| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 101 | Apparatus and method for regenerating the catalyst | JP2008554215 | 2006-02-13 | JP4887379B2 | 2012-02-29 | パルマス，パオロ; ロマス，デイヴィッド・アルフレッド |
| 102 | A method and apparatus for processing a particulate material | JP2003505383 | 2002-05-28 | JP4647206B2 | 2011-03-09 | アルベルト・シェッシェ; ミヒャエル・ナグル; ヨハネス・シェンク |
| 103 | Fluidized bed device | JP2008293458 | 2008-11-17 | JP2010119912A | 2010-06-03 | RYU SHIKO; SUDA TOSHIYUKI |
| <P>PROBLEM TO BE SOLVED: To provide a fluidized bed device of a simplified structure attained by eliminating a need for installing a partition in a fluidized bed container, capable of solving problems associated with its abrasion and cost, of making the fluidizing velocity of fluidizing media in the fluidized bed container uniform, of eliminating a dead space therein, and of extending the retention time of the fluidizing media. <P>SOLUTION: The fluidized bed device 3 including a fluidized bed container 1 in which a fluidized bed 2 of fluidizing media is formed by a gas, is characterized in that the width of a feed port 4a of a feed nozzle 4 connected to the upstream end in the flow direction of the fluidizing media in the longitudinal direction of the fluidized bed container 1 is made equal to the width of the fluidized bed 2, and the width of a discharge port 5a of a discharge nozzle 5 connected to the downstream end of the flow direction of the fluidizing media in the longitudinal direction of the fluidized bed container 1 is made equal to the width of the fluidized bed 2. <P>COPYRIGHT: (C)2010,JPO&INPIT | ||||||
| 104 | Processing method of the particulate material in the fluidized bed process as well as the reaction vessel and the plant for carrying out this method | JP54125197 | 1997-05-15 | JP4316673B2 | 2009-08-19 | ヴォルネル，フェリクス; ヴェーナー ケプリンゲル，レオポルト; シェンク，ヨハネス―レオポルト; ハウゼン―ベルガー，フランツ; リー，イル―オック |
| 105 | Combined conduction/convection furnace | JP2007335342 | 2007-12-26 | JP2008151500A | 2008-07-03 | CRAFTON SCOTT P; LEWIS JAMES L JR |
| PROBLEM TO BE SOLVED: To provide a single furnace system combining and integrating a plurality of distinct heating environments. SOLUTION: The single furnace system 10 integrates a combination of two or more distinct heating environments (including a conduction heating environment 23 and a convection heating environment 24 in a preferred embodiment). As a result, the plurality of environments specify a continuous heating chamber 14 through which a moving workpiece 50 (such as a casting) is shifted from one heating environment to the other heating environment without being exposed to the atmosphere. In accordance with a preferred method, the transition of the casting from the one environment to the other environment is achieved with no meaningful change in temperature. COPYRIGHT: (C)2008,JPO&INPIT | ||||||
| 106 | Combining conduction/convection furnace | JP2005219699 | 2005-07-28 | JP2006016694A | 2006-01-19 | CRAFTON SCOTT P; LEWIS JAMES L JR |
| PROBLEM TO BE SOLVED: To provide a single furnace system which integrates, in combination, a plurality of distinct heating environments. SOLUTION: The single furnace system (10) integrates, in combination, two or more kinds of distinct heating environments (which in the preferred embodiment, include a conduction heating environment (23) and a convection heating environment (24)). In this way, the multiple environments define a continuous heating chamber (14) through which a moving-workpiece (50) ( such as a casting) transitions from one heating environment to the other without being exposed to the atmosphere. In accordance with the preferred methods, the transition of the casting from one environment to the other is accomplished with no meaningful change in the temperature. COPYRIGHT: (C)2006,JPO&NCIPI | ||||||
