Low-Temperature Rheology and Thermoanalytical Investigation of Lubricating Greases: Inﬂuence of Thickener Type and Concentration on Melting, Crystallization and Glass Transition

: This study investigates crystallization, melting and glass transition of Li- and Ca-12-hydroxystearate greases in relation to the pour point of the corresponding oils. The base oils for the greases are mineral oil, polyalphaoleﬁn, alkylated naphthalene, propylene glycol, and trimellitate. For the mineral oil-based greases the crystallization temperature T c increases and the melting temperature T m decreases upon addition of thickener. The pour point of the mineral oil then is 3 K below T c and does not properly deﬁne the lowest application temperature for mineral oil (MO) based greases. Both thickeners induce a small increase of the glass transition temperature (1–3 K) of the synthetic oils polyalphaoleﬁn, alkylated naphthalene, propylene glycol. The pour point of the base oils correlates well with the onset of the glass transition in the corresponding grease indicated by a sharp increase in grease viscosity. Pure trimellitate with unbranched alkyl chains does not crystallize upon cooling but shows noticeable supercooling and cold crystallization. As the percentage of thickener in corresponding greases increases, more oil crystallizes upon cooling 20 K above the crystallization temperature of the trimellitate without thickener ( − 44 ◦ C). Here, the thickener changes the crystallization behavior from homogeneous to heterogeneous and thus acts as a crystallization nucleus. The pour point of the base oil does not provide information on the temperature below which the greases stiffen signiﬁcantly due to crystallization.


Introduction
Concerning the lubrication conditions in operation, the higher viscosity of the base oils and higher consistency of the greases at low temperatures, the friction factor increases slightly [1]. In the case of mineral oils, as the proportion of paraffin crystals increases with decreasing temperature, the sliding friction also increases. Nonetheless, the outflow of mineral oil provides adequate lubrication during sliding [2]. Unlike mineral oil, ester oils crystallize to the extent of blocking the rheometer [3]. Thus, it would also block a tribological contact during operation. Practical test methods such as the low-temperature torque test for wheel bearings (ASTM D4693 [4]) or ball bearings (ASTM D1478 [5]) determine the suitability of greases for low temperatures. Although these standards are close to practical experience, they do not provide information on whether the base oil in lubricating greases precipitate crystals and thus change their flow properties upon cooling. In practice, the pour point according to ASTM D97 [6] is measured for this purpose. The pour point indicates the temperature when the base oil stops flowing as a sample vessel is tilted. Previous research Table 1 lists the base oils used with the kinematic viscosities at 40 and 100 • C, the viscosity index, and the respective pour point. The crystallization behavior and lowtemperature rheology is previously examined in detail and the base oils are classified in three groups [3]. Group I contains a mineral oil (MO), Group II includes amorphously solidifying synthetic lubricating oils (PAG, KR-008, PAO8), and Group III comprises a crystallizing synthetic lubricating oil (EO). Table 1. Classification (Group I-III), kinematic viscosity (ν), viscosity index (VI), pour point (ASTM D7346 [16]), and chemical nature of the base oils.

Chemical Nature
Group ν @40 • C/cSt. ν @100 From the base oils listed in Table 1, lubricating greases with Li-and Ca-12-hydroxystearate were prepared. Ca-12-hydroxystearate greases were prepared by melting the Ca-12hydroxystearate in the base oil at 120 • C for 30 min, while the Li-12-hydroxystearate lubricating greases were prepared by melting Li-12-hydroxystearate above the melting point of 212 • C. After cooling to room temperature, homogenization of the cooled suspensions was carried out on a three-roll mill (Exakt Advanced Technologies GmbH, 50I, Norderstedt, Germany). Greases with thickener concentrations lower than 5 wt.% were homogenized with an Ultra-Turrax (IKA GmbH, Staufen, Germany). Table A1 in the appendix lists the exact composition of the lubricating greases with the respective worked penetration P w (DIN ISO 2137 [17]) and corresponding NLGI class (DIN 51818 [18]).

