Rheology of Filled and Unfilled Polyurethanes for Reactive Extrusion-Based Applications

Abstract

Additive manufacturing (AM) is a form of production that directly processes raw materials into their final form by building the product in a layer-by-layer fashion. Numerous types of AM exist, including selective laser sintering (SLS) of polymeric powders, vat polymerization (VP) of low viscosity photocurable resins, and material extrusion (MatEx) of thermoplastic or high viscosity composite materials. Because of its ability to reduce material waste while printing complex geometries, AM has the potential to revolutionize the manufacturing industry for a diverse set of materials and products. MatEx of thermoplastic feedstocks is most commonly performed using fused filament fabrication (FFF) – a form of melt extrusion. A solid filament is fed directly into a heated nozzle, where it melts onto a build bed before resolidifying in a matter of seconds. While this is the most common form of AM, especially among hobbyists, the material catalog is limited to thermoplastic polymers, and difficulties arise when fillers are introduced (e.g. reactions at elevated temperatures, clogging, disruption of polymer chain diffusion, and large increases in viscoelastic properties). To combat these challenges, direct ink write (DIW) AM extrudes highly viscous composites by applying pneumatic backpressure to a syringe, such that the material can be extruded in ambient conditions. This method enables processing of unreacted, thermosetting resins which have been filled with a large proportion of solid particulate fillers, called "highly filled" inks. The interparticle network formed from particle-particle interactions in the form of weak surface forces (e.g. Van der Waals forces) provides structural stability of the printed lines, such that they can sustain the weight of subsequent layers. In the realm of DIW 3D printing material discovery and processing, there are currently three major challenges. First, the high shear region of the nozzle frequently disrupts the interparticle network through a de-agglomeration process, such that there is a finite timescale for the interparticle network to reestablish itself. During this timeframe, the deformation/reformation process causes printed lines to sag, which negatively impacts both print quality and mechanical properties. Second, printed parts require a post-processing step to develop adequate mechanical properties suitable for the final product. The kinetics of this cure process are extremely slow, often taking multiple days or weeks to reach completion. Third, high shear rheological characterization of highly filled inks is challenging because of the numerous artifacts of error associated with high shear testing environments (e.g. sample loss/edge fracture, slip, and large sample size requirements). A literature review in Chapter 2 outlines the most recent advances in highly filled polyurethane processing for DIW, with a particular focus on how interparticle network recovery – in the form of thixotropy – can be tailored using a variety of reactive inks. The subsequent chapters of this dissertation address these challenges by systematically downselecting reactive inks appropriate for highly filled DIW extrusion while introducing numerous process relevant rheological protocols. An initial discussion in Chapter 3 covers the potential drawbacks of thermoplastic polyurethane (TPU) processing as it relates to industrial scale melt extrusion. Specifically, multiple side reactions and degradation processes are identified for a variety of TPU manufacturers. Such reactions elicit undesirable solid-like particulate buildup within the extrusion line, and the impacts/causes of these reactions are quantified using rheological criteria. These protocols offer evidence that differences in processability can arise not just between manufacturers, but also between lots of TPU from the same manufacturer. To address these concerns, Chapter 4 offers an alternative form of polyurethane processing in the form of a thermosetting reaction between hydroxyl-terminated polybutadiene (HTPB) and isophorone diisocyanate (IPDI). When uncatalyzed at room temperature, full conversion takes place over the course of multiple weeks which necessitates an accelerated kinetic analysis. Hence, a combination of chemorheological and spectroscopic methods are used to rapidly probe for changes in isocyanate reactivity using limited sample quantities, which substantiate the advantages and disadvantages of chemorheology and spectroscopy in the context of curing studies. While this synthetic pathway provides mechanical properties appropriate for the final printed product, a major concern is retention of green body strength post deposition. In order to maintain the shape of printed beads, ultraviolet (UV) light can be shined in-situ onto the nozzle of a DIW printhead, which actively cures the urethane acrylate ink through free radical polymerization. This technique, termed UV-assisted direct ink write (UV-DIW), assists recovery of the interparticle network. A novel rheological method proposed in Chapter 5, termed the "UV-assisted three interval thixotropy test" (UV-3ITT), quantifies the contribution of UV light towards structural stability and printability. This is accomplished by applying stepwise changes in strain on a torsional photorheometer, optionally applying UV light in the third interval, and then quantifying the contribution of UV light towards process-relevant recovery parameters. Resultingly, the threshold of solid particulate fillers required for UV light to improve print fidelity is determined. While most discussions revolve around torsional rheology, this method has one major drawback: it cannot probe the high shear properties of high solids content materials due to sample loss/edge fracture during steady shear measurement. Capillary rheometers are able to probe the viscosity profiles of highly filled materials in high shear environments, but the cost of the device and the sample requirements are burdensome. To resolve this challenge, the "microcapillary rheometer" is developed in Chapter 6 using common laboratory equipment at a fraction of the cost of a full-scale capillary rheometer, which enables rapid characterization of high solids content materials at extrusion-relevant conditions while exploiting small sample quantities. This study illustrates the accuracy and precision of the microcapillary rheometer when comparing the high shear properties of several highly filled systems to the full-scale capillary rheometer. Results highlight that application of the Bagley and Weissenberg-Rabinowitsch corrections is possible using this novel device, which facilitates calculation of true shear viscosity of high solids content systems. The limited sample requirement facilitates characterization of novel or potentially hazardous materials in a much safer, efficient manner, which accelerates material discovery while improving safety standards.