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국가과학기술정보센터(ScienceON) 특허검색
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1 EXPANDER / EMERSON CLIMATE TECHNOLOGIES (SUZHOU) CO., LTD.
An expander (1), comprising an expansion mechanism and a valve assembly (100, 300); the expansion mechanism comprises: an enclosed expansion chamber (EC) having a gradually increasing volume for expanding a working fluid; a discharge chamber (CC) for receiving the working fluid discharged from the expansion chamber (EC); and discharge channels (83a, 83b) for communicating the discharge chamber (CC) with a discharge space outside the expansion mechanism. The valve assembly (100, 300) is mounted to the expansion mechanism, and the valve assembly (100, 300) is configured such that: when the pressure of the working fluid in the discharge chamber (CC) is less than or equal to a predetermined expansion pressure, the valve assembly (100, 300) is in a closed state so as to prevent the working fluid in the discharge chamber (CC) from flowing to the discharge space; and when the pressure of the working fluid in the discharge chamber (CC) is greater than the predetermined expansion pressure, the valve assembly (100, 300) is in an open state so as to allow the working fluid in the discharge chamber (CC) to flow into the discharge space.
2 PROCESS FOR PRODUCING OPTICAL FILM, OPTICAL FILM AND POLARIZING PLATE / SHIBUYA, Masahiro
A process for producing an optical film, in which even when inorganic microparticles are contained, mixing of cellulose ester insoluble matter into the film can be satisfactorily prevented to thereby enable effective prolongation of filter paper exchange cycle; an optical film produced by the process; and a polarizing plate making use of the optical film. There is provided a process for producing an optical film, comprising preparing a dope containing a cellulose ester and inorganic microparticles, filtering the same and forming the dope into an optical film according to a solution casting technique, wherein the filtration is carried out with the use of filter paper (X) of 10 sec/300 cc to 15 sec/300 cc air permeability and filter paper (Y) of 5 sec/300 cc to below 10 sec/300 cc air permeability.
3 METHOD OF MANUFACTURING OPTICAL FILM, OPTICAL FILM OBTAINED BY THE METHOD AND POLARIZING PLATE USING THE OPTICAL FILM / KONICA MINOLTA OPTO INC
PROBLEM TO BE SOLVED: To provide a method of manufacturing an optical film by which contamination of a cellulose ester insoluble material in a film can be sufficiently prevented and an exchanging cycle of filter paper can be effectively prolonged and further to provide the optical film obtained by the method and a polarizing plate using the optical film.SOLUTION: Dope obtained by dissolving cellulose ester is filtered and then the optical film is manufactured by a solution flowing-out method using the dope. In the manufacturing method of the optical film, filtration is carried out by using the filter paper X having air permeability of ≥10second/300cc and ≤15second/300cc and the filter paper Y having air permeability of ≥5second/300cc and <10second/300cc.
4 ENGINE WITH MINIMUM HEAT TRANSFERRED STRUCTURE / Hyundai Motor Company
An engine with a reduced cooling loss, may include a cylinder block and a cylinder head, wherein an entire combustion chamber volume of the cylinder block and the cylinder head is 300 cc-700 cc, a compression ratio is 10.0 or more, and the volume of the cylinder head is 40%-70% of the entire combustion chamber volume.
5 농산물을 이용한 과실주 제조방법 / 박춘희
본 발명은 각종 농산물의 열매와 같은 과실들을 탁주,약주 또는 소주와 혼합시켜서 되는 과실주의 제조 방법에 관한 것으로, 농산물의 과실은 딸기즙 약 20cc에 약주 약 80cc를 혼합하여 20℃에서 12시간 숙성하는 딸기주와, 수박즙 약 40cc에 도마도 10cc와 소주 10cc에 약주 40cc를 20℃에서 약 12시간 혼합숙성한 수박주와, 삶거나 생호박을 믹서한 호박즙 40cc에 당근 10cc와 소주, 약주 40cc를 혼합 숙성시켜서되는 호박주와, 오레지즙 10cc에 소주 90cc를 혼합숙성시킨 오렌주와, 바나나 100g에 소주 100cc및 약주 300cc를 혼합숙성한 바나나주, 를 제조함에 있어 약 20℃의 온도에서 딸기즙, 수박즙, 삶은 호박즙, 오렌지즙, 바나나즙을 숙성혼합한 과실주는 약 12-15시간 숙성하고 생호박즙은 약 3일간 혼합숙성시켜 과실주를 생산하여 우리의 토속술과 농산물을 혼합숙성한 과실주를 제공하게 한 것이다.