Rheological Measurements
The steady shear measurements were performed with MCR301 and 702 rheometers from Anton Paar (Ostfildern-Scharnhausen, Germany). A plate-plate geometry with 25 mm in diameter (PP25) made of stainless steel was used as measuring system with a gap of 1 mm. In the temperature range between 20 and −40 • C the Peltier unit was purged with dry air (dew point: −80 • C) to prevent condensation and freezing of humidity. Measurements below −40 • C were performed using a PP25 geometry covered by a low-temperature CTD450 cell and an EVU10 controller for liquid nitrogen, both from Anton Paar (Ostfildern-Scharnhausen, Germany). Temperature-dependent oscillatory shear measurements were performed at an angular frequency of ω = 10 rad s −1 and an amplitude of γ = 0.05%. Strict care was taken to ensure that the linear viscoelastic (LVE) range was maintained in the temperature range investigated. All rheological experiments were performed in triplicate with fresh samples for each measurement.

Differential Scanning Calorimetry (DSC)
Heat flow measurements during the cooling and heating cycles were performed with a DSC 204 F1 Phoenix ® (Netzsch, Selb, Germany) in a pierced aluminum pan with a sample weight of approx. 10 mg to detect glass transition, crystallization, and melting of the lubricating greases. The measurements were carried out in the temperature range from 25 to −60 • C with heating and cooling rate of 2 K min −1 . For the extended temperature range down to −180 • C, a Netzsch DSC 204 cell with a CC 200 L controller for liquid nitrogen was used. The lubricating grease samples were cooled with −20 K min −1 from 25 • C to −180 • C, held for 5 min, and then heated with a rate of +10 K min −1 . All thermoanalytical experiments were performed in triplicate with fresh samples for each measurement.  Figure 1 shows the absolute value of the complex viscosity |η*| as a function of the temperature for the pure mineral oil (MO) and two mineral oil greases, with different Li-(a) and Ca-12-hydroxystearate (b) concentrations during cooling (empty symbols) and heating (filled symbols). Upon cooling, the complex viscosity increases steadily until the crystallization temperature T c,rheo is reached. Below T c,rheo , the slope of the complex viscosity curve increases sharply. The complex viscosity increases levels off below −20 • C. On reheating, the complex viscosity of the greases first decreases sharply until the melting temperature T m,rheo is reached, which is always higher than T c,rheo . Above T m,rheo , the absolute values of the complex viscosities of the cooling and heating cycles overlap. The reason for the sharp change in slopes on cooling and heating, respectively, is the formation and dissolution of paraffin crystals. Previous investigations on the mineral oil MO have shown that the MO changes from a Newtonian liquid to a shear-thinning suspension below T c,rheo [3]. Figure 1 shows the absolute value of the complex viscosity ‫|*‪η‬|‬ as a function of the temperature for the pure mineral oil (MO) and two mineral oil greases, with different Li-(a) and Ca-12-hydroxystearate (b) concentrations during cooling (empty symbols) and heating (filled symbols). Upon cooling, the complex viscosity increases steadily until the crystallization temperature Tc,rheo is reached. Below Tc,rheo, the slope of the complex viscosity curve increases sharply. The complex viscosity increases levels off below −20 °C. On reheating, the complex viscosity of the greases first decreases sharply until the melting temperature Tm,rheo is reached, which is always higher than Tc,rheo. Above Tm,rheo, the absolute values of the complex viscosities of the cooling and heating cycles overlap. The reason for the sharp change in slopes on cooling and heating, respectively, is the formation and dissolution of paraffin crystals. Previous investigations on the mineral oil MO have shown that the MO changes from a Newtonian liquid to a shear-thinning suspension below Tc,rheo [3].

