Chemical Engineering and Processing: Process Intensification
Rheology and microstructure of lithium lubricating greases modified with a reactive diisocyanate-terminated polymer: Influence of polymer addition protocol
Introduction
Lubricating greases are usually made from petroleum oils thickened with metal soaps. Particularly, lithium 12-hydroxystearate soap is the most widely used thickening agent. In addition, lubricating greases usually contain some performance additives [1], [2]. Thus, the use of polymers is a common practice to modify the rheological properties of greases by reinforcing the role of the thickening agent [3], [4]. A new generation of polymeric additives consisting of polyolefins containing grafted anhydride functional groups are being progressively introduced in grease formulations [5], [6]. These additives are usually added during or prior to the saponification step in grease manufacturing process. Similarly, in a previous work [7], we have shown that reactive diisocyanate-terminated polymeric materials can be satisfactorily used as rheology modifiers of lubricating greases by promoting the reaction between terminal isocyanate groups and the hydroxy groups located in the hydrocarbon chain of the 12-hydroxystearate lithium soap. It was demonstrated that the poly(1,4-butanediol) tolylene 2,4-diisocyanate (PBTDI), with a relatively low molecular weight, shows an effectiveness similar to that achieved with non-reactive polymers of much higher molecular weights, being the mechanical stability of PBTDI-based greases under operating conditions even better.
However, taking into account both the very high potential reactivity of the isocyanate groups [8], [9] and the complex mixture of components and thermo-mechanical conditions involved in the processing of lubricating greases, the process stage at which this reactive polymer must be added is not trivial. It must be noted that the manufacture of lubricating greases, with generation in situ of the soap thickener, is a rather complex process, consisting of the saponification reaction of fatty acids, followed by dehydration, heating up to near the phase transition temperature of soap crystallites, cooling down to crystallize the soap, and final milling treatment [10], [11]. Mixing efficiency is important during the whole manufacturing process [12]. The high temperatures achieved during processing may significantly increase the reactivity of isocyanate groups [13], or even cause some thermally induced degradation [13], [14]. This research deals with the optimization of PBTDI addition during the manufacture of a traditional lithium lubricating grease. Therefore, the main objective of this work was to study the effectiveness of PBTDI as grease thickener by analysing the rheological response of PBTDI-based greases differing in the stage at which this polymer was added during processing.
Section snippets
Materials
12-Hydroxystearic acid, lithium hydroxide and a naphtenic mineral lubricating oil (density at 20 °C: 916 kg/m3; kinematic viscosity at 40 °C: 115 mm2/s) were used to prepare conventional lithium 12-hydroxystearate lubricating greases (14%, w/w, soap). All the components were kindly supplied by Verkol, S.A. (Spain). Poly(1,4-butanediol) tolylene 2,4 diisocyanate terminated prepolymer (PBTDI) from Aldrich (Mn 1600 g/mol) was used as thickening additive. Fig. 1 shows the chemical structure of this
Rheological behaviour
Figs. 3a and 4a show the evolution of the storage (G’) and loss (G”) moduli with frequency, within the linear viscoelasticity range, for the different lubricating greases studied. As can be observed, the values of the storage modulus, G’, are always significantly higher than those found for the loss modulus, G”, in the whole frequency range studied. Moreover, the so called “plateau region” is always noticed, where G’ slightly increases and G” displays a clear minimum. The values of the
Discussion
As has been previously reported [8], [9], isocyanate groups (NCO) are highly reactive, specially with nucleophilic compounds such as alcohols and amines. This attribute makes PBTDI suitable to be used as a reactive polymer in lithium 12-hydroxystearate grease formulations, by inducing the selective reaction of these isocyanate groups with the hydroxy group located in the hydrocarbon chain of the lithium soap. However, this high reactivity of NCO may lead to secondary reactions, especially in
Conclusions
The rheological behaviour of lithium 12-hidroxystearate lubricating greases can be modified upon addition of a reactive diisocyanate-terminated polymer. Thus, the addition of poly(1,4-butanediol) tolylene 2,4-diisocyanate terminated prepolymer (PBTDI) significantly increases the values of the linear viscoelastic functions when it is added during the final cooling step of the lubricating grease manufacturing process. This increase over the values found for the additive-free lubricating grease is
Acknowledgements
This work is part of a research project (CTQ2004-02706) sponsored by a MEC-FEDER programme. The authors gratefully acknowledge its financial support.
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