子分类：
- B01D2009/0086： .方法或其所用设备
- B01D9/0004： .{通过热交换冷却(通过蒸发混合物组分进行分离入B01D9/0013;制冷机入F25B)}
- B01D9/0018： .{通过蒸发混合物组分进行分离}
- B01D9/0036： .{在结晶床上结晶;晶种}
- B01D9/004： .{分布结晶;分馏塔或精馏塔}
- B01D9/005： .{辅助条件的选择,例如,控制结晶成核,晶体生长,壳的稳固;及其排列的介绍}
- B01D9/0059： .{结晶装置的总布置图,例如,流程图}
- B01D9/0063： .{控制或调节(控制本身入G05)}
- B01D9/0068： .{预防结晶}
- B01D9/0072： .{在微流体装置中结晶}
- B01D9/0077： .{结晶条件或晶形的筛选}
- B01D9/0081： .{使用振荡;例如,超声}
- B01D9/02： .从溶液{未使用}
| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 141 | Solid - liquid separation method | JP2006526891 | 2004-08-04 | JP2007505735A | 2007-03-15 | ウィルサック，リチャード・エイ; コムストック，ディーン・ビー; ステファンスキ，ロナルド; ハフ，ジョージ・エイ; ロバーツ，スコット・エイ |
| フィルターによって分離されている高濃度ゾーン及び低濃度ゾーンによって画定された濾過ゾーン内で液体から固体を分離する方法。 本方法は、液体及び固体を含むスラリー供給物を高濃度ゾーンに送る工程、置換流体を高濃度ゾーンに送る工程、液体の少なくとも一部をフィルターを通して濾液ゾーンに送り、濾液を生じさせる工程を含む。 | ||||||
| 142 | Imaging of automated protein crystallisation | JP2003584270 | 2003-04-10 | JP2005520174A | 2005-07-07 | リリング デイブ; グリーンウエイ ブライアン |
| 多くの結晶化プレートに含まれる結晶化実験の画像を自動的に取得、分析及び蓄積する装置である。 本装置は、複数の種類の蛋白質結晶化プレートを収容可能なプレートネストと、対物レンズと結晶化ウェルの画像に焦点を合わる画像取得装置とを含む画像取得光学系と、明領域照射装置と暗領域照射装置を含む光源と、ウェルの内容物の画像化をする前記対物レンズを様々な選択したウェルに対して位置合わせをするために画像取得光学系に対してプレートネストの位置を移動させるネスト位置決めコントローラとを含む。 データベースは、個々の結晶化プレートに関連付けられた実験情報で、固有の識別コードによってデータベース内で個々の結晶化プレートが識別される特定の結晶形成パラメータ値の識別を含む実験情報を蓄積する。 結晶化画像化コントローラは、本装置に挿入された個々の結晶化プレートの情報を検索し、検索された実験情報に基づいてネスト位置決めコントローラと画像取得光学系を制御することにより結晶化画像化を制御する。 本装置は、異なる光源及び偏光条件を用いる個々の結晶サイトの複数画像を取得し、拡大された融合画像を形成するために個々の結晶サイトの複数画像を処理する。 | ||||||
| 143 | Processes and process container with integrated evaporator of evaporation | JP2003576101 | 2003-03-10 | JP2005519750A | 2005-07-07 | アレクザニアン，アラ．ジェイ．; エンゲダール，ジョニイ; カールソン，アーニ; クラウクジイック，マーク，エイ．; ダール，アイバー，エム． |
| 供給原料液体を蒸発させるためのプロセス、及び、液体供給原料を蒸発させるための蒸発ゾーン（18）及びその結果生じた蒸気を処理するための処理ゾーン（26）の両方を含んでいるプロセス容器（10）は、蒸発表面部（82）を用いて液体小滴の形成を防ぐ。 上記装置は、蒸発ゾーン（18）内にあるオリフィス（66）を有する注入器（48）、蒸発ゾーン（18）内に配置されていて供給原料を蒸発させて蒸気を発生させるための少なくとも１つの蒸発表面部（82）、蒸気を処理するための処理ゾーン（26）、及びプロセス容器の少なくとも一部に連結される少なくとも１つの加熱器（20）で構成され、注入器オリフィス及び蒸発表面部（82）は、オリフィス（66）での滴形成を防ぐために配置されることを特徴とする。 | ||||||
| 144 | Protein crystallization condition-screening device | JP2003124085 | 2003-04-28 | JP2004194647A | 2004-07-15 | MOGI ITSURO; MATSUZAKI HIROFUMI; KITAHARA HIDEYOSHI; TSUKAMOTO MITSUHAYA; SHIMOKAWA KOJI; MAGOORI MASAKI; HIGUCHI AKIRA |
| PROBLEM TO BE SOLVED: To provide a protein crystallization condition-screening device capable of performing the protein crystallization condition screening efficiently a vapor diffusion method by using a sitting drop method. SOLUTION: This protein crystallization condition-screening device capable of performing the protein crystallization condition screening by using the sitting drop method which is a kind of the protein crystallization by using the vapor diffusion method is constituted by joining a crystallization plate-forming device 2 equipped with a separate injection means for separately injecting a protein solution and a crystallization solution into wells of the crystallization plate and a seal-pasting part for tightly closing the injected wells, with a protein crystal-detecting device 5 for detecting the protein crystals in a thermostat chamber for housing the crystallization plate after the injections in a prescribed environment and performing the crystallization plate conveyance automatically to perform the screening automatically in a good efficiency. COPYRIGHT: (C)2004,JPO&NCIPI | ||||||
| 145 | Method for purifying cyclic ester | JP2000096713 | 2000-03-31 | JP2001278877A | 2001-10-10 | EJIRI TETSUO; YAMANE KAZUYUKI; OTAWARA KENTARO |
| PROBLEM TO BE SOLVED: To provide a method by which a cyclic ester can simply, efficiently and continuously be purified. SOLUTION: A crude cyclic ester as a raw material crystal is charged into a charging port 3 for the raw material crystal provided in the lower part of a cyclindrical purifying column 1 extending in the vertical direction and stirred while making the raw material ascend with a stirring device 2 arranged in the purifying column 1 and the raw material crystal is purified by countercurrent contact of a descending molten liquid of a purified crystal component with the ascending raw material crystal in the purifying column 1 to take out the crystal after the purification as a product from a takeout port 4 installed in the upper part of the purifying column 1 in the method for purifying the crystal of the cyclic ester. COPYRIGHT: (C)2001,JPO | ||||||
