Improved Stability of Emulsions in Preparation of Uniform Small-Sized Konjac Glucomanna (KGM) Microspheres with Epoxy-Based Polymer Membrane by Premix Membrane Emulsification

Uniform small-sized (<10 μm) Konjac glucomanna (KGM) microspheres have great application prospects in bio-separation, drug delivery and controlled release. Premix membrane emulsification is an effective method to prepare uniform small-sized KGM microspheres. However, since KGM solution bears strong alkalinity, it requires the membrane to have a hydrophobic surface resistant to alkali. In this study, uniform small-sized KGM microspheres were prepared with epoxy-based polymer membrane (EP) we developed by premix membrane emulsification. It was found that emulsion coalescence and flocculation occurred frequently due to the high interface energy and sedimentation velocity of KGM emulsions. Emulsion stability had a significant influence on the uniformity and dispersity of the final KGM microspheres. To improve the stability of the emulsions, the effects of the concentration of the emulsifier, the viscosity of the KGM solution, the oil phase composition and the feeding method of epoxy chloropropane (EC) on the preparation results were studied. Under optimal preparation conditions (emulsifier 5 wt % PO-5s, KGM III (145.6 mPa·s), weight ratio of liquid paraffin (LP) to petroleum ether (PE) 11:1), uniform and stable KGM emulsions (d = 7.47 μm, CV = 15.35%) were obtained and crosslinked without emulsion-instable phenomena.


Introduction
Konjac glucomannan (KGM), as a high-molecular-weight polysaccharide, has special physical characteristics such as moisture retentivity, thickening, and gelling properties [1] and bears so many hydroxyl groups that various chemical modifications can be realized on KGM molecular chains [2][3][4][5][6]. KGM microspheres based on KGM powder have great application prospects in the fields of separation and purification [7], cell culture [8], enzyme and cell immobilization [9], drug delivery [10] and controlled release [11]. At present, the research on the preparation of KGM microspheres is insufficient, especially on those with small particle size (<10 µm). The most commonly used method to prepare KGM microspheres is mechanical stirring. In our previous work [12], a technology was developed to prepare KGM microspheres, which included acid degradation, alkali dissolution of KGM powder, emulsion preparation by mechanical stirring, and crosslinking steps. Compared with the traditional provided by Xilong Co. Ltd. (Guangdong, China) was used as crosslinking agent. Other reagents were of analytical purity and were purchased from Beijing Chemical Reagent Company (Beijing, China).

Preparation of KGM Solutions and Determination of the Viscosities of KGM Solutions and Oil Phases
Since 1% (w/w) KGM dissolved in water takes on a gelatin texture, it is too viscous to disperse in oil phase. Therefore, it is necessary to degrade the KGM molecules into small ones to improve its flowability. Here, KGM solutions with different viscosities were obtained by acid degradation. The preparation procedure was shown in Figure 1. A certain amount of hydrochloric acid (HCl, 0.5 M) was mixed with deionized water, and then the Konjac powder was added. With enough stirring, the mixture became jelly and then was heated at 115˝C for 55 min. After that, 45% (w/w) sodium hydroxide was added under vigorous stirring. Finally, 8% (w/w) KGM solutions with different viscosities were prepared ( Table 1).
The viscosities of KGM solutions and oil phases were measured with a Brookfield viscometer (DV-II+Pro) using spindle 62 (50 rpm and 40˝C) and spindle 61 (50 rpm and 25, 40, 50, 60, 70, and 80˝C), respectively. were of analytical purity and were purchased from Beijing Chemical Reagent Company (Beijing, China).

