• 한국염색가공학회지
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• 제34권1호
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• pp.27-37
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• 2022

In this study, a study and interpretation of the spinning process in copolymerized aramid spinning was conducted. In order to proceed with the spinning process modeling and analysis, the spinning process was modeled through the physical property modeling of the spinning solution and the structural modeling of the spinneret, and structural stability and flow of the spinneret for this spinning were analyzed. After modeling the spinning solution and the spinneret in a virtual space, the pack pressure and flow rate when the spinning solution was discharged were simulated. Macroscopically, the structural stability of the spinneret was confirmed at the standard pack pressure (100 kg·f/cm²), and microscopically, the flow rate and pressure drop data of the spinning solution according to the L/D(Length (L)/Diameter (D)) value were analyzed. Based on the research and development of virtual engineering modeling and analysis, we present the possibility of changing the shape and mechanical properties of copolymer aramid fibers according to the spinning process.

• 한국염색가공학회지
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• 제14권2호
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• pp.109-109
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• 2002

A study has been made of the dry-jet-wet spinning of PAN copolymer fibers using 60% aqueous zinc chloride solution as solvent and 25∼40% aqueous zinc chloride solution as non-solvent. The technological characteristics of this method were that small streams of dope were extruded from the die and allowed to pass through a short distance of air gap(about 10mm) before entering the spinning bath for full coagulation. This work showed the importances which coagulation condition, stretch ratio and fiber tenacity up to 10.5 g/d could be obtained with elongation of 11∼16%. Individual fibers were evaluated on the basis of density and mechanical properties such as tenacity and elongation etc.

• 한국염색가공학회지
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• 제14권2호
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• pp.33-39
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• 2002

A study has been made of the dry-jet-wet spinning of PAN copolymer fibers using 60% aqueous zinc chloride solution as solvent and 25∼40% aqueous zinc chloride solution as non-solvent. The technological characteristics of this method were that small streams of dope were extruded from the die and allowed to pass through a short distance of air gap(about 10mm) before entering the spinning bath for full coagulation. This work showed the importances which coagulation condition, stretch ratio and fiber tenacity up to 10.5 g/d could be obtained with elongation of 11∼16%. Individual fibers were evaluated on the basis of density and mechanical properties such as tenacity and elongation etc.

• Membrane and Water Treatment
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• 제9권1호
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• pp.43-51
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• 2018

Hollow fiber (HF) membranes are gaining wide interest over flat membranes due to their compaction and high area to surface volume ratio. This work addresses the fabrication of HF from polysulfone (PS) and polyethersulfone (PES) using N-methylpyrrolidone (NMP) as solvent in addition to other additives to achieve desired characteristics. The semi-pilot spinning system includes jacketed vessel, four spinneret block, coagulation and washing baths in addition to dryer and winder. Different parameters affecting dry-wet spinning phase inversion process were investigated. Dope compositions of PES, NMP and polyvinyl pyrrolidone (PVP) of varying molecular weights as additive were addressed. Some critical parameters of importance were also investigated. Those include dope flow rate, air gap, coagulation & washing baths and drying temperatures. The measured dope viscosity was in the range from 1.7 to 36.5 Pa.s. Air gap distance was adjusted from 20 to 45 cm and coagulation bath temperature from 20 to $46^{\circ}C$. The HF membranes were characterized by scanning electron microscope (SEM), atomic force microscope (AFM) and mechanical properties. Results indicated prevalence of finger like structure and average surface roughness from about 29 to 78.3 nm. Profile of stress strain characteristics revealed suitability of the fibers for downstream interventions for fabrication of thin film composite membrane. Different empirical correlations were formulated which enable deeper understanding of the interaction of the above mentioned variables. Data of pure water permeability (PWP) confirmed that the fabricated samples fall within the microfiltration (MF)-ultrafiltration (UF) range of membrane separation.

• 멤브레인
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• 제22권3호
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• pp.224-233
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• 2012

기체분리용 분리막의 투과성능을 향상시키기 위해 비이온성 첨가제로 Triton X-100을 사용하여 건습식 상분리법에 의하여 polysulfone 중공사 막을 제조하였으며, 첨가제에 따른 기체투과 거동의 변화를 관찰하였다. 또한 에어갭, 고분자의 농도, 도프탱크 온도와 같은 다양한 방사 조건을 조절하여 그 영향을 관찰하였다. 제조된 중공사 막은 전자주사현미경(SEM)과 bubble flow meter를 통해 각각 모폴로지와 기체투과 특성에 대한 평가를 실시하였다. SEM 분석을 통해 Triton X-100이 첨가된 막은 다양한 에어갭에서도 매끄러운 외부 스킨층을 가지는 것을 확인하였다. 중공사 막의 거대기공은 에어갭이 4에서 90 cm로 증가함에 따라 더욱 발달하며, 높은 투과도를 나타내는 것을 확인하였다. 또한 상대적으로 낮은 고분자 농도(30 wt% polysulfone)와 높은 첨가제 농도(15 wt% Triton X-100) 조건에서 높은 투과도를 나타내었다. 도프 탱크 온도를 조절하였을 때, $100^{\circ}C$에서 제조된 막은 첨가제와 용매의 휘발로 인해 낮은 투과특성을 나타냈다.

• 멤브레인
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• 제15권2호
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• pp.147-156
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• 2005

폴리이서설폰은 상용화된 엔지니어링 고분자 소재 중에서 이산화탄소/질소 및 이산화탄소/메탄의 분리 능력이 아주 우수하면서 이산화탄소에 대한 가소화에 대한 저항력이 아주 뛰어난 것으로 알려져 있다[1-4]. 본 연구에서는 연소 배가스내 이산화탄소의 분리/회수를 위하여 건-습식 상전이법에 의해 비대칭구조의 폴리이서설폰 중공사막을 제조하였다. 제막용액은 고비점이면서 폴리이서설폰의 용매인 NMP와 저 비점의 폴리이서설폰의 팽윤제인 acetone를 일정한 조성으로 함께 녹여서 제조하였다. 방사용액의 농도, NMP와 acetone의 비, 방사높이, 증발조건, 실리콘 코팅조건을 변화시키면서 중공사를 제조하였으며, 얻어진 중공사막의 이산화탄소와 질소에 대한 기체투과도와 선택도는 순수기체를 통하여 측정하였다. 최적의 PES 중공사막은 PES/Acetone/NMP = 30/35/35 $wt\%$ 방사용액과 실리콘의 코팅조건하에 제조된 것으로 폴리이서설폰 소재 자체의 고유선택도인 $30\~40$의 $CO_2/N_2$ 선택도를 보였으며 $25\~50$ GPU의 이산화탄소 투과플럭스를 보였다. 이러한 선택도와 투과도로부터 계산된 중공사 외표면의 선택층의 두께는 $0.1\;{\mu}m$였다. 제조된 폴리이서설폰중공사막이 향후 연소 배가스내 이산화탄소 분리/회수용 막분리 공정에 적용될 경우 우수한 결과를 보일 것으로 예측된다.