poster - International Conference of Agricultural Engineering

poster - International Conference of Agricultural Engineering poster - International Conference of Agricultural Engineering

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THERMOFHYSICS PROPERTIES OF THE OIL EXTRACTED OF THE GENOTYPES OF CASTOR BEAN Katcilanya Menezes de Almeida 1 , Av. Aprígio Veloso, 882, Campina Grande, PB, 58429-900, Brazil Juarez Paz Pedroza Av. Aprígio Veloso, 882, Campina Grande, PB, 58429-900, Brazil Napoleão Esberard de M. Beltrão, Av. Oswaldo Cruz, 1143, Campina Grande, PB, 58428-095, Brazil katcilanya@yahoo.com.br Abstract: The objective of this work was to evaluate the possible changes in the thermophysics properties between the oil extracted from three different genotypes of castor bean, two modified cultivars (BRS Paraguaçu e BRS Energia) and other wild genotype caught in a vacant land, just for a standard comparison. The oil was characterized through analysis thermo-physics: density, point of minimum flow, viscosity and specific heat. The data were statistically analyzed and compared by analysis of variance for a randomized design using ASSISTAT program 7.0 version. The specific heat found to each genotype was: 0,2742 cal/gºC to BRS Paraguaçu; 0,3653 cal/gºC to BRS Energia and 0,2792 cal/gºC to the wild one. The point of minimum flow ranged from -18,17 to -18,47 ºC. In relation to density variable there was no significant interaction between the genotypes, but it’s reduced significantly with the increase of the temperature. The viscosity showed significant differences between the genotypes and also reduced significantly with the increase of the temperature. Key-words: Ricinus communis L., oil, thermo-physics. 1. Introduction The oil extracted from castor bean seeds has a high industrial value, due to versatility of applications constituting a raw material for the manufacture of plastics, synthetic fibers, enamels, resins and lubricants (Freire, 2001; O `Brien et al. 2000). In addition to the various uses of castor oil, it has been widely studied for biodiesel production, because of the specific characteristics: high productivity, it can be miscible in methanol and ethanol, it can be used as an additive until 10% (v/v) and high viscosity (Delgado et al., 2011). Although many applications recognized, there are still incipient technological information about the variability among genotypes of castor oil, which makes a more complete exploration of the industrial potential of this product for other applications (COSTA et al., 2008). 2. Materials and Methods The seeds of castor beans Energy BRS, BRS Paraguaçu (produced by the Empresa Brasileira de Pesquisas Agropecuária – Embrapa/CNPA) and wild one were subjected to cold pressing in a mechanical press with manual pressure capacity of 30 tons without any pretreatment. After extraction the samples, it were subjected to centrifugation at a speed of 3000 rpm during five minutes, to remove some impurities and waste.

The density analysis was performed with the aid of a 25 mL beaker where the sample was weighed and measured, then subjected to the desired temperature, -15, -10, -5, and 0 o C in vertical freezer, 20, 40 and 60 o C in B.O.D, 80 o C in an oven, monitored by a thermocouple, after get the temperature, the sample was weighed again and it was checked to made a relationship between the mass and volume (Equation 1) to obtain the density. m ρ = v (1) where: ρ = Density (g/cm 3 ); m = mass (g); v = volume (cm 3 ) Determination of the point of minimum flow was second 1149 NBR- Oil Product - The point of minimum flow is the lowest temperature at which the lubricating oil is still flowing. In the test, it cooled the oil sample within a tube and each decrease of 3 °C in temperature, it was observed whether or not the movement of the surface of the oil inside the tube and, after 5 seconds is lacking movement that temperature, it will have reached the freezing point and a temperature of 3 °C above this temperature will be at the point of minimum flow. It was used to determine the viscosity, the B3 Hoppler viscosimeter. The viscosity of castor oil was determined in a temperature range of -15, -10, -5, 0, 20, 40, 60 and 80 0 C with the aid of a thermostated bath for obtaining the same. This is done through the time interval (Δt) that particular sphere of specific mass (ρ), constant (K) and diameter (D) known travels a distance (ΔL). The calculation is done by Equation 2: µ = K (δ 2 - δ 1 ) ∆t (2) which: μ = viscosity, mPas -1 K = constant of the sphere, mPacm -3 δ 2 = specific mass of the sphere, gcm -3 δ 1 = density of sample, gcm -3 ∆t = fall time, s. The specific heat was determined using a handmade colorimeter constructed in a thermical bottle with a layer of glass fiber placed inside of a PVC tube, where a digital thermometer measures the temperature inside the calorimeter. To determine the heat capacity of the calorimeter are placed 100 g of water at environmental temperature (25 °C) within the calorimeter; this, in turn, it is sealed with a rubber coupled to a thermometer indicating a temperature T 1 within the calorimeter and then are placed in the container in 100 g of water at an average temperature of approximately 3 °C, corresponding to the temperature T 2 ; stir the calorimeter at the time of 10 min until they reach the equilibrium temperature T 3 . The heat capacity was determined by Equation 3: C 1 m 1 (T 1 -T 3 ) + Ccal (T 1 -T 3 ) = C 2 m 2 (T 3 -T 2 ) (3)

