanocomposites

This study investigated the development and characterization of activated carbon (AC), magnesium oxide (MgO), and a combination of AC and MgO nanocomposite for abattoir wastewater treatment. Activated carbon was derived from Hura crepitans pods, whereas MgO nanoparticles were produced through biosynthesis. Different composite (AC/MgO) ratios (1:1, 1:2, and 2:1) were prepared using a wet impregnation technique. The efficiency of these nanoadsorbents in eliminating heavy metal pollutants were tested through batch adsorption experiments under the influence of the dosage, temperature, and contact time. Various analytical tools were used to characterize the prepared nanoadsorbents. XRD confirmed the formation of a pure MgO periclase phase, indicating a reduction in particle size with the increase in pH. The HRSEM images of the nanocomposites showed porous carbon structures with regular mesopores and spherical MgO nanoparticles. The uniform granules with agglomerated spherical shapes were confirmed by the SAED patterns, suggesting the core/shell structure of MgO from the HRTEM images. Further imaging confirmed the dispersion of carbon and magnesium in the nanocomposites, without the formation of distinct dopant oxides. The specific surface areas were determined as 2.74 m2/g for activated carbon, 27.57 m2/g for MgO, and 40.82 m2/g for activated carbon/MgO, indicating enhanced surface area due to the addition of activated carbon. Batch adsorption studies indicated that the AC/MgO nanocomposite in the 1:2 ratio exhibited the highest pollutant adsorption rate under similar conditions. The adsorption study was calculated by the pseudo-second-order and Langmuir isotherm models. The AC/MgO nanocomposite demonstrated reusability over six cycles, with a slight reduction in removal efficiency from the first cycle (98.05 % for Fe, 96.50 % for Cd, and 94.32 % for Pb) to the sixth cycle (91.10 % for Fe, 86.56 % for Cd, and 84.03 % for Pb). Overall, these findings suggest that AC/MgO nanocomposites can effectively eliminate pollutants from abattoir wastewater.

Performance evaluation of a two-phase anaerobic reactor coupled with microalgae photobioreactors for slaughterhouse wastewater treatment in Ethiopia

Performance evaluation of a two-phase anaerobic reactor coupled with microalgae photobioreactors for slaughterhouse wastewater treatment in Ethiopia

Pilot plant approach combining photocatalysis and adsorption for antibiotics removal from slaughterhouse and urban wastewater treatment plant effluents

The main objective of this research is to perform a real case-study of antibiotic decontamination from real slaughterhouse and wastewater effluents by applying a sequential treatment of TiO2/UV–vis photocatalysis and adsorption. More precisely, the removal of five classes of antibiotics: enrofloxacin, sulfadiazine, trimethoprim, azithromycin, amoxicillin and amoxicillin degradation products was studied in an 80 L/h photocatalytic and adsorption pilot-scale plant over multiple cycles, operating in semi-continuous mode. The results exhibited significant removal rates, ranging from 77% to 100% for the slaughterhouse effluent, and 61–89% for the wastewater treatment plant effluent, thus demonstrating that the treatment is more effective when it is applied directly in the emission source, previous to antibiotic dilution in the municipal collector. Using the two processes sequentially results in greater efficiency than when they are used in isolation. After photocatalysis, antibiotic degradation products are easily adsorbed, since they have more affinity for the adsorbent, and the presence of competing compounds decreases considerably. After applying several cycles of treatment, the adsorption performance remains almost constant. By contrast, the photocatalysis performance decreased, which was attributed to catalyst agglomeration determined by Asymmetric Flow Field-Flow Fractionation (AF4) coupled with Dynamic Light Scattering (DLS) and Inductively Coupled Plasma Mass Spectrometry (ICP-MS).