Preparation of KGM Solutions and Determination of the Viscosities of KGM Solutions and Oil Phases
Since 1% (w/w) KGM dissolved in water takes on a gelatin texture, it is too viscous to disperse in oil phase. Therefore, it is necessary to degrade the KGM molecules into small ones to improve its flowability. Here, KGM solutions with different viscosities were obtained by acid degradation. The preparation procedure was shown in Figure 1. A certain amount of hydrochloric acid (HCl, 0.5 M) was mixed with deionized water, and then the Konjac powder was added. With enough stirring, the mixture became jelly and then was heated at 115 °C for 55 min. After that, 45% (w/w) sodium hydroxide was added under vigorous stirring. Finally, 8% (w/w) KGM solutions with different viscosities were prepared ( Table 1). The

Preparation of KGM Microspheres by Premix Membrane Emulsification
The schematic diagram of premix membrane emulsification was shown in Figure 2. The coarse emulsions prepared by traditional method were pressed through a membrane with narrow pore size distribution under high pressure. The particle size of the obtained emulsions became smaller and more uniform. The tubular EP membrane used in this study has inside diameter of 0.8 cm, outside diameter of 1.0 cm and length of 2 cm.

Preparation of KGM Microspheres by Premix Membrane Emulsification
The schematic diagram of premix membrane emulsification was shown in Figure 2. The coarse emulsions prepared by traditional method were pressed through a membrane with narrow pore size distribution under high pressure. The particle size of the obtained emulsions became smaller and more uniform. The tubular EP membrane used in this study has inside diameter of 0.8 cm, outside diameter of 1.0 cm and length of 2 cm. were of analytical purity and were purchased from Beijing Chemical Reagent Company (Beijing, China).

Preparation of KGM Solutions and Determination of the Viscosities of KGM Solutions and Oil Phases
Since 1% (w/w) KGM dissolved in water takes on a gelatin texture, it is too viscous to disperse in oil phase. Therefore, it is necessary to degrade the KGM molecules into small ones to improve its flowability. Here, KGM solutions with different viscosities were obtained by acid degradation. The preparation procedure was shown in Figure 1. A certain amount of hydrochloric acid (HCl, 0.5 M) was mixed with deionized water, and then the Konjac powder was added. With enough stirring, the mixture became jelly and then was heated at 115 °C for 55 min. After that, 45% (w/w) sodium hydroxide was added under vigorous stirring. Finally, 8% (w/w) KGM solutions with different viscosities were prepared ( Table 1).

Preparation of KGM Microspheres by Premix Membrane Emulsification
The schematic diagram of premix membrane emulsification was shown in Figure 2. The coarse emulsions prepared by traditional method were pressed through a membrane with narrow pore size distribution under high pressure. The particle size of the obtained emulsions became smaller and more uniform. The tubular EP membrane used in this study has inside diameter of 0.8 cm, outside diameter of 1.0 cm and length of 2 cm.  The preparation of KGM microspheres by premix membrane emulsification was as follows: the mixture of liquid paraffin and petroleum ether (weight ratio 7:5, 10:2, 11:1, 12:0) with an emulsifier PO-5s (3%, 4%, 5%, 6%) was chosen as oil phase. Aqueous phase of KGM solution (8.0 wt %, 3 mL) was emulsified in oil phase (40 mL) by homogenization (3600 rpm, 1 min) to form coarse emulsion. Then the coarse emulsion was poured into storage tank and pressed through EP membrane five times under nitrogen pressure to achieve uniform emulsions. EC (2 mL) as crosslinking agent was slowly added into the emulsions at 60˝C by burette, and then the mixtures were kept at 60˝C for 8 h to obtain the particles. Finally, the KGM particles were collected and successively washed by petroleum, ethanol and water. The pore sizes of EP membranes were 14.80 µm with operating pressure of 85 kPa. Recipe for the preparation of KGM microspheres was shown in Table 2.

Determination of the Size and Size Distribution of KGM Emulsions
The average KGM emulsions size and size distribution coefficient of variation (CV) were determined by automatic analysis software on the basis of optical photographs taken by optical microscope (XSZ-H3). Diameters of over 500 droplets were analyzed to calculate the average particle size and particle size coefficient variation according to Equations (1) and (2). Wherein, d i was the diameter of a single microsphere, d was the number-average particle diameter.

