Academic literature on the topic 'Intermeshing counter-rotating twin screw extruders'

Create a spot-on reference in APA, MLA, Chicago, Harvard, and other styles

Select a source type:

Consult the lists of relevant articles, books, theses, conference reports, and other scholarly sources on the topic 'Intermeshing counter-rotating twin screw extruders.'

Next to every source in the list of references, there is an 'Add to bibliography' button. Press on it, and we will generate automatically the bibliographic reference to the chosen work in the citation style you need: APA, MLA, Harvard, Chicago, Vancouver, etc.

You can also download the full text of the academic publication as pdf and read online its abstract whenever available in the metadata.

Journal articles on the topic "Intermeshing counter-rotating twin screw extruders"

1

Hong, M. H., and J. L. White. "Fluid Mechanics of Intermeshing Counter-Rotating Twin Screw Extruders." International Polymer Processing 13, no. 4 (1998): 342–46. http://dx.doi.org/10.3139/217.980342.

Full text
APA, Harvard, Vancouver, ISO, and other styles
2

Wilczynski, Krzysztof, and James L. White. "Melting model for intermeshing counter-rotating twin-screw extruders." Polymer Engineering & Science 43, no. 10 (2003): 1715–26. http://dx.doi.org/10.1002/pen.10145.

Full text
APA, Harvard, Vancouver, ISO, and other styles
3

Jiang, Qibo, Jinhai Yang, and James L. White. "Simulation of screw pumping characteristics for intermeshing counter-rotating twin screw extruders." Polymer Engineering & Science 51, no. 1 (2010): 37–42. http://dx.doi.org/10.1002/pen.21789.

Full text
APA, Harvard, Vancouver, ISO, and other styles
4

Chen, L., G. H. Hu, and J. T. Lindt. "Residence time distribution in non-intermeshing counter-rotating twin-screw extruders." Polymer Engineering and Science 35, no. 7 (1995): 598–603. http://dx.doi.org/10.1002/pen.760350706.

Full text
APA, Harvard, Vancouver, ISO, and other styles
5

Zhang, Yuan, Xiaohan Jiang, Huaping Fan, and Xihan Li. "Optimization and Numerical Simulation of Outlet of Twin Screw Extruder." MATEC Web of Conferences 153 (2018): 05004. http://dx.doi.org/10.1051/matecconf/201815305004.

Full text
Abstract:
In view of the unreasonable design of non-intermeshing counter-rotating twin screw extruder die, the problem of productivity reduction was discussed. Firstly, the mathematical model of extruder productivity was established. The extruder die model was improved. Secondly, the force analysis of twin screw extruder physical model was carried out. Meanwhile, A combination of mechanical analysis and numerical simulation was adopted. The velocity field, pressure field and viscosity field were calculated by Mini-Element interpolation method, linear interpolation method and Picard iterative convergence method respectively. The influence of die model on the quantity of each field before and after improvement was analyzed. The results show that the improved model had increased the rheological parameters of the flow field, the leakage and reverse flow decreased. Through post-processing calculation, the productivity of the third dies extruder was 10% higher than before. The research results provide a theoretical basis for the design and optimization of die model of non intermeshing counter-rotating twin screw extruder.
APA, Harvard, Vancouver, ISO, and other styles
6

White, James L., and Witold Szydlowski. "Composite models of modular intermeshing corotating and tangential counter-rotating twin screw extruders." Advances in Polymer Technology 7, no. 4 (1987): 419–26. http://dx.doi.org/10.1002/adv.1987.060070407.

Full text
APA, Harvard, Vancouver, ISO, and other styles
7

Potente, H., J. Ansahl, and B. Klarholz. "Design of Tightly Intermeshing Co-Rotating Twin Screw Extruders." International Polymer Processing 9, no. 1 (1994): 11–25. http://dx.doi.org/10.3139/217.940011.

Full text
APA, Harvard, Vancouver, ISO, and other styles
8

Wang, G., X. Z. Zhu, and Chun Yi Sun. "Numerical Simulation of Mixing Performance of Intermeshing Co-Rotating Tri-Screw and Twin-Screw Extruders." Advanced Materials Research 468-471 (February 2012): 2211–14. http://dx.doi.org/10.4028/www.scientific.net/amr.468-471.2211.