| 146 | Dry fractionation of oil and fat | JP24060297 | 1997-09-05 | JPH1180776A | 1999-03-26 | YONEDA MAKOTO; HIGUCHI KIYOYUKI; TANIGUCHI ATSUSHI; KUWABARA YUJI |
| PROBLEM TO BE SOLVED: To make possible to largely save labors and obtain oils and fats stabilized in qualities, because a filter press process can be adopted without sacrificing the yields of high melting point fractions by preliminarily cooling oils and fats and subsequently pouring the oils and the fats into crystallizing trays by a specific method. SOLUTION: Oils and fats as raw materials to be crystallized in a stationary state are preliminarily cooled preferably at a lower temperature by 1 deg.C or larger than a stationary crystallization temperature (the temperature of a cooling medium), divided into small divisions in a large vessel, poured into many crystallization trays disposed in parallel to each other, crystallized in a stationary crystallization state and finally subjected to a solid-liquid separation treatment. Concretely, for example, a large volume vessel 1 in which a plurality of small communicating chambers vertically divided with division plates in a constant height from the bottom and having openings enabling the pouring of the oils and the fats at the upper ends of the chambers are disposed is used. The oils and the fats as the raw materials are introduced into the large volume vessel 1 from an opening 3 for supplying the liquid to be poured. The small chambers are uniformly filled with the oils and fats to divide the oils and the fats into the small portions. Subsequently, the oils and the fats are simultaneously poured into parallel crystallization trays through oil-pouring pipes 5 connected to the bottom portions of the small chambers. | ||||||
| 147 | Crystallizer | JP19904788 | 1988-08-11 | JPH0692437B2 | 1994-11-16 | アンドレアス・プラース‐リンク |
| 148 | JPH0153081B2 - | JP16210881 | 1981-10-13 | JPH0153081B2 | 1989-11-13 | KURAUSU RATOIEN; MARUTEIN URURITSUHI |
| The product which is present in the form of a melt is cooled and thereby crystallized in a double-shaft worm machine which has self-cleaning worm shafts rotating in the same direction. The crystallizing material is continually crushed in a repeatedly cutting manner during solidification and during the subsequent cooling operation, while maintaining the main transporting direction in the worm. In this manner, crystal agglomerates are prevented from forming which have only solidified on the surface, while still containing liquid portions inside. The process is carried out using a worm machine, the worm profile of which is repeatedly interrupted by introducing grooves, so that only small segment ridges remain. | ||||||
| 149 | Vertical vortex cell tower | JP4456683 | 1983-03-18 | JPS58174234A | 1983-10-13 | GEORUKU SHIYURAIBAA; HAINRITSUHI ROOPU |
| 150 | Purification of sodium hydroxide | JP5067775 | 1975-04-28 | JPS51126399A | 1976-11-04 | NAKAYA KEIICHI; HIRATA SUEICHI; SATOU KUNIO |
| PURPOSE: Production of high concentration and high purity sodium hydrizede from its solution containing sodium chloride and other impurities. COPYRIGHT: (C)1976,JPO&Japio | ||||||
| 151 | Kinzokunorenzokushikirifuratsukusurifuainingu | JP11732175 | 1975-09-30 | JPS5176103A | 1976-07-01 | JEIMUZU DEYURII ESUDEIRU; GUREIMU UIRIAMU WARUTAAZU |
| 152 | Crystallization apparatus | US229950 | 1988-08-09 | US5009861A | 1991-04-23 | Andreas Plaas-Link |
| A crystallization apparatus 2, in particular for crystallizing proteins at zero gravity, comprises a crystallization cell consisting of an elastic tube 8 of which the ends can be sealed. Using a clamp means 10the tube cavity can be reversibly divided into several cells 14, 14', 14" to receive various solutions depending on the particular crystallization. | ||||||
| 153 | Small volume rotary filter | US160693 | 1988-02-26 | US4876013A | 1989-10-24 | Iosif Shmidt; Mario Badiali |
| An improved method and apparatus for filtration includes an outer stationary body, an inner rotating body defining a gap with the outer body for receiving a fluid sample, the surface of one of the bodies defining the gap being a filter. The rotation of the inner body creates Taylor vortices which continuously displace occluded solute on the filter surface. The filter can be a membrane. In one embodiment the device may be used to filter very small volumes of fluid such as are handled in clinical and other laboratories. | ||||||
| 154 | Solvent recovery system | US57494 | 1987-06-03 | US4743380A | 1988-05-10 | Edwin H. Royse |
