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Production of Nano Beta-Glucans From Baking Yeast Saccharomyces cerevisiae and Its Comparison With Extracted Beta-Glucans
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Abstract<p>In this study, the valid bread yeast <italic>Saccharomyces cerevisiae</italic> was used for the purpose of the polysaccharide beta-glucan, and the diagnosis of lyophilization was confirmed, as the biological cell of the yeast was grown in SDA Agar medium and incubated at a temperature of 37 degrees Celsius for 48 hours, and the sugar fermentation test was conducted and completed. Identifying its microscopic and cultural characteristics, diagnostic tests showed that it was <italic>Saccharomyces cerevisiae</italic> yeast. Beta-glucan was extracted from yeast cells using the (acid-base) method. The extracted beta-glucan was diagnosed using Infrared rays (FT-IR) and (HPLC) technology. Comparing the results of the tests with the standard beta-glucan compound. The extracted beta-glucan was converted into a nanocomposite by (base - acid) method. The physical, chemical and functional properties of the nanocomposite were determined. The ability to bind water to the nanocomposite was (293%) and the ability to bind fat (254%). The average size of the nano-beta-glucan particles included in Soft cheese manufacturing using the Size Analyzer device reached 189.4 nm.Filed Emission Scanning electron microscope (FESEM) was used to detect the surface of the extracted and prepared Nano beta-glucan compound, which reached, respectively. As for the (XRD), UV-Vis, Fourier spectrometer was determined. The inhibitory effectiveness of the extracted and Nano beta-glucan compound against pathogenic bacteria was estimated, while Gram-negative bacteria was inhibited as well, as it was for <italic>E. coli</italic> and <italic>Pseudomonas aeruginosa</italic> 23 and 21 mm, respectively, The results showed that there was no growth inhibition zone for lactic acid bacteria.</p>
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Publication Date
Sat Oct 01 2011
Journal Name
Journal Of Engineering
Production of Biodiesel Fuel from Used vegetable Oil
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Used vegetable oil was introduced to transesterfication reaction to produce Biodiesel fuel suitable for diesel engines. Method of production was consisted of filtration, transesterfication, separation and washing. Transesterfication was studied extensively with different operating conditions, temperature range (35-80oC), catalyst concentration (0.5-2 wt. % based on oil), mixing time (30-120 min.) with constant oil/methanol weight ratio 5:1 and mixing speed 1300 rpm. The concentration of Fatty acid methyl esters (Biodiesel) was determined for the transesterficated oil samples, besides of some important physical properties such as specific gravity, viscosity, pour point and flash point. The behavior of methyl esters production and the physica

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Publication Date
Wed Mar 01 2006
Journal Name
Journal Of Engineering
Production of Graphite Electrodes Binder from Iraqi Asphalt
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Basrah crude oil Vacuum residue 773+ K with specific gravity 1.107 and 4.87wt. % sulfur, was treated with hexane commercial fraction provided from Al-Taji Gas Company for preparing deasphaltened oil(DAO)suitable for hydrotreating process. Deasphaltening was carried out with 1h mixing time, 10ml:1g solvent to oil ratio and at room temperature. Hexane deasphaltened oil was hydrotreated on presulfied commercial Co-Mo/γ-Al2O3 catalyst in a trickle bed reactor. The hydrotreating process was carried out at temperature 660 K,LHSV 1.3 h^ –1, H2/oil ratio 300 l/l and constant pressure of 4MPa. The hydrotreated product was distillated under vacuum distillation unit. It is found that the mixture of 75% of vacuum residue with 25% anthracene satisfie

