Data on the application of the focused beam reflectance measurement (FBRM): A process parameters dataset for the ethyl cellulose (EC) microparticles preparation by the solvent evaporation method

The data article refers to the paper “Effect of solvent type on preparation of ethyl cellulose microparticles by solvent evaporation method with double emulsion system using focused beam reflectance measurement” [1]. Data presented here include the effect of solvent type, method of emulsification (an oil-in-water (O/W) or a water-in-oil-in-water (W/O/W)), external aqueous phase volume, stirring speed and ethyl cellulose concentration on the preparation of ethyl cellulose microparticles. Data also refer to the effect of above mentioned factors on the solidification rate, hardening time, particle size, particle size mean, chord length distribution (CLD) and chord count of microparticles. Additionally, data exhibit process parameters when emulsion droplets transformed into solid microparticles during fabrication. The transformation of the emulsion droplets into solid microparticles occured within the first 10, 10.5, 12 and 60 minutes (O/W), and the first 12, 11.5, 10 and 90 minutes (W/O/W) when dichloromethane/methanol (1:1), dichloromethane, ethyl acetate and chloroform were used respectively. Either in O/W and W/O/W emulsion system, Chloroform gave smallest square weighted mean chord length. In contrast, its chord counts was not to be the highest.


a b s t r a c t
The data article refers to the paper "Effect of solvent type on preparation of ethyl cellulose microparticles by solvent evaporation method with double emulsion system using focused beam reflectance measurement" [1] . Data presented here include the effect of solvent type, method of emulsification (an oil-in-water (O/W) or a water-in-oil-in-water (W/O/W)), external aqueous phase volume, stirring speed and ethyl cellulose concentration on the preparation of ethyl cellulose microparticles. Data also refer to the effect of above mentioned factors on the solidification rate, hardening time, particle size, particle size mean, chord length distribution (CLD) and chord count of microparticles. Additionally, data exhibit process parameters when emulsion droplets transformed into solid microparticles during fabrication. The transformation of the emulsion droplets into solid microparticles occured within the first 10, 10.5, 12 and 60 minutes (O/W), and the first 12, 11.5, 10 and 90 minutes ( -To measure solidification time, data were collected from emulsion droplet which in time showed constant particle size which is assumed as formation of solid microparticles.
-At the time when solid microparticles were formed, the FBRM will count particle size means as well as the distribution of particle size of those solid microparticles. Description of data collection When a particle is crossed by the beam of FBRM, its reflection will be detected as a chord. The length of solid microparticles were collected as the particle size data, while amount of particles distributed and detected by beam was recorded as particle count as well as the distribution of particle size.

Value of the data
• The data can be used as reference in determining the solvent to be used in microparticles fabrication • The data can be used as reference in determining which method of emulsification to be employed in fabrication of microparticles • The data proved that FBRM can be used for on line monitoring of microparticle using solvent evaporation method • The data can be used for further study on parameters which affect microparticles fabrication by solvent evaporation method when FBRM is used as on line monitoring tools

Data Description
The data presented here describe the influence of solvent type and emulsification method, on particle size of ethyl cellulose microparticles ( Table 1 ). Tables 2 and 3 Table 1 Effect of solvent type and preparation method on particle size mean of microparticles using different method of emulsification.

Solvent
Particle size mean (μm) ( ± SD)    weighted) during evaporation process when using different method of emulsification was shown in Fig. 3 a-  As an addition, on line monitoring by FBRM can study the effect of stirring speed on (a) square weighted mean chord length and on (b) the number of chord counts during evaporation process ( Fig. 6 ). The effect of stirring speed on distribution of square weighted chord length can also be monitored ( Fig. 7 ). Data on the effect of external phase volume on square weighted mean chord length (a) and the number of chord counts (b) during solvent evaporation process was also presented ( Fig. 8 ). Effect of volume of external phase on distribution of square weighted chord length was also studied by FBRM ( Fig. 9 ). The effect of ethyl cellulose concentration on CLD, chord counts, square weighted mean chord length and hardening rate of microparticles from emulsion droplets presented in Fig. 10 while the distribution of hardening time from droplets to solid microparticles presented in Fig. 11 . Moreover, data on the effect of solvent on the morphological surface of microparticles with different as O/W ( Fig. 12 ) or as W/O/W system ( Fig. 13 ) were also presented. Further, different polymer concentration effect on surface morphology of microparticles was shown in Fig. 14 .

Microparticle preparation
Microparticles were prepared by solvent evaporation methods using either W/O/W or O/W emulsion system [1 , 5] . In W/O/W emulsion, water was emulsified with solution of ethylcellulose in different solvent, to which dichloromethane, chloroform, ethyl acetate or dichloromethane:methanol (1:1) (7.5% w/v). Sonication was performed for 30 s (Sonoplus® HD 250, Bandelin Electronic GmbH & Co. KG, Berlin, Germany) under ice-cooling. This primary W/O emulsion was then dispersed into 800 ml 0.25% PVA (w/v) solution as external aqueous phase. Next, the emulsion was stirred for 4 h at 500 rpm using a propeller stirrer (Heidolph Elektro GmbH & Co. KG, Kelheim, Germany). Microparticles were collected by wet sieving and were washed with deionized water. The microparticles were dried at ambient temperature for 24 h and kept in a desiccator during storage.
In O/W-dispersions method, polymer Ethylcellulose (7.5% w/v) was dissolved in either dichloromethane, chloroform, ethyl acetate or dichloromethane:methanol (1:1) and then was dispersed into 0.25% PVA (w/v) solution (800 ml) as external aqueous phase. The emulsion was       Investigation on the effect of external aqueous phase volume were conducted by using a solution of Ethylcellulose (7.5% w/v) in dichloromethane using 400 ml and 800 ml water with 0.25% PVA (w/v) as stabilizer. The emulsion was stirred with a propeller stirrer for 4 h at 200 rpm. The next steps of microparticle collection and drying were similar with processes mentioned above.

Viscosity measurement
The viscosity were measured using an Ostwald viscometer type 50111/Ia by dissolving 7.5% w/v Ethylcellulose 4 cP in either dichloromethane, dichloromethane:methanol (1:1), chloroform or ethyl acetate as solvent. The instrument constant was K = 0.05152 mm 2 /s 2 (Schott-Geräte GmbH, Hofheim, Germany) at 25 °C (n = 3). The viscosity of emulsion system as O/W or W/O/W were analysed as well. The viscosity were calculated as follows and listed in Table 2 :

Solubility determination
The solubility of ethyl cellulose 4 cP was determined in 1 ml of four different solvents (dichloromethane, dichloromethane:methanol (1:1), chloroform and ethyl acetate). To assure that the saturated solution has already obtained, samples were sealed and shaken at 37 °C and 75 rpm (horizontal shaker GFL 3033, Gesellschaft für Labortechnik GmbH, Burgwedel, Germany) for 24 h (n = 3). The saturated solution was filtered and the solvent was evaporated at room temperature. The mass of ethyl cellulose film was determined by an analytical balance (Analytical Balance Sartorius Research A200S, Sartorius GmbH, Göttingen, Germany). Result of ethyl cellulose solubility test shown in Table 2 .

Online investigation by FBRM measurement
The probe of FBRM (Lasentec® FBRM D600T, Mettler Toledo AutoChem, Inc., Redmond, WA, USA) was positioned in the emulsification vessel to ensure good flow against the probe window.