Treatment of Slaughterhouse Wastewater through a Series System: Upflow Anaerobic Reactor and Artificial Wetland

Slaughterhouse wastewater is characterized by high concentrations of organic matter. This creates a need to explore methods for its treatment before discharge. This study evaluated the efficiency of an integrated treatment process consisting of a laboratory-scale upflow anaerobic sludge blanket reactor and a pilot-scale horizontal subsurface flow wetland. This treatment was used for (i) the removal of organic matter through anaerobic–aerobic microbiological processes, (ii) the conversion of organic matter from hydraulic processes, and (iii) for bioremediation and phytoremediation. The treatment system was evaluated at hydraulic retention times (HRTs) of 7.5, 5.0, and 2.5 d; during the investigation, the influence of the HRTs on the removal efficiency of the system was evaluated. High efficiencies of 85% and 75% were obtained for CODT and BOD, respectively, at an HRT of 7.5 d. The highest overall efficiency for the removal of total solids was observed at an HRT of 2.5 d. The results obtained confirm the feasibility of implementing the suggested system as an alternative for the adequate and sustainable treatment of slaughterhouse wastewater, and the system can be applied to slaughterhouses with similar conditions to those in this study.

Electrode material impact on microbial fuel cell and electro-Fenton systems for enhanced slaughterhouse wastewater treatment: A comparative study of graphite and titanium.

The treatment of slaughterhouse wastewater is a complex task demanding careful consideration due to its challenging nature. Therefore, exploring more sustainable treatment methods for this particular type of wastewater is of utmost significance. This research focused on the impact of electrode materials, specifically graphite and titanium, on the efficiency of microbial fuel cells (MFCs) and electro-Fenton systems in treating slaughterhouse wastewater. Both graphite and titanium electrodes displayed increasing current density trends, with titanium outperforming graphite. Titanium showed superior electron transfer and current generation (2.2 to 21.2 mA/m2 ), while graphite ranged from 2.4 to 18.9mA/m2 . Titanium consistently exhibited higher power density, indicating better efficiency in converting current to power (0.059 to 22.68 mW/m2 ), compared to graphite (0.059 to 12.25 mW/m2 ) over the 48-h period. In removal efficiency within the MFC system alone, titanium exhibited superior performance over graphite in key parameters, including zinc (45.5% vs. 37.19%), total hardness (39.32% vs. 29.4%), and nitrates (66.87% vs. 55.8%). For the electro-Fenton system with a graphite electrode, the removal efficiency ranged from 34.1% to 87.5%, with an average efficiency of approximately 56.2%. This variability underscores fluctuations in the efficacy of the graphite electrode across diverse wastewater treatment scenarios. On the other hand, the electro-Fenton system employing a titanium electrode showed removal efficiency values ranging from 26.53% to 89.99%, with an average efficiency of about 68.4%. The titanium electrode exhibits both a comparatively higher and more consistent removal efficiency across the evaluated scenarios. On the other hand, the integrated system achieved more than 90% removal efficiency from most of the parameters. The study underscores the intricate nature of slaughterhouse wastewater treatment, emphasizing the need for sustainable approaches. PRACTITIONER POINTS: Microbial fuel cell (MFC) and electro-Fenton were investigated for slaughterhouse wastewater treatment. The MFC microbial activity started to decrease after 24 h. The integrated system achieved up to 99.8% removal efficiency (RE) for total coliform bacteria. Up to 99.4% of RE was also achieved for total suspended solids (TSS). The integrated system highly improved RE of the pollutants.

Enhancing slaughterhouse wastewater treatment through the integration of microbial fuel cell and Electro-Fenton systems: A comprehensive comparative analysis