6 바이모달 파이프 수지 및 이로부터 제조된 생성물 / 피나 테크놀러지, 인코포레이티드
본 발명은, 0.930 g/cc 내지 0.960 g/cc의 밀도 및 10 내지 25의 분자량 분포를 갖는 지글러-나타 촉매화된 바이모달 폴리에틸렌에 관한 것이며, 이로부터 생성된 제품은 1500 이상의 PENT를 갖는다. 본 발명은 또한 0.930 g/cc 내지 0.960 g/cc의 밀도 및 10 내지 25의 분자량 분포를 갖는 바이모달 폴리에틸렌을 수득하고, 상기 폴리에틸렌을 비에너지 인풋(SEI)이 300 kW.h/톤 미만인 조건 하에 가공하는 것을 포함하는 관형 제품을 제조하는 방법에 관한 것이며, 제품은 1500 이상의 PENT를 갖는다. 또한, 본 발명은 에틸렌 단량체를 중합시키는 단계; 폴리에틸렌을 회수하는 단계; 상기 폴리에틸렌을 압출시키고, 압출기에 대한 SEI를 측정하고 처리량 및/또는 기어 흡입 압력을 조절하여 SEI를 300 kW,h/톤 미만으로 조절하는 단계 및 제품을 생성시키는 단계를 포함하여 폴리에틸렌의 분해를 조절하는 방법에 관한 것이다.
7 Bimodal pipe resin and products made therefrom / Fina Technology, Inc.
Disclosed is a bimodal Ziegler-Natta catalyzed polyethylene, having a density of from 0.930 g/cc to 0.960 g/cc, and a molecular weight distribution of from 10 to 25, wherein an article formed therefrom has a PENT of at least 1500. Also disclosed is a method of preparing a tubular article including obtaining a bimodal polyethylene having a density of from 0.930 g/cc to 0.960 g/cc and a molecular weight distribution of from 10 to 25, and processing the polyethylene under conditions where a specific energy input (SEI) is less than 300 kW·h/ton, and wherein the article has a PENT of at least 1500. Further disclosed is a method for controlling the degradation of polyethylene including polymerizing ethylene monomer, recovering polyethylene, extruding the polyethylene, and controlling the degradation of polyethylene by measuring the SEI to the extruder and adjusting throughput and/or gear suction pressure keep SEI less than 300 kW·h/ton, and forming an article.
8 Bimodal pipe resin and products made therefrom / Fina Technology, Inc.
Disclosed is a bimodal Ziegler-Natta catalyzed polyethylene, having a density of from 0.930 g/cc to 0.960 g/cc, and a molecular weight distribution of from 10 to 25, wherein an article formed therefrom has a PENT of at least 1500. Also disclosed is a method of preparing a tubular article including obtaining a bimodal polyethylene having a density of from 0.930 g/cc to 0.960 g/cc and a molecular weight distribution of from 10 to 25, and processing the polyethylene under conditions where a specific energy input (SEI) is less than 300 kW·h/ton, and wherein the article has a PENT of at least 1500. Further disclosed is a method for controlling the degradation of polyethylene including polymerizing ethylene monomer, recovering polyethylene, extruding the polyethylene, and controlling the degradation of polyethylene by measuring the SEI to the extruder and adjusting throughput and/or gear suction pressure keep SEI less than 300 kW·h/ton, and forming an article.