Crystallization and Melting of Lubricating Greases Based on Mineral Oil (Group I)
Above the melting temperature Tm,rheo, the temperature range in which the oil behaves Newtonian, the level of the complex viscosity increases with increasing thickener concentration from 0.5 Pas without thickener to approx. 10 4 Pas with 15.0 wt.% Li-12-hydroxystearate and 15.8 wt% Ca-12-hydroxystearate as thickener, respectively. Below the temperature of −20 °C, the viscosity reaches a level of about 10 5 Pas regardless of thickener type and concentration. The complex viscosity of the greases at temperatures lower than −20 °C is affected mainly by the presence of paraffin crystals.   Above the melting temperature T m,rheo , the temperature range in which the oil behaves Newtonian, the level of the complex viscosity increases with increasing thickener concentration from 0.5 Pas without thickener to approx. 10 4 Pas with 15.0 wt.% Li-12hydroxystearate and 15.8 wt% Ca-12-hydroxystearate as thickener, respectively. Below the temperature of −20 • C, the viscosity reaches a level of about 10 5 Pas regardless of thickener type and concentration. The complex viscosity of the greases at temperatures lower than −20 • C is affected mainly by the presence of paraffin crystals. Figure 2 depicts the crystallization temperatures T c,rheo and melting temperatures T m,rheo of mineral oil greases with Li-(a) and Ca-12-hydroxystearate (b) as a function of thickener concentration. T c,rheo and T m,rheo were obtained by intersecting two tangents above and below the significant slope change in Figure 1. The mineral oil without thickener exhibits a crystallization temperature T c,rheo of −11.7 ± 0.15 • C and a melting temperature T m,rheo of −0.8 ± 1 • C. Regardless of Li-or Ca-12-hydroxystearate greases, the crystallization temperatures increase to values between −8 and −10 • C, and the melting temperatures decrease to values between −5 and −7 • C. The supercooling (∆T = T c − T m ) decreases from approx. 11 K without thickener to approx. 3 K for Li-12-hydroxystearate and approx. 5 K for Ca-12-hydroxystearate greases at a thickener concentration of about 5 wt.% and essentially remains constant when the fraction of thickener is further increased. thickener concentration. Tc,rheo and Tm,rheo were obtained by intersecting two tangents above and below the significant slope change in Figure 1. The mineral oil without thickener exhibits a crystallization temperature Tc,rheo of −11.7 ± 0.15 °C and a melting temperature Tm,rheo of −0.8 ± 1 °C. Regardless of Li-or Ca-12-hydroxystearate greases, the crystallization temperatures increase to values between −8 and −10 °C, and the melting temperatures decrease to values between −5 and −7 °C. The supercooling (ΔT = Tc − Tm) decreases from approx. 11 K without thickener to approx. 3 K for Li-12-hydroxystearate and approx. 5 K for Ca-12-hydroxystearate greases at a thickener concentration of about 5 wt.% and essentially remains constant when the fraction of thickener is further increased.
The increase in crystallization temperature Tc,rheo is presumably caused by the thickener particles in the base oil. The thickener particles provide crystal nuclei, favoring the formation of paraffin crystals at higher temperatures, here about −8 °C [9,10]. Consequently, the crystallization temperature of the lubricating greases is 4 K above the pour point of the mineral oil (−12 °C). A small amount of dissolved thickener in the base oil presumably causes the decrease in Tm [19].  Figure 1) with an angular frequency ω = 10 rad s −1 , deformation γ = 0.05% cooling and heating rate of β = 2 K min −1 . T c,rheo , and T m,rheo are obtained by intercepting two tangents above and below the significant slope change in Figure 1. The supercooling (∆T = T c − T m ) decreases from approx. 11 K without thickener to approx. 3 K with Li-12-hydroxystearate and approx. 5 K with Ca-12-hydroxystearate. A dashed line marks the pour point of −12 • C.