| 107 | Multi-layer heat treatment furnace, heat treatment apparatus, and heat treatment method | JP2000397093 | 2000-12-27 | JP2002195759A | 2002-07-10 | SAKAI TAKAYUKI |
| PROBLEM TO BE SOLVED: To provide a heat treatment apparatus wherein prior art heat treatment apparatus is improved, and it can provide required preferred mechanical properties for respective portions of a metal article, without increasing the installation cost. SOLUTION: A heat treatment apparatus is provided, which is adapted such that a multi-layer heat treatment furnace 1 is used with one layer of the multi- layer comprising a particulate structure as a fluidized bed layer 2 which is superior in heat efficiency and uniformity of a thermal distribution, and with an atmospheric layer 3 comprising a gas formed as the other layer. Each of the layers 2, 3 has different temperatures, and a part of a workpiece that is an article to be heat treated is immersed in the fluidized layer 2 at a prescribed temperature, with the other part of the workpiece exposed to the atmospheric layer 3 at a prescribed temperature for heat treatment. COPYRIGHT: (C)2002,JPO | ||||||
| 108 | Surface treatment equipment | JP16633293 | 1993-06-11 | JP3189507B2 | 2001-07-16 | 和之 中西; 英男 太刀川; 裕正 武田 |
| 109 | Method and system for manufacturing anhydrous product gypsum calcined at multiple stages | JP50931197 | 1996-08-07 | JP2001507662A | 2001-06-12 | エル． クラウド，マイケル; エス． モア，カーク |
| (57)【要約】 石膏を焼成して実質的に硫酸カルシウム硬石膏でなる石膏粉を回収する方法およびシステムであり、この方法にはコンベア（18）により石膏粉（20）を第１のケツトル（11）内に供給する工程と石膏粉を好ましくは400°F（約204℃）より低い温度まで加熱する工程とが包有され、次にこの石膏粉はオーバフロー管（26）を経て第２のケツトル（12）内に流入され500（約260℃）〜800°F（約426℃）の温度まで加熱され、更に石膏粉は別のオーバフローチューブ（27）を経て第３のケツトル（13）内に流入され少なくとも900°Ｆ（約482℃）の最終温度まで加熱されて硬石膏製品が製造される。 | ||||||
| 110 | Method of manufacturing the external circulation fluidized bed furnace | JP29057992 | 1992-10-28 | JP3135392B2 | 2001-02-13 | 敏雄 上村; 泰彦 上條; 吉信 佐藤; 稔 守田; 尚武 山田; 泰也 沖野 |
| 111 | Furnace having a fluid flow heating zone of the annular | JP50671998 | 1997-07-23 | JP2000515234A | 2000-11-14 | コスタッチ、ジャセック、アントーニ; ドッドソン、クリストファー、エドワード |
| (57)【要約】 環状の流体流加熱区域を確立することのできる種類の加熱炉が説明されている。 本加熱炉は、内部に内部ブロックが供給されているチャンバ（７ａ）と、内部ブロックとチャンバ（７ａ）の内壁との間の複数の斜めブレードによるリング（２１）と、を含んでいる。 手段（４ａ）は、流体がブレードの間を通過して斜めブレードのリングより上のチャンバ内に環状の流体流加熱区域を確立するような方法で、流体をチャンバへと送るために供給されている。 また手段（２３）は、チャンバ内の環状の流体流加熱区域が確立される領域に供給粒子材料を噴射するために供給されている。 ある装置に於いては、加熱区域が確立されるチャンバ内の領域が斜めブレードのリングより上へと高められるように、燃料をチャンバ内の斜めブレードのリングより上の領域に噴射するための手段（４９）が追加供給されている。 他の装置に於いては、内部ブロックを冷却するための手段（３３）が供給されている。 | ||||||
| 112 | Cooling method and apparatus of the hot gas | JP51176194 | 1993-11-15 | JPH08503292A | 1996-04-09 | アルパラティ，オルリ; イコネン，オシ; ヤーンティ，アルト |
| (57)【要約】 本発明は溶融炉の排出ガスを冷却する方法および装置に関する。 この方法は、炉胸（３）が垂直であり、排出ガスが炉天井の出口を通されて、炉上方の壁部を経て排出ガスからの熱回収を行わずに冷却装置へ送られるような炉構造に関する。 排出ガスは２段階で冷却され、第１段階では循環質量体による冷却器（１）で間接冷却され、次ぎに廃熱回収ボイラーで冷却される。 本発明による装置において、炉上方の垂直炉胸は質量体循環式冷却器に連結され、この冷却器は炉および（または）炉胸に並んで配置された廃熱回収ボイラーに連結される。 | ||||||
| 113 | Surface treatment device | JP16633293 | 1993-06-11 | JPH0673525A | 1994-03-15 | TACHIKAWA HIDEO; TAKEDA HIROMASA; NAKANISHI KAZUYUKI |