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Publication Date
Sun Dec 30 2001
Journal Name
Iraqi Journal Of Chemical And Petroleum Engineering
Production of Methyl Ethyl Ketone from N-Butane
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Publication Date
Sun Oct 30 2011
Journal Name
Journal Of Engineering
Production of Biodiesel Fuel from Used vegetable Oil
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Used vegetable oil was introduced to transesterfication reaction to produce Biodiesel fuel suitable for diesel engines. Method of production was consisted of filtration, transesterfication, separation and washing. Transesterfication was studied extensively with different operating conditions, temperature range (35-80o C), catalyst concentration (0.5-2 wt. % based on oil), mixing time (30-120 min.) with constant oil/methanol weight ratio 5:1 and mixing speed 1300 rpm. The concentration of Fatty acid methyl esters (Biodiesel) was determined for the transesterficated oil samples, besides of some important physical properties such as specific gravity, viscosity, pour point and flash point. The behavior of methyl esters production and the

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Publication Date
Sat Oct 01 2011
Journal Name
Journal Of Engineering
Production of Biodiesel Fuel from Used vegetable Oil
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Used vegetable oil was introduced to transesterfication reaction to produce Biodiesel fuel suitable for diesel engines. Method of production was consisted of filtration, transesterfication, separation and washing. Transesterfication was studied extensively with different operating conditions, temperature range (35-80oC), catalyst concentration (0.5-2 wt. % based on oil), mixing time (30-120 min.) with constant oil/methanol weight ratio 5:1 and mixing speed 1300 rpm. The concentration of Fatty acid methyl esters (Biodiesel) was determined for the transesterficated oil samples, besides of some important physical properties such as specific gravity, viscosity, pour point and flash point. The behavior of methyl esters production and the phys

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Publication Date
Mon Jul 31 2017
Journal Name
Journal Of Engineering
Production of Biofuels from Selected Cellulosic Waste materials
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Publication Date
Sat Oct 01 2011
Journal Name
Journal Of Engineering
Production of Biodiesel Fuel from Used vegetable Oil
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Used vegetable oil was introduced to transesterfication reaction to produce Biodiesel fuel suitable for diesel engines. Method of production was consisted of filtration, transesterfication, separation and washing. Transesterfication was studied extensively with different operating conditions, temperature range (35-80oC), catalyst concentration (0.5-2 wt. % based on oil), mixing time (30-120 min.) with constant oil/methanol weight ratio 5:1 and mixing speed 1300 rpm. The concentration of Fatty acid methyl esters (Biodiesel) was determined for the transesterficated oil samples, besides of some important physical properties such as specific gravity, viscosity, pour point and flash point. The behavior of methyl esters production and the

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Publication Date
Sat Jan 09 2021
Journal Name
Medico Legal Update
Production of Bioemulsifiers from Bacteria Grown on Hydrocarbons
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This work aimed to identify biosurfactant-producing bacterial strains isolated from hydrocarbon-contaminatedsites and to evaluate their biosurfactant properties. The drop-collapse method and minimal agar added witha layer of diesel as carbon source were used for screening, positive strains were able to grow in a liquidmedium, and surface tension and emulsification index were determined in cell-free supernatant and cellsuspension. 250 bacterial isolate were tested, and 16 were positive for the drop-collapse and hydrocarbonlayer agar method. Most of the strains were Pseudomonas, except for three strains (Acinetobacter, Bacillus,and Rhodococcus). Surface tension was similar in cell-free and cell suspension measurements, with valuesin t

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Publication Date
Thu Oct 01 2015
Journal Name
Iraqi Journal Of Science
improvement and partial purification for pectinase production from pseudomonas aeuroginosa
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Publication Date
Tue Sep 30 2025
Journal Name
Iraqi Journal Of Science
A Study on Using Molasses Production Waste Powder as a Green Adsorbent for Cu (II) Ions from its Aqueous Solution
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This study utilized low-cost agricultural waste (molasses production waste powder) to extract copper ions from aqueous solutions. The present investigation explored a range of factors that influence the adsorption process, including temperature, pH, ionic strength, contact time, quantity of adsorbent, and particle size. Spectrophotometric analysis was used to determine the solution's absorbance both before and after the adsorption procedure. The Langmuir and Freundlich adsorption models were used to match the equilibrium data. The Freundlich model was determined to be the best isotherm model using the linear regression coefficient R2=0.9868. Thermodynamic parameters, including enthalpy, entropy, and Gibbs free energy, were calculate

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