Lubricating Greases Based on Non-Crystallizing Synthetic Base Oils (Group II)
The increase in crystallization temperature T c,rheo is presumably caused by the thickener particles in the base oil. The thickener particles provide crystal nuclei, favoring the formation of paraffin crystals at higher temperatures, here about −8 • C [9,10]. Consequently, the crystallization temperature of the lubricating greases is 4 K above the pour point of the mineral oil (−12 • C). A small amount of dissolved thickener in the base oil presumably causes the decrease in T m [19]. q as a function of temperature for the grease with the synthetic base oil PAO8 and 22 wt.% Li-12-hydroxystearate (PAO8-22) as a thickener. In the logarithmic plot, the complex viscosity increases approximately linearly with decreasing temperature up to the onset of the glass transition (T G,PAO8-22 = −83 ± 0.2 • C). The absolute value of the complex viscosity increases sharply in the temperature interval between −66 • C and T G , but remains constant at a high level of 10 7 Pas below T G . The lubricating greases based on KR-008 ( Figure A1) and PAG ( Figure A2) behave similarly, see Appendix A. Notably, the temperature at which the two tangents fitted to the sections of the |η*| curve with different slope agrees with the pour point and the end of the section in which |η*| steeply increases corresponds to the glass transition temperature. According to the nucleation theory, for Lubricants 2022, 10, 1 6 of 14 oils such as PAO8, the maximum temperature of crystal growth rate is below the glass temperature T G [10,11].

Lubricating Greases Based on Non-Crystallizing Synthetic Base Oils (Group II)
but remains constant at a high level of 10 7 Pas below TG. The lubricating greases based on KR-008 ( Figure A1) and PAG ( Figure A2) behave similarly, see Appendix A. Notably, the temperature at which the two tangents fitted to the sections of the ‫|‬ η*‫|‬ curve with different slope agrees with the pour point and the end of the section in which ‫|*‪η‬|‬ steeply increases corresponds to the glass transition temperature. According to the nucleation theory, for oils such as PAO8, the maximum temperature of crystal growth rate is below the glass temperature TG [10,11].  Figure 4 compares the glass transition temperatures TG of the base oils PAO8, KR-008 and PAG (abscissa) and the corresponding lubricating greases (ordinate) with Li and Ca-12-hydroxystearate as a thickener. Glass transition temperature of the lubricating greases is always slightly higher (≈2 K) than that of the corresponding base oil but hardly depends on the thickener concentration at least in the investigated concentration range and stays always below −70 °C. The solidification behavior of greases based on non-crystallizing synthetic base oils does not change significantly due to the added thickener. The pour point as well as the glass transition temperature for these base oils and lubricating greases, respectively, are good indicators for their lowest application temperature.  Figure 4 compares the glass transition temperatures T G of the base oils PAO8, KR-008 and PAG (abscissa) and the corresponding lubricating greases (ordinate) with Li and Ca-12hydroxystearate as a thickener. Glass transition temperature of the lubricating greases is always slightly higher (≈2 K) than that of the corresponding base oil but hardly depends on the thickener concentration at least in the investigated concentration range and stays always below −70 • C. The solidification behavior of greases based on non-crystallizing synthetic base oils does not change significantly due to the added thickener. The pour point as well as the glass transition temperature for these base oils and lubricating greases, respectively, are good indicators for their lowest application temperature.

Greases Based on Crystallizing Synthetic Base Oils (Group III)
The absolute value of the complex viscosity of the lubricating greases based on the trimellitate EO increases uniformly on cooling down to the crystallization temperature T c and then rises abruptly. The ester crystallizes to such an extent that the rheometer blocks, and no further measurements are possible [3]. For this reason, the crystallization behavior of trimellitate greases was investigated primarily using differential scanning calorimetry (DSC). Figure 5 shows the heat flux from DSC measurements during cooling (a) and reheating (b) for Ca-12 hydroxystearate lubricating greases with thickener concentrations between 0.5 and 13 wt.%. During cooling, in the temperature range between −10 • C and −50 • C, an exothermic signal arises at thickener concentrations higher than 1 wt.%, which increases in magnitude with increasing thickener concentration and the peak shifts to higher temperatures. The onset temperature increases slightly.

