gels have been described as materials that are  easier to recognize than define  . most of the times this problem comes from industry , which develops products with a gel name , just to be attractive to consumers . however , gels have been accepted as semisolid materials comprising low concentrations ( < 15% ) of gelator molecules to form a network self - assembly that entraps the solvent ( in organogels both nonpolar components ) , preventing flow due to surface tension . gels can be defined both from a rheological behavior and from a structural feature . in a rheological point of view , a gel is a system that does not flow and has the presence of a plateau region of storage modulus and a low tan ( < 0.1 ) at an angular frequency from 10 to 10  rad / s . the structural definition is based on the connectivity of the system . gel is a system consisting of molecules , particles , and chains , which are partially connected to each other in a fluid medium by crosslinks to the macroscopic dimensions . organogels have been attracting much attention in biomedical and pharmaceutical fields , where the erosion of gels in stomach and intestines is important for drug delivery [ 4 , 5 ] ; therefore gels erosion has been applied for this purpose . as oils are safe materials and are suitable for lipophilic components , they are considered a good option for organogels elaboration . that is why food industry is very interested in this type of systems as a replacement of hydrogenated fats . thus , understanding organogels , definition is closely related to their characteristics and their crucial potential to develop new applications . the case of fat oils is very important due to their applications in food industry . the study of crystal nucleation , dissolution , and agglomeration in the overall precipitation scheme implies practical difficulties . nucleation and crystal growth are spontaneous processes , which diminish the energy of the growing particle and nucleation process in order to overcome activation energy ; that is , the critical cluster ( critical size ) is the cluster with maximum gibbs free energy . the activation barrier may be represented by three parameters : supersaturation ratio , reaction temperature , and interfacial energy . following crystal formation in organogels can give detailed information on how their preparation is affecting their final structure . the crystallization behavior is related to concentration of gelator , cooling rate [ 11 , 12 ] , and shear rate on fat crystals [ 13 , 14 ] . depending on the system , gels are formed by different forces and interactions and there are some parameters that affect , such as ph , ionic force , and mechanical forces . the plastic fat gels are formed due to the aggregation of fat crystals by several forces as van der waals , dipole - dipole , hydrophobic , and hydrogen bond interactions between crystals . fractal is a geometric pattern that is repeated at every smaller scale to produce irregular shapes and surfaces . hence , since the study of organogels is very complex , it must include structural analysis and rheological and thermal behaviors in order to have a clear understanding on how preparation parameters are affecting the final product . thus , our objective was to evaluate the influence of gelator ( type and concentration ) , type of vegetable oil , stirring speed , and temperature preparation on the physical properties of obtained organogels . three different vegetable oils ( soybean , canola , and corn oil ) were used . they have important differences in composition of saturated fatty acids ( sfa ) , monounsaturated fatty acids ( mufa ) , and polyunsaturated fatty acids ( pufa ) . the approximate compositions of soybean ( sfa 15.65% , mufa 22.78% , and pufa 57.74% , wesson brand ) , canola ( sfa 7.36% , mufa 63.27% , and pufa 28.14% , wesson brand ) , and corn ( sfa 12.94% , mufa 27.57% , and pufa 54.67% , mazola brand ) were considered . these oils were bought at a local supermarket in new brunswick ( new jersey , usa ) . myverol ( mainly monoglycerides glyceryl monostearate 49% , glyceryl monopalmitate 48% , and calcium silicate 3% ) and myvatex ( mixture of monoglycerides and diglycerides , soy monoglycerides 3545% , stearic acid monoester with propane-1 - 2-diol 4050% , sodium 2-stearoyl lactate 1015% , and calcium silicate 3% ) were provided by kerry , mexico / usa , and used as gelator agents . gelators myverol ( mv ) and myvatex ( mx ) at three different concentrations ( 8 , 9 , and 10% ) were heated ( 70 , 80 , and 90c ) on glass containers until complete melting , and then either vegetable oil ( soy ( sy ) , canola ( ca ) , or corn ( cn ) ) was added . samples were stirred ( t 25 digital ultra - turrax , ika , north carolina , usa ) for five minutes at three independent speeds ( 3600 , 7200 , and 12000  rpm ) to homogenize them ; then , samples were cooled to room temperature and stored in refrigerator for 24 hours . dynamic frequency sweep tests were performed in a rheometer ( ares rheometer 902 - 30004 , ta instruments , new castle , de , usa ) using parallel plates geometry ( 25  mm