This research examined the viability of combining the Microbial Fuel Cell (MFC) and Electro-Fenton (EF) system to treat slaughterhouse wastewater. The study compared three different setups: the first utilizing only the MFC, the second employing solely EF, and the third integrating both systems for wastewater treatment (MFC and EF). In the case of Microbial Fuel Cell treatment, notable removal efficiencies were observed, including 58.8 % for turbidity, 41.2 % for color, 69.9 % for chemical oxygen demand, 72.2 % for biochemical oxygen demand, and 69.9 % for total coliform bacteria. EF treatment demonstrated substantial Removal efficiencies of 72.5 % for turbidity, 81.6 % for Chemical Oxygen Demand (COD), 86.5 % for biochemical oxygen demand, and 84.3 % for Escherichia coli (E. coli) bacteria. Integrated treatment yielded exceptional Removal efficiencies of 98.9 % for turbidity, 95.5 % for chemical oxygen demand, 95.4 % for biochemical oxygen demand, and 100 % for E. coli bacteria. After computing water quality indices, it was found that raw wastewater had an extremely high water quality index (1.087 × 1012), indicating severe pollution. Despite lower water quality indices from MFC and EF treatments, the water remained unsuitable for drinking. Integrated treatment significantly reduced the water quality index (1.67 × 104), indicating enhanced water quality, though it remained non-potable.

Investigation Removal Efficiency of Electrocoagulation Process as A Slaughterhouse Wastewater Treatment Technique: Toxicity Assessment

Investigation Removal Efficiency of Electrocoagulation Process as A Slaughterhouse Wastewater Treatment Technique: Toxicity Assessment

Efficiency of Some Chemical Reagents with Ultrafiltration System in the treatment of Abattoir Wastewater

The study seeks to evaluate the concentration of some toxicants in abattoir wastewater prior to treatment and after treatment using ultrafiltration system. Samples of water were gathered from the reservoir of wastewater in the Gwagwalada abattoir, Abuja, Nigeria without treatment and labelled S1. Some of the water was subjected to treatment using Chlorine + Alum + Lime (S2), another with Chlorine + Alum + Lime + Activated carbon (S3). Physico-chemical parameters such as: pH, colour, nitrates etc. were analyzed. Trace metals (Zn, Cu, Fe, Pb, Mn, Ni, Co and Cd) levels in the water samples were investigated using Atomic Absorption Spectrophotometer (AAS). Concentration of pesticide residues (μg/L), antibiotics and bacterial growth were also evaluated. The S1, S2 and S3 nitrate concentrations were 271.20, 22.40 and 26.57 mg/L respectively. Level of Zinc, Copper and Lead in the trio samples investigated were within the range 0.14 to 0.24 mg/L, 0.15 to 0.24 mg/L and 0.06 to 0.17 mg/L respectively. Dichlorvos, Lambda-cyhalothrin and Chlorpyrifos were found in the 3 water samples in varying concentration. Only sample S1 shows microbial growth of Salmonella spp., Escherichia coli, Pseudomonas spp., and Shigella spp. at 52.00 ± 8.49, 58.00±31.11, >100 and 10.50 ±0.71 CFU/100ml respectively. In S1, 0.05 μg/L of oxytetracycline and 0.34 μg/ of levofloxacin were found. This study has shown that treating wastewater from the abattoir using ultrafiltration method with some reagents such as Chlorine, Alum, Lime and Activated Carbon can help in removing toxicants and purify it before releasing it into the environment.

Enhancing industrial swine slaughterhouse wastewater treatment: Optimization of electrocoagulation technique and operating mode

In this study, industrial swine slaughterhouse effluents were treated by an electrocoagulation process (EC) with aluminum and iron electrodes. Batch and semicontinuous operation were performed. EC tests were carried out in batch operating mode for 2.5 h using fixed current densities (j = 10, 20, and 30 mA cm−2) in sulfate and chloride media. At the laboratory scale, higher TOC removal efficiencies were observed using aluminum electrodes at 20 mA cm−2 without the addition of a supporting electrolyte (82.7%). However, the EC process with Fe electrodes consumed 43.6% less energy.After the best operating parameters were found at the laboratory scale, the process was tested as a semicontinuous prepilot process using a filter-press FM01-LC-type electrochemical reactor equipped with flat plate aluminum electrodes. In this stage, current densities and mean linear flow rates were assessed. The highest TOC removal efficiency of 72.7% (i.e., residual TOC concentration of 85.18 mg L−1) in the semicontinuous process was achieved by the application of j = 25 mA cm−2 and ur = 0.64 cm s−1 with an energy consumption of 19.80 kW h m−3. The residual COD and TP concentrations met the international standard limits. Moreover, complete decoloration and disinfection were accomplished. EDXRF, SEM, EDAX, XRD, and FTIR analyses indicated that pollutants were removed by adsorption on aluminum/iron hydroxides/oxyhydroxides.