Greases Based on Crystallizing Synthetic Base Oils (Group III)
The absolute value of the complex viscosity of the lubricating greases based on the trimellitate EO increases uniformly on cooling down to the crystallization temperature Tc and then rises abruptly. The ester crystallizes to such an extent that the rheometer blocks, and no further measurements are possible [3]. For this reason, the crystallization behavior of trimellitate greases was investigated primarily using differential scanning calorimetry (DSC). Figure 5 shows the heat flux from DSC measurements during cooling (a) and reheating (b) for Ca-12 hydroxystearate lubricating greases with thickener concentrations between 0.5 and 13 wt.%. During cooling, in the temperature range between −10 °C and −50 °C, an exothermic signal arises at thickener concentrations higher than 1 wt.%, which increases in magnitude with increasing thickener concentration and the peak shifts to higher temperatures. The onset temperature increases slightly.
In addition, an exothermic peak is observed during heating in the temperature range between −45 °C and −30 °C. The crystallization enthalpy during heating Δhc,heating decreases with increasing thickener concentration and is not measurable anymore for thickener concentrations > 9 wt.%; peak temperatures and peak widths remain the same. Above −10 °C, melting of the sample begins. Melting temperature and area of the endothermic peak do not change with thickener concentration. However, the peak becomes somewhat flatter and broader with increasing thickener concentration.  Figure 6 shows melting temperature Tm and crystallization temperature during cooling (Tc,cooling) and heating (Tc,heating) of the trimellitate (EO) based Li-and Ca-12-hydroxystearate greases as a function of thickener content. The melting temperature Tm = 7.8 ± 0.4 °C is independent of thickener type and concentration and the same is true for the crys- q as obtained from DSC measurements during cooling (a) and reheating (b) for Ca-12 hydroxystearate greases with thickener concentrations of 0.5, 1, 2, 7, 9, and 13 wt.% with trimellitate (EO) as base oil at a cooling (a) and heating (b) rate of 2 K min −1 . The integral of the exothermic signals during cooling and heating represent the crystallization enthalpy ∆h c,cooling and ∆h c,heating , respectively. The integral of the endothermic peak represents the enthalpy of fusion (i.e., melting) ∆h f . T c,cooling and T c,heating are the onset temperatures of the crystallization peaks. T m is the offset of the melting peak. In addition, an exothermic peak is observed during heating in the temperature range between −45 • C and −30 • C. The crystallization enthalpy during heating ∆h c,heating decreases with increasing thickener concentration and is not measurable anymore for thickener concentrations >9 wt.%; peak temperatures and peak widths remain the same. Above −10 • C, melting of the sample begins. Melting temperature and area of the endothermic peak do not change with thickener concentration. However, the peak becomes somewhat flatter and broader with increasing thickener concentration. Figure 6 shows melting temperature T m and crystallization temperature during cooling (T c,cooling ) and heating (T c,heating ) of the trimellitate (EO) based Li-and Ca-12-hydroxystearate greases as a function of thickener content. The melting temperature T m = 7.8 ± 0.4 • C is independent of thickener type and concentration and the same is true for the crystallization temperature determined during the heating cycle T c,heating = −46.1 ± 1.9 • C. The trimellitate (EO) in Ca-12-hydroxystearate greases crystallizes at thickener concentrations between 0.5 and 9 wt.% during cooling and heating and above 9 wt.% only during cooling. With increasing thickener concentration, the crystallization temperature upon cooling increases slightly from −22.1 ± 1.1 °C to −19.0 ± 1.0 °C, whereas the crystallization temperature upon reheating remains constant at −43.7 ± 0.4 °C, irrespective of thickener concentration.
The enthalpy of fusion Δhf = 92.5 ± 3.0 J g −1 (endothermic, Figure 5b) is larger than the crystallization enthalpy Δhc = 73.5 ± 6.0 J g −1 because crystal growth is to some extent too slow to cause a detectable heat flux signal. Furthermore, the total enthalpy of fusion Δhf and crystallization Δhc are independent of the thickener concentration, indicating that only the base oil crystallizes. Figure 7 shows the specific enthalpies of crystallization of the greases based on trimellitate (EO) during cooling Δhc,cooling (a) and heating Δhc,heating (b) relative to the total enthalpy of crystallization Δhc = Δhc,cooling + Δhc,heating as a function of Li-and Ca-12-hydroxystearate concentration. The pure ester (EO) does not crystallize upon cooling but only upon heating (T c,heating = −43 ± 0.3 • C). The presence of thickener causes the oil to crystallize during both, cooling and heating cycles. For Li-12-hydroxystearate contents between 1 and 11 wt.