Full text
Abstract:
Parallel arranged tri-screw extruder (PATSE) is a new machine of polymer processing and first manufactured in recent years in China. Compared with the traditional twin-screw extruder, PATSE adds a screw, and added an intermeshing region. It is well known that material going though intermeshing region will acquire higher shear rate and stretching rate, which is beneficial to mixing processing. In order to know the mixing performance in cross-section for PATSE, polymer melt flow field simulation and mixing simulation were conducted on PATSE with 2D model and a Carreau flow model to evaluate velocity profiles, particle trajectories, max shear rate, max stretching rate, dispersive mixing, distributive mixing, segregation scale, length of stretch, mixing efficiency with the commercial CFD package Polyflow and compared with those of twin screw extruder (TSE). The results show that PATSE has better mixing performance than TSE.
APA, Harvard, Vancouver, ISO, and other styles
9

Jiang, Q., J. L. White, and J. Yang. "A Global Model for Closely Intermeshing Counter-rotating Twin Screw Extruders with Flood Feeding." International Polymer Processing 25, no. 3 (2010): 223–35. http://dx.doi.org/10.3139/217.2333.

Full text
APA, Harvard, Vancouver, ISO, and other styles
10

Ganzeveld, K. J., and L. P. B. M. Janssen. "Scale-up of counter-rotating closely intermeshing twin screw extruders without and with reactions." Polymer Engineering and Science 30, no. 23 (1990): 1529–36. http://dx.doi.org/10.1002/pen.760302307.

Full text
APA, Harvard, Vancouver, ISO, and other styles
More sources

Dissertations / Theses on the topic "Intermeshing counter-rotating twin screw extruders"

1

Jiang, Qibo. "Modeling Flow, Melting, Solid Conveying and Global Behavior in Intermeshing Counter-Rotating Twin Screw Extruders." University of Akron / OhioLINK, 2008. http://rave.ohiolink.edu/etdc/view?acc_num=akron1216142037.

Full text
APA, Harvard, Vancouver, ISO, and other styles
2

Ban, Kyunha. "Mechanism and Significance of Slip and New Mixing Elements During Flow in Modular Intermeshing Co-Rotating Twin Screw Extruders." University of Akron / OhioLINK, 2008. http://rave.ohiolink.edu/etdc/view?acc_num=akron1218132059.

Full text
APA, Harvard, Vancouver, ISO, and other styles
3

Lai-F. "Melt conveying in counter-rotating twin-screw extruders." Thesis, Imperial College London, 1985. http://hdl.handle.net/10044/1/37751.

Full text
APA, Harvard, Vancouver, ISO, and other styles
4

Singh, D. P. "Flow and mixing studies in a co-rotating intermeshing twin screw extruder." Thesis, Brunel University, 1988. http://bura.brunel.ac.uk/handle/2438/5548.

Full text
Abstract:
The basic understanding of mixing in the process of polymer melt extrusion by twin screw extruder is limited by their geometrical complexity and the interactions of the process parameters. Mixing and flow in a 100mm diameter, trapezoidal channeled, intermeshing co-rotating twin-screw extruder have been characterised by determination of residence time distribution (RTD) and of the paths taken by tracers added to the melt. The axial mixing and the effects of varius parameters on it were established by studying RTD using tracer techniques. As the tail of the distribution is of paramount importance, the reproducibility of the RTD curve was extensively studied. Radioactive NnO2 was used as a tracer and detected by gamma ray spectroscopy giving more reproducible results than added barytes estimated gravimetrically after ashing. Shock cooling of the extruder and sectioning of the solidified compound in the screw channels was used to-study the flow mechanism. The maximum throughput achieved, polymer melting mechanism, filled volume and axial mixing Are interrelated, and are dependent on the configuration and position of segmented mixing discs present in the screw profile. In the upstream position these act as melting discs and their efficiency is increased in a closed configuration. Initial melting is achieved over a remarkably short distance along the screw profile. The screw speed affects the axial mixing which is shown to be related to the net relative pressure change at the screw tips. A flow model is proposed such that the overall material flow taking place in an anticlockwise direction along the screw channel comprises two separate flow regimes. The upper regime rotates anti-clockwise and is made up of main and small tetrahedron flow and calender flow. The lower flow regime rotates clockwise and is made up of main and small side leakage flows and a portion of the main tetrahedron flows together with a central flow. The flow studies show conclusively that the melt from a particular site ahead of the intermeshing zone occupies a predestined site after passing through the intermeshing zone.
APA, Harvard, Vancouver, ISO, and other styles
5

Bruce, David P. "Flow field analysis of some mixing and conveying screw element regions, within a closely intermeshing, co-rotating twin-screw extruder." Thesis, Aston University, 1997. http://publications.aston.ac.uk/9602/.