diameter ) under the following experimental settings : strain 0.1% , temperature 20c , frequency sweep 0.1100  rad  s , and a gap of 1  mm . the g and g modules , complex viscosity , and delta tangent for each experimental sample were obtained . polarized light microphotographs of organogels were obtained using a polarized light microscope linkam brand ( t95 system controller ; t95 linksys 32 soft , 2009 , tadworth , uk ) . it was equipped with a q imaging camera ( color rtv 10 bit ) using an olympus th4 - 100 halogen lamp power supply unit ( lts120 temp . controlled stage ) . images were taken at 20c , and video was taken using the camtasia studio v 7.0 ( build 1426 , 2010 , techsmith corporation , okemos , mn , usa ) . thermal behavior of samples was studied using a differential scanning calorimeter ( dsc q2000 ta instruments , schaumburg , ill , usa ) equipped with refrigerated cooling system ( rcs 40 ta instruments , schaumburg , ill , usa ) . samples were heated at 120c ( 30  min ) for deleting fat thermal memory . x - ray diffraction experiment was developed by the use of a pxrd conduced with a d / m-2200 t automated system ( ultima rigaku , tokyo , japan ) with cu k radiation  = 1.5406  a. patterns were collected at 2 angles of 3 to 50 at a scan rate of 2/min . a graphite monochromator was used and the generator power settings were fixed at 40  kv and 40  ma . 2010.01.30 , woburn , massachusetts , usa ) for clarifying peaks , applying a single functional filter smoothing and five cycles of fourier deconvolution . the fractal dimension of the samples was calculated using ( 1 ) according to a described method , which is based on the avrami relationship . consider 
 ( 1)ln(1xcr)=ktd , 
 where xcr is the crystallinity of the system ; t is time ; k is a constant ; and d denotes the dimension of growing . d and k were calculated by nonlinear estimation using levenberg - marquardt algorithm ( statistica v 7.0 , tulsa , ok , usa ) . crystalline fraction of samples was calculated adjusting values from complex viscosity of the system removing complex viscosity of the solvent : 
 ( 2)xcr=(t)(). a universal relation has been developed , but in the present work a previous relationship was used , supported by earlier theoretical work   in order to evaluate structural parameters . in this experimental work , a three - dimensional colloidal network was considered as being composed of interconnected flocs and the fractal dimension was used to quantify the relationship between the average floc size and the particle concentration of the colloidal network . the fractal nature of fat crystal networks has been already presented   and explained the power - law relationship followed by g and the solid fat content ( sfc ) data for fat samples with low solid fat content ( < 10% ) . rheological data from experimental work can lead us to obtain a parameter related to elastic modulus  ( the solid fraction previously obtained by xcr ) ,  , and m , obtained by nonlinear estimations ( statistica v 7.0 , levenberg - marquardt algorithm , tulsa , ok , usa ) . the hamaker constant was determined following reported methodology [ 18 , 22 ] where a is the hamaker constant , a is the diameter of the particles within a floc , and d is the average distance between clusters . 14.0.0.567 , menlo park , ca , usa ) applying channel separation ( cmyk ) in order to obtain floc and distance parameters as clearly as possible . consider 
 ( 4)~a3ad2 . comparisons and calculations of parameters were obtained by nonlinear estimation with statistica software ( ver . 7.0 , 2007 , tulsa , ok , usa ) using levenberg - marquardt algorithm . mean effects on interactions between processing parameters and fractal dimensions and microstructural parameters were determined by screening design ( jmp ver . higher values of g were observed for mv gels at higher frequencies used at 10% gelator concentration , 70c , and 12000  rpm . the elastic module ( g ) thus , this value may indicate that , at higher shear rates , structural order produced by lipid chains ( i.e. , acylglycerides ) is organized in a more stable configuration , as a function of more contact between molecules that lower the necessary energy for self - organization and structure building . theoretical analysis of gels indicated that small particles could be aggregated to form large clusters with tenuous , chain - like , and self - similar structures that eventually span the entire enclosing space . this behavior not only was influenced by shear rate , but also seems to be influenced by the type of gelator used as can be seen in figures 1 , 2 , and 3 . from these figures it can be observed that at the same conditions mv organogels always give higher elastic modules in comparison with the mx . the mechanisms of aggregation of gelators in organogels occur primarily through van der waals forces , specific intermolecular hydrogen bonding , electrostatic forces , - stacking , or london dispersion forces . thus , in function of the solvent and the gelator molecule , which type of intermolecular force predominates to stabilize the self - assembly primary structure , the growth mode , and finally the organogel microstructure and its thermomechanical properties is determined . however , the relationship between gelator chemical structure and its gelling capability is not evident a priori in most cases . however , it is desirable for gel modules to maintain a stable behavior during the complete frequency range . solid behavior is predominant in all samples at the experimental shear range used , so it can be considered suitable for an excipient . similar behavior was observed in the organogels prepared with different oils ( figure 3 ) , except for soy oil ( sy ) , which seems to have a different effect , producing more elastic gels at the same conditions . sy seems to be favored by its higher solid fatty acids content , which gives more elastic modules to myvatex gelator samples . an explanation of this behavior has been already reported . in there , candelilla wax and amides derived from ( r)-12-hydroxystearic acid were tested as gelators of safflower oil , observing that the increase in the hydrocarbon chain length raises both the organogel resistance to deformation and its instant recovery capacity . however , the extended recovery capacity of the gel decreased . as can be seen in figure 3 , the behavior of each sample made with different oil at the same conditions changes significantly . this may be related to the different composition of vegetable oil and how each component is reacting at different preparation conditions . although the higher elastic modules are obtained with canola ( ca ) and corn ( cn ) oil samples , in general ca gave the higher elasticity samples in comparison with those made with cn and sy . this behavior could be related to the monounsaturated fatty acids ( msfa ) and polyunsaturated fatty acids ( pufa ) contents . obtained micrographs ( figure 4 ) showed that myvatex tends to crystallize as spherulitic forms , some of them with larges spaces between these spherulites , while samples prepared with myverol crystallized as fibrillar networks . it was reported   that the higher number of hydroxyl groups related to the diacylglycerides was correlated with a lack of gelation into the organogels . this gives further evidence to the fact that hydrogen bonding is critical to the organogelation . statistical analysis of enthalpy data showed that gelator type and its concentration ( p < 0.05 ) were the most important factors that influence enthalpy ( table 1 ) . the statistical analysis showed a very complex phenomenon influenced by the following interactions : oil  oil , concentration  gelator , and gelator  temperature . organogels obtained with myvatex gelator showed two different nucleation stages related to the presence of two main types of molecules ( mono- and diacylglycerides ) ; so probably distributed free energy makes gels tend to crystallize as spherulites rather than as a needle shaped network . however , not only the gelator is important , but also its concentration and several interactions including vegetable oil type and temperature are important . at this point , it is interesting to highlight that the temperature factor does not have influence on the enthalpy of organogels . thus during cooling , both components might develop a mixed molecular packing with vegetable oils . on the other hand , myvatex gelator ( mx ) does not seem to be affected significantly by any preparation conditions . finally , it is clear that the use of myverol at higher concentrations produces organogels with higher values of gelation enthalpies , indicating more stable structures . a comparison of d spacing data was done in order to elucidate not only possible arrangements in packing , but also the most probable polymorphic forms in batches . since they were complex mixtures of components ( nonpure components ) , at least two different packings and polymorphs were selected . it can be noticed that most of the structures obtained are mainly  polymorphs , because most of them are amorphous materials and b crystals are present only in part . although mx also gave a good structure , it was only possible under the highest energy conditions . in order to compare different samples behaviors with a representative value , samples fractal dimensions ( table 3 ) were obtained from rheological behavior according to others , on which we should obtain crystalline fraction of each sample based on complex viscosity behavior and then get fractal parameter from nonlinear estimation . once fractal data was obtained , anova test was developed looking for some important influence . the model obtained was too complex and t - student was not sensitive enough to detect means without a significant error . even in general no means were detected ; some interesting effects were found when gelators and oils were blocked . also , several works on formation of organogels studied and correlated by avrami exponent ( n ) with fractal dimensionality have been reported [ 17 , 28 ] . however , it was indicated   that it may be inappropriate to compare avrami derived fractal dimensionalities from several systems in which different nucleation mechanisms