| PURPOSE: To provide the surface treatment device capable of preventing the solidification of fluidized bed powder which impairs the uniformity of the fluidization of powder constituting a fluidized bed. CONSTITUTION: This surface treatment device is constituted to fluidize the fluidized powder consisting of the refractory powder and metal and/or alloy powder disposed in the upper part of a gas diffusion plate 12 to form the fluidized bed 4 and to form a surface treatment layer on the surface of a material 3 to be treated in the presence of a halide under heating within this fluidized bed 4. A coarse grain bed 7 consisting of the powder of the average grain size D(m) satisfying the following relation formula is disposed between the fluidized bed 4 and gas diffusion plate 12 of this device: (1650Vμ/PG) 1/2<D<6.5d (V: flow velocity (m/s) of fluidizizing gas, μ: the vicosity coefft. (kg/m.s of the fluidizing gas, P: the average density (kg/m 3) of the powder constituting the coarse grain layer), G: gravity acceleration (9.8m/s 2), (d): the average grain size (m) of the metal and/or alloy). COPYRIGHT: (C)1994,JPO&Japio | ||||||
| 114 | Method and device for treating gas and particulate solid in fluid bed | JP25617492 | 1992-09-25 | JPH05248769A | 1993-09-24 | GUREGORII JIEI HAADEI; JIYON EMU GANSAA; IAN DEII UEBU; TEIMO HIPEENEN; KARI MIYOOHEENEN; ISUMO NOPANEN |
| PURPOSE: To apply heat to reduction of a metal ore due to exhaust gas by loading gas into a mixing chamber at specific speed or higher. CONSTITUTION: Gas and a particulate are solid loaded into a mixing chamber 14 for mixing, the gas and particulate solid being discharged from the mixing chamber 14 are sent to a cyclone 16, and the separated solid is partially circulated in the mixing chamber 14. In this case, the gas is loaded into the mixing chamber 14 at a speed of 35 m/sec or more. The density of the flow of the product of the suspension object of solid particles and the gas is adjusted to 10-200 kg/m 3 in the mixing chamber 14 and is adjusted to 2-30 kg/m 3 in a riser pipe 9 in front of the cyclone, thus applying to the reduction a metal ore due to hot reduction gas, especially hot exhaust gas from a refining reduction container. COPYRIGHT: (C)1993,JPO | ||||||
| 115 | Flash smelting furnace and operating method thereof | JP5603289 | 1989-03-10 | JPH02236234A | 1990-09-19 | IEMORI NOBUMASA; OSHIMA YASUO; KONDO YASUHIRO |
| PURPOSE: To accelerate concentrate reaction according to operating conditions by blowing a gas for reaction at the same angle from blasting nozzles disposed to face each other freely turnably near the central part of the side wall of a reaction column provided with a concentrate burner in the top part. CONSTITUTION: The melt formed by blowing raw materials for refining and the preheated gas for reaction, such as air, from the concentrate burner 2 in the peak part of the reaction column 3 to effect reaction is stored into a settler 6 provided successively in the lower part. One or more sets of the blasting nozzles 19 are disposed in the positions line symmetrical with a perpendicular line 18 running the central point 17 of the reaction column in the side wall near the central part of the side wall of the reaction column 3 in the above-mentioned flash smelting furnace. The blast axis direction of the nozzles 19 are set respectively in the above-mentioned perpendicular line 18 direction and are constructed turnable within the perpendicular plane around the mounting positions. The gas for reaction is partly blown at a prescribed rate from the above-mentioned blasting nozzles 19 at the time of refining sulfide ore, etc., in this flash smelting furnace. Further, the gas is so blasted that the blasting direction is upper than lower 45° of the horizontal plane and the blasting directions from one set of the blasting nozzles 19 are of the same angle. COPYRIGHT: (C)1990,JPO&Japio | ||||||
