ABSTRACT

Feasibility of dissolution and utilization of expanded polystyrene in cycloalkane solutions was investigated in this work. The dissolution process of expanded polystyrene in several cycloalkane solutions decalin, cyclohexane and methyl cyclohexane was studied. The effect of dissolution temperature, mechanical agitation, ultrasonic wave and stirring rate was studied under optimized conditions. Mass transfer coefficients were fitted. The results showed that the dissolution rate of expanded polystyrene in different cycloalkane solutions was ranked as decalin > methyl cyclohexane > cyclohexane; higher dissolution temperature and faster stirring rate could speed up the dissolution of expanded polystyrene; the effect of mechanical agitation was superior to ultrasonic condition; the solubility of top face was better than side face and under face.

Keywords:

Expanded Polystyrene, Cycloalkane, Dissolution, Mass Transfer Coefficient

1. Introduction

Polystyrene is one of the general plastics. It is widely used in packaging container materials, insulation materials, daily necessities, electrical and electronic fields because of its high transparency, good insulation performance, water resistance, corrosion resistance, easy processing and molding. However, the discarded polystyrene products cause white pollution to the environment. China is facing the problems of large amount of waste foamed polystyrene (EPS) and low recycling efficiency of it [1] . Therefore, the recycling of EPS has always been one of the hot issues concerned by scholars, and solvent regeneration is one of the important recycling ways [2] - [7] . A new material, polycyclohexyl ethylene, can be obtained by catalytic hydrogenation after polystyrene is dissolved in solvents [8] [9] [10] . In this paper, the dissolution process of EPS was studied indifferent cycloalkane solvents, like decalin, cyclohexane and methylcyclohexane which were frequently used as solvent system in the catalytic hydrogenation of polystyrene. It is desirable to provide theoretical support for the development of high value-added polycyclohexane ethylene (PCE) by direct catalytic hydrogenation from waste EPS after dissolution.

2. Experimental

2.1. Materials and Methods

EPS was obtained from the local market. Decalin, cyclohexane and methylcyclohexane with reagent grade were bought from Sinopharm Chemical Reagent Co., Ltd (Shanghai, China). The concentration of polystyrene was determined with a UV-7504C UV-vis Spectro-photometer at 261.5 nm. The ultrasonic wave was generated by BL10-250A ultrasonic generator.

2.2. Standard Curve of Polystyrene

The EPS was dissolved in different cycloalkane solutions and diluted to form solutions with different polystyrene concentrations. The data of the concentration (c) of polystyrene and absorbance (a) were fitted to a standard curve, namely a = 2.39702c − 0.02258 (R = 0.99967).

2.3. Dissolution Process

A certain amount of cycloalkane solution was put into a beaker and then the beaker was placed in a water bath with stirring and temperature control device. EPS was made into a rectangular strip with a cross-sectional area of 2 cm × 2 cm and inserted vertically into the solvent (cycloalkane solution). After isolation, only one side of the EPS was in contact with the solvent in the dissolution process. Sampling and analysis were carried out to calculate the thickness (d) of the EPS.

2.4. Dissolution Coefficient

The thickness of a single EPS face would decrease in the process of dissolution. In this condition, mass transfer is the rate control step. The dissolution rate per unit cross-sectional area of EPS is expressed as:

$-\frac{1}{A}\frac{\text{d}W}{\text{d}t}=-{\rho }_s\frac{\text{d}L}{\text{d}t}=k\Delta C$ (1)

where A is the cross-sectional area of the solvent surface in the unit of cm², W is the weight of EPS in the unit of g, L is the thickness of EPS in the unit of cm, ρ_s is the density of EPS in the unit of g/cm³, ΔC is the difference between the saturation concentration of solute in the sphere and the overall concentration in the solvent in the unit of mg/ml, k is a constant.

In the initial condition of t = 0 and d = 0, the expression of (1) could be rewritten as:

$d=\frac{k\Delta C}{{\rho }_s}t$ (2)

where d has a linear relationship with t, and the slope is mass transfer coefficient (m).

3. Results and Discussion

3.1. Effect of Solvent on EPS Dissolution

EPS strips were dissolved in three cycloalkane solvents (decalin, cyclohexane and methylcyclohexane) at the temperature of 25˚C and stirring rate of 200 rpm, respectively. The effect of solvent on EPS dissolution strips is shown in Figure 1.

As shown in Figure 1, the dissolution rate of EPS in the three solvents increases linearly in the first 4minutes, and then gradually become constant, respectively. It can be seen that the dissolution rates of EPS in the three solvents are in the order of decalin (m = 0.19525) > methyl cyclohexane (m = 0.13650) > cyclohexane (m = 0.11372). A large number of bubbles rise during the dissolution process, which will adhere to the dissolving face of EPS, preventing the dissolution process. Meanwhile, the increment of the distance between the blades of the mixer and the dissolving face weaks the influence of the stirring on the dissolution. So the dissolution curve gradually becomes stable. Decalin was used as solvent for subsequent experiments as the dissolution rate of EPS in it is higher than that of the other two solvents.