for gelators are involved . thus , there are reports   on homogeneous nucleation with a fractal dimensionality near 2 , while others   found a fractal dimensionality near 1 in a heterogeneous nucleation system . thus in the present experimental work , fractal dimensionality was in that range ( lower than 2 ) , particularly when using mono- and diacylglyceride blends , indicating a possible heterogeneous nucleation process . as an example , when the variable gelator ( myvatex ) was blocked on canola oil ( p = 0.047 ) , the fractal dimension ( d ) was affected by the gelator concentration . also , when corn oil temperature was blocked , the results indicated that higher temperatures render higher fractal dimensions . the fractal dimensions ( d ) determined by the particle counting method are sensitive to the spatial distribution of particles in the crystal network . higher fractal dimensions occur in networks that are more ordered , whereas networks that arise from a more disordered nucleation and growth process result in lower fractal dimensions . the fractal dimension value found in the present work was lower , similar , and higher   than other reports . even though we did not find any significant mean on rpm versus d parameters , independently of the gelator , d fractal dimension tends to decrease as rpm increases . this could mean that as the shear rises there is an increase in disorder of the structure , which is contrary to reports from others [ 13 , 14 ] . this could also indicate that different conditions are affecting gels structure and there is not necessarily a codependence on shear rate and order of the structure . the highest value of  was found for myverol ( mainly monounsaturated fatty acids ) in comparison with myvatex . the gelator molecules are related to the nature of the short - range weak forces and the strong solvent dependence on the molecular self - assembling capabilities , so that molecules with higher molecular weight could affect crystal growth and its consequence on fiber interpenetration among vicinal spherulites . however , not only gelator molecule is important , but solvent nature and interaction solvent - gelator are important too . in this way , experimental data was blocked for the two gelators in separated assessments . results showed that myverol is affected by the type of oil used for the sample ( p = 0.0085 ) , by the oil - concentration interaction ( p = 0.04 ) , and the concentration quadratic effect as well ( p = 0.0072 ) . meanwhile for myvatex , the oil effect was also important ( p = 0.0766 ) , but contrary to myverol , it was affected by the oil quadratic ( p = 0.43 ) and the temperature quadratic effects ( p = 0.032 ) . thermal parameters could be helpful to explain this behavior , because they are associated with the molecules polarity and the energy of the molecular interactions that are established with the crystal structure of gelators in their neat and organogel states . thus , the energy related to the organogel depends on the energy of the noncovalent interactions involved during the molecular self - assembly . as can be seen , higher enthalpies were observed for myverol in comparison to myvatex , like a structural parameter . monoglycerides are known to be good initiators of fat crystallization and the matching in saturation and carbon chain length of both the gelator fatty acids and the oil phase are important in the particular lipid - lipid interactions . for the hamaker constant ( table 3 ) , gelator appears as a main effect ( p  0.0001 ) , followed by the stirring speed ( p = 0.052 ) , as well as the interaction gelator - stirring speed ( p = 0.088 ) . also the bilayer packing seems to be favored by the particularities on ca oil composition of mainly the high mufa and low pufa contents . also the first gelator tends to form needle shaped network structures with better intermolecular forces according to their hamaker constant and xrd analysis . the stirring speed should be an important parameter to take into account , as well as the gelator and its concentration . it was found that temperature does not seem to be an important parameter in gels preparation . finally , it is important to point out that most of the influence of the stirring speed conditions is apparently related to the oils higher mufa and low pufa contents .
the objective of this study was to evaluate the influence of gelator , vegetable oil , stirring speed , and temperature on the physical properties of obtained organogels . 
 they were prepared under varying independent conditions and applying a fractional experimental design . from there 
 a rheological characterization was developed . 
 the physical characterization also included polarized light microscopy and calorimetric analysis . 
 once these data were obtained , x - ray diffraction was applied to selected samples and a microstructure lattice was confirmed . 
 commonly , the only conditions that affect crystallization have been analyzed ( temperature , solvent , gelator , and cooling rate ) . 
 we found that stirring speed is the most important parameter in the organogel preparation .