% crystallization can be observed upon cooling and heating, for thickener contents above 11 wt.% only during cooling. Up to a thickener concentration of 11 wt.% the crystallization temperature T c,cooling increases linearly from −34 • C to −17 • C, but the crystallization temperature during heating T c,heating remains constant at −46.1 ± 1.9 • C. Above 11 wt.% the Li-12-hydroxystearate greases crystallize only during cooling and the crystallization temperature is T c,cooling = −16.7 ± 0.7 • C. The trimellitate (EO) in Ca-12-hydroxystearate greases crystallizes at thickener concentrations between 0.5 and 9 wt.% during cooling and heating and above 9 wt.% only during cooling. With increasing thickener concentration, the crystallization temperature upon cooling increases slightly from −22.1 ± 1.1 • C to −19.0 ± 1.0 • C, whereas the crystallization temperature upon reheating remains constant at −43.7 ± 0.4 • C, irrespective of thickener concentration.
The enthalpy of fusion ∆h f = 92.5 ± 3.0 J g −1 (endothermic, Figure 5b) is larger than the crystallization enthalpy ∆h c = 73.5 ± 6.0 J g −1 because crystal growth is to some extent too slow to cause a detectable heat flux signal. Furthermore, the total enthalpy of fusion ∆h f and crystallization ∆h c are independent of the thickener concentration, indicating that only the base oil crystallizes. Figure 7 shows the specific enthalpies of crystallization of the greases based on trimellitate (EO) during cooling ∆h c,cooling (a) and heating ∆h c,heating (b) relative to the total enthalpy of crystallization ∆h c = ∆h c,cooling + ∆h c,heating as a function of Li-and Ca-12hydroxystearate concentration. According to ISO 11357-7 [20] the exothermic peaks' total area during cooling and heating corresponds to complete crystallization, and thus the percentage of crystallization during cooling and heating can be calculated. Figure 7 depicts that the percentage of crystallizing base oil upon cooling increases with increasing thickener concentration. As already shown in Figure 5, this indicates a monotonically increasing proportion of heterogeneous crystallization. At thickener concentrations > 9 wt.% Ca-12-hydroxy stearate and >11 wt.% Li-12-hydroxystearate, respectively, only crystallization during cooling occurs because heterogeneous nucleation is predominant.
In the case of the pure trimellitate (EO), nuclei form below the temperature range in which crystal growth is optimal. In case of greases, the thickener creates interfaces at which nuclei can form in the temperature range in which crystal growth takes place. Since nuclei are present, crystal growth is detectable as an exothermic DSC signal [9][10][11].
At low thickener concentrations (0-9 wt.% for Ca-12-hydroxystearate and 0-11 wt.% Li-12-hydroxystearate) only a few nuclei are present. Therefore, only a few crystals start According to ISO 11357-7 [20] the exothermic peaks' total area during cooling and heating corresponds to complete crystallization, and thus the percentage of crystallization during cooling and heating can be calculated. Figure 7 depicts that the percentage of crystallizing base oil upon cooling increases with increasing thickener concentration. As already shown in Figure 5, this indicates a monotonically increasing proportion of heterogeneous crystallization. At thickener concentrations >9 wt.% Ca-12-hydroxy stearate and >11 wt.% Li-12-hydroxystearate, respectively, only crystallization during cooling occurs because heterogeneous nucleation is predominant.
In the case of the pure trimellitate (EO), nuclei form below the temperature range in which crystal growth is optimal. In case of greases, the thickener creates interfaces at which nuclei can form in the temperature range in which crystal growth takes place. Since nuclei are present, crystal growth is detectable as an exothermic DSC signal [9][10][11].
At low thickener concentrations (0-9 wt.% for Ca-12-hydroxystearate and 0-11 wt.% Li-12-hydroxystearate) only a few nuclei are present. Therefore, only a few crystals start to grow, and the crystal growth rate is not fast enough for complete crystallization before reaching the lowest measuring temperature (see Figure 5a).
At thickener concentrations >9 wt.% for Ca-12-hydroxystearat and >11 wt.% for Li-12-hydroxystearate, sufficient amounts of nuclei are present to allow for complete crystallization of the ester upon cooling.
Due to heterogeneous crystallization, the lubrication greases crystallize approximately 37 K above the pour point. Thus, the pour point is not suitable to judge the low temperature application behavior of greases based on trimellitate (EO) with linear alkyl chains (C8-C10).