3.2. Effect of Temperature on EPS Dissolution

The dissolution of EPS at temperatures of 15˚C, 25˚C and 35˚C was carried outin 300 ml of decal insolvent with stirring rate of 200 rpm. The experimental result is shown in Figure 2.

The temperature has a significant impact on dissolution rate. It is observed that there is an obvious increase of dissolved thickness of EPS at the temperature

of 25˚C and 35˚C. The smooth curve of 15˚C indicats that low temperature is not good for EPS dissolving. The effect of temperature was confirmed by the value of tree mass transfer coefficients, m = 0.03582, 0.19525 and 0.32996, representing for that of 15˚C, 25˚C and 35˚C, respectively.

3.3. Effect of Ultrasonic Wave on EPS Dissolution

To compare the effect of mechanical agitation andultrasonic wave on EPS dissolution. The dissolution process was conducted in 300 ml of decal insolvent at temperature of 25˚C. The result is shown in Figure 3.

At the same condition, the dissolution curve of mechanical stirring indicated a faster dissolution rate (m = 0.19525) than that of ultrasonic wave (m = 0.10404). This could be attributed to the fact that the bubble appeared in the ultrasonic wave-assisted dissolution process attached finely to the dissolution interface, which impeded the mass transfer.

3.4. Effect of Stirring Rate on EPS Dissolution

The EPS dissolution at stirring rate of 200 rpm, 300 rpm and 400 rpm was studied in 300 ml decalin solvent at 25˚C. The effect of stirring rate on EPS dissolution is shown in Figure 4.

The dissolution rate of EPS increased steadily with dissolution time, and higher dissolution rate appeared at the faster stirring rate. The fitted mass transfer coefficients for three dissolution process is 0.19525 (200 rpm), 0.22792 (300 rpm) and 0.38521 (400 rpm), respectively. The transition of the curve of 200 rpm after 3 minutes indicates that low stirring rate could not cause enough disturbance to the EPS dissolution. It is more difficult to dispel the attached bubbles attached at the lower stirring rate as the dissolving face gradually become farther from the stirring blade.

3.5. Effect of Dissolution Face on EPS Dissolution

The effect of dissolution face on EPS dissolution was conducted under temperature of 25˚C and stirring rate of 200 rpm in 300 ml of decal insolvent. The result is shown in Figure 5. It is found that the dissolution rate increases similarly for

the three faces in the first 3 minutes. However, the dissolution rate increases higher for the upper face in the stage of 3 to 5 minute. This trend can be explained by the observation that the number of attached bubbles to the upper face is less than that of the down face. While disturbance generated by bubbles in the process of upward floating could enhance mass transfer of the side face and top face of EPS. The mass transfer coefficient (m) of three dissolving face are 0.19525 (down face), 0.24372 (side face) and 0.27775 (top face), respectively.

4. Conclusion

The dissolution process of expanded polystyrene in three cycloalkane solutions (decalin, cyclohexane and methyl cyclohexane) was studied in this work. The results reveals that the dissolution rate of expanded polystyrene in decalin is the fastest with the solubility mass transfer coefficient of 0.19525 under temperature of 25˚C and stirring rate of 200 rpm, when compared with that of methyl cyclohexane, 0.13650, and cyclohexane, 0.11372. The solubility mass transfer coefficient increases with temperature in the range of 15˚C to 35˚C, and reached the maximum of 0.32996. The solubility mass transfer coefficient increases with stirring rate in the range of 200 rpm to 400 rpm, and reached the maximum of 0.38521. Influenced by bubbles generated in the dissolution process, the dissolution rate under ultrasonic wave condition showed no superiority to that of mechanical stirring condition. At the temperature of 25˚C and stirring rate of 200 rpm, the solubility mass transfer coefficient was 0.27775, 0.24372 and 0.19525, with the dissolution surface of upper face, side face and under face, respectively.

Acknowledgements

This work is financially supported by Zhejiang Xinmiao Talent Program (2018R428012) and Ningbo Natural Science Foundation (2017A610066).

Conflicts of Interest

The authors declare no conflicts of interest regarding the publication of this paper.

Cite this paper

Tao, S.Y., Li, B.Y. and Huang, H. (2018) Dissolution of Expanded Polystyrene in Cycloalkane Solutions. Open Journal of Applied Sciences, 8, 465-471. https://doi.org/10.4236/ojapps.2018.810037

References