Moroccan employers have a strong responsibility for the safety and health of their employees in the workplace and for protecting them from the risk of COVID-19 and any occupational hazards, as required by Moroccan law. As a consequence, industries, including the agri-food sector, have put in place preventive measures to deal with this pandemic on several fronts, including the use of hydroalcoholic products and bleach for personal and surface disinfection. These disinfection actions may eliminate or reduce the risk of coronavirus infection, but the increased use of these products by employees could lead to serious health problems and increase the occupational chemical risk in the event of uncontrolled exposure. In order to analyze this risk in the dairy industry in Morocco, we have launched a qualitative and quantitative study to identify and assess the severity of chemical risk to which its employees are exposed. This involves an analysis of the safety data sheets [MSDS] of the disinfectants used and a health and safety survey of the users of these products, particularly for hand disinfection. This analysis showed that this chemical risk is omnipresent and prevention measures are partially adopted. Indeed, the strengthening of health safety measures to combat COVID-19 has significantly increased this risk, resulting in a remarkable imbalance in the assessment and management of occupational risks in this industry. These results have led us to propose corrective and preventive measures against this risk to interested parties and to adopt an integrated management of food and occupational health risks in a single system. This is the use of the Risk Analysis—Critical Control Points (HACCP)-Tool for a First Risk Assessment by Activity Analysis (OPERA) approach, which we developed and proposed in a previous study, for a simplified management of chemical risk in the food industry, especially in small- and medium-sized enterprises.

Hydraulic retention time (HRT) influence improving sludge flocculation with adding the polyelectrolytes (non-ionic, anionic, and cationic) was studied on an activated sludge (AS) system fed with synthetic domestic wastewater (SDW), dairy industry wastewater (DIW), and caramel industry wastewater (CIW). The sludge volumetric index, food/microorganism ratio (F/M), and mixed liquor volatile suspended solids at different HRTs (6, 8 and 10 h) were monitored on an experimental model. Results showed that both SDW and IW had the best sludge flocculation conditions at 8 h and 100 mL of non-ionic polyelectrolyte (0.2 mg L⁻¹). In addition, this phenomenon reached the organic matter removal efficiencies of 95.9, 95.7, and 94.2% for SDW, DIW, and CIW, respectively. Therefore, optimum HRT increased the organic matter removal efficiencies by 10%, sludge concentration by 37% (22–55%), and F/M ratio by 70%. Moreover, the polyelectrolytes used in AS improved the sludge flocculation by 2.9 times.

Sweet whey is a waste product from the dairy industry that is difficult to manage. High hopes are fostered regarding its neutralization in the methane fermentation. An economically viable alternative to a typical mesophilic fermentation seems to be the process involving psychrophilic bacteria isolated from the natural environment. This study aimed to determine the feasibility of exploiting psychrophilic microorganisms in methane fermentation of sweet whey. The experiments were carried out under dynamic conditions using Bio Flo 310 type flow-through anaerobic bioreactors. The temperature inside the reactors was 10 ± 1 °C. The HRT was 20 days and the OLR was 0.2 g COD/dm³/day. The study yielded 132.7 ± 13.8 mL biogas/gCODᵣₑₘₒᵥₑd. The CH₄ concentration in the biogas was 32.7 ± 1.6%, that of H₂ was 8.7 ± 4.7%, whereas that of CO₂ reached 58.42 ± 2.47%. Other gases were also determined, though in lower concentrations. The COD and BOD₅ removal efficiency reached 21.4 ± 0.6% and 17.6 ± 1.0%, respectively.

Direct ultrafiltration and its combination with pretreatment by coagulation/flocculation/sedimentation using Moringa oleifera as coagulant to treat dairy industry wastewater were investigated. A single-channel tubular ceramic membrane with an average porosity of 0.1 μm was used at transmembrane pressures of 1, 2, and 3 bars, using the cross-flow filtration principle in a membrane filtration unit. Process efficiency was evaluated in terms of chemical oxygen demand (COD), apparent color, and turbidity removal, along with major requirements such as average permeate flux, percentage of fouling, and contribution of different resistances (resistances in series model) to the total resistance of the membrane. The highest removals for the evaluated parameters occurred in the combined coagulation/flocculation/sedimentation/ultrafiltration process. At a pressure of 2 bar, the removal of turbidity and apparent color was 99.9 % and that of COD was 98.5 %. For the combined process, the lowest percentage of fouling was 59.8 %, which occurred at 1 bar. The fraction of resistance due to fouling, which may indicate irreversible damage of the membrane, was lower in the process of coagulation/flocculation/sedimentation using M. oleifera as coagulant followed by ultrafiltration than in the process that treated dairy wastewater with direct ultrafiltration for all pressures. © 2013 Springer Science+Business Media Dordrecht.

Processed milk waste (MW) presents a serious problem within the dairy industries due to its high polluting load. Its chemical oxygen demand (COD) can reach values as high as 80,000 mg O₂ L⁻¹. This study proposes to reduce the organic load of those wastes using thermal coagulation and recover residual valuable components via fermentation. Thermal process results showed that the COD removal rates exceeded 40% when samples were treated at temperature above 60 °C to reach 72% at 100 °C. Clarified supernatants resulting from thermal treatment of the samples at the temperatures of 60 (MW₆₀), 80 (MW₈₀), and 100 °C (MW₁₀₀) were fermented using lactic acid bacteria strains without pH control. Lactic strains recorded important final cell yields (5–7 g L⁻¹). Growth mediums prepared using the thermally treated MW produced 73% of the bacterial biomass recorded with a conventional culture medium. At the end of fermentation, mediums were found exhausted from several valuable components. Industrial scale implementation of the proposed process for the recycling of industrial MWs is described and discussed.

Although the long incubation time of biochemical oxygen demand (BOD₇) measurements has been addressed by the use of microbial biosensors, the resulting sensor-BOD values gained from the measurements with specific industrial wastewaters still underestimates the BOD value of such samples. This research aims to provide fast and more accurate BOD measurements in the dairy wastewater samples. Unlike municipal wastewater, wastewater from the dairy industry contains many substrates that are not easily accessible to a majority of microorganisms. Therefore, a bacterial culture, Microbacterium phyllosphaerae, isolated from dairy wastewater was used to construct a semi-specific microbial biosensor. A universal microbial biosensor based on Pseudomonas fluorescens, which has a wide substrate spectrum but is nonspecific to dairy wastewater, was used as a comparison. BOD biosensors were calibrated with OECD synthetic wastewater, and experiments with different synthetic and actual wastewater samples were carried out. Results show that the semi-specific M. phyllosphaerae-based microbial biosensor is more sensitive towards wastewaters that contain milk derivates and butter whey than the P. fluorescens-based biosensor. Although the M. phyllosphaerae biosensor underestimates the BOD₇ value of actual dairy wastewaters by 25–32 %, this bacterial culture is more suitable for BOD monitoring in dairy wastewater than P. fluorescens, which underestimated the same samples by 46–61 %.