• Korean Chemical Engineering Research
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• 제46권2호
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• pp.414-422
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• 2008

활성탄과 제올라이트에 대한 $H_2$, $CH_4$, CO, $CO_2$에 대한 흡착평형 실험을 정적부피법에 의해 수행하였다. 활성탄과 제올라트를 이용한 4탑 PSA 공정을 통하여 다성분 혼합기체($H_2$ 72.2%, $CH_4$ 4.06%, CO 2.03%, $CO_2$ 21.6%)로부터 수소를 분리하는 연구를 수행하였다. 흡착평형 실험결과 각각의 기체들에 대하여 dual-site langmuir(DSL) 모델이 잘 예측을 하였으며, 활성탄과 제올라이트의 충전비율에 따른 파과특성을 살펴본 결과 최적의 활성탄 층의 높이는 전체 탑 길이 80 cm 중 55 cm로 나타났다. PSA 공정에서 공정 변수인 총 주기시간($T_c$), 세정기체 공급압력차(${\Delta}P$) 그리고 흡착압력이 공정효율에 미치는 영향을 실험과 전산모사를 통해 그 결과를 비교하였다.

• 폴리머
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• 제38권2호
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• pp.144-149
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• 2014

일반사출성형은 공정 중 보압단계에서 캐비티에 높은 압력이 작용하여 성형품에 큰 잔류응력이 남게 된다. 또한 캐비티 내 위치 별로 압력분포가 달라 균일한 물성의 제품을 얻는데 한계가 있다. 다수 개 빼기 일반사출성형에서는 캐비티간 충전 불균형이 일어나 캐비티간 품질의 편차를 일으킨다. 이와 같은 한계를 극복하기 위해 사출압축성형 공정을 사용하는 경우가 많다. 본 연구에서는 다수 개 캐비티를 갖는 금형을 이용하여 일반사출성형과 사출압축성형을 비교 분석하였다. 실험과 해석을 통하여 연구를 수행하였으며 투명한 수지인 PC와 PS를 이용하여 시편에 나타나는 복굴절을 관찰하여 일반사출성형과 사출압축성형에서 나타나는 성형특성을 비교하였다. 연구결과, 사출 압축성형으로 제작된 시편에서 캐비티 내의 압력이 균일하여 복굴절과 성형수축률이 낮고 균일하게 나타났다. 그리고 일반사출성형에서 나타나는 캐비티간 충전 불균형에 의한 캐비티간 물성의 편차가 사출압축성형에서는 크게 줄어들었다. 본 연구를 통하여 사출압축성형은 다수 개 빼기 사출성형에서 캐비티 내 균일한 물성확보뿐만 아니라 캐비티간 품질 불균형을 해소하는데 유용함을 확인할 수 있었다.

• 한국수산과학회지
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• 제9권3호
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• pp.215-221
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• 1976

1976년 6월 10일부터 동년 8월 30일까지 본학 해양과학 연구소 하층 실험실에서 실험하였고 1975년 6월 7일에서 동년 8월 11일까지 약 2개월 동안에 풍양호, 척양호, 관악산호 등의 선박소음을 녹음한 테프로서 재생방음한 것을 음원으로 이용하였다. 이때 소음제어의 효과를 찾기 위해 A,B,C,D형의 실험용 직육면체인 방음실을 제작하여 실험실내에 배치하고 기관실소음과 발진기에 스피커를 연결해서 방음된 음압이 각방음제어실에 투과되는 음압 100분률과 또 각 방음제어실내에서 같은 조건으로 방음되는 경우에 자재와 형상이 다른 방음실내부 구조물에 따른 흡음효과를 조사 비교한 결과를 요약하면 다음과 같다. 1. 소음투과율은 실험실 외부음압이 60dB 일때 A형은 $69.7\%$였고 계속 10dB 증가함에 따라 $3.3\%$씩 증가하였고 D형에서는 $53.9\%$인 것이 10dB 증가함에 따라 $4.5\%$씩 증가했다. 2. 실험실인 외부음압이 100dB일 때 A,B,C,D형의 음압투과율은 81.6, 78.9, 75.3, $71.0\%$의 순으로 D형의 투과율이 낮아서 방음실로서는 D형이 가장 좋았다. 3. 대화에 지장이 없는 소음압은 75dB 이하이므로 A,B형을 제외하고 C,D형은 선박소음 제어실로서 유효했다. 4. 방음제어실내부 구조에 따른 흡음효과를 A,D형에서 비교하면 A형은 발진음일 때 거리 20cm에서 82dB로 가장 높고 80cm에서 76dB로 가장 낮았으며 100cm에서 77dB였고 140cm에서 78dB 정도 다시 증가해 반사음 현상이 일어났다. D형은 발진음일 때 거리 20cm에서 A와 같이 82dB였는데 80cm에서 72.5dB, 100cm에서 73dB, 140cm서에는 67dB로 A보다 12dB가 낮았다. 선박소음도 거리 20cm에서 A형은 77.5dB, D형은 77dB였는데 140cm에서는 A형이 74dB, D형이 63dB로 11dB의 차이로 D형이 낮아 역시 흡음효과가 A형 보다 D형이 좋았고 완벽한 무향실로서 반사음의 영향은 찾아 볼 수 없었다. 5. 매우 낮은 발진음일 때 흡음관계를 1000Hz를 기준삼아 보면 거리 20cm에서 C형은 44.7dB, D형은 45.4dB로 C형이 0.3dB로 악간 낮았으나 140cm에서 C,D형 모두가 44.3dB로서 같았다. 값싼 자재로서도 C형이 가장 흡음효과가 좋았다.

