Application and functional properties of millet starch: Wet milling extraction process and different modification approaches

In the past decade, the demand and interest of consumers have expanded for using plant-based novel starch sources in different food and non-food processing. Therefore, millet-based value-added functional foods are acquired spare attention due to their excellent nutritional, medicinal, and therapeutic properties. Millet is mainly composed of starch (amylose and amylopectin), which is primary component of the millet grain and defines the quality of millet-based food products. Millet contains approximately 70 % starch of the total grain, which can be used as a, ingredient, thickening agent, binding agent, and stabilizer commercially due to its functional attributes. The physical, chemical, and enzymatic methods are used to extract starch from millet and other cereals. Numerous ways, such as non-thermal physical processes, including ultrasonication, HPP (High pressure processing) high-pressure, PEF (Pulsed electric field), and irradiation are used for modification of millet starch and improve functional properties compared to native starch. In the present review, different databases such as Scopus, Google Scholar, Research Gate, Science Direct, Web of Science, and PubMed were used to collect research articles, review articles, book chapters, reports, etc., for detailed study about millet starch, their extraction (wet milling process) and modification methods such as physical, chemical, biological. The impact of different modification approaches on the techno-functional properties of millet starch and their applications in different sectors have also been reviewed. The data and information created and aggregated in this study will give users the necessary knowledge to further utilize millet starch for value addition and new product development

Temperature control of fermentation bioreactor for ethanol production using IMC-PID controller

The state-space model is identified using the identification tool of MATLAB, and the best fit of 99% of measured and simulated data was obtained. Further, state-space model was converted to a transfer function model and finally simplified to an unstable second order time-delay transfer function model. Internal model control based proportional integral derivative (IMC-PID) controller design method was proposed for unstable second order time delay with RHP zero (USOPDT) and successfully tested to the nonlinear bioreactor process model. The temperature of the bioreactor was successfully controlled by proposed controller in both cases setpoint and disturbance change. The performance of the controller was evaluated in terms of IAE, ISE, ITAE and the corresponding values of 20.99, 49.02 and 292.50 were obtained respectively. Proposed method shows better closed-loop performance in terms of IAE and settling time than the other reported methods for temperature control of bioreactor. Keywords: Bioreactor, Identification tool, IMC-PID, MATLAB, USOPD

Methyl 1-imidazolecarbodithioate as a thiocarbonyl transfer reagent: a facile one-pot, three-component synthesis of novel 2-substituted-5-aryl-1-oxo-3-thioxo-1,2,3,5,11,11a-hexahydro-6H-imidazo-[1,5-b]-β-carbolines

An efficient one-pot, three-component synthesis of novel 2-substituted-5-aryl-1-oxo-3-thioxo-1,2,3,5,11,11a-hexahydro-6H-imidazo-[1,5-b]-β-carbolines employing 1-aryl-1,2,3,4-tetrahydro-β-carboline-3-carboxylates, primary amines (or amino acid esters) and methyl 1-imidazolecarbodithioate as the thiocarbonyl transfer reagent is reported

Sustainable Pathways For Solar Desalination Using Nanofluids: A Critical Review

Water is a fundamental requirement for the survival of human beings. Although water is abundantly available across the globe, access to freshwater still remains a major concern. Most of the water available is saline or brackish, which is not fit for human consumption. Desalination is the optimum solution for production of potable water from saline water. A major shortcoming of conventional desalination technologies is their dependence on fossil fuel that results in environmental degradation, global warming, etc. Therefore, sustainable desalination technology has evolved as a need of hour. Among all renewable energy resources, solar energy is abundantly available and can be potentially harvested. Therefore, solar energy can be used to drive sustainable desalination technologies. A solar still converts saline water into freshwater in a single step using solar energy. But the major drawbacks of solar still are relatively lower efficiency and lower yield. Nanofluids are widely used to overcome these limitations due to their extraordinary and unique properties. This paper critically reviews the recent research performed on the application of nanofluids in solar desalination systems. Methods of nanofluid preparation, their types and properties are also discussed in detail. Application of nanofluids in solar desalination systems is discussed with special attention on performance enhancement of solar stills. Combinations of nanofluids with various other performance enhancement techniques are also considered. The effectiveness of nanofluids in solar stills is found to be dependent majorly on the nature and concentration of the nanofluid used

Performance evaluation and kinetic study of fluorene biodegradation in continuous bioreactor using polyurethane foam as packing media

