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Evaluation of Some Migration Parameters Between the Virgin Olive Oil and the High Density Polyethylene

تقييم إمكانية حدوث هجرة متبادلة بين زيت الزيتون البكر و البولي إيثيلين عالي الكثافة

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 Publication date 2012
  fields Food Sciences
and research's language is العربية
 Created by Shamra Editor




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References used
AOCS Cd3D-63 (1990), Free Fatty Acid Evaluation, Official Methods and Recommended Practices of the AOCS, 6th Edition, 2nd printing
AOCS Cd3D-62 (1990). Peroxide Value Evaluation, Official Methods and Recommended Practices of the AOCS, 6th Edition, 2nd printing
ISO 2555, (1989 E), Determination of apparent viscosity by the Brookfield Test Method
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The study was conducted on randomized samples of virgin olive oils collected from Hama, Aleppo, Daraa, Latakia, Homs and Idleb to investigate the relationship between the quality indices of oil purity (peroxide value, the figure iodine, coefficien t of acidity, the absorption coefficient qualitative Xultraviolet K270 and distributed fatty acids) and related volatile flavor components compared with what is published in the literature. The results also showed that the quality indices of Hama and Lattakia، s samples in terms of extra virgin olive oil and the first class of virgin olive oil were not compatible with the Syrian Standards and metrology (2000/182) while the concentrations of fatty acids for samples of Idleb, Homs, Latakia, Deraa and Aleppo were within the scope of Syrian standard. However, their distribution in Hama samples did not comply with the ratios set forth in the Syrian specifications. Forty three volatile compounds were isolated and they correspond with what is published. The samples of research showed somewhat of similarity to a large extent with the exception of a sample of Hama, where a decline was observed in the content of volatile flavored materials. It was noticed that the essential composition of volatile compounds of the samples was aldehydes followed by ester of fatty acids and then hydrocarbons. The study showed that the technique used in this research was fast and efficient in extraction and identification of volatile compounds.
The aim of this research is to study the absorptive effect of high density (HDPE) polyethylene pipes for the hydrocarbon compounds on the characteristic (Force, Elongation) curves. To verify this, we immerse some parts of the pipe in different hydroc arbon mediums containing gasoline, diesel, and motor oils of (10 and 40) calibre. The result show that these compounds have a bad effect on the submission force, neck formation, and damage force. The experimental results also show that motor (engine) oils have a similar effect on gasoline despite low absorption percentages.
The aim of this work is to study the rheological and mechanical properties of Poly(lactic acid) and High density polyethylene and blends (PLA/HDPE) in the molten state with recpect to shear stress, temperature and blends compositions using brabender mixer.
The objective of this research was to identify the potentials of Syrian olive oil exports through studying the current situation of the Syrian olive oil in the world and local markets and the most important factors effecting its competitiveness ca pabilities in the world markets. This study was built on analyzing the primary data obtained from the delivered questionnaires, searches lists and personal interviews with the exporting and manufacturing companies (30 companies) of Syrian olive oil. Some of the economic indicators were calculated to determine the competiveness status in the import markets. Results indicated that the Syrian olive oil exports had suffered from low competitiveness indicators of production which was 0.12 in the most important import markets for the studied period. In addition, the increased pricing levels compared with other competitors in the same markets had reached an average of 3083.98 dollars per ton representing 106% of world export price, high production costs, the reduction of the market penetration rate related to Syrian olive oil exports in the most important markets amounted to about 0.245 during the second period of the study. The low value of the dependence on export indicator compared with the competitive countries where Syria occupied the seventh place .This means that Syria doesn’t have a good export efficiency, lack of marketing researches on the foreign markets, the absence of promotional programs the restrictions applied by the European Union on the exports of Syrian olive oil, lack of access to all distribution outlets due to the dependence of the exported companies on the exclusive agents in the process of distribution and marketing. The results had recommended that the establishment of a comprehensive database and accurate studies is very necessary for the Syrian exported products, in addition to detailed studies about the major and promising markets to Syrian olive oil exports, iImproving the Syrian business environment to encourage the foreign direct investment to support the competitiveness of Syrian olive oil exports.
Some kinetic parameters have been determined in this work for thermal and catalytic cracking of the mixed of polyethylene and polypropylene using batch method. The cracking reaction was carried out at different temperature 470,490 and 510oC under atmospheric pressure. The mass of products (liquid and gas fractions) were determined and used to plot the curves of the thermal and catalytic decomposition. We used two types of catalysts: Syrian natural Zeolite and the same after loading with sulfate ions using impregnation method. The thermal cracking has a long time and has firs-pseud order reaction. While in the case of catalytic process we note that the reaction finished in the short time and the process is the Zero-pseud order reaction. The rate of the cracking increased very much, the rate constant was k1=0.0032.min-1 in the thermal cracking at 4700C and ko=0.111.min-1 in the case of catalytic cracking in presence of Z catalyst and ko= 0.206 min-1 in presence of 15-SO4 2-/Z as catalytic at the same temperature. In the other hand activation energy was 208.7 kj/mol in the thermal process and decreased to 116.6 kj/mol at Z catalytic presence and to 87.3 kj/mol at 15-SO4 2-/Z catalytic presence.
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