Determination of Interfacial Tension between Aqueous and Oil Phases
The interfacial tension between aqueous and oil phases was determined by Contact angle system OCA (Dataphysics, Berlin, Germany). The aqueous phase was injected into the oil phase through the pinhole under the action of the microflow pump. This process would be recorded by video imaging system and then the interface tension was calculated through the video.

Results
In the preparation process of KGM microspheres with small particle size, emulsion coalescence and flocculation occurred due to the high interface energy and sedimentation velocity of KGM emulsions. Emulsion stability had a significant influence on the uniformity and dispersity of the final KGM microspheres. To improve the stability of emulsions, the effects of the concentration of the emulsifier, the viscosity of the KGM solution, the oil phase composition and the feeding method of EC on the preparation of KGM microspheres were studied.

Effects of Emulsifier Concentration on the Preparation of KGM Microspheres
Emulsifier adsorbed on the interface between oil and water could improve the stability of emulsions by forming a layer of viscoelastic membrane with a certain strength [26]. The emulsifier concentration has an important effect on the performance of membrane emulsification. After preliminary investigation, PO-5s was chosen as an emulsifier and the effects of its concentration on the preparation of KGM microspheres were investigated. Preparation parameters are shown in Table 2 (S1, S2, S3, S4).
The emulsification results are found in Figure 3 (S1, S2, S3, and S4). It shows that when the emulsifier concentration was increased from 3 wt % to 5 wt %, both the CV values and particle sizes of the KGM emulsions changed little. When the emulsifier concentration reached 6%, the CV value (20.64%) and the particle size (7.84 µm) had marked changes. The effects of the emulsifier concentration were not obvious until it was seriously excessive. The emulsifier played two main roles in the formation of the emulsions. One was lowering the interfacial tension between the oil and water, and the other one was stabilizing the emulsion droplets against coalescence and/or flocculation [27]. Increasing the amount of emulsifier to a proper amount could improve emulsion stability. However, when the emulsifier was excessive, it would play the opposite role [28]. The excess emulsifier will not further reduce the interfacial energy; instead, it will adsorb on the surface of the membrane pores. The more emulsifier was added, the more likely the EP membrane was covered with emulsifier following when it was wetted by the aqueous phase in the emulsification process. In this process, large-size droplets would be produced.

Effects of Emulsifier Concentration on the Preparation of KGM Microspheres
Emulsifier adsorbed on the interface between oil and water could improve the stability of emulsions by forming a layer of viscoelastic membrane with a certain strength [26]. The emulsifier concentration has an important effect on the performance of membrane emulsification. After preliminary investigation, PO-5s was chosen as an emulsifier and the effects of its concentration on the preparation of KGM microspheres were investigated. Preparation parameters are shown in Table  2 (S1, S2, S3, S4).
The emulsification results are found in Figure 3 (S1, S2, S3, and S4). It shows that when the emulsifier concentration was increased from 3 wt % to 5 wt %, both the CV values and particle sizes of the KGM emulsions changed little. When the emulsifier concentration reached 6%, the CV value (20.64%) and the particle size (7.84 μm) had marked changes. The effects of the emulsifier concentration were not obvious until it was seriously excessive. The emulsifier played two main roles in the formation of the emulsions. One was lowering the interfacial tension between the oil and water, and the other one was stabilizing the emulsion droplets against coalescence and/or flocculation [27]. Increasing the amount of emulsifier to a proper amount could improve emulsion stability. However, when the emulsifier was excessive, it would play the opposite role [28]. The excess emulsifier will not further reduce the interfacial energy; instead, it will adsorb on the surface of the membrane pores. The more emulsifier was added, the more likely the EP membrane was covered with emulsifier following when it was wetted by the aqueous phase in the emulsification process. In this process, large-size droplets would be produced. In the following crosslinking process of the KGM emulsions, the effects brought by the changes of emulsifier concentration cannot be ignored. The crosslinking results are shown in Figure 4 (S1-Crosslinking, S2-Crosslinking, S3-Crosslinking, and S4-Crosslinking). It was found that flocculation and coalescence occurred in S1-Crosslinking. Meanwhile, there were two sizes of particles which conglutinated to the gobbet. With the increase of emulsifier concentration, the phenomena of flocculation and coalescence were weakened and finally disappeared when the emulsifier concentration reached 5%. Emulsifier was the key factor in keeping the stability of the emulsions. Emulsions a with low content of emulsifier were unstable due to the high interface energy [29]. Increasing the emulsifier concentration would reduce the interfacial energy and improve the stability of the emulsions against the occurrence of flocculation and coalescence. In summary, the stability of In the following crosslinking process of the KGM emulsions, the effects brought by the changes of emulsifier concentration cannot be ignored. The crosslinking results are shown in Figure 4 (S1-Crosslinking, S2-Crosslinking, S3-Crosslinking, and S4-Crosslinking). It was found that flocculation and coalescence occurred in S1-Crosslinking. Meanwhile, there were two sizes of particles which conglutinated to the gobbet. With the increase of emulsifier concentration, the phenomena of flocculation and coalescence were weakened and finally disappeared when the emulsifier concentration reached 5%. Emulsifier was the key factor in keeping the stability of the emulsions. Emulsions a with low content of emulsifier were unstable due to the high interface energy [29]. Increasing the emulsifier concentration would reduce the interfacial energy and improve the stability of the emulsions against the occurrence of flocculation and coalescence. In summary, the stability of the emulsions was important for the crosslinking results and 5% (w/w) was the optimal emulsifier concentration in terms of the uniformity and stability of emulsions. the emulsions was important for the crosslinking results and 5% (w/w) was the optimal emulsifier concentration in terms of the uniformity and stability of emulsions.