Full text
Abstract:
Grafting of antioxidants and other modifiers onto polymers by reactive extrusion, has been performed successfully by the Polymer Processing and Performance Group at Aston University. Traditionally the optimum conditions for the grafting process have been established within a Brabender internal mixer. Transfer of this batch process to a continuous processor, such as an extruder, has, typically, been empirical. To have more confidence in the success of direct transfer of the process requires knowledge of, and comparison between, residence times, mixing intensities, shear rates and flow regimes in the internal mixer and in the continuous processor. The continuous processor chosen for the current work in the closely intermeshing, co-rotating twin-screw extruder (CICo-TSE). CICo-TSEs contain screw elements that convey material with a self-wiping action and are widely used for polymer compounding and blending. Of the different mixing modules contained within the CICo-TSE, the trilobal elements, which impose intensive mixing, and the mixing discs, which impose extensive mixing, are of importance when establishing the intensity of mixing. In this thesis, the flow patterns within the various regions of the single-flighted conveying screw elements and within both the trilobal element and mixing disc zones of a Betol BTS40 CICo-TSE, have been modelled using the computational fluid dynamics package Polyflow. A major obstacle encountered when solving the flow problem within all of these sets of elements, arises from both the complex geometry and the time-dependent flow boundaries as the elements rotate about their fixed axes. Simulation of the time dependent boundaries was overcome by selecting a number of sequential 2D and 3D geometries, used to represent partial mixing cycles. The flow fields were simulated using the ideal rheological properties of polypropylene and characterised in terms of velocity vectors, shear stresses generated and a parameter known as the mixing efficiency.
APA, Harvard, Vancouver, ISO, and other styles
6

Hojabr, Sassan. "Mathematical modeling and process investigation of melt grafting reactions in an intermeshing co-rotating twin screw extruder." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1998. http://www.collectionscanada.ca/obj/s4/f2/dsk2/tape17/PQDD_0004/NQ27829.pdf.

Full text
APA, Harvard, Vancouver, ISO, and other styles

Books on the topic "Intermeshing counter-rotating twin screw extruders"

1

Shah, Khalid H. Reactive polymerisation of caprolactam in a co-rotating intermeshing twin screw extruder. Brunel University, 1992.

Find full text
APA, Harvard, Vancouver, ISO, and other styles
2

Singh, Devendra Pal. Flow and mixing studies in a co-rotating intermeshing twin screw extruder. Brunel University, 1988.

Find full text
APA, Harvard, Vancouver, ISO, and other styles
3

Orchard, Stephen Frederick. Reactive extrusion: The use of a co-rotating, intermeshing twin-screw extruder to perform catalytic hydrogenation of soya bean oil using immobilised and slurry catalysts. University of Birmingham, 1998.

Find full text
APA, Harvard, Vancouver, ISO, and other styles

Book chapters on the topic "Intermeshing counter-rotating twin screw extruders"

1

Sämann, Hans-Joachim. "Screw Elements for Co-rotating, Closely Intermeshing, Twin-Screw Extruders." In Co-Rotating Twin-Screw Extruder. Carl Hanser Verlag GmbH & Co. KG, 2007. http://dx.doi.org/10.3139/9783446433410.012.

Full text
APA, Harvard, Vancouver, ISO, and other styles
2

Malik, Moinuddin, David Fair, Richard Muscato, et al. "Continuous Processing and Shaping Using a Fully Intermeshing Co-Rotating Twin Screw Extruder." In Energetic Materials. CRC Press, 2017. http://dx.doi.org/10.1201/9781315166865-12.