Life cycle environmental impact assessment of slaughterhouse wastewater treatment

Slaughterhouses are significant industrial water users, ranking second highest in the livestock processing sector, and a potential pollution source for water bodies due to effluent discharge. This paper uses the wastewater composition of an actual slaughterhouse and models three alternative scenarios for the wastewater management; no treatment and discharge, primary treatment and discharge, and tertiary treatment followed by partial water reuse. All three scenarios are assessed in terms of their environmental performance following a Life Cycle Assessment, by using the Environmental Footprint 3.0 method. The results revealed that the best scenario for the slaughterhouse wastewater treatment is the third scenario with an overall footprint of 0.255 milliEcopoints (mPt), compared to 2.45 mPt and 1.31 mPt of the first and the second scenario, respectively.

Carbon-based materials boost the anaerobic treatment of slaughterhouse wastewater

Carbon-based materials were tested as methanogenic boosters to enhance the anaerobic treatment slaughterhouse wastewater, which included an organic xerogel (OX) doped with graphene oxide, a peach stone carbon (PSC), and a monolithic whey carbon (MWC). Enhanced treatment by the carbon-based boosters was evident in terms of organic matter removal and methane production rate, which was globally reflected on a superior methanogenic conversion efficiency as compared to the unamended control. OX appeared as the best methanogenic booster increasing up to 77 % and 12 % the methane production rate and organic matter removal, respectively. The obtained results suggest that hydrolysis and acidification of the complex wastewater were the limiting steps during the treatment of this industrial effluent. This observation is consistent with the higher production of ammonium, derived from protein hydrolysis, which occurred in bioreactors amended with carbon-based materials, as compared to the unamended control. Several changes in the relative abundance of key microbial taxa occurred; particularly, members of the bacterial families Synergistaceae and Anaerolineaceae, as well as the archaeal Methanolinea and Proteiniclasticum genera, increased significantly in the presence of OX. The synthesized materials are proposed to improve the performance of anaerobic treatment systems dealing with complex wastewaters.

Treatability of high-strength real sheep slaughterhouse wastewater using struvite precipitation coupled Fenton's oxidation: The MAPFOX process