| A solvent recovery system (10) is disclosed which separates material from a solution by refrigeration. The solution is used to wash a printing plate and the material is washed from the plate by the solution. The contaminated solution is refrigerated within a disposable container (32) to separate the material from a solution. The purified solution is then drawn off from the container, leaving the material as residue for disposal in the container. | ||||||
| 155 | Process for purifying sodium hydroxide | US901032 | 1978-04-28 | USRE30411E | 1980-10-07 | Keiichi Nakaya; Suekazu Hirata; Kunio Sato |
| An aqueous solution of sodium hydroxide containing soluble impurities such as a concentrated catholyte produced by a diaphragm electrolysis is cooled by a coolant or a heat-exchanger to form a slurry containing sodium hydroxide hydrate crystals and fine impurity crystals. The fine impurity crystals are adsorbed on bubbles which are formed by vaporizing a dissolved coolant or introducing a gas in the slurry and separated from the slurry. | ||||||
| 156 | Continuous reflux refining of metals | US808387 | 1977-06-20 | US4133517A | 1979-01-09 | James D. Esdaile; Graeme W. Walters |
| A method is provided for the continuous purification of an impure metal in a column consisting of a slurry of metal crystals in liquid metal, said column having a relatively hot zone and a continuous temperature gradient between said zones; the temperature of the cool zone being such as to permit coexistence of liquid and crystalline metal, and said hot zone being at a temperature sufficient to melt the crystals. A portion of the column in the said cool zone is chilled to form a coherent mass of crystals of the metal; then incipient melting in the mass is allowed to occur to release crystals from the mass into the column of the crystals in the liquid metal in the cool zone of said column. The crystals are transported through the temperature gradient and into the hot zone, wherein melting of the crystals occurs and the hot zone thereby becomes enriched with the pure liquid metal.In normal operation, impure feed metal is supplied to the column; purified liquid metal is withdrawn from the hot zone; and impurity-enriched metal is withdrawn from the cool zone. | ||||||
| 157 | Continuous reflux refining of metals | US616816 | 1975-09-25 | US4043802A | 1977-08-23 | James Durie Esdaile; Graeme William Walters |
| A method is provided for the continuous purification of an impure metal in a column consisting of a slurry of metal crystals in liquid metal, said column having a relatively hot zone and a continuous temperature gradient between said zones; the temperature of the cool zone being such as to permit coexistence of liquid and crystalline metal, and said hot zone being at a temperature sufficient to melt the crystals. A portion of the column in the said cool zone is chilled to form a coherent mass of crystals of the metal; then incipient melting in the mass is allowed to occur to release crystals from the mass into the column of the crystals in the liquid metal in the cool zone of said column. The crystals are transported through the temperature gradient and into the hot zone, wherein melting of the crystals occurs and the hot zone thereby becomes enriched with the pure liquid metal.In normal operation, impure feed metal is supplied to the column; purified liquid metal is withdrawn from the hot zone; and impurity-enriched metal is withdrawn from the cool zone. | ||||||
| 158 | Sharpening device for a writing element | US3561507D | 1968-12-04 | US3561507A | 1971-02-09 | DZIUK PETER |
| A device for sharpening a writing element mounted in a holder when the writing element is inserted into an eccentric opening in the device and moved in a circular path to rotate a sharpening tool round the element. The opening is formed in a rotary part of a casing and the sharpening tool is carried in a toolholder mounted adjacent said opening, as in a ball-and-socket joint, so that the toolholder may tilt during sharpening and so minimize the danger of breakage of said writing element but the toolholder is held against rotation with the writing element.
|
||||||
| 159 | Crystal growing apparatus | US77352758 | 1958-11-12 | US2990258A | 1961-06-27 | FRANK AUGUSTINE |
| 160 | Method of protecting the surfaces of soluble salt crystals | US51439855 | 1955-06-09 | US2835606A | 1958-05-20 | LADD WILLIAM A |
QQ群二维码
意见反馈
意见反馈