Full text
APA, Harvard, Vancouver, ISO, and other styles
3

Geng, Xiaozheng, and Ruiju Sang. "The Investigation on Melt Pumping Mechanisim of Counter–rotating Intermeshing Twin Screw Extruders." In Theoretical and Applied Rheology. Elsevier, 1992. http://dx.doi.org/10.1016/b978-0-444-89007-8.50171-4.

Full text
APA, Harvard, Vancouver, ISO, and other styles
4

Nichols, Russell J., and J. Thomas Lindt. "Devolatilization in Counter-Rotating Nonintermeshing, Twin-Screw Extruders." In Polymer Devolatilization. Routledge, 2017. http://dx.doi.org/10.1201/9780203742914-13.

Full text
APA, Harvard, Vancouver, ISO, and other styles

Conference papers on the topic "Intermeshing counter-rotating twin screw extruders"

1

Nixon, Jason R., and David I. Bigio. "Effects of Variable Fiber Microstructure in Composite Fused Filament Fabrication on Physical Properties Using High Aspect Ratio Short Fibers." In ASME 2015 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2015. http://dx.doi.org/10.1115/imece2015-51903.

Full text
Abstract:
Polymeric fused filament fabrication technology (FFF), a subfield within additive manufacturing (AM), is becoming a contender for the reintroduction of the small-scale manufacturing of customized consumer products to a mass-production dominated world market. However, before this technology can be widely implemented, there remain significant technological hurdles to overcome. One issue that has been addressed at great length in other traditional polymer manufacturing fields is the inclusion of fillers in the component for physical property enhancement or the introduction of entirely new properties to the matrix material. Experiments conducted in this study examined the inclusion of carbon microfibers (CMFs) into the matrix material prior to the printing process, and the effect of different processing parameters on the final filler structure of the composite parts post printing. Prior work on microstructural evolution during extrusion in a 3D printer has been conducted computationally to study the effects of extrusion rate, matrix rheology, and nozzle geometry on fiber orientation [1]. It was found that varying the nozzle geometry generated significantly different microstructures, and that the remainder of the parameters could be varied to fine-tune microstructural characteristics. Findings indicated that, by varying the nozzle geometry from a converging to a diverging conical section, microstructures ranging from axially oriented (with respect to the extrusion direction) to radially oriented are theoretically possible. Current work performed on extruders and FFF platforms indicates that during the extrusion process, fibers tend to align very closely to the axis of extrusion in shear flow (i.e. converging or straight dies). However, in some applications, this may not be the most effective filler structure for property enhancement, so there remains interest in exploring methodologies for fiber rotation during extrusion. For this study, CMFs and acrylonitrile butadiene styrene (ABS) were compounded using a 28mm fully-intermeshing co-rotating twin-screw (CoTSE) extruder. 3D printer feedstock was manufactured in-house. A range of concentrations from 0%wt to 15%wt fabricated and tested. Analysis of the feedstock indicated nearly axial fiber alignment post-manufacture. This feedstock was then used in a Lulzbot TAZ4 printer to manufacture composite tensile testing specimens. Printed composite properties were then identified and compared to neat ABS and bulk composite properties. It was found that using a purely converging die, highly aligned filler structures were produced (with respect to the bead laid by the printer). Using a diverging nozzle, more random filler structures were produced. Improvements in both intra-layer properties were observed using the diverging nozzle geometries to reorient fibers during extrusion. Property improvements were not found to be as high as longitudinal properties for highly aligned filler structures. Using insights gained through these experiments, we are currently working on exploring added functionality for the composites using different types of fillers as well as multi-scale filler combinations.
APA, Harvard, Vancouver, ISO, and other styles
2

Zhang, Jing-Jing, Han-Xiong Huang, and Yu-Huan Wang. "Online Measurement of Viscosity of HDPE-Wood Flour Composites Compunded in Different Processing Condition." In ASME 2006 International Mechanical Engineering Congress and Exposition. ASMEDC, 2006. http://dx.doi.org/10.1115/imece2006-14015.