Effects of the Viscosity of KGM Solution on the Preparation of KGM Microspheres
The content of KGM solution has great significance for the application of KGM microspheres. Since viscosities were the main difference in KGM solutions with different contents, the effects of the viscosity of KGM solution on the preparation of microspheres were studied. By changing the amount of acid in the process of acid degradation, four kinds of KGM solutions (Table 1)  KGM emulsions prepared with different viscosities of KGM solutions as aqueous phase are shown in Figure 5 (S5, S6, S3, and S7). The emulsification results varied little in the particle size and uniformity of emulsions, except for the emulsions prepared with a low viscosity of KGM solutions ( Figure 5 (S5)), the uniformity of which was relatively poor (CV = 22.55%). Coalescence could occur in the emulsification process due to the low viscosity of the aqueous phase, which would decrease the uniformity of the final emulsions. Therefore, high viscosity of aqueous phase showed advantages for obtaining uniform emulsions. Figure 6 (S5-Crosslinking, S6-Crosslinking, S3-Crosslinking, and S7-Crosslinking) shows the crosslinking results. With a low viscosity of the KGM solution ( Figure 6 (S5-Crosslinking)), the final microspheres had a much larger size compared with those before crosslinking. These large microspheres adhered to each other. By increasing the viscosity of KGM solution (Figure 6 (S6-Crosslinking)), two sizes of microspheres were produced. Compared with those in S5, the flocculation and coalescence were apparently weakened. The dispersity and uniformity of the final microspheres got much better after a further increase of the viscosity of the KGM solution ( Figure 6 (S6-Crosslinking and S7-Crosslinking)). Low viscosity of the KGM solution possessed good liquidity contributing to mass transfer, which would induce coalescence in the collision process between emulsion droplets. In addition, low viscosity of KGM solution had low viscoelasticity, which would cause flocculation [30]. In the viscosity range we have studied, the KGM microspheres prepared with high viscosity of aqueous phases had good uniformity and dispersity. The greater the viscosity of the

