子分类：
| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 81 | 電子デバイスを乾燥させるための方法及び装置 | JP2014555734 | 2013-02-01 | JP2015505606A | 2015-02-23 | ゼレンスキー，ルーベン，クインシー; トラスティ，ジョエル，クリストファー |
| 【解決手段】電子デバイスを乾燥させるための方法及び装置が開示される。実施形態は、電子デバイスを加熱し、かつ電子デバイス内の圧力を下げる方法及び装置を含む。幾つかの実施形態は、圧力を上げ下げしながら、熱を加える。他の実施形態は、電子デバイスから排気されるエアから、エアが排気ポンプに達する前に水分を除去するデシケータを備える。さらなる実施形態は、低圧チャンバの湿度を検出し、湿度に基づいて圧力を上げる及び/又は下げる時点を決定する。またさらなる実施形態は、検出された湿度に基づいて、適切な機能を回復させる程十分にデバイスが乾燥していると判定し、幾つかの実施形態では、圧力が上げ下げされている間の湿度の変化に基づいて判定される。またさらなる代替的な実施形態は、電子デバイスの乾燥おける一部又は全ての局面を、自動的に制御する。追加の実施形態は、電子デバイスの殺菌をする。【選択図】図5 | ||||||
| 82 | Supercritical drying method and supercritical drying apparatus | JP2010058281 | 2010-03-15 | JP5426439B2 | 2014-02-26 | 由貴子 北島; 寿史 大口; 寛 冨田; 秀和 林; 辰彦 小出 |
| 83 | Apparatus and method for thermally processing a sheet material which is continuously transported | JP2012546368 | 2009-12-30 | JP2013516590A | 2013-05-13 | フリッカー，ポール; ノイマイヤー，トーマス; メルクル，アンドレアス; ベークマン，トーマス |
| 本発明は、少なくとも１つの処理モジュール（１０）を含む、熱処理を行うための装置に関する。 少なくとも１つの処理モジュール（１０）は、第１および第２の加熱部（１１ａ，１１ｂ）を有する。 熱空気（Ｌ）が加熱部（１１ａ，１１ｂ）へライン接続部（１３）を介して導入される。 処理の後、この熱空気（Ｌ）は吸引手段（１４）を介して排出される。 吸引手段は、加熱部（１１ａ，１１ｂ）の端面に配される。 | ||||||
| 84 | Disc drying equipment and disk drying method | JP2009146118 | 2009-06-19 | JP5011351B2 | 2012-08-29 | ラットレイ ブライアン; 誠 丸山 |
| 85 | Enhanced heat transfer system | JP54754298 | 1998-05-06 | JP2001524149A | 2001-11-27 | コノシェ，デビッド，スチュワート; デービス，マーク，ハワード; ハウィズン，キャサリーン，フィオナ |
| (57)【要約】 処理容器（８０）内の固体材料（９３）を加熱または冷却するための方法および装置が開示されている。 この方法は、固体材料の充填層（９３）を保持する容器に対する作用流体の供給を含む。 この方法は、作用流体の流れを反転させることによって、熱交換流体と固体材料の間の熱伝導を強化することを特徴とする。 | ||||||
| 86 | Drying method | JP50331089 | 1989-02-27 | JP2747072B2 | 1998-05-06 | FURONHAISAA DENISU AARU; HEIWAADO JATSUKU; RIIFURAA JERARUDO JII; SHURAA JEEMUSU AARU |
| 87 | Device for continuous filtration and drying of solid supension | JP28239694 | 1994-10-24 | JPH07185221A | 1995-07-25 | DEIITORIHI GEERUMAN; NORUBERUTO SHIYUBAIKURAA |
| PURPOSE: To treat a thermally unstable material without deteriorating the quality by filtering a solid suspension with a belt filter in resting state and moving the deposited cake to put forward to a dryer to dry by convection and contact heating. CONSTITUTION: This solid suspension flows down on a gas permeable belt filter 1 in resting state to form a filtration cake 7. When becoming a 50 mm, preferably ≤20 mm thick layer, the filtration cake is moved by a porous conveyer belt 3 to be introduced into the belt dryer 2. A heating device in the belt dryer 2 has a hot gas chamber 8 for generating a hot gas flowing downwardly through the solid bed and on the other hand, contact heating elements 10, 15 above and/or below the conveyer belt 3. The filter cake 7 is dried by convection and contact heating. COPYRIGHT: (C)1995,JPO | ||||||
| 88 | Method and device for drying powder and granular material | JP19385292 | 1992-07-21 | JPH0634271A | 1994-02-08 | HASHIMOTO IORI; NUMATA MOTOMIKI; NISHIZAWA ATSUSHI; KAMATA TOMIYUKI |