9 Bimodal Pipe Resin and Products Made Therefrom / Fina Technology, Inc.
Disclosed is a bimodal Ziegler-Natta catalyzed polyethylene, having a density of from 0.930 g/cc to 0.960 g/cc, and a molecular weight distribution of from 10 to 25, wherein an article formed therefrom has a PENT of at least 1500. Also disclosed is a method of preparing a tubular article including obtaining a bimodal polyethylene having a density of from 0.930 g/cc to 0.960 g/cc and a molecular weight distribution of from 10 to 25, and processing the polyethylene under conditions where a specific energy input (SEI) is less than 300 kW·h/ton, and wherein the article has a PENT of at least 1500. Further disclosed is a method for controlling the degradation of polyethylene including polymerizing ethylene monomer, recovering polyethylene, extruding the polyethylene, and controlling the degradation of polyethylene by measuring the SEI to the extruder and adjusting throughput and/or gear suction pressure keep SEI less than 300 kW·h/ton, and forming an article.
10 BIMODAL PIPE RESIN AND PRODUCTS MADE THEREFROM / FINA TECHNOLOGY, INC.
Disclosed is a bimodal Ziegler-Natta catalyzed polyethylene, having a density of from 0.930 g/cc to 0.960 g/cc, and a molecular weight distribution of from 10 to 25, wherein an article formed therefrom has a PENT of at least 1500. Also disclosed is a method of preparing a tubular article including obtaining a bimodal polyethylene having a density of from 0.930 g/cc to 0.960 g/cc and a molecular weight distribution of from 10 to 25, and processing the polyethylene under conditions where a specific energy input (SEI) is less than 300 kW.h/ton, and wherein the article has a PENT of at least 1500. Further disclosed is a method for controlling the degradation of polyethylene including polymerizing ethylene monomer, recovering polyethylene, extruding the polyethylene, and controlling the degradation of polyethylene by measuring the SEI to the extruder and adjusting throughput and/or gear suction pressure keep SEI less than 300 kW.h/ton, and forming an article.

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1 300cc급 소형엔진 흡기시스템의 성능 해석
한국산학기술학회 , 2009 ; Vol. 10 , Issue 11
2 300cc급 소형엔진 흡기시스템의 성능 해석
한국산학기술학회 , 2009 ; Vol. 10 , Issue 11
3 The Technical Ramifications of Downsizing HSDI Diesel Technology to the 300 cc Displacement Class
SAE International , 1998 ; Vol. 1 , Issue 11
4 The Technical Ramifications of Downsizing HSDI Diesel Technology to the 300 cc Displacement Class
SAE International , 1998 ; Vol. 1998 , Issue 11
5 Measurement of Br(H<SUP>0</SUP> -> cc + gg)/Br(H<SUP>0</SUP> -> bb) at ? = 300 GeV
SAE International , 1996 ; Vol. 1996 , Issue 11
6 PENYUSUNAN STANDAR OPERASIONAL PROSEDUR PERAWATAN HARIAN DAN BULANAN PADA SARANA LOKOMOTIF CC 300 DI BALAI PERAWATAN PERKERETAAPIAN NGROMBO
SAE International , 2021 ; Vol. 12 , Issue 2
7 Analisis Umur Fatigue Rubber Spring pada Draft Gear Lokomotif CC300
Lembaga Penelitian dan Pengabdian kepada Masyarakat ITS , 2021 ; Vol. 10 , Issue 2
8 Reviewing the Speaker's Decision: A Brief Synopsis of UDM v Speaker of the National Assembly 2017 5 SA 300 (CC)
Academy of Science of South Africa , 2021 ; Vol. 24 , Issue 2
9 Measurement ofB(H→cc&macr;, gg)B(H→bb&macr;)ine+e&#x2212;colliders at a center-of-mass energy of 300 GeV
American Physical Society , 1996 ; Vol. 54 , Issue 5
10 Gain curves for direct-drive fast ignition at densities around 300g&#x2215;cc
American Institute of Physics , 2006 ; Vol. 13 , Issue 10

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