Effects of the Viscosity of KGM Solution on the Preparation of KGM Microspheres
The content of KGM solution has great significance for the application of KGM microspheres. Since viscosities were the main difference in KGM solutions with different contents, the effects of the viscosity of KGM solution on the preparation of microspheres were studied. By changing the amount of acid in the process of acid degradation, four kinds of KGM solutions (Table 1)  KGM emulsions prepared with different viscosities of KGM solutions as aqueous phase are shown in Figure 5 (S5, S6, S3, and S7). The emulsification results varied little in the particle size and uniformity of emulsions, except for the emulsions prepared with a low viscosity of KGM solutions ( Figure 5 (S5)), the uniformity of which was relatively poor (CV = 22.55%). Coalescence could occur in the emulsification process due to the low viscosity of the aqueous phase, which would decrease the uniformity of the final emulsions. Therefore, high viscosity of aqueous phase showed advantages for obtaining uniform emulsions. Figure 6 (S5-Crosslinking, S6-Crosslinking, S3-Crosslinking, and S7-Crosslinking) shows the crosslinking results. With a low viscosity of the KGM solution ( Figure 6 (S5-Crosslinking)), the final microspheres had a much larger size compared with those before crosslinking. These large microspheres adhered to each other. By increasing the viscosity of KGM solution ( Figure 6 (S6-Crosslinking)), two sizes of microspheres were produced. Compared with those in S5, the flocculation and coalescence were apparently weakened. The dispersity and uniformity of the final microspheres got much better after a further increase of the viscosity of the KGM solution ( Figure 6 (S6-Crosslinking and S7-Crosslinking)). Low viscosity of the KGM solution possessed good liquidity contributing to mass transfer, which would induce coalescence in the collision process between emulsion droplets. In addition, low viscosity of KGM solution had low viscoelasticity, which would cause flocculation [30]. In the viscosity range we have studied, the KGM microspheres prepared with high viscosity of aqueous phases had good uniformity and dispersity. The greater the viscosity of the KGM solution, the higher the transmembrane pressure needed in premix membrane emulsification was. So considering the transmembrane pressure, we chose KGM III as the optimal aqueous phase. KGM solution, the higher the transmembrane pressure needed in premix membrane emulsification was. So considering the transmembrane pressure, we chose KGM III as the optimal aqueous phase.

Effects of Oil Phase Composition on the Preparation of KGM Microspheres
As one of the major components of emulsions, the continuous phase has a decisive influence on the stability of emulsions. We investigated the effects of oil phase composition in the following work. Figure 7 (S8, S9, S3, and S10) shows the preparation results of KGM emulsions by premix membrane emulsification. We found that the oil phase composition had little effect on the droplet size and size  KGM solution, the higher the transmembrane pressure needed in premix membrane emulsification was. So considering the transmembrane pressure, we chose KGM III as the optimal aqueous phase.

Effects of Oil Phase Composition on the Preparation of KGM Microspheres
As one of the major components of emulsions, the continuous phase has a decisive influence on the stability of emulsions. We investigated the effects of oil phase composition in the following work. Figure 7 (S8, S9, S3, and S10) shows the preparation results of KGM emulsions by premix membrane emulsification. We found that the oil phase composition had little effect on the droplet size and size