| PURPOSE:To develop a method for controlling the temperature distribution inside a drier, which is for achieving a desirable value with respect to the quality of a processed powder material such as carbon black, and obtain a method and device for the drying which enable operating the drier with the temperature distribution therein in a stabilized state over a long time. CONSTITUTION:Into a granulator 3 carbon black is fed through an entry 1 and water, through an entry 2; the granulated carbon black is fed by a line 4 into a cylindrical rotary drier 5 for the drying; the processed carbon black is discharged by a line 6. On the basis of the temperatures inside the drier 5 measured by a plurality of thermometers 10 a combustion controller 13 performs operation to calculate the time of change of the processing of the powder and granular material from the constant-rate drying to the decreasing-rate drying; with the time of change and the temperature of the powder and granular material at the outlet of the drier as controlled variables the flowrates of fuel fed by lines 7, 8 respectively to burners 9 for the 1 upstream half of the drier 5 and those for its downstream half are controlled to regulate the amounts of heat so that the drier 5 can be operated with the temperature distribution with respect to the powder and granular material therein in a stabilized state over a long time. | ||||||
| 89 | JPH05504505A - | JP50451690 | 1990-03-01 | JPH05504505A | 1993-07-15 | |
| 90 | Material drying method for trunk shaped drying apparatus not discharging harmful material | JP11358291 | 1991-05-18 | JPH04227463A | 1992-08-17 | BERUNAA KUNTSU; ARUMIN FUONPURON |
| PURPOSE: To prevent odor and dust from being produced, by removing vaporized water from a drying/circulating passage, condensing and removing water vapor, and supplying non-condensable gas into a combustion chamber at specific temperature. CONSTITUTION: A dehydrated sludge 2 is supplied to a biaxial mixer 3, and a dried material 5 is supplied from a silo 6, and further a fluidized mixture 8 is dried with a drum-type drying apparatus 11 and is separated with a cyclon 12. Grains are fed to a vibrating sieve 17, and some of the grains passing through cooling silos 18, 19 is fed to a storage apparatus, etc., and part thereof is recycled. Gas from a processing/conveying apparatus and a grain cooling apparatus is heated to 750°C or higher in a combustion chamber 24 using a fossil fuel, and heat is applied to a vapor/air mixture in a drying/circulating passage, whereby an article to be processed in the drum type drying apparatus 11 is dried. The vapor/air mixture separate in the cyclon 12 is supplied to a condenser 26, and air from the silo and a moving apparatus is supplied to the combustion chamber 24 together with the air from the drying/circulating passage. COPYRIGHT: (C)1992,JPO | ||||||
| 91 | JPH0447235B2 - | JP50211482 | 1982-07-16 | JPH0447235B2 | 1992-08-03 | KUERU JATSUKU |
| 92 | Drying method and apparatus using hot pure water | JP33259590 | 1990-11-29 | JPH04197479A | 1992-07-17 | YOSHIKAWA HARUO |
| PURPOSE: To drain and dry a work by a method wherein pure water whose dissolved air is reduced up to the saturated air quantity or less at set temp. is sent to a heater to obtain hot pure water with the set temp. by the heater and this hot pure water is supplied to a hot pure water tank to dip the work wetted with water in the hot pure water and the heated work is drawn up. CONSTITUTION: Pure water from which impurities are removed is sent to a degassing apparatus 5 from a pure water source 4 to remove the dissolved air in pure water and the degassed pure water is heated by a heater 7 to obtain hot pure water with predetermined temp. and this hot