Conclusions
This study investigates the influence of thickener type and concentration on the crystallization, melting and glass transition of greases made from three different base oil types (Groups I-III) using rheological and thermoanalytical measurements. Group I is represented by a mineral oil (MO), Group II includes amorphously solidifying synthetic lubricating oils (PAG, KR-008, PAO8), and Group III comprises the crystallizing synthetic lubricating ester oil (EO).

Lubricating Greases Based on Mineral Oil (Group I)
During cooling below the crystallization temperature T c,rheo , mineral oils precipitate paraffin crystals. Upon further cooling the complex viscosity reaches an absolute value of about 10 5 Pas, regardless of the thickener type and concentration. The suspension formed by the deposition of paraffin crystals is responsible for the increasingly stiff consistency of the lubricating greases. On reheating, above the melting temperature T m,rheo , the absolute value of the complex viscosity returns to the initial level. The different thickener types (Li-or Ca-12-hydroxystearate) have a significant effect on crystallization (+4 K) and melting temperature (−4 K). The pour point (−12 • C) of the mineral oil is 3 K lower than the crystallization temperature of the lubricating grease and 7 K lower than the melting temperature. This indicates that the pour point does not properly define the lowest application temperature for mineral oil (MO) based greases.

Lubricating Greases Based on Non-Crystallizing Synthetic Oils (Group II)
Group II oils do not crystallize but solidify glass-like at temperatures below −70 • C. This group includes polyalphaolefin (PAO8), alkylated naphthalene (KR-008), and polypropylene glycol (PAG). The addition of Li-12-hydroxystearate does not change the glass transition temperature significantly. The absolute value of the complex viscosity of these greases increases steadily with decreasing temperature. At about 20 K above T G , however, the absolute value of the complex viscosity increases sharply, i.e., the slope of the |η*| vs. T curve changes significantly. The onset of this steep viscosity increase is equal to the pour point of the corresponding oil and the latter thus is an appropriate measure for the lowest application temperature of these greases.

Lubricating Greases Based on Crystallizing Synthetic Oils (Group III)
Group (III) oils crystallize with strong supercooling effects up to cold crystallization. Trimellitate (EO) with linear C8-C10 alkyl chains belongs to this group. This ester oil (EO) shows that adding minor thickener concentrations (about 0.5 wt.% Ca-12-hydroxystearate, 1 wt.% Li-12-hydroxystearate) causes the ester to crystallize partly upon cooling and partly upon heating. The fraction of crystallization during cooling rises with increasing thickener concentration until the ester oil crystallizes only upon cooling. This is due to heterogeneous nucleation, which becomes more significant with increasing thickener concentration. As a result of heterogeneous nucleation, the crystallization temperature rises from −45 • C to −20 • C. In contrast, the melting temperature T m remains constant at 7 • C independent of the thickener concentration and thickener type. The investigations show that using lubricating greases based on this ester oil below the melting temperature is not advisable. Especially for lubricating greases based on trimellitate (EO), the pour point of −57 • C is inappropriate as indicator for the lowest application temperature.      q of the PAG-10 grease at a heating rate of 10 K min −1 . The grease shows a glass transition temperature T G at −77 ± 0.2 • C, marked by a solid line. The dashed line marks the pour point for the base oil PAG of −51 • C.