Effects of Oil Phase Composition on the Preparation of KGM Microspheres
As one of the major components of emulsions, the continuous phase has a decisive influence on the stability of emulsions. We investigated the effects of oil phase composition in the following work. Figure 7 (S8, S9, S3, and S10) shows the preparation results of KGM emulsions by premix membrane emulsification. We found that the oil phase composition had little effect on the droplet size and size uniformity of the emulsions. However, the changes of the oil phase composition had considerable influence in the crosslinking process.  Since the viscosity of liquid paraffin was much higher than that of petroleum ether, the viscosity of the mixed oil phase decreased with the increase of the amount of petroleum ether (shown in Figure  8). In Figure 9 (S8-Crosslinking, S9-Crosslinking, S3-Crosslinking, and S10-Crosslinking), the crosslinking results with different oil phase composition are shown. Serious flocculation occurred in Figure 9 (S8-Crosslinking) due to the low viscosity of the oil phase. By increasing the viscosity of the oil phase, flocculation was weakened (Figure 9 (S9-Crosslinking)). As the viscosity of the oil phase was further increased, the dispersity of the final microspheres became better (Figure 9 (S3-Crosslinking and S10-Crosslinking)). When droplets approached each other, the discharging rate of the liquid between the deformed droplets partly depended on the viscosity of the continuous phase. The greater the viscosity was, the lower the liquid discharging rate and the flocculation rate were [31]. Considering the effects of oil phase composition on emulsification and crosslinking results, the optimum oil phase composition was 11:1 (w/w, LP/EP).  Since the viscosity of liquid paraffin was much higher than that of petroleum ether, the viscosity of the mixed oil phase decreased with the increase of the amount of petroleum ether (shown in Figure 8). In Figure 9 (S8-Crosslinking, S9-Crosslinking, S3-Crosslinking, and S10-Crosslinking), the crosslinking results with different oil phase composition are shown. Serious flocculation occurred in Figure 9 (S8-Crosslinking) due to the low viscosity of the oil phase. By increasing the viscosity of the oil phase, flocculation was weakened (Figure 9 (S9-Crosslinking)). As the viscosity of the oil phase was further increased, the dispersity of the final microspheres became better (Figure 9 (S3-Crosslinking and S10-Crosslinking)). When droplets approached each other, the discharging rate of the liquid between the deformed droplets partly depended on the viscosity of the continuous phase. The greater the viscosity was, the lower the liquid discharging rate and the flocculation rate were [31]. Considering the effects of oil phase composition on emulsification and crosslinking results, the optimum oil phase composition was 11:1 (w/w, LP/EP).  Since the viscosity of liquid paraffin was much higher than that of petroleum ether, the viscosity of the mixed oil phase decreased with the increase of the amount of petroleum ether (shown in Figure  8). In Figure 9 (S8-Crosslinking, S9-Crosslinking, S3-Crosslinking, and S10-Crosslinking), the crosslinking results with different oil phase composition are shown. Serious flocculation occurred in Figure 9 (S8-Crosslinking) due to the low viscosity of the oil phase. By increasing the viscosity of the oil phase, flocculation was weakened (Figure 9 (S9-Crosslinking)). As the viscosity of the oil phase was further increased, the dispersity of the final microspheres became better (Figure 9 (S3-Crosslinking and S10-Crosslinking)). When droplets approached each other, the discharging rate of the liquid between the deformed droplets partly depended on the viscosity of the continuous phase. The greater the viscosity was, the lower the liquid discharging rate and the flocculation rate were [31]. Considering the effects of oil phase composition on emulsification and crosslinking results, the optimum oil phase composition was 11:1 (w/w, LP/EP).

Effects of the Feeding Methods of EC on the Preparation of KGM Microspheres
In the crosslinking process, flocculation and coalescence occurred frequently. Figure 10 shows the evolution of emulsions with time in the absence of a crosslinking agent. Flocculation and aggregation occurred at different times in the emulsions with different stabilities. The results indicated that low temperature contributed to the stability of the emulsions. An increase in the temperature increased the solubility of the emulsifier in the oil and aqueous phases, so that part of the emulsifier would be desorbed from the oil-water interface, leading to the reduction of the interfacial film strength and the decline of the emulsion stability [32]. Meanwhile, the viscosities of the oil phase and aqueous phase increased with temperature (Figure 11a). The collision energy between the emulsion droplets would decrease for the high motion resistance resulting from the high viscosity of the oil phase. The high viscosity of the aqueous phase could partly inhibit flocculation due to the high viscoelasticity. In addition, high temperature would promote the Brown movement and increase the chance of collision between droplets which would induce the flocculation and coalescence of the emulsions. Although the interfacial tension got larger at low temperature ( Figure  11b), it played a minor role. Temperature had an important influence on the stability of the emulsions.
Before coalescence and flocculation occurred, emulsions generally kept stable for a period. During this period, increasing the crosslinking rate would partly inhibit the coalescence and flocculation. So it was very important to increase the crosslinking rate at the beginning of the crosslinking process. Here, we adjusted the crosslinking rate by changing the feeding method of the crosslinking agent (EC). In the traditional method, the EC was added slowly at the crosslinking temperature (60 °C). Here, two different methods were proposed. In the first one, EC was added at 40 °C and then the temperature was increased gradually to 60 °C. Sufficient dispersion of EC in the oil phase could be achieved at 40 °C. During this period the emulsions were in stable state because that low temperature contributed to emulsion stability. As the crosslinking temperature (60 °C) was reached, the well-dispersed EC would react more rapidly with the emulsion droplets. In the second one, EC solution (20 wt %, EC was mixed with oil phase adequately) was added in one batch at the reaction temperature (60 °C). It was easier for the EC solution to spread to the microsphere surface. It can be seen from the results in Figure 12 that flocculation and coalescence occurred in S5-Crosslinking 1 which was cured by the traditional method. In S5-Crosslinking 2, emulsions were stirred at 60 °C for 1 h after emulsification and then EC was added. In this process, emulsion