The density analysis was performed with the aid <strong>of</strong> a 25 mL beaker where the sample was<br />

weighed and measured, then subjected to the desired temperature, -15, -10, -5, and 0 o C in<br />

vertical freezer, 20, 40 and 60 o C in B.O.D, 80 o C in an oven, monitored by a thermocouple,<br />

after get the temperature, the sample was weighed again and it was checked to made a<br />

relationship between the mass and volume (Equation 1) to obtain the density.<br />

m<br />

ρ =<br />

v<br />

(1)<br />

where:<br />

ρ = Density (g/cm 3 );<br />

m = mass (g);<br />

v = volume (cm 3 )<br />

Determination <strong>of</strong> the point <strong>of</strong> minimum flow was second 1149 NBR- Oil Product - The<br />

point <strong>of</strong> minimum flow is the lowest temperature at which the lubricating oil is still flowing. In<br />

the test, it cooled the oil sample within a tube and each decrease <strong>of</strong> 3 °C in temperature, it<br />

was observed whether or not the movement <strong>of</strong> the surface <strong>of</strong> the oil inside the tube and, after<br />

5 seconds is lacking movement that temperature, it will have reached the freezing point and<br />

a temperature <strong>of</strong> 3 °C above this temperature will be at the point <strong>of</strong> minimum flow.<br />

It was used to determine the viscosity, the B3 Hoppler viscosimeter. The viscosity <strong>of</strong><br />

castor oil was determined in a temperature range <strong>of</strong> -15, -10, -5, 0, 20, 40, 60 and 80 0 C with<br />

the aid <strong>of</strong> a thermostated bath for obtaining the same. This is done through the time interval<br />

(Δt) that particular sphere <strong>of</strong> specific mass (ρ), constant (K) and diameter (D) known travels a<br />

distance (ΔL). The calculation is done by Equation 2:<br />

µ = K (δ 2 - δ 1 ) ∆t (2)<br />

which:<br />

μ = viscosity, mPas -1<br />

K = constant <strong>of</strong> the sphere, mPacm -3<br />

δ 2 = specific mass <strong>of</strong> the sphere, gcm -3<br />

δ 1 = density <strong>of</strong> sample, gcm -3<br />

∆t = fall time, s.<br />

The specific heat was determined using a handmade colorimeter constructed in a<br />

thermical bottle with a layer <strong>of</strong> glass fiber placed inside <strong>of</strong> a PVC tube, where a digital<br />

thermometer measures the temperature inside the calorimeter.<br />

To determine the heat capacity <strong>of</strong> the calorimeter are placed 100 g <strong>of</strong> water at<br />

environmental temperature (25 °C) within the calorimeter; this, in turn, it is sealed with a<br />

rubber coupled to a thermometer indicating a temperature T 1 within the calorimeter and then<br />

are placed in the container in 100 g <strong>of</strong> water at an average temperature <strong>of</strong> approximately 3<br />

°C, corresponding to the temperature T 2 ; stir the calorimeter at the time <strong>of</strong> 10 min until they<br />

reach the equilibrium temperature T 3 . The heat capacity was determined by Equation 3:<br />

C 1 m 1 (T 1 -T 3 ) + Ccal (T 1 -T 3 ) = C 2 m 2 (T 3 -T 2 ) (3)

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