| 116 | JPH01501158A - | JP50689987 | 1987-10-15 | JPH01501158A | 1989-04-20 | |
| 117 | JPS6328675B2 - | JP14243778 | 1978-11-20 | JPS6328675B2 | 1988-06-09 | TOOMASU EBARETSUTO TEIRAA |
| 118 | JPS591943B2 - | JP8202875 | 1975-07-04 | JPS591943B2 | 1984-01-14 | KURISUTOFU HAINTSUE |
| 119 | Preparation of silicon carbide | JP9679182 | 1982-06-04 | JPS58213698A | 1983-12-12 | TANAKA MINORU; KAWABE TADASHI; OFUNE MASABUMI |
| PURPOSE: To prepare SiC whiskers of high purity, by introducing a raw material containing Si and C into a trays, and moving the trays to higher temperature region one after another in an atmosphere of a nonoxidizable gas other than N. CONSTITUTION: A boron compound or lathanum compound which is a crystal growth promoter is added to a raw material 8 containing C and Si e.g. carbonized chaff, together with voids, and the resultant mixture is then introduced into trays 7 having many pores 6 to such an extent as not to leak the raw material 8. The trays 7 are then introduced into a preparation furnace, and moved on many small chambers 3 packed with carbon pellets 5 one after another to a higher temperature zone in the small chambers 3 heated by resistance heating elements 10 while blowing a nonoxidizable gas, e.g. Ar, other than N from gas blowing ports 4 thereinto. The trays 7 are finally heated at 1,350W 1,450°C to form SiC whiskers in the voids of the raw material 8. The resultant whiskers are then treated in the wet state to separate and collect the aimed SiC whiskers. COPYRIGHT: (C)1983,JPO&Japio | ||||||
| 120 | Chlorination furnace and its operation | JP5845181 | 1981-04-20 | JPS57175701A | 1982-10-28 | ISHIZUKA HIROSHI |
| PURPOSE: To increase the production capacity per unit volume of a chlorination furnace, by encasing the reaction zone with a metallic case having double-walled structure, filling the space between walls with a gas, and carrying out the chlorination reaction under pressure. CONSTITUTION: The furnace 1 containing the reaction zone is encased with a double-walled metallic case 2. The space between the walls is devided with the partition wall 3 into the upper and the lower chambers furnished with the gas- introducing ports 4, 5 and the discharge ports 6, 7. The raw materials, e.g. rutile and coke, are charged into the furnace through the charging means 12, and the furnace is heated by burning the coke with air blasted through the bottom of the furnace. The jacket is also fed with dehydrated not air through the gas- introducing ports 4, 5. When the fluidized bed is stabilized, the gas introduced into the furnace through the bottom is changed to Cl and O 2, and the chlorination reaction is carried out by raising the furnace pressure to about 1kg/cm 2 while keeping the pressure difference between the furnace and the jacket to about +0.5kg/cm 2. COPYRIGHT: (C)1982,JPO&Japio | ||||||
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