2015
DOI: 10.1007/s00397-015-0835-1
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Critical quantities on the yielding process of waxy crude oils

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Cited by 51 publications
(19 citation statements)
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“…In fact, the attempt to find the critical stress is very common for the case of waxy crude oils, which is a very complex elasto-viscoplastic gel. Typically, the critical stress for a waxy oil is the yield stress, the stress necessary to break the material's viscoplastic structure [9,10,24,32,35]. Here, the critical stress is that necessary to overcome the adhesive force between the gel and the wall, as stated in [24].…”
Section: Resultsmentioning
confidence: 99%
“…In fact, the attempt to find the critical stress is very common for the case of waxy crude oils, which is a very complex elasto-viscoplastic gel. Typically, the critical stress for a waxy oil is the yield stress, the stress necessary to break the material's viscoplastic structure [9,10,24,32,35]. Here, the critical stress is that necessary to overcome the adhesive force between the gel and the wall, as stated in [24].…”
Section: Resultsmentioning
confidence: 99%
“…For low values of applied stress, the shear rate develops a trajectory in time that ends in a negligible shear rate. For high stress values, this phenomenon can also be detected in a deformation versus time plotting where an almost constant plateau is reached for low stress values ( Tarcha, Forte, Soares, & Thompson, 2015 ). The difficulties in experimentally determining the yield stress of a material are known in the literature and are more pronounced in thixotropic and other time-dependent systems as discussed in Møller et al (2006) and Soares, Thompson, and Machado (2013) .…”
Section: Viscoplastic Time-dependent Phenomenamentioning
confidence: 86%
“…The instrument used was the MCR 301 controlled stress rheometer from Anton Paar operating in the shear stress range 10 -7 -10 5 Pa and shear rate range 10 -6 -10 4 s -1 with Peltier temperature control of ±0.5 o C and cooling rates in a range varying from 0.01 to 6.5 o C/min. The recommended (see Tarcha et al (2015) study with different geometries) cone and plate geometry (stainless steel plate, diameter 25 mm and cone angle 0.991 0 ) was used as this provided no slip, a uniform shear rate and uses a small sample (0.60ml) suitable for effective temperature control. The critical difference between this and earlier work (Chang et al, 1998) is the resolution in the shear stress/rate achievable, enabling to zoom into the elastic region and probing the creep-fracture region in very small steps and rates.…”
Section: Rheometry Methodologymentioning
confidence: 99%
“…Restarting a gelled pipeline is thus a common problem in the oil industry which can be very expensive without a good understanding of the rheology of the cooled static gel to enable a correct prediction of an appropriate re-start pressure to be made. Because of the importance of the problem, gelled waxy crude oils have been extensively studied and from several perspectives, morphology (Kok et al, 1996, Singh et al, 2001, Chen et al, 2004, Visintin et al, 2008, Yi and Zhang, 2011, Lin et al, 2011, rheology (Wardhaugh and Boger, 1991a, 1991b, Rønningsen, 1992, Chang et al, 1998, Chang et al, 2000, da Silva and Coutinho, 2004, Kane et al, 2004, Venkatesan et al, 2005, Visintin et al, 2005, Visintin et al, 2008, Magda et al, 2009, Hou and Zhang, 2010, Dimitriou et al, 2011, Rønningsen, 2012, Marchesini et al, 2012, Tarcha et al, 2015, Andrade et al, 2015, Van Der Geest et al, 2017, Andrade et al, 2018 and modelling of pipe flow restart (Chang et al, 1999, Davidson et al, 2004, Vinay et al, 2006, Huang et al, 2011, Van Der Geest et al, 2015, Oliveira et al, 2015.…”
Section: Introductionmentioning
confidence: 99%