• 한국대기환경학회지
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• 제26권3호
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• pp.330-338
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• 2010

In this study, removal characteristics of nitrogen oxides $(NO_x)$ from road transport by using peat as the packing media for biodegradation have been investigated in the long term. Physicochemical and biological treatment of peatmixed media eliminates any requirement to use chemical substances and also facilitates the biodegradable actions of microorganism. Safe biodegradation of pollutants, no need to apply additional microbes owing to their active growth, and no generation of secondary pollutants were found in this experiment. It was concluded that average removal efficiencies of nitric oxide (NO) and nitrogen dioxide $(NO_2)$ were 80% and 97% respectively with respect to the linear velocity 35~40 mm/s and 0.3 ppm ozone concentration in the long period operation. Inflow concentration of nitric oxide over 0.05 ppm was suitable when pretreated with ozone. Non-ozone stage was performed with linear velocity 20~100 mm/s and then the average removal efficiency of nitric oxide and nitrogen dioxide were 38% and 94% respectively. Other results showed that the apparent static pressure was raised with increases in applied water content and aerial velocity in mixed media during fan operation.

• 접착 및 계면
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• 제10권3호
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• pp.141-147
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• 2009

본 연구는 web spray 분사방식으로 핫멜트 접착제를 이용하여 high performance hybrid chemical filter (HPHCF)를 제조하였다. HPHCF은 이온교환 수지와 PP 부직포를 사용하였고, HPHCF의 제조 시 최적 조건은 핫멜트의 온도는 $170^{\circ}C$에서 분사압력은 50 psi일 때 최적의 제조 조건을 나타내었다. 제조된 HPHCF의 특성 및 암모니아 흡착성능을 측정하였다. HPHCF 이온교환용량은 수지 부착량이 증가함에 따라 증가하였으며 단일 수지와 이온교환섬유의 이온교환용량보다 크게 나타났다. 또한 암모니아의 제거율은 HPHCF의 충진 밀도가 증가할수록 증가하였으며 흡착 파과시간은 13 min으로 단일 섬유나 수지에 비해 길게 나타났고 최대 암모니아 흡착량은 98%이었다. 또한 암모니아 흡착 파과시간은 유량 및 농도가 증가함에 따라 빠르게 진행되었다.

• E2M - 전기 전자와 첨단 소재
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• 제10권5호
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• pp.440-446
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• 1997

This research has been performed for the fabrication of high quality ferrite plastic magnet. The magnetic properties of S $r_{5.9}$F $e_2$ $O_3$ ferrite bonded magnets by injection moulding with a variety of applied magnetic field were investigated. 0.3wt% CaCO3, 0.2wt% $SiO_2$, 0.5wt% $Al_2$ $O_3$and 0.5wt% N $a_2$ $SiO_3$are added in order to improve the magnetic properties of Sr-ferrite plastic magnets during the powder fabrication. For carbon coating on chemical compound specimen, 5wt% polyvinyl alcohol is added, and then calcinated under $N_2$ environment of 12$25^{\circ}C$. The particle size is distributed from 0.9~1.2${\mu}{\textrm}{m}$ which approximates to the single domain. The obtained Sr ferrite powder is well mixed with silane coupling and calcium stearate of 1wt%. Nest, the specimen is pelleted after kneading each of them with polyamidel2 as a binder. When the temperature of injection and mould were 25$0^{\circ}C$ and 8$0^{\circ}C$ respectively at injection pressure of 200kgf/$\textrm{cm}^2$, the degree of orientation was 85.3% under the applied magnetic field of 12kOe. As the results, when the packing density of Sr ferrite powder was 90wt%, the magnetic properties of Sr ferrite bonded magnet were follows : $_{B}$ $H_{c}$=2.41kOe, Br=3.1kG, (BH)$_{max}$=2.21MgOe. Especially, the Sr-ferrite bonded magnet with 10wt% N $d_2$F $e_{14}$B additive were as follows : $_{B}$ $H_{c}$=2.57kOe, Br=3.14kG and (BH)$_{max}$=2.39MGOe.GOe.GOe.GOe.e.

