• Proceedings of the Korean Society of Machine Tool Engineers Conference
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• 2001.10a
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• pp.292-297
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• 2001

Twin screw extruders are the heart of the polymer processing industry. They are used at some stage in nearly all polymer processing operations. This paper is concerned with the basic elements of the extruder design. The proper design of the geometry of the extruder screw is of crucial importance to the proper functioning of the extruder. If the material transport instabilities occur as a result of improper screw geometry, even the most sophisticated computerized control system cannot solve the problem. For this purpose, a characteristic design on flights shape of the extruder screw. This paper presents cross section designs of a closely intermeshing twin screw extruder with double-flighted screw elements, and channel depth characteristics for a double flighted corotating self-wiping twin screw extruder.

• Journal of the Korean Society for Precision Engineering
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• v.20 no.7
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• pp.217-226
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• 2003

Twin screw extruders are the heart of the polymer processing industry. They are used at some stage in nearly all polymer processing operations. This paper is concerned with the basic elements of the extruder design. The proper design of the geometry of the extruder screw is of crucial importance to the proper functioning of the extruder. If the material transport instabilities occur as a result of improper screw geometry, even the most sophisticated computerized control system cannot solve the problem. For this purpose, a characteristic design on the screw flights shape of the closely intermeshing co-rotating twin screw extruder. This paper presents design parameters of double flighted screw and triple flighted screw elements, and characteristics of various screw channel area versus screw diameter ratio, K value, in the barrel of screw extruder.

• Tribology and Lubricants
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• v.25 no.3
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• pp.182-186
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• 2009

Extruders can be basically divided into bisk and screw type of extruders. Though plastic extruders are often used for its simplicity for water and oil transportation pumps, these days screw extruders are mostly used. Screws are used in many extrusion processes to manufacture complex and complicated shaped parts made of plastics, medicine materials, food, polymer composites, iron and ceramic powders, etc. Also, material correction of deformities is caused by flow and physicochemical reaction phenomenonand material extrusion is processed according to heat transfer. various material comes to hopper because extruder has function by blender and mixing of materials can go well before come out through dice. These change process is so complicated that process condition is decided by trial and error that process condition is underground mainly at extrusion molding process.

• The Korean Journal of Rheology
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• v.10 no.3
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• pp.152-159
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• 1998

폴리카보네이트와 스티렌-아크릴로니트릴 공중합체의 블렌드를 이축 압출기에서 용 융혼련할 경우의 분산혼련 작용기구를 연구하였다. 분산상 형성에 관계되는 지배적인 과정 은 sheet, lace 및 ligament 생성에 이어 Rayleigh 형태의 불안정성에 기인한 구형의 분산상 (droplet) 형성으로 확인되었다. 분산상과 연속상의 점도비와 분산상의 크기에 대한 상관관 계의 조사에서는 주어진 점도비의 범위에서 점도비 약 70인 경우를 제외하고는 거의 무관한 관계를 나타내었으며 이는 이축 압출기의 강력한 혼련요소인 kneading 부위에서 주어지는 연신 흐름장에 의한 영향을 반영한 것으로 해석되었다. 분산상의 최종크기는 오히려 분산상 들간의 coales-cence 정도에 크게 영향을 받았으며 연속상의 점도가 상대적으로 낮은 경우 에 동일한 분산상에 대한 coalescence 정도가 심화되어 분산상의 크기가 증가되었다.

• Bulletin of Food Technology
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• v.4 no.4
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• pp.35-40
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• 1991

• Rubber Technology
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• v.7 no.1
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• pp.1-7
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• 2006

• Rubber Technology
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• v.7 no.2
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• pp.71-81
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• 2006

• Proceedings of the Korean Vacuum Society Conference
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• 2016.02a
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• pp.118.1-118.1
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• 2016

포항가속기연구소 PLS-II 저장링에 설치 운용을 위한 타원편광 언듈레이터(EPU114)용 초고진공 진공 챔버는 전체를 기계가공 후 용접하여 제작하는 기존의 방식을 바꾸어 알루미늄 압출 공법을 적용한 진공 챔버의 개발과 본제품 제작을 완료하였다. 압출 공법을 이용한 초고진공용 진공 챔버 제작은 기계가공 및 용접비용의 절감과 동일 형상의 진공 챔버를 상대적으로 쉽게 대량 생산을 할 수 있는 장점이 있다. 알루미늄 압출형 초고진공 진공 챔버의 기계, 진공 특성을 달성하기 위하여 정밀금형 제작기술, 특수압출기술, 표면처리기술 등이 필수적이다. 본 발표에서는 초고진공 진공 챔버 개발을 위하여 적용된 압출 공법의 소개와 함께 압출 공법이 적용된 타원편광 언듈레이터(EPU114)진공 챔버의 제작, 초고진공 진공달성, 설치 등의 과정을 내용으로 한다.

• Korean Journal of Food Science and Technology
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• v.31 no.4
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• pp.1011-1016
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• 1999

This study was performed to search a physical method having high yield and quality and minimum environmental pollution for extraction of pectin from apple pomace. Based on the physical solubilization of plant cell wall under the condition of high temperature, pressure and shearing stress, apple pomace was treated by a corotating intermeshing type twin-screw extruder with the diameter-to-length ratio of 1/20. The specific mechanical energy of extruder was introduced as system parameter for extrusion process modeling and the shaft speed, feed rate and moisture content as process variables. The yield, average molecular weight and galacturonic acid content of water-soluble polysaccharides obtained by extrusion were, respectively, modeled with the linear functions of the system parameter which was of the form as a linear function of process variables. The specific mechanical energy increased with increase of shaft speed and with decrease of feed rate and moisture content. Out of process variables, moisture content had the greatest effect on specific mechanical energy. The yield increased with increase of specific mechanical energy while the average molecular weight and galacturonic acid content increased with its decrease. In aspects of yield and quality of pectin, the results from this study showed the possibility to replace a traditional acidic method with the extrusion treatment of this study.

• Applied Chemistry for Engineering
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• v.25 no.1
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• pp.90-95
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• 2014

Nylon66 extrudates as a function of the extrusion number were prepared by a twin screw extruder. Chemical structures, thermal properties, melt index, crystal structures, mechanical properties such as the tensile strength, elongation at break and impact strength, and rheological property were measured by FT-IR, $^1H$-NMR, melt indexer, DSC, TGA, XRD, universal tensile tester, Izod impact tester, and rheometer. FT-IR and $^1H$-NMR characterizations indicated that the number of extrusions did not affect the chemical structure. The decrease in the molecular weight was checked by the melt index of extrudates. There were no effects of the thermal history on the melting and degradation temperature. The tensile and impact strength and modulus were found to be similar, regardless of the number of extrusions, but the elongation decreased significantly. The complex viscosity of extrudates at low frequencies decreased with the extrusion number. No structural changes after extrusion were confirmed from the fact that there was no change in the slope and shape of G'-G" plot.