Effects of the Feeding Methods of EC on the Preparation of KGM Microspheres
In the crosslinking process, flocculation and coalescence occurred frequently. Figure 10 shows the evolution of emulsions with time in the absence of a crosslinking agent. Flocculation and aggregation occurred at different times in the emulsions with different stabilities. The results indicated that low temperature contributed to the stability of the emulsions. An increase in the temperature increased the solubility of the emulsifier in the oil and aqueous phases, so that part of the emulsifier would be desorbed from the oil-water interface, leading to the reduction of the interfacial film strength and the decline of the emulsion stability [32]. Meanwhile, the viscosities of the oil phase and aqueous phase increased with temperature ( Figure 11a). The collision energy between the emulsion droplets would decrease for the high motion resistance resulting from the high viscosity of the oil phase. The high viscosity of the aqueous phase could partly inhibit flocculation due to the high viscoelasticity. In addition, high temperature would promote the Brown movement and increase the chance of collision between droplets which would induce the flocculation and coalescence of the emulsions. Although the interfacial tension got larger at low temperature (Figure 11b), it played a minor role. Temperature had an important influence on the stability of the emulsions.
Before coalescence and flocculation occurred, emulsions generally kept stable for a period. During this period, increasing the crosslinking rate would partly inhibit the coalescence and flocculation. So it was very important to increase the crosslinking rate at the beginning of the crosslinking process. Here, we adjusted the crosslinking rate by changing the feeding method of the crosslinking agent (EC). In the traditional method, the EC was added slowly at the crosslinking temperature (60˝C). Here, two different methods were proposed. In the first one, EC was added at 40˝C and then the temperature was increased gradually to 60˝C. Sufficient dispersion of EC in the oil phase could be achieved at 40˝C. During this period the emulsions were in stable state because that low temperature contributed to emulsion stability. As the crosslinking temperature (60˝C) was reached, the well-dispersed EC would react more rapidly with the emulsion droplets. In the second one, EC solution (20 wt %, EC was mixed with oil phase adequately) was added in one batch at the reaction temperature (60˝C). It was easier for the EC solution to spread to the microsphere surface. It can be seen from the results in Figure 12 that flocculation and coalescence occurred in S5-Crosslinking 1 which was cured by the traditional method. In S5-Crosslinking 2, emulsions were stirred at 60˝C for 1 h after emulsification and then EC was added. In this process, emulsion coalescence was almost fully developed before crosslinking and the new emulsions were in stable state, so the obtained microspheres had better dispersity than those in S5-Crosslinking 1. Both of the methods (Figure 12 (S5-Crosslinking 3 and S5-Crosslinking 4)) improved the crosslinking results. The final microspheres prepared with the two different feeding methods had better dispersity and the coalescence and flocculation were effectively suppressed. coalescence was almost fully developed before crosslinking and the new emulsions were in stable state, so the obtained microspheres had better dispersity than those in S5-Crosslinking 1. Both of the methods (Figure 12 (S5-Crosslinking 3 and S5-Crosslinking 4)) improved the crosslinking results. The final microspheres prepared with the two different feeding methods had better dispersity and the coalescence and flocculation were effectively suppressed.   coalescence was almost fully developed before crosslinking and the new emulsions were in stable state, so the obtained microspheres had better dispersity than those in S5-Crosslinking 1. Both of the methods (Figure 12 (S5-Crosslinking 3 and S5-Crosslinking 4)) improved the crosslinking results. The final microspheres prepared with the two different feeding methods had better dispersity and the coalescence and flocculation were effectively suppressed.    Microscopic photographs of KGM microspheres prepared by different feeding modes of EC: S5 was KGM emulsions before crosslinking and S5-Crosslinking 1 (EC was added slowly at 60 °C), S5-Crosslinking 2 (emulsions were stirred at 60 °C for 1 h and then EC was added), S5-Crosslinking 3 (EC solution (20 wt %, EC was mixed with oil phase adequately) was added in one batch at 60 °C) and S5-Crosslinking 4 (EC was added at 40 °C and then the temperature was increased to 60 °C) were the crosslinking results of S5.