• Journal of the Korean Association of Oral and Maxillofacial Surgeons
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• 제35권6호
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• pp.431-436
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• 2009

There are five principal causes for excessive bleeding in the immediate postextraction phase ; (1) Vascular wall alteration (wound infection, scurvy, chemicals, allergy) (2) Disorders of platelet function (genetic defect, drug-aspirin, autoimmune disease) (3) Thrombocytopenic purpuras (radiation, leukemia), (4) Inherited disorders of coagulation (hemophilia, Christmas disease, vitamin deficiency, anticoagulation drug-heparin, coumarin). If the hemorrhage from postextraction wound is unusually aggressive, and then dehydration and airway problem are occurred, the socket must be packed with gelatine sponge(Gelfoam) that was moistened with thrombin and wound closure & pressure dressing are applied. The thrombin clots fibrinogen to produce rapid hemostasis. Gelatine sponges moistened with thrombin provide effective coagulation of hemorrhage from small veins and capillaries. But, in dental alveoli, gelatine sponges may absorb oral microorganisms and cause alveolar osteitis (infection). This is a case report of bleeding control by continuous rubber strip & iodoform gauze drainage (without gelfoam packing) of active bleeding infection sites of three teeth extraction wounds in a 46-years-old female patient with advanced liver cirrhosis.

• Maxillofacial Plastic and Reconstructive Surgery
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• 제32권6호
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• pp.592-596
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• 2010

The common local causes of active gingival bleeding are the vessel engorgement and erosion by severe inflammation and injury to hypervascularity lesion. Abnormal gingival bleeding is also associated with systemic bleeding disorders (liver disease, leukemia etc.). There are many conventional methods for gingival bleeding control, such as, direct pressure, packing, electrocoagulation, tight suture and application of hemostatic agents. If the continuous gingival bleeding is not stopped in spite of the all local application methods, the medical consultation should be obtained for systemic condition care and the major feeding arterial embolization. This is a case report of severe gingival bleeding and periodontitis control in a patient with liver cirrhosis and oral metastatic lesion of hepatocellular carcinoma. The bleeding lesion was placed in left buccal mucosa and gingiva of the left mandibular molars. The control methods were dental crown removal, primary endodontic drainage, gingival sulcus drainage and maxillary arterial embolization with medical consultation.

• Korea-Australia Rheology Journal
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• 제19권4호
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• pp.183-190
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• 2007

Injection molding is one of the most common operations in polymer processing. Good quality products are usually obtained and major post-processing treatment is not required. However, residual stresses which exist in plastic parts affect the final shape and mechanical properties after ejection. Residual stresses are caused by polymer melt flow, pressure distribution, non-uniform temperature field, and density distribution. Residual stresses are predicted in this study by numerical methods using commercially available softwares, $Hypermesh^{TM},\;Moldflow^{TM}\;and\;ABAQUS^{TM}$. Cavity filling, packing, and cooling stages are simulated to predict residual stress field right after ejection by assuming an isotropic elastic solid. Thermo-viscoelastic stress analysis is carried out to predict deformation and residual stress distribution after annealing of the part. Residual stresses are measured by the hole drilling method because the automotive part selected in this study has a complex shape. Residual stress distribution predicted by the thermal stress analysis is compared with the measurement results obtained by the hole drilling method. The molded specimen has residual stress distribution in tension, compression, and tension from the surface to the center of the part. Viscoelastic deformation of the part is predicted during annealing and the deformed geometry is compared with that measured by a three dimensional scanner. The viscoelastic stress analysis with a thermal cycle will enable us to predict long term behavior of the injection molded polymeric parts.

• Environmental Engineering Research
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• 제13권1호
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• pp.19-27
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• 2008

Simultaneous removal of ternary gases of $NH_3$, $H_2S$ and toluene in a contaminated air stream was investigated over 180 days in a biofilter. A commercially available inorganic/polymeric composite chip with a large void volume (bed porosity > 0.80) was used as a microbial support. Multiple microorganisms including Nitrosomonas and Nitrobactor for nitrogen removal, Thiobacillus thioparus (ATCC 23645) for $H_2S$ removal and Pseudomonas aeruginosa (ATCC 15692), Pseudomonas putida (ATCC 17484) and Pseudomonas putida (ATCC 23973) for toluene removal were used simultaneously. The empty bed residence time (EBRT) ranged from 60 - 120 seconds and the inlet feed concentration was $0.0325\;g/m^3-0.0651\;g/m^3$ for $NH_3$, $0.0636\;g/m^3-0.141\;g/m^3$ for $H_2S$, and $0.0918\;g/m^3-0.383\;g/m^3$ for toluene, respectively. The observed removal efficiency was 2% - 98% for $NH_3$, 2% - 100% for $H^2S$, and 2% - 80% for toluene, respectively. Maximum elimination capacity was about $2.7\;g/m^3$/hr for $NH_3$, > $6.4\;g/m^3$/hr for $H_2S$ and $4.0\;g/m^3$/hr for toluene, respectively. The inorganic/polymeric composite carrier required 40 - 80 days of wetting time for biofilm formation due to the hydrophobic nature of the carrier. Once the surface of the carrier was completely wetted, the microbial activity became stable. During the long-term operation, pressure drop was negligible because the void volume of the carrier was two times higher than the conventional packing materials.