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1. 发明专利

JP5318803B2 Method and apparatus for producing nitride crystal 有权
公开(公告)号：JP5318803B2
公开(公告)日：2013-10-16
申请号：JP2010055705
申请日：2010-03-12
申请人：日本碍子株式会社
发明人：均酒井 , 克宏今井 , 真岩井
IPC分类号： C30B29/38 , C30B19/04 , C30B19/06 , H01L21/208
摘要： PROBLEM TO BE SOLVED: To enhance the growth rate of a crystal and to grow a high quality large crystal in a short period of time when the crystal is grown in a melt containing a flux and a raw material. SOLUTION: In a method for growing a nitride crystal, a growing container 2 for accommodating a melt 27 and growing the nitride crystal 14 by holding the melt in a supersaturated state; a first nitrogen dissolution container 1 for dissolving nitrogen into a melt 6 by heating the melt 6 and holding the resulting melt in an unsaturated state; a second nitrogen dissolution container 3 for dissolving nitrogen into a melt 28 by heating the melt 28 and holding the resulting melt in an unsaturated state; a first connection section 4 which connects the growing container 2 and the first nitrogen dissolution container 1 and communicates the melt in the growing container 2 to the melt in the first nitrogen dissolution container 1; and a second connection section 5 which connects the growing container 2 and the second nitrogen dissolution container 3 and communicates the melt in the growing container 2 to the melt in the second nitrogen dissolution container 3 are used. The growing container, the first nitrogen dissolution container, the second nitrogen dissolution container, the first connection section, and the second connection section are put in motion during growth of the crystal. COPYRIGHT: (C)2011,JPO&INPIT

2. 发明专利

JP4367694B2 Selectively permeable membrane reactor 有权
公开(公告)号：JP4367694B2
公开(公告)日：2009-11-18
申请号：JP2003207486
申请日：2003-08-13
申请人：日本碍子株式会社
发明人：伸彦森 , 修酒井 , 均酒井 , 章高橋
IPC分类号： B01D53/22 , B01J8/02 , C01B3/26 , C01B3/38

3. 发明专利

JP4860851B2 Zeolite laminated composite and zeolite membrane reactor using the same 有权
公开(公告)号：JP4860851B2
公开(公告)日：2012-01-25
申请号：JP2001285740
申请日：2001-09-19
申请人：日本碍子株式会社
发明人：俊弘富田 , 伸彦森 , 均酒井
IPC分类号： B01D69/12 , B01D53/22 , B01D65/10 , B01D71/02 , B01J19/24 , B01J20/28 , B01J29/06 , B01J29/18 , B01J29/40 , B01J29/65 , B01J29/70 , B01J35/06 , C01B39/02 , C01B39/36
CPC分类号： B01J19/2475 , B01D53/228 , B01D67/0051 , B01D71/028 , B01D2325/10 , B01J29/06 , B01J29/18 , B01J29/40 , B01J29/65 , B01J29/7007 , B01J35/065 , B01J2229/62

4. 发明专利

JP4519225B2 Fuel cell system and a method of controlling the same 有权
标题翻译：空值
公开(公告)号：JP4519225B2
公开(公告)日：2010-08-04
申请号：JP29682399
申请日：1999-10-19
申请人：日本碍子株式会社
发明人：均酒井 , 知典高橋
IPC分类号： B01D53/22 , H01M8/04 , B01D63/06 , B01D71/02 , H01M8/06
CPC分类号： Y02E60/50

5. 发明专利

JP4494685B2 Zeolite laminated composite and a method of manufacturing the same 有权
公开(公告)号：JP4494685B2
公开(公告)日：2010-06-30
申请号：JP2001281675
申请日：2001-09-17
申请人：日本碍子株式会社
发明人：俊弘富田 , 伸彦森 , 均酒井
IPC分类号： B01D71/02 , B01D53/22 , B01D65/10 , B01D69/10 , B01D69/12 , B01J37/02 , C01B39/02 , C01B39/36 , C07C7/144
CPC分类号： B01D67/0048 , B01D53/228 , B01D71/028 , B01D2323/12 , C07C7/144 , Y02P20/52 , Y10T428/24942 , Y10T428/249953 , Y10T428/249967 , Y10T428/249969 , C07C11/06

6. 发明专利

JP4006107B2 Of high purity co manufacturing method and apparatus 有权
公开(公告)号：JP4006107B2
公开(公告)日：2007-11-14
申请号：JP24731898
申请日：1998-09-01
申请人：日本碍子株式会社
发明人：孝行川江 , 啓司石井 , 均酒井 , 知典高橋 , 昭久高部
IPC分类号： B01D53/22 , B01D71/02 , C01B32/40
摘要： PROBLEM TO BE SOLVED: To provide a method and apparatus for preparing CO with a high purity by which only H2 can be perfectly separated from a mixed gas such as a synthetic gas contg. H2 and CO as main ingredients and CO with a high purity of at least 99 vol.% can be obtd. without recycling process. SOLUTION: The method for preparing CO by separating and purifying CO by using a gas separating membrane from a mixed gas contg. H2 and CO as main ingredients is provided and as the gas separating membrane, a metal membrane with H2 selective permeability is used. The apparatus for preparing CO is provided with a container 2 into which the mixed gas is introduced, a sweep gas flow path 4 which is disposed on the inside of the container 2 and is formed so as to be separated from the mixed gas in the container 2 with a metal membrane 1 with H2 selective permeability and makes an O2-contg. gas flow so as to make it to be a counter flow to the flow of the mixed gas on the permeation side of the metal membrane 1, an inlet part 6 for feeding the mixed gas into the container 2 and an outlet part 8 for taking out CO gas separated and purified from the mixed gas from the container.

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