870-878Polycyclic aromatic hydrocarbons (PAHs) are precarious persistent pollutants derived from incomplete combustion of fossil fuel and petroleum products. Due to adverse effects of PAHs on the environment, the wastewater contaminated with PAHs needs to be treated prior to discharge in the water bodies. In the present study, we used immobilized polyurethane foam Pseudomonas pseudoalcaligenes NRSS3 for degradation of fluorene in packed bed bioreactor (PBBR) to stimulate biofilm and possibly enhance removal efficiency. The most affecting process parameters, such as pH, process time and temperature were optimized at batch mode and found to be 7.0, 8.0 days, and 30 °C, respectively. At the optimum condition, the bioreactor was operated in continuous mode up to 45 days and obtained results demonstrate that the maximum removal efficiency (RE) of 91.1% along with 27.3 mg/L day-1 of elimination capacity (EC) were observed. Biodegradation kinetics of fluorene were evaluated by Monod growth and Andrew-Haldane inhibition models and parameters were obtained to be µmax: 0.32 day-1; Ks: 10.8 mg/L by Monod while µmax: 0.47 day-1; Ks: 12.3 mg/L; 27.5 mg/L by Andrews-Haldane

Combination of UV-Fenton oxidation process with biological technique for treatment of polycyclic aromatic hydrocarbons using <em>Pseudomonas pseudoalcaligenes</em> NRSS3 isolated from petroleum contaminated site

460-469Polycyclic aromatic hydrocarbons (PAHs), often from petroleum oil spill, by-product of petroleum refining, incomplete combustion of fossil fuel, leakage in pipeline and underground storage, apart from the effluents of pesticide, dye, pigment, and drug industries, are considered carcinogenic and mutagenic. As the abundance of PAHs in the environment cause adverse effects on humans and ecosystem, the PAHs contamination needs to be monitored and such polluted sites require remediation. Conventional methods available for remediation of PAHs are adsorption, advance oxidation process, electrochemical remediation, solvent extraction, use of synthetic surfactants and photocatalytic remediation. These methods including the alternative Fenton oxidation technology are not only expensive but also produce secondary pollutants. In this study, we evaluated the performance of UV-Fenton-PBBR (Packed bed bioreactor) hybrid system for the treatment of polycyclic aromatic hydrocarbons (naphthalene and fluorene). Pseudomonas pseudoalcaligenes NRSS3 isolated from petroleum contaminated site and immobilized on Sterculia alata was used as packing media in the PBBR. The naphthalene and fluorene were taken as model polycyclic aromatic hydrocarbon (PAHs) with initial concentration of 400 mg/L. The optimum conditions for UV-Fenton oxidation were (pH: 3, Fe2+: 2.5 g/L, H2O2: 1000 mg/L) for naphthalene and (pH: 3, Fe2+: 3.0 g/L, H2O2: 1200 mg/L) for fluorene. The overall maximum removal efficiency of the combined system was found to be 96 and 94.7% for naphthalene and fluorene, respectively. GC-MS analysis confirmed the formation of catechol, 1-napthol, salicylic acid and phthalic anhydride as metabolites during degradation process. Biodegradation kinetics of naphthalene and fluorene were studied using Monod model and kinetics constants were found to be µmax: 0.3057 per day; Ks: 112.87 mg/L for naphthalene and µmax: 0.2921 per day; Ks: 114.75 mg/L for fluorene

Removal of Atrazine by coupling Fenton reaction with bioreactor in series

498-505Atrazine is a commonly used weedicide in agriculture fields. Owing to its long half-life (125 days) and slow-biodegradability, it adds to problematic residues in the environment. It is known to disrupt endocrine and reproductive systems and has potential to damage vital organs such as liver, kidney and heart. While atrazine is banned in European countries, many countries, such as India, China, and the USA it is still in use widely. In atrazine biodegradation, batch bioreactors are most commmon cost effective alternative to conventional methods. However, it has only major limitation of slow rate of degradation. In this work, we explored coupling of UV-Fenton and biological method for atrazine removal and also optimized the process parameters. In the bioreactor, Loofa was used as the packing media on which consortia was immobilized. The performance of coupled system was studied with an initial atrazine concentration of 300 mg/L. Overall, maximum removal efficiency of 93% was achieved for the coupled system. GC-MS analysis of residual treated effluent sample was performed to identify the intermediate compound. Two metabolites biuret and urea were identified which confirmed the degradation of atrazine. The growth kinetic parameters µmax (0.224 per day) and KS (106.64) were calculated using Monod model. The coupling method was found superior than individual chemical and biological methods for treatment of atrazine

Adsorption of Patent Blue V from Textile Industry Wastewater Using Sterculia alata Fruit Shell Biochar: Evaluation of Efficiency and Mechanisms

