Elsevier

Carbohydrate Polymers

Volume 74, Issue 4, 21 November 2008, Pages 907-913
Carbohydrate Polymers

Amylose content and chemical modification effects on the extrusion of thermoplastic starch from maize

https://doi.org/10.1016/j.carbpol.2008.05.017Get rights and content

Abstract

The effects of starch structural properties and starch modification on extruder operation were monitored via die pressure, motor torque, mean residence time and specific mechanical energy (SME). The structural properties studied involved variations in the ratios of amylose and amylopectin as well as the effect of a hydroxypropylated starch on the fore mentioned extruder properties. A full factorial design of experiments (DOE) was used to then determine the influence of starch type (unmodified starches with 0%, 28%, 50% and 80% amylose; 80% amylose hydroxypropylated starch) and screw speed (250, 300 and 350 rpm) on these processing parameters. The effects of starch type and screw speed on extrusion operation that were systematically investigated using the DOE and have provided valuable insight into the relationships between starch structure and processing. The design of experiments showed that starch type for both unmodified and modified maize had a statistically significant effect on parameters such as torque, die pressure and specific mechanical energy and that screw speed also significantly effected specific mechanical energy. Residence time distributions differed according to starch type (amylose content, hydroxypropylation) and screw speed. The additional study of residence time distribution also gave an indication of the degree of mixing in the extruder. Starch type variations were apparent at low screw speed however at higher screw speed the influence of starch type decreased significantly.

Introduction

The development of a fully biodegradable, natural, renewable thermoplastic is of increasing interest due to its low environmental impact when compared to current petroleum based products that contribute to litter and landfill problems (Swift, 1996). In response to these problems, research into the synthesis of materials from natural sources such as starch and cellulose is being undertaken with the aim of replacing their non-biodegradable counterparts.

Starch is a polymeric material that is biodegradable, renewable and also available worldwide at low cost, which makes it attractive as a substitute for petroleum based plastics (Trommsdorff & Tomka, 1995). However, simple extruded starches with water products are brittle and highly sensitive to water (Ollett et al., 1991, Slade and Levine, 1993). As a result, development of practical thermoplastic starch resins includes the addition of processing aids and plasticisers to aid gelatinisation during processing thus producing suitable mechanical properties in the finished product (Doane, 1992, Shogren et al., 1992). Recently, commercially biodegradable packaging has been developed to overcome these problems (Halley, Mcglashan, & Gralton, 2006 Patent No. 7094817), giving the opportunity to manufacture products from starch-based thermoplastic resins (Plantic Technologies Ltd YeBiodegradable Lethal Ovitrapar, 2007).

Prior to thermoplastic processing such as injection moulding, starch is extruded and gelatinised to form a thermoplastic material that can be subsequently processed into viable products (Wiedmann & Strobel, 1991). Different extrusion processing conditions will alter the transformation of the starch during the preparation of the thermoplastic starch resin (Wiedmann & Strobel, 1991), which ultimately affects the mechanical properties of the finished product (Van Soest, De Wit, & Vliegenthart, 1996). Screw speed is a particularly useful processing variable, since it is readily altered during extrusion operation, controls the amount of work done on the material during processing, affects the extent of degradation of starch and alters the rheology of starch melts (Tolstoguzov, 1993, Van Soest et al., 1996).

Just as there is a wide variety of synthetic thermoplastic polymers available which differ in their monomers, their structure (molecular weight of chains, extent of branching), particular processing characteristics, and desired products physical properties (e.g. mechanical properties, barrier properties, appearance), similarly, with thermoplastic starches, the type of starch, chemical modification of the starch and tailored processing conditions has been shown to be able to be optimised for particular of the finished product (Halley, et al. 2006).

When starch type and screw speed are considered together, they have been shown to have a major effect on extrusion and finished product properties. In a study of (Van Soest, De Wit, et al., 1996) it was shown that increasing the screw speed, increased single helical type crystallinity for higher amylose content starches, thus affecting the final product mechanical properties.

The objective of our research was to study the effects of varying amylose/amylopectin ratios of maize starches when processed using a twin screw extruder. Hydroxypropylated starch was used for two reasons. Firstly, starch modification is carried out to improve the functional and physicochemical parameters in various industries since native starch itself may not give optimal performance (Lawal, 2004) and it is high amylose hydroxypropylated starch that is commercially available in Australia to produce thermoplastic materials. The effects of starch type (0–80% amylose maize starch; hydroxypropylation of 80% amylose maize starch) and mechanical processing conditions (screw speed) on extruder operation (motor torque, SME, die pressure, mean residence time) were analysed.

Section snippets

Materials

All of the maize starches (Table 1) were supplied by Penford Australia and New Zealand Limited (Lane Cove, Australia) and included four unmodified maize starches (Mazaca 3401X, Avon Maize Starch, Gelose 50, Gelose 80) that differ in their amylose content, and a hydroxypropylated high amylose starch (Gelose 939).

Plasticisers and emulsifiers were added [in accordance to US Patent No. 7094817 (Halley, et al. 2006) to the starch with an increased level of polyols to produce a thermoplastic starch

Extruder torque and die pressure

Motor torque in the extruder, barrel pressures and die pressure were monitored and recorded during the extrusion process using a configured spreadsheet with process status displayed in real time (RSLinx software, version 3.12, Entek Extruders, Oregon, USA).

Residence time distribution

A tracer (allura red dye) was dropped into the feed port of the extruder and this was labelled as time zero. Changes in time interval collection (listed below) were based on colour concentration, the more concentrated the colour the more

Extruder operation

Extrusion stability and quality were be monitored by observing the flow rate, melt temperature, motor torque, and barrel and die pressures (Stevens & Covas, 1995). After start-up, it took approximately 15 min for the process to stabilise (constant barrel and die pressures, flow of extrudate out of the die, and motor torque). The process did not experience any surging (i.e. variation in die pressure, motor torque, or flow of extrudate out of the die), and the melt exiting die was uniform and

Overall discussion

The processing behaviour of the five starch types showed that starch structure (amylose and amylopectin) have an individual effects on extrusion processing parameters. The results show that from a processing point of view, the amylose content and the modification of starch greatly affect the behaviour of the material; however, screw speed influence does to a lesser degree and is primarily due to the viscosity changes during gelatinisation transitions and the interactions between the amylose and

Conclusion

Starch with low amylose content gave lower torque values, die pressure values and was subjected to a reduced amount of mechanical work, which resulted in a reduced axial mixing at slower screw speeds. However, these effects were less apparent as screw speed increased.

The results showed that processing hydroxypropylated 80% amylose starch was substantially different to unmodified 80% amylose starch. Modification due to hydroxypropylation of the starch affects its gelatinisation behaviour

Acknowledgements

The authors thank Dr. Kishan Khemani, Mr. Nick McCaffery (Plantic Technologies) and Dr. Deeptangshu Chaudhary (Curtin University) for their valuable advice and insight given during this study.

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      There is an excellent potential for producing improved films by using a combination of HAS and HPT. Flexibility, transparency, and processibility are the favorable and desirable characteristics of hydroxypropylated starch for film application (Chaudhary, Miler, Torley, Sopade, & Halley, 2008; Lafargue, POntoire, Buleon, Doublier, & Lourdin, 2007). It has also been documented that the EAB and TS of maize starch films can be enhanced by dual modification involving de-branching and HPT (Hu, Jia, Zhi, Jin, & Miao, 2019).

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