Struvite (MAP, magnesium ammonium phosphate hexahydrate, MgNH4PO4.6H2O) precipitation-aided Fenton's OXidation (MAPFOX process) was explored in the treatment of high-strength real sheep slaughterhouse wastewater (RSSW) for the first time under a comprehensive soft-computing-based modeling study. The experimental results showed that under the highest-efficiency conditions (chemical combination of MgCl2.6H2O + NaH2PO4.2H2O, a molar ratio of Mg2+:NH4+-N:PO43–P = 1.2:1:1, a reaction pH of 9.0 ± 0.10, [NH4+-N]0 = 240 ± 20 mg/L, and a reaction time of 15 min), MAP precipitation could effectively remove more than 80 %, 60 %, 55 %, and 70 % of color, total chemical oxygen demand (TCOD), soluble COD (SCOD), and ammonium nitrogen (NH4+-N) from the raw RSSW. The results of the Fenton's oxidation used as the post-treatment unit of the proposed MAPFOX system indicated that the integrated advanced oxidation process (AOP) was able to reduce the residual pollutant levels in the MAP-pretreated RSSW to the relevant discharge standards. Under the subsequent condition of [Fe2+]0 = 90 mmol/L, [H2O2]0 = 180 mmol/L, reaction pH = 3.25, and total reaction time = 60 min, more than 97 % of color, TCOD, SCOD, and NH4+-N could be removed from the RSSW via the Fenton's oxidation after the MAP-based physicochemical treatment. According to SEM micrographs, surface morphology of dehydrated struvite exhibited irregular-shaped and overlapping sharp-edged particles of various sizes with an average size of about 50.9 μm. The Fourier Transform Infrared (FTIR) spectroscopy confirmed the active functional groups and type of bonds for the high-strength RSSW-oriented struvite (heated) within the spectral range of 4000–450 cm−1. Thermogravimetric Analysis (TGA), Derivative Thermogravimetry (DTG), Differential Thermal Analysis (DTA), and Differential Scanning Calorimetry (DSC) of the dehydrated struvite revealed that the weight loss occurred in three temperature zones, the maximum weight loss rate of 0.252 mg/min was recorded at around 224 °C and at time of 20.83 min, and the sample had strong endothermic and medium exothermic peaks at about 241 °C and 679 °C, respectively. The predictive successes of the implemented soft-computing approaches were benchmarked in terms of various statistical goodness-of-fit parameters. The performance assessment indices corroborated the superiority of the support vector machines-Pearson VII universal kernel function (SVM-PUKF)-based model (correlation coefficient (CC) = 0.9999–1.0000), mean absolute error (MAE) = 0.0222–0.0389 %, mean absolute percentage error (MAPE) = 0.0270–0.0506 %, root mean squared error (RMSE) = 0.0258–0.0415 %, coefficient of variation of RMSE (CV(RMSE) = 0.0003–0.0008, Nash–Sutcliffe efficiency (NSE) = 0.9998–1.000, Legates and McCabe's index (LMI) = 0.9894–0.9952) over other data-intelligent models in predicting the pollutant removal efficiencies. The computational results also indicated that the narrowest uncertainty bands (±1.96Se = 0.0537–0.1483 %) and the lowest amounts of expanded uncertainty (U95 = 3.1224–5.3124 %) values for all efficiency sets were achieved for the applied SVM-PUKF-based strategy. This study demonstrated the first-ever and successful application of the proposed MAPFOX process in treatability of the RSSW and capability of the implemented soft-computing strategy in modeling a highly nonlinear treatment system.

Treatment of abattoir wastewater using <i>Moringa oleifera</i> seed and snail shell in Rivers State, Nigeria

The practice of discharging abattoir wastewater into a receptacle without treatment is most likely to alter its physicochemical and microbiological properties. Against this background, this study is aimed at determining the efficacy of Moringa oleifera and snail shells as bio-coagulants for treatment of abattoir wastewater using the jar. The mean values of monitored physicochemical parameters were electrical conductivity (1227.7), total organic carbon (224.4%), biochemical oxygen demand (362.3 mg/l), chemical oxygen demand (1001.5g), total dissolved solids (462.5 mg/l), total suspended solids (1562.5) mg/l and turbidity (190.6 NTU). The mean total heterotrophic bacteria count (THBC) for untreated wastewater was 1.4 x 108 CFU/ml, total coliform count (TCC) was 5.6 x 105 CFU/ml, and total fungal count (TFC) was 1.6 x 102 CFU/ml. After treatment, the biocoagulants caused 82.5-84.2% reduction in EC, TOC (59-88.3%), BOD (90.8-93.7%), COD (94.4-95.3%), TDS (89.6-91.9%), TSS (93.3-94.5%) and turbidity (80.8-84.5%). The bio-coagulants were able to remove 92.2-95.4% of Zn, Pb (97-97.5%), Cr (97.2-98.8%) and Cd (86.7-89.3%). After treatment with the bio-coagulants, THBC dropped from 4.7 x 103-5.3 x 102 CFU/ml to 8-10 CFU/ml on day 6, TCC dropped from 4.2 x 102 – 6.7 x 10 CFU/ml to 5-7 CFU/ml on day 6 while TFC dropped from 1.1 x 102 - 1.5 x 10 CFU/ml to 2-4 CFU/ml on day 6, representing approximately 99.9% reduction in microbial load. Thus, the bio-coagulants were as good at removing pollutants in water as alum, but with the added advantages of being natural, cost-effective, and readily available.

