The potential growing of mobile devices, in terms of hardware
and operating systems, has led to rise new innovative methods of
work depending on new generations of mobile phones and tablet
computers in the completion of various works. Therefore a
new
wave arises moving towards the development (or rewriting)
software applications for this type of devices, rather than for
desktop computers. From this perspective, it has been working in
this research on the design of application for technological
calculations of sugar extraction unit working on Android system,
which is the most prevalent system in smartphones and tablets.
Although, this work is devoted to calculate mass balance of
extraction unit, the main interface of the application has been
developed for integrated application which allows moving between
the various operating stations in a sugar factory.
Running the application shows that it is easy to input data,
navigate between multiple interfaces and accuracy of results.
The optimal conditions for the extraction of polyphenolic compounds from hard
Syrian wheatvarieties (Hourani, Doma1,Bohoos11) were determined using response
surface methodology. A Central Composite Design was used to investigate the effects of
thr
ee independent variables, namely solvent concentration, extraction temperature and
time on the response phenolic content. The independent variables were at three levels and
their actual values selected on the basis of preliminary experimental results. A secondorder
polynomial model was used for predicting the response.
Regression analysis showed that more than 95-97% of the variation was explained by
the models. The optimal conditions for phenolic compounds extraction were found to be
acetone concentration of 49.5 %v/v, extraction temperature of 55.5°C, extraction time of
42.5min, for wheat. Under the optimum conditions the corresponding predicted response
values for polyphenolic compounds were 0.976 mg EGA forHourani, 0.947 mg EGA
forDoma1 and 1.316 mg EGA for Bohoos11. The phenlics were extracted under optimum
conditions to check the validity of model, and the experimental values were 0.969±0.05
,0.932±0.03 and 1.214±0.06 mggalic acid equivalent /g dry weight from wheatvarieties
(Hourani, Doma1,Bohoos11) respectively. The good agreement between predicted and
,experimental values indicated suitability of the model employed and the success of
response surface methodology in optimizing the extraction conditions.
Grapefruit (Citrus Paradisi) is one of many citrus species that are widely cultivated
in the west Mediterranean coast of Syria, the fruit is rich in flavonoid (a natural medical
compounds), naringin considered the major flavonoid in Grapefruit.
Pr
evious studies have documented a wide range of biological effects and therapeutic
properties that belong to naringin; therefore, it became a raw material in pharmaceutical
industries.
It was the aim of this study is to have naringin extracted from grapefruit by an
economic method, and assign its levels, in preparation for industrial investment.
Two types (red blush) and (march) where collected from three districts in Syrian
coast, they were collected at the beginning of harvest season and at the end of it, fruits
grown in sun light and those grown in shade were collected tow, so that healthy fruit and
partly infected.
A water alkaline method was applied to extract naringin, then a quantitive and
qualitative determination was made to the resulting compound.
Results revealed that naringin content in March grapefruit at the beginning of the
harvest season was 45.53 g/kg and 44.8 g/kg in Red Blush grapefruit so on at the end of the
harvest season it was 10.29 g/kg in March and 9.32 g/kg in Red Rlush.
We have concluded that that Syrian Grapefruit have sufficient naringin cotent for
economical investment, and that water alkaline method is a suitable economic method to
extract naringin from grapefruit white peels.
In October 2014, the collected air-green samples of Basil herb were gathered from the region of MashtaAlhulu in the ,Then the volatile oil from fresh samples was extracted with N-Hexane and other samples with steam distilled water, and we have found
the percentage of the volatile oil in the first sample (N-Hexane) is 2,7% , and 2,5% in the second sample (steam distilled water). Suitable conditions were chosen to separate the components of the volatile oil by GC-MS and we noticed : - the first sample (extracted with N-hexane) contain 18 compounds, and they are: Six Terpenes compounds and they form 21.22%,Hydrocarbon compounds form 21.8% from the total weight and they are 7 compounds, and one compound from Ketone class dicycle and its percentage is 2.32%,and two Ester compound and they form 18.96%, One phenolic compound and forms 21.60%, one Ether compound and forms 14.08%. -the volatile oil from the second sample (extracted with steam distilled water) contains 11 compounds, and they are: 6 compounds belong to Hydrocarbon class and they are the main components in the volatile oil with a 91.24% of the oil total weight, One compoundfrom Ether class forms 1.62%, one phenolic compound which forms 3.93%, and three Terpenes compounds and they form 3.17%.
desulfurization study of gas oil is very important, in
order to reduce the resulted pollution from acidic gas SO2, which
results by burning the fuel, and to prevent poisoning of sensitive
catalysts with sulfur, in subsequent processes, and to prev
ent
corrosion of engines and equipment in refineries. So, refineries
have been restricted by very low sulfur content, in their products.
Because the hydrodesulphurization did not demonstrate good
efficiency in reducing the sulfur and aromatics content to the
required limits, it has been to search for alternative or completed
methods for it .One of these processes is the oxidation –extraction
method, which has been studied in our work. We used hydrogen
peroxide as oxidant, and acetonitrile as extraction solvent. We
studied Operation conditions in terms the proportion of oxidant and
extraction solvent to fuel, and we chose the operation temperatures
to suit the specifications of the oxidant and extraction solvent. We
studied diesel specifications, which we applied at it the process of
oxidation and extraction.
In September 2014 the collected air-green samples of Fennel herb
were gathered. Then the volatile oil from fresh samples was
extracted with N-hexane and other samples with steam distilled
water.
The study addresses the synthesis of two organic phosphoric compounds that have
the P-NH-c bridge, They have the following chemical formula (PhO)2P(O)-NH-C(CH3)=CHCN
( abbreviated as PCNO) and The compound (abbreviated as PCNS) The compound
were s
ynthesized in the center of acetonitrile and having a strong base of sodium hydride
NaH by Diphenyl chloro phosphate (PhO)2POCl compounds and Diphenyl chloro thio
phosphate (PhO)2PSCl compound Respectively . Some of the physical and chemical
properties of the synthetic composites, such as the melting point, dissolution , and the
withdrawal of some important spectra such as the IR spectra and the NMR spectra were
used in the extraction of the copper(II) Ions from the of medium sulphates, Lesson of
Partition Coefficient Copper Dcu between aqueous medium of organic medium containing
different concentrations of organic phosphorus compounds prepared previously. Partition
Coefficient copper(II) ion distribution was studied in terms of the change in the value of
PH (PH = 4 --- 6) at the constant concentration of the extract used previously .The
Spectrophotometer for calculating copper concentrations was used Depending on absorption ,
and the two previous components were compared .