Biochar prepared from Sterculia alata fruit shell showed a better performance for dye removal than the biomass from Sterculia alata fruit shell. The important process parameters&mdash;namely the pH, the amount of biochar, the initial dye concentration and the contact time&mdash;were optimized in order to maximize dye removal using biochar of Sterculia alata fruit shell as the bio-sorbent. The results from this study showed that the maximum adsorption of dye on the biochar was obtained at a biochar dosage of 40 g/L, at a contact time of 5 h, and an initial dye concentration of 500 mg/L (pH 2.0; temperature 30 &plusmn; 5 &deg;C). The increase in the rate adsorption with temperature and the scanning electron microscopic (SEM) images indicated the possibility of multilayer type adsorption which was confirmed by better fit of the Freundlich adsorption isotherm with the experimental data as compared to the Langmuir isotherm. The values n and R2 in the Freundlich isotherm were found to be 4.55 and 0.97, respectively. The maximum adsorption capacity was found to be 11.36 mg/g. The value of n &gt; 1 indicated physical nature of the adsorption process. The first and second order kinetics were tested, and it was observed that the adsorption process followed the first-order kinetics (R2 = 0.911)

Left bundle branch block in type 2 diabetes mellitus: a sign of advanced cardiovascular involvement.

OBJECTIVE: To evaluate left bundle branch block (LBBB) as an indicator of advanced cardiovascular involvement in diabetic (DM) patients by examining left ventricular systolic function and proteinurea. METHODS: Data of 26 diabetic patients with left bundle branch block (DM with LBBB) were compared with data of 31 diabetic patients without left bundle branch block (DM without LBBB) and 18 nondiabetic patients with left bundle branch block (non-DM with LBBB). The inclusion criteria were age \u3e45 years, and diabetes mellitus type 2 of \u3e5 years. RESULTS: Mean ages of patients in DM with LBBB, DM without LBBB, and non-DM with LBBB groups were 67 +/- 8, 68 +/- 10, and 65 +/- 10 years, respectively (P = NS). Females were 65%, 61%, and 61%, respectively (P = NS). Left ventricular ejection fraction in DM with LBBB was significantly lower than in DM without LBBB and non-DM with LBBB (30 +/- 10% vs 49 +/- 12% and 47 +/- 8%, P \u3c 0.01). Left ventricular end-diastolic volume was significantly higher in DM with LBBB than in DM without LBBB and non-DM with LBBB (188.6 +/- 16.4 mL vs 147.5 +/- 22.3 mL and 165.3 +/- 15.2 mL, P \u3c 0.03). Similarly, left ventricular end-systolic volume was significantly higher in DM with LBBB than in DM without LBBB and non-DM with LBBB (135.4 +/- 14.7 mL vs 83.7 +/- 9.5 mL and 96.6 +/- 18.4 mL, P \u3c 0.02). No statistically significant difference was seen in left atrial size. Proteinurea in DM with LBBB (79.4 +/- 18.9 mg/dL) was significantly higher than in DM without LBBB (35.6 +/- 8.5 mg/dL, P \u3c 0.05) and non-DM with LBBB (12 +/- 3.5 mg/dL, P \u3c 0.05); however, there was no significant difference in Hb A1c levels in DM with LBBB and DM without LBBB (9.01% vs 7.81%, P = NS). CONCLUSIONS: Left bundle branch block in diabetic patients indicates advanced cardiovascular involvement manifesting with more severe left ventricular systolic dysfunction and proteinurea compared to both diabetic patients without left bundle branch block and nondiabetic patients with left bundle branch block

Biodegradation of methylene blue dye in a batch and continuous mode using biochar as packing media

Bacterial species for metabolizing dye molecules were isolated from dye rich water bodies. The best microbial species for such an application was selected amongst the isolated bacterial populations by conducting methylene blue (MB) batch degradation studies with the bacterial strains using NaCl-yeast as a nutrient medium. The most suitable bacterial species was Alcaligenes faecalis (A. faecalis) according to 16S rDNA sequencing. Process parameters were optimized and under the optimum conditions (e.g., inoculum size of 3 mL, temperature of 30 °C, 150 ppm, and time of 5 days), 96.2% of MB was removed. Furthermore, the effectiveness for the separation of MB combining bio-film with biochar was measured by a bio-sorption method in a packed bed bioreactor (PBBR) in which microbes was immobilized. The maximum MB removal efficiencies, when tested with 50 ppm dye using batch reactors containing free A. faecalis cells and the same cells immobilized on the biochar surface, were found to be 81.5% and 89.1%, respectively. The PBBR operated in continuous recycle mode at high dye concentration of 500 ppm provided 87.0% removal of MB through second-order kinetics over 10 days. The % removal was found in the order of PBBR>Immobilized batch>Free cell. The standalone biochar batch adsorption of MB can be described well by the pseudo-second order kinetics (R2 ≥0.978), indicating the major contribution of electron exchange-based valence forces in the sorption of MB onto the biochar surface. The Langmuir isotherm suggested a maximum monolayer adsorption capacity of 4.69 mg g−1 at 40 °C which was very close to experimentally calculated value (4.97 mg g−1). Moreover, the Casuarina seed biochar was reusable 5 times