pure water is quantitatively and continuously supplied to a hot pure water tank 1 from a supply port 1a while the hot pure water overflowing from the tank 1 flows in a recovery trough 50 to be discharged through a recovery pipe 51. At this time, since the pure water is heated by the heater 7 after the dissolved air in the pure water is removed up to saturated air quantity or less by the degassing apparatus 5, the generation of air bubbles accompanied by heating is eliminated and, therefore, the disturbance of the surface of water due to the appearance of air bubbles on the surface of the water is eliminated. The heat efficiency of the heater 7 is enhanced by the removal of dissolved air and the temp. rise at the time of heating becomes fast and, in holding hot pure water to constant temp., the surface temp. of the heater 7 can be lowered. COPYRIGHT: (C)1992,JPO&Japio | ||||||
| 93 | Drying of belt-like object | JP28140888 | 1988-11-09 | JPH02131174A | 1990-05-18 | OGAWA MASAHARU; HAMANAKA TATSUYA |
| PURPOSE: To make possible efficient drying of a belt-like object at high speed and without large space by combining hot air drying with heating roll drying in the continuous drying process of a belt-like object with applied coating liquid containing an organic solvent. CONSTITUTION: A belt-like object 1 which is fed out of a material roll 2 and is coated with a coating liquid 6 using an application roller 5 is sent to a hot air dryer 8. Then the object is subjected to a hot air adjusted to the temperature level of about 50 to 150°C at a velocity of about 3 to 30m/s. A solvent contained in the coating liquid evaporates gradually in the hot air dryer 8 and the strap- like object 1 reaches a 'set to touch' state at the outlet. The strap-like object 1 in this state is sent to a heating roll dryer 9 for evaporation of a residual solvent and complete drying. After this, the belt-like object is taken up by a winding roll 3. Consequently, the drying capability is significantly increased and the drying process is shortened to utilize the space effectively and increase an application speed. In addition, the quality difference due to a difference in the thickness of the belt-like object can be minimized because the thermal conductivity of the heating roll is significantly high. COPYRIGHT: (C)1990,JPO&Japio | ||||||
| 94 | JPS6148922B2 - | JP50065380 | 1980-12-31 | JPS6148922B2 | 1986-10-27 | SUPEIDOMAN RICHAADO JOOJI |
| 95 | Conduction heat receiving type agitating drier | JP5305382 | 1982-03-30 | JPS58168880A | 1983-10-05 | KIRIE RIYOUZOU; TAKAHASHI KANICHI; MIZUTA KOUJI; OOHASHI KOUJI; HIZUKA KAZUHIKO |
| 96 | Method of heat treating many coal flows simultaneously | JP9001382 | 1982-05-28 | JPS57200495A | 1982-12-08 | YANFURIITO GATSUPU; GOTSUTOHARUTO TSUIIGAN |
| 97 | Method of and apparatus for drying material containing solvent by removing solvent | JP18056480 | 1980-12-22 | JPS5760167A | 1982-04-10 | ROJIYAA JIEE HANSOTSUTO |
| 98 | Device for drying and granulating wet* soluble and*or pasty material | JP3600880 | 1980-03-21 | JPS55167037A | 1980-12-26 | ISUTOPAN TAKAKUSU; PEETAA RUDORUFU; BERA SUZABO; GIYORUGII KEREI |
| 99 | JPS4997952A - | JP433974 | 1973-12-26 | JPS4997952A | 1974-09-17 | |
| 100 | JPS4872302A - | JP94972 | 1971-12-29 | JPS4872302A | 1973-09-29 | |
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