Effect of slaughterhouse waste on sewage channel

The meat producing sector are among primary users of global freshwater resources within the sector of agriculture and livestock. Processing of meat facilities known as MPP’s generate substantial volumes of wastewater during both the slaughtering process and facility cleaning. This wastewater, referred to as slaughterhouse wastewater (SWW), requires substantial treatment to ensure safe and environmentally friendly discharge because it contains high levels of organic materials and proteins. As a result, SWW treatment and disposal are crucial for maintaining public health. In that chapter, we study about the regulatory system pertinent management of slaughterhouse wastewater (SWW), its environmental ramifications, health implications, and the distinctive attributes of slaughterhouse waste. Due to the varying pollutant levels resulting from the type and quantity of killed flora and fauna, which can change within the meat industry, SWWs are typically assessed through bulk parameters. The characteristics of SWW, such as Chemical Oxygen Demand (COD), Biochemical Oxygen Demand (BOD), and Total Suspended Solids (TSS), are key pollutant affecting sewage system. When SWW combines with the sewage system, it adds to the burden on both the sewage network and sewage treatment plants (STP). Therefore, employing on-site treatment utilizing integrated processes emerges as the optimal approach for treating and disinfecting slaughterhouse effluents, ensuring their safe discharge into receiving waters.

Comparison of the Optimization of the Coagulation-Flocculation and Electrocoagulation Treatment of Slaughterhouse Wastewater Using the Response Surface Method

In this work, the coagulation-flocculation and electrocoagulation treatments were compared in the removal of pollutants from wastewater from the Conchucos slaughterhouse, Lima. For the coagulation-flocculation treatment, we worked with 4 independent variables with their respective experimental ranges, coagulant dose (600-1000 mg / L), flocculant dose (4-8 mg/L), fast stirring speed (250-350 rpm), slow stirring speed (80-100 rpm), for electrocoagulation the parameters of stirring speed (250-350 rpm) and stirring time (15-30 rpm). The central compound design method (DCC) optimizing by response surface (RSM) was used as an experimental method for the reduction of pollutants as a function of chemical oxygen demand (% COD), a jar test equipment was used for the coagulation-flocculation and a one-liter shaker with aluminum plate electrodes at 30 V. The results show that coagulation/flocculation and electrocoagulation presented statistical models with F-values of 5.33, 20.30, significance p<0.05, with adjustments of R2 of 0.6179, and 0.7571 for an optimal arrangement with %COD reduction prediction, respectively. The electrocoagulation treatment presented a reduction of 75.43% similar to the predicted model, of the 2 treatments compared, the electrocoagulation is below the maximum admissible values (VMA) in COD, BOD and Oils and Fats, complying with the necessary parameters for the discharge to the sewerage system.

Determination and monitoring of tetracycline and degradation products in livestock slaughterhouse wastewater treatment plant effluent

Aim of our study was the determination and monitoring of tetracycline (TC) and degradation products (DEP) in livestock slaughterhouse wastewater treatment plant (SWWTP) effluent. For this purpose, TC and DEP values in SWWTP were investigated. The concentrations of TC and DEP were monitored for 12 months. TC, 4-epitetracycline (ETC), 4-epianhydrotetracycline (EATC), anhydrotetracycline (ATC), and physicochemical parameters of pH, suspended solids (SS), BOD5, COD, and TP were calculated. The maximum TC concentration was determined as 1.68±0.08 µg/L in March and the minimum TC was 1.08±0.05 µg/L in January. The maximum ETC was 2.93±0.14 µg/L in March and April. The minimum ETC was 1.98±0.1 µg/L in January. EATC was 10.82±0.5 µg/L in September, and minimum EATC value was determined as 9.14±0.4 µg/L in March. The maximum ATC value was 8.62±0.4 µg/L in June and the lowest ATC value was 6.61±0.3 µg/L in September. Concentrations of TC and DEP detected in SWWTP effluent were listed in descending order as EATC> ATC> ETC> TC.