Conclusions
Uniform small-sized KGM microspheres were successfully prepared with the EP membrane we developed by premix membrane emulsification. The stability of emulsions had an important influence on the uniformity and dispersity of the final KGM microspheres. It was found that the preparation condition of the emulsifier 5 wt % PO-5s, KGM III (145.6 mPa·s), and weight ratio of LP to PE 11:1 was in favor of the uniformity and dispersity of the final KGM microspheres. The addition of emulsifier was beneficial to the stability of emulsions, but the excess emulsifier would increase the hydrophilicity of the membrane and produce large droplets. High viscosity of the KGM solution could partly improve the uniformity and stability of emulsions and the greater the oil phase viscosity was, the better the emulsion stability was. In addition, the feeding methods of EC played a significant role in the crosslinking results. Different from the traditional feeding method of EC, the two feeding methods proposed in this study could partly inhibit the coalescence and flocculation, which effectively improved the crosslinking results. Figure 12. Microscopic photographs of KGM microspheres prepared by different feeding modes of EC: S5 was KGM emulsions before crosslinking and S5-Crosslinking 1 (EC was added slowly at 60˝C), S5-Crosslinking 2 (emulsions were stirred at 60˝C for 1 h and then EC was added), S5-Crosslinking 3 (EC solution (20 wt %, EC was mixed with oil phase adequately) was added in one batch at 60˝C) and S5-Crosslinking 4 (EC was added at 40˝C and then the temperature was increased to 60˝C) were the crosslinking results of S5.

Conclusions
Uniform small-sized KGM microspheres were successfully prepared with the EP membrane we developed by premix membrane emulsification. The stability of emulsions had an important influence on the uniformity and dispersity of the final KGM microspheres. It was found that the preparation condition of the emulsifier 5 wt % PO-5s, KGM III (145.6 mPa¨s), and weight ratio of LP to PE 11:1 was in favor of the uniformity and dispersity of the final KGM microspheres. The addition of emulsifier was beneficial to the stability of emulsions, but the excess emulsifier would increase the hydrophilicity of the membrane and produce large droplets. High viscosity of the KGM solution could partly improve the uniformity and stability of emulsions and the greater the oil phase viscosity was, the better the emulsion stability was. In addition, the feeding methods of EC played a significant role in the crosslinking results. Different from the traditional feeding method of EC, the two feeding methods proposed in this study could partly inhibit the coalescence and flocculation, which effectively improved the crosslinking results.
Author Contributions: Guanghui Ma suggested and supervised the work and performed the article editing. Zhiguo Su provided lots of constructive suggestions about this work. Yace Mi and Weiqing Zhou designed and performed the experiments and analyzed the data. Juan Li provided significant guidance on the preparation of KGM microspheres. Rongyue Zhang contributed to the design of EP membrane.

Conflicts of interest:
The authors declare no conflict of interest.

Abbreviations
The following abbreviations are used in this manuscript: