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J Dent Res 84(4):376-381, 2005
© 2005 International and American Associations for Dental Research


RESEARCH REPORTS
Biomaterials & Bioengineering

Viscoelasticity of Dental Tissue Conditioners during the Sol-gel Transition

H. Murata1,*, H. Chimori1, T. Hamada1, and J.F. McCabe2

1 Department of Prosthetic Dentistry, Graduate School of Biomedical Sciences, Hiroshima University, 1-2-3 Kasumi, Minami-ku, Hiroshima, 734-8553, Japan; and
2 Dental Materials Science Unit, The Dental School, University of Newcastle upon Tyne, Framlington Place, Newcastle upon Tyne, NE2 4BW, UK;

* corresponding author, hmurata{at}hiroshima-u.ac.jp


   ABSTRACT
 TOP
 ABSTRACT
 INTRODUCTION
 MATERIALS & METHODS
 RESULTS
 DISCUSSION
 REFERENCES
 
Formation of tissue conditioners is a process of polymer chain entanglements. This study evaluated the influence of composition and structure on dynamic viscoelasticity of concentrated polymer solutions based on poly(ethyl methacrylate) (PEMA) used as tissue conditioners through the sol-gel transition. The hypothesis was that the ethanol content is the most influential factor in determining gelation speed. Rheological parameters were determined with the use of a controlled-stress rheometer. Analysis of variance by orthogonal array L16(45) indicated that the strong polar bonding of ethanol (contribution ratio {rho} = 53.8%; confirming the hypothesis) and molecular weight of polymer powders ({rho} = 26.7%) had a greater influence on the gelation times of PEMA-based systems than did the molar volume of plasticizers ({rho} = 9.0%) and concentration of polymers (i.e., powder/liquid ratio) ({rho} = 4.5%). The results suggest that the gelation of tissue conditioners based on PEMA can be controlled over a wide range by varying the polymer molecular weight, and especially ethanol content.

KEY WORDS: tissue conditioners • sol-gel transition • dynamic viscoelastic properties • activation energy • orthogonal array


   INTRODUCTION
 TOP
 ABSTRACT
 INTRODUCTION
 MATERIALS & METHODS
 RESULTS
 DISCUSSION
 REFERENCES
 
Concentrated polymer solutions based on poly(ethyl methacrylate) (PEMA) are widely used as tissue conditioners in prosthetic dentistry (Braden, 1970). The liquid consists of ester plasticizer and ethanol (Jones et al., 1988). When mixed, the solvents diffuse into the polymer powders, thereby causing the polymers to swell and then dissolve. The result is polymer chain entanglements and formation of a physical gel (Parker and Braden, 1990).

A wide range of gelation characteristics is found in commercial tissue conditioners, due to differences in composition and structure (Jones et al., 1986; Murata et al., 1998). The gelation of the materials has previously been characterized with the use of a reciprocating rheometer (Jones et al., 1986) and oscillating rheometer (Murata et al., 1993, 1998). These methods provide a comparative evaluation among the materials, but do not measure absolute values of elasticity and viscosity.

In general, the gelation of a physical gel is rheologically described by three stages: pre-gelation (sol), sol-gel transition, and post-gelation (gel). During the transition through these stages, materials undergo marked changes in rheological properties, and the monitoring of these changes offers a means of studying the influence of composition on gelation. This requires a sophisticated approach which enables well-defined rheological parameters to be determined. One method which is suitable for meeting this requirement is a dynamic mechanical test. Such a test measures the response of a material to a sinusoidal or other periodic stress (Nielsen and Landel, 1994). Previous studies evaluated the dynamic viscoelasticity of elastomers during setting by means of a controlled-stress rheometer (McCabe and Carrick, 1989; McCabe and Arikawa, 1998). However, little information is available on dynamic viscoelasticity of tissue conditioners during gelation.

The purpose of this investigation was to evaluate the influence of molecular weight of polymer powders, plasticizer type, ethanol content in liquids, and powder/liquid ratio on dynamic viscoelastic properties of concentrated polymer solutions based on PEMA, i.e., tissue conditioners, in sol-gel transition by the orthogonal array in addition to the one-way layout method. The relationship between activation energy of gelation and the above factors was also examined. Our hypothesis was that the gelation speed would be influenced most by the ethanol content of the materials.


   MATERIALS & METHODS
 TOP
 ABSTRACT
 INTRODUCTION
 MATERIALS & METHODS
 RESULTS
 DISCUSSION
 REFERENCES
 
Four PEMA polymer powders, with average molecular weight (Mw) of 1.08 x 105, 2.39 x 105, 3.75 x 105, and 5.30 x 105, were used. The average particle size was approximately 20 µm, and polydispersity coefficients were approximately 2. Three aromatic esters—butyl phthalyl butyl glycolate, dibutyl phthalate, and benzyl benzoate—and an aliphatic ester (dibutyl sebacate) containing ethanol at 2, 5, 10, and 20 wt% were used as liquid components. The powder/liquid (P/L) ratio was varied from 0.8 to 1.4 by weight.

Analysis of Dynamic Viscoelastic Properties
Dynamic viscoelastic properties of the test materials during gelation were determined at 37°C. A controlled-stress rheometer (CSL500, Carri-Med Ltd., Dorking, Surrey, England) was used with a parallel plate test configuration (diameter = 20 mm, gap = 1000µm) in oscillatory mode (Fig. 1Go). Immediately after the powders and liquids were mixed for 15 sec at 23 ± 1°C, the resulting paste was placed on the plate of the rheometer. Torque was monitored every 30 sec at constant oscillating frequency (1 Hz) and angular displacement (3 mrad).



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Figure 1. Measurement of dynamic viscoelastic properties during the sol-gel transition. (A) Schematic diagram of a controlled-stress rheometer in a parallel plate configuration. In the parallel plate system, the shear strain ({gamma}) and shear stress ({tau}) are determined experimentally as follows: {gamma} = F{gamma} {omega}, {tau} = F{tau} T, where F{gamma} (= R/d) is the shear strain factor; F{tau} (= 2/{pi}R3) the shear stress factor; {omega} the angular displacement; T the torsional force; R the radius of the plate; and d the shear gap. (B) Schematic representation of dynamic viscoelastic properties of gelation system as a function of reaction time. G' represents the elastic component of material behavior, whereas G'' represents the viscous component of material behavior. The gelation time was defined as the time to reach the gel point at which tan {delta} = 1 (G' = G'').

 
The complex dynamic shear modulus (G*), shear storage modulus (G'), shear loss modulus (G''), and loss tangent (tan {delta}) are defined as follows:


where i2 = –1, and {delta} is the phase angle between stress and strain.

Determination of Gelation Times
The gelation time was defined as the time at which tan {delta} = 1 (G' = G'') was reached, that is, the gel point (Fig. 1Go) (Winter and Chambon, 1986; Nielsen and Landel, 1994).

The various combinations of the 16 different materials were tested to determine the contribution ratio ({rho}) of each factor to the gelation times by means of an orthogonal array L16(45) (Taguchi, 1991) (Appendix Table A1Go, www.dentalresearch.org). Second, 26 different materials were used for the determination of the effect of each factor by a one-way layout method.


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Table A1. Assignment by Orthogonal Array L16(45)
 
Results were compared by both orthogonal arrays and a one-way layout method. Statistical tests were performed by ANOVA and regression analysis.

Determination of Activation Energies
The gelation times of 13 different materials were also determined at 4 temperatures: 25, 30, 35, and 40°C. An apparent activation energy of gelation (Ea) was determined according to the following kinetic equation (Oyanguren and Williams, 1993; Parker and Braden, 1996; Ponton et al., 2002):


where tgel is the gelation time, C a pre-factor, R the gas constant, and T the absolute temperature.

Five tests were carried out for each material and temperature.


   RESULTS
 TOP
 ABSTRACT
 INTRODUCTION
 MATERIALS & METHODS
 RESULTS
 DISCUSSION
 REFERENCES
 
Results from the orthogonal array L16(45) indicate significant effects of all factors for the gelation time at 37°C (p < 0.0005, ANOVA) (Appendix Table A2Go, www.dentalresearch.org). The ethanol content ({rho} = 53.8%) had more influence on gelation time than the molecular weight of polymer powders ({rho} = 26.7%), which in turn had more influence than the type of plasticizer ({rho} = 9.0%) and the P/L ratio ({rho} = 4.5%).


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Table A2. ANOVA for the Gelation Time by Orthogonal Array L16(45)
 
A greater rate of increase of G' and G'' and a decrease of tan {delta} with time were noted with the higher-molecular-weight polymer powders, with the higher P/L ratio materials, and with liquids containing the larger percentages of ethanol (Fig. 2Go). A negative linear relationship was found between the log of the gelation time and both the log of the polymer molecular weight (r = –0.960 and –0.992, p < 0.0005) and the ethanol content (r = –0.995 and –0.979, p < 0.0005) (Fig. 3Go). There was also a negative linear relationship between the gelation time and the P/L ratio (r = –0.924 and –0.904, p < 0.0005). (The first r was for the materials containing butyl phthalyl butyl glycolate, and the second for dibutyl sebacate in the regression analyses for each factor.) With regard to plasticizer type, the greatest rate of increase of G' and G'' and decrease of tan {delta} with time were noted for liquids containing benzyl benzoate, and the smallest rate of change in these values was noted with dibutyl sebacate (Fig. 2Go). The shortest gelation time was with benzyl benzoate, and the longest was observed with dibutyl sebacate (Student-Newman-Keuls test, p < 0.05) (Fig. 3Go).



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Figure 2. Relationship between variations of G', G'', and tan {delta} of concentrated polymer solutions based on PEMA with time and each factor at 37°C. The material that had a median value of gelation time was selected from 5 materials measured. Data are given as median values (n = 5). (A) Influence of molecular weight (Mw) of polymer powders. PEMA polymer powders of various molecular weight were mixed with 10 wt% ethanol/90 wt% dibutyl sebacate at a P/L ratio of 1.2. (B) Influence of P/L ratio. PEMA polymer powders of molecular weight of 3.75 x 105 were mixed with 10 wt% ethanol/90 wt% dibutyl sebacate at various P/L ratios. (C) Influence of plasticizer type. PEMA polymer powders of molecular weight of 3.75 x 105 were mixed with various plasticizers/10 wt% ethanol at a P/L ratio of 1.2. (D) Influence of ethanol content in liquids. PEMA polymer powders of molecular weight of 3.75 x 105 were mixed with various rates of ethanol/dibutyl sebacate at a P/L ratio of 1.2. The materials containing no ethanol were also measured, so that the effect of ethanol could be demonstrated. A greater rate of changes in G', G'', and tan {delta} with time was noted with the higher-molecular-weight polymer powders, with the higher P/L ratio materials, with the lower molar-volume plasticizer, and with liquids containing the larger percentages of ethanol.

 


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Figure 3. Relationship between gelation times of concentrated polymer solutions based on PEMA and each factor at 37°C. The materials consisting of the PEMA polymer powder of molecular weight of 3.75 x 105 and the liquid containing 10 wt% ethanol/90 wt% plasticizer [butyl phthalyl butyl glycolate (aromatic ester), dibutyl sebacate (aliphatic ester)] (P/L = 1.2) were used as baseline, because they represented an average composition and structure of tissue conditioners. We determined the 26 materials by varying the levels of each factor of the standard materials (baseline). (A) Influence of molecular weight (Mw) of polymer powders. Four PEMA polymer powders, with Mw of 1.08 x 105, 2.39 x 105, 3.75 x 105, and 5.30 x 105, were used. There was a negative linear relationship between the log of the gelation time and the log of the polymer molecular weight (p < 0.0005). (B) Influence of P/L ratio. Four P/L ratios, 0.8, 1.0, 1.2, and 1.4, were used. There was a negative linear relationship between the gelation time and the P/L ratio (p < 0.0005). (C) Influence of plasticizer type. Four ester plasticizers—butyl phthalyl butylglycolate (BPBG), dibutyl phthalate (DBP), benzyl benzoate (BB), and dibutyl sebacate (DBS)—were used. All differences were significant (p < 0.05, ANOVA and Student-Newman-Keuls test). (D) Influence of ethanol content in liquids. Four ethanol contents, 2, 5, 10, and 20 wt%, were used. There was a negative linear relationship between the log of the gelation time and the ethanol content (p < 0.0005). Data are given as means and standard deviations (n = 5).

 
The apparent activation energies of gelation decreased with increases in the polymer molecular weight, P/L ratio, and especially ethanol content and with decreases in molar volume of plasticizers (TableGo; Appendix Table A3Go). Increasing the polymer molecular weight from 1.08 x 105 to 5.30 x 105, the P/L ratio from 0.8 to 1.4, and ethanol content from 2 to 20 wt% led to reductions in the activation energy of 32.2, 8.9, and 46.3 kJmol–1, respectively. Differences in plasticizer type led to a change in activation energy of 19.7 kJmol–1.


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Table. Influence of Each Factor on Activation Energies of Gelation of Concentrated Polymer Solutions Based on PEMAa,b
 

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Table A3. Characteristics and Solubility Parameters of Plasticizers and Ethanol
 

   DISCUSSION
 TOP
 ABSTRACT
 INTRODUCTION
 MATERIALS & METHODS
 RESULTS
 DISCUSSION
 REFERENCES
 
Polymers undergo phase transition from liquid to solid at a critical extent of reaction during gelation. The instant of this transition is called the gel point (Nielsen and Landel, 1994). The polymer is said to be at the gel point if its steady shear viscosity is infinite and its equilibrium modulus is zero, and at least one chain of infinite molecular weight has been created. Winter and Chambon (1986) suggested the following scaling law at the gel point:


At the gel point, G' and G'' are congruent, i.e., tan {delta} = 1, and this behavior is valid in the entire range 0 < frequency {delta} < {infty}. It has been reported that monitoring tan {delta} is an effective way of evaluating the viscoelasticity of impression materials during setting (McCabe and Arikawa, 1998). Therefore, in this study, the gelation time was defined as the time to reach tan {delta} = 1.

Viscoelasticity of the tissue conditioners during gelation can conveniently be discussed if the curves of tan {delta} are divided into 3 regions: region 1, where tan {delta} decreases with time rapidly; region 2, where tan {delta} = 1 (the gel point); and region 3, where tan {delta} continues to decrease. At the initial stage in region 1, the PEMA polymers dissolve in the plasticizer, and polymer chain entanglements are still scarce. All the solutions are essentially viscous Newtonian fluids. Entanglements then begin to occur, and the viscosity gradually increases with time until the solutions can no longer be described as viscous fluids. Before the gel point, although G' is always smaller than G'', G' increases much more rapidly than G'', and thus tan {delta} decreases rapidly. In region 2, an infinitely long molecule is produced, and the system reaches the gel point (liquid-solid transition), which occurs near where tan {delta} = 1. In region 3, pseudo cross-links consisting of chain entanglements are forming. The samples behave more elastically with increasing reaction time. G' increases rapidly and becomes larger than G'', and thus tan {delta} continues to decrease.

In the orthogonal array method, stress is laid on only factors that have a consistent effect, even when the conditions of other factors differ, because such factors are regarded as having great effect (Taguchi, 1991). Therefore, although the statistical results in this study were based on a limited number of compositions, the tendency of main effects, i.e., relationship between the levels of the factor and measured values, can be determined. It was found that the orthogonal array method was useful for evaluation of the relationship among many factors, such as composition and structure.