Full text
Abstract:
In this study, the viscosity of high-density polyethylene (HDPE)-wood flour composites compounded in different processing condition was measured using the Hakke online rheometer (Hakke Proflow). Composites were prepared in an intermeshing co-rotating twin-screw extruder. Influence of HDPE melt index on the melt shear viscosities of the composites was studied. To investigate the viscosity in different processing condition, two screw configurations and three screw speeds were considered. The results showed that the effect of wood on increasing the viscosity was more pronounced in higher melt index HDPE composites. The viscosity decreased with increasing screw speed from 100rpm to 300rpm. In terms of screw configuration, both small-pitch conveying screw element and kneading elements with wide disks and large staggering angle were benefit to the flow of HDPE-wood composites. Medium shear should be selected to optimize the flow. Higher HDPE melt index wood composites processed in shear and longitudinal mixing flow field presented more shear-thinning behavior.
APA, Harvard, Vancouver, ISO, and other styles
3

Huang, Han-Xiong, Guo Jiang, and Shan-Qiang Mao. "Effect of Flow Fields on Morphology of PP/Nano/CaCO3 Composite and Its Rheological Behavior." In ASME 2005 International Mechanical Engineering Congress and Exposition. ASMEDC, 2005. http://dx.doi.org/10.1115/imece2005-80830.

Full text
Abstract:
Polypropylene (PP)/nano-calcium carbonate (nano-CaCO3) composite was prepared using a co-rotating, intermeshing twin-screw extruder. The effect of flow fields on the morphology of the nanocomposite was investigated. Transmission electron microscopy (TEM) was used for the determination of the morphology in the nanocomposite. The crystallization behavior of the nanocomposite was studied by using differential scanning calorimetry (DSC) and the melt shear viscosity was investigated by a melt flow index tester. The study showed that the flow field, through appropriately combining the type of the screw elements in this work, plays an important role in developing morphology of the nanocomposite. In addition, it was shown that the melt viscosity for the nanocomposite at the filler content less than 10 wt% is lower than that of neat PP.
APA, Harvard, Vancouver, ISO, and other styles
4

Nixon, Jason R., Inna Lempert, Hyunjo Choi, Jeremy McFarlane, and David I. Bigio. "Characterization of Material Properties for Multi-Scale Polymer Composites Extruded From Straight and Divergent Die Geometries Using Various Filler Concentrations." In ASME 2015 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2015. http://dx.doi.org/10.1115/imece2015-51919.

Full text
Abstract:
The addition of nano-scale and micro-scale fillers has been proven to increase tensile and thermal properties in polymer composites. Orientation of high aspect fillers, however, has not been studied before despite being crucial to altering physical properties. When fibers are included during extrusion, they tend to align in the direction of the flow. This phenomena leads to longitudinal improvements in mechanical properties, and thus provides great benefits in some applications; however, it is beneficial to have improved properties in the transverse direction as well. Therefore, it is crucial to study reorientation phenomena in composites. The purpose of this experiment is to study property enhancement resulting from fiber structure. The material properties are compared for the range of weight percentages of fillers. This is done for the purpose of finding an ideal fill concentration. Two dies are used to study different orientation distributions: straight and divergent. Thermal and tensile properties and optical micrographs are analyzed and compared. Composites were processed on a Coperion ZDSK-28mm co-rotating, fully-intermeshing, twin-screw extruder. Polybutylene terephthalate (PBT) was used as the polymer matrix. 0 W% to 2 W% multi-walled carbon nanotubes (CNTs) and 0 W% to 30 W% carbon microfibers (CMFs) were used as fillers. Preliminary results showed a clear trend in increased tensile strength of the composite with the increase of concentration of CMFs and CNTs in the slit die up to 25 W% CMF. After 25 W% CMF, however, there was a depreciation in properties. Similarly, thermal conductivity results have shown a clear peak at 25 W% CMF with 30 W% showing a decrease in thermal properties. Preliminary results for the divergent die showed that, with addition of carbon microfibers to the polymer matrix, thermal properties of the composite increased up to 15 W%, then dropped and increased again as more CMFs were added. In addition, on average, material extruded through the divergent die showed better results of thermal conductivity than that extruded through the slit die. This indicates that when using a diverging die, fiber become oriented perpendicular in relation to the direction of the flow, thus improving heat flow in the transverse direction.
APA, Harvard, Vancouver, ISO, and other styles
We offer discounts on all premium plans for authors whose works are included in thematic literature selections. Contact us to get a unique promo code!