The compatibility of different polymers and solvents can be predicted by means of the solubility parameter (SP), which is the square root of the cohesive energy density or vaporization energy ({Delta}Ev) divided by the molar volume (V):


In general, polymers and solvents should be mutually soluble when their solubility parameters are equal. It has been reported that a method which considers solvents as poorly, moderately, or strongly hydrogen-bonded could give relatively accurate predictions of the solubility of a solvent in a polymer (Bellenger et al., 1997).

Plasticizers are added to a polymer to lower the glass transition temperature and soften the rigid polymer. The solubility parameters of plasticizers, which are moderately hydrogen-bonded solvents, are within the range of those of PEMA and poly(methyl methacrylate) (PMMA) (Appendix Tables A3Go, A4Go, www.dentalresearch.org), resulting in mutual solubility. Gelation times were independent of the solubility parameters and molecular weight of plasticizers. Diffusion of the plasticizer into the polymer would be influenced more by the molar volume, which expresses the effect of molecular size, than by the solubility parameter, which is a measure of all of the intermolecular forces, consisting of dispersion forces, dipole-dipole interactions, and hydrogen bonding. It has also been reported that the miscibility of a given polymer-solvent pair is a decreasing function of the molar volume of the solvent (Bellenger et al., 1997). Therefore, higher-molar-volume plasticizers tended to lead to longer gelation times. However, the effect of plasticizer type was small compared with that of other factors.


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Table A4. Solubility Parameters of Polymers for Solution
 
The gelation time decreased exponentially with an increase in ethanol content. The plasticizers containing no ethanol would not produce a clinically acceptable gelation time, because polymer particles are penetrated only very slowly by large plasticizer molecules (Braden, 1970; Parker and Braden, 1990). Therefore, ethanol, which is a highly polar constituent, is essential for the PEMA-based system, because ethanol rapidly swells the polymer particles and accelerates the penetration of the plasticizer into the polymer. In contrast, PMMA is not a suitable polymer, because its solubility parameter for the strongly hydrogen-bonded solvent is 0 (Appendix Tables A4Go, www.dentalresearch.org), and it is not dissolved by ethanol.

The higher-molecular-weight polymer powders produced the shorter gelation times. This can be explained by two contradictory factors. First, the plasticizer takes longer to diffuse into the higher-molecular-weight polymer powders, because the diffusion coefficient of polymer in the solvent is inversely proportional to (Mw)2. However, the higher-molecular-weight polymer powders would produce greater polymer chain entanglements (Han and Bae, 1998), because the distance between polymer chains is closer in polymer solutions with higher molecular weight and concentration (P/L ratio) (Hong and Chen, 1998). The gelation time, which was determined by the variation of viscoelasticity resulting from chain entanglements, would be influenced more by the entanglements than by the diffusion, resulting in shorter gelation times.

A higher P/L ratio also produced shorter gelation times. Although a longer time would be necessary for saturating the liquid with polymer powders at a higher P/L ratio, the higher concentration would also be associated with more entanglements. The influence of the entanglement would be greater, resulting in shorter gelation times.

The materials with the shorter gelation times were found to give lower values of activation energy. Gelation takes place through the activated state, when the system has greater energy than the activation energy. The greater entanglements and diffusion produced by varying composition and structure would lead more easily to the activated state. These changes in the activation energies were found to reflect the contribution of each factor to the gelation process.

The hypothesis that ethanol content is the most influential factor in determining the gelation times of the PEMA-based systems can be supported by the orthogonal array approach, by regression analyses, and by activation energies. Furthermore, it was also found that the polymer molecular weight has a great influence on the gelation process. An ideal tissue conditioner should have stable durability when applied in the mouth. However, it has been reported that materials based on PEMA exhibit a marked reduction in their flow properties with time, due to leaching out of ethanol (Jones et al., 1988; Murata et al., 1996, 1998). From the standpoint of gelation and manipulation after mixing, ethanol is considered to be an essential additive of these materials. Thus, if tissue conditioners which contain less or no alcohol are to be developed, PEMA with higher molecular weight should be used, or, alternatively, a new type of polymer should be developed. The findings of this study may help in the development of improved materials.

In conclusion, the strong polar bonding of ethanol and polymer molecular weight have a greater influence on the entanglement speed of concentrated polymer solutions based on PEMA than do the molar volume of plasticizers and concentration of polymers. The results suggest that the gelation of the PEMA-based system can be controlled over a wide range by varying the polymer molecular weight and especially ethanol content.


   ACKNOWLEDGMENTS
 
The authors thank Rosalina C. Haberham for technical assistance. This research was supported by Grants-in-Aid (Nos. 11671936, 13672036) for Scientific Research from the Ministry of Education, Culture, Sports, Science and Technology, Japan, and by a Grant from Japanese Association for Dental Science.


   FOOTNOTES
 
A supplemental appendix to this article is published electronically only at http://www.dentalresearch.org.

Received September 19, 2003; Last revision December 16, 2004; Accepted January 2, 2005


   REFERENCES
 TOP
 ABSTRACT
 INTRODUCTION
 MATERIALS & METHODS
 RESULTS
 DISCUSSION
 REFERENCES
 
Bellenger V, Kaltenecker-Commercon J, Verdu J, Tordjeman P (1997). Interactions of solvents with poly (methyl methacrylate). Polymer 38:4175–4184.

Braden M (1970). Tissue conditioners: I. Composition and structure. J Dent Res 49:145–148.[Abstract/Free Full Text]

Han CK, Bae YH (1998). Inverse thermally-reversible gelation of aqueous N-isopropylacrylamide copolymer solutions. Polymer 39:2809–2814.[ISI]

Hong P-D, Chen J-H (1998). Network structure and chain mobility of freeze-dried polyvinyl chloride/dioxane gels. Polymer 39:5809–5817.

Jones DW, Sutow EJ, Graham BS, Milne EL, Johnston DE (1986). Influence of plasticizer on soft polymer gelation. J Dent Res 65:634–642.[Abstract/Free Full Text]

Jones DW, Sutow EJ, Hall GC, Tobin WM, Graham BS (1988). Dental soft polymers: plasticizer composition and leachability. Dent Mater 4:1–7.[ISI][Medline]

McCabe JF, Arikawa H (1998). Rheological properties of elastomeric impression materials before and during setting. J Dent Res 77:1874–1880.[Abstract/Free Full Text]

McCabe JF, Carrick TE (1989). Rheological properties of elastomers during setting. J Dent Res 68:1218–1222.[Abstract/Free Full Text]

Murata H, Iwanaga H, Shigeto N, Hamada T (1993). Initial flow of tissue conditioners—influence of composition and structure on gelation. J Oral Rehabil 20:177–187.[ISI][Medline]

Murata H, McCabe JF, Jepson NJ, Hamada T (1996). The influence of immersion solutions on the viscoelasticity of temporary soft lining materials. Dent Mater 12:19–24.[ISI][Medline]

Murata H, Hamada T, Djulaeha E, Nikawa H (1998). Rheology of tissue conditioners. J Prosthet Dent 79:188–199.[ISI][Medline]

Nielsen LE, Landel RF (1994). Mechanical properties of polymers and composites. 2nd ed. New York: Marcel Dekker Inc.

Oyanguren PA, Williams RJ (1993). Cure of epoxy novolacs with aromatic diamines. I. Vitrification, gelation, and reaction kinetics. J Appl Polym Sci 47:1361–1371.

Parker S, Braden M (1990). Formulation of tissue conditioners. Biomaterials 11:579–584.[ISI][Medline]

Parker S, Braden M (1996). Effect of composition on the gelation of tissue conditioners. Biomaterials 17:1827–1832.[ISI][Medline]

Ponton A, Warlus S, Griesmar P (2002). Rheological study of the sol-gel transition in silica alkoxides. J Colloid Interface Sci 249:209–216.

Taguchi G (1991). System of experimental design. 4th ed. New York: Quality Resources. Dearborn, MI: American Supplier Institute Inc.

Winter HH, Chambon F (1986). Analysis of linear viscoelasticity of a crosslinking polymer at the gel point. J Rheol 30:367–382.





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