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1. 发明授权

US08857207B2 Refrigerant dryer 有权
标题翻译：制冷干燥机
公开(公告)号：US08857207B2
公开(公告)日：2014-10-14
申请号：US12579046
申请日：2009-10-14
申请人： Kristian Dering , Michael Feisthauer , Andreas Fredenhagen , Andreas Foerster , Klaus-Ulrich Kobelt
发明人： Kristian Dering , Michael Feisthauer , Andreas Fredenhagen , Andreas Foerster , Klaus-Ulrich Kobelt
IPC分类号： F25D11/00 , F25D17/06 , F25D17/02 , F28D20/02 , B01D53/26
CPC分类号： B01D53/265 , F25B2400/24 , F28D20/02 , Y02E60/145
摘要： A refrigerant dryer, in particular a compressed air refrigerant dryer, is provided for drying a gaseous fluid while cooling the gaseous fluid using a refrigerant. The dryer includes a pressure fluid-refrigerant agent-heat exchanger (30) in which a cooling of the gaseous fluid takes place directly or indirectly by a refrigerant conveyed in a primary loop (16), one or more refrigerant compressor/compressors (24) for operating the primary loop, and a cold accumulator (13) with an accumulator-side heat exchanger (20) which couples an accumulator discharge fluid to a cold accumulator medium (14). The pressure fluid-refrigerant agent-heat exchanger (30) and the cold accumulator (13) are fluidically connected or can be brought into fluidic connection via a discharge loop (15) for an accumulator discharge fluid. The cold accumulator (13) is arranged, relative to gravity, above the pressure fluid-refrigerant agent-heat exchanger (30), in such a manner that the heated accumulator discharge fluid is conveyed through the discharge loop (15) for cooling in the cold accumulator (13), is cooled there, and subsequently re-conveyed to the pressure fluid-refrigerant agent-heat exchanger (30).
摘要翻译：提供制冷剂干燥器，特别是压缩空气制冷剂干燥器，用于干燥气态流体，同时使用制冷剂冷却气态流体。干燥机包括压力流体 - 制冷剂 - 热交换器（30），在该压力流体 - 制冷剂 - 热交换器（30）中，气态流体的冷却直接或间接地由在主回路（16），一个或多个制冷剂压缩机/压缩机（24）以及具有将蓄能器排出流体连接到蓄冷介质（14）的蓄能器侧热交换器（20）的蓄冷器（13）。压力流体 - 制冷剂 - 热交换器（30）和蓄冷器（13）流体连接或者可以通过用于蓄能器排出流体的排放回路（15）进行流体连接。蓄冷器（13）相对重力设置在压力流体 - 制冷剂 - 热交换器（30）的上方，使得加热的蓄能器排出流体通过排出回路（15）输送，以便在蓄冷器（13）在那里被冷却，随后被重新输送到压力流体 - 制冷剂 - 热交换器（30）。

2. 发明申请

US20130032315A1 REFRIGERANT DRYER SUCH AS A COMPRESSED AIR REFRIGERANT DRYER, AND HEAT EXCHANGER FOR A REFRIGERANT DRYER SUCH AS A COMPRESSED AIR REFRIGERANT DRYER 审中-公开
标题翻译：作为压缩式空气制冷干燥机的制冷干燥机和用于制冷干燥机的热交换器如压缩空气制冷干燥机
公开(公告)号：US20130032315A1
公开(公告)日：2013-02-07
申请号：US13641254
申请日：2011-04-12
申请人： Andreas Förster , Andreas Fredenhagen , Michael Feisthauer , Andreas Walter , Kristian Dering
发明人： Andreas Förster , Andreas Fredenhagen , Michael Feisthauer , Andreas Walter , Kristian Dering
IPC分类号： F28C3/00
CPC分类号： B01D53/265 , F28D7/0008 , F28D9/0093 , F28D20/02 , F28D2021/0038 , F28F3/027 , Y02E60/145
摘要： The invention relates to a heat exchanger for a refrigerant dryer such as a compressed air refrigerant dryer comprising at least one first inflow surface element, past which a fluid to be dried such as compressed air can flow during operation of the heat exchanger, and comprising at least one second inflow surface element, past which a refrigerant fluid can flow as required during operation of the heat exchanger, wherein the first and second inflow surface elements are or can be coupled at least in some areas to at least one cold store chamber that is provided for filling with a cold accumulator medium, and wherein the first and/or second inflow surface element(s) (is) are connected to at least one heat transfer element which extends into the cold store chamber, e.g. penetrates the cold store chamber.
摘要翻译：本发明涉及一种用于诸如压缩空气制冷剂干燥器的制冷剂干燥器的热交换器，其包括至少一个第一流入表面元件，待热干燥的流体例如压缩空气可在热交换器的操作期间流动，并且包括在至少一个第二流入表面元件，制冷剂流体可以在热交换器的操作过程中根据需要流动，其中第一和第二流入表面元件至少在一些区域中至少可耦合到至少一个冷储存室，提供用于填充冷藏介质，并且其中第一和/或第二流入表面元件（一个或多个）连接到至少一个延伸到冷存储室中的传热元件，例如穿透冷藏室。

3. 发明授权

US10143962B2 Refrigerant dryer, in particular compressed air refrigerant dryer, and heat exchanger for a refrigerant dryer, in particular a compressed air refrigerant dryer 有权
公开(公告)号：US10143962B2
公开(公告)日：2018-12-04
申请号：US13641254
申请日：2011-04-12
申请人： Andreas Förster , Andreas Fredenhagen , Michael Feisthauer , Andreas Walter , Kristian Dering
发明人： Andreas Förster , Andreas Fredenhagen , Michael Feisthauer , Andreas Walter , Kristian Dering
IPC分类号： B01D53/26 , F28D7/00 , F28D9/00 , F28D20/02 , F28F3/02 , F28D21/00
摘要： The invention relates to a heat exchanger for a refrigerant dryer such as a compressed air refrigerant dryer comprising at least one first inflow surface element, past which a fluid to be dried such as compressed air can flow during operation of the heat exchanger, and comprising at least one second inflow surface element, past which a refrigerant fluid can flow as required during operation of the heat exchanger, wherein the first and second inflow surface elements are or can be coupled at least in some areas to at least one cold store chamber that is provided for filling with a cold accumulator medium, and wherein the first and/or second inflow surface element(s) (is) are connected to at least one heat transfer element which extends into the cold store chamber, e.g. penetrates the cold store chamber.

4. 发明授权

US08349054B2 Adsorption drying apparatus and adsorption drying method 有权
标题翻译：吸附干燥装置和吸附干燥方法
公开(公告)号：US08349054B2
公开(公告)日：2013-01-08
申请号：US12957468
申请日：2010-12-01
申请人： Andreas Fredenhagen , René Martin , Michael Feisthauer , Michael Rohdenburg
发明人： Andreas Fredenhagen , René Martin , Michael Feisthauer , Michael Rohdenburg
IPC分类号： B01D53/06 , B01D53/26
CPC分类号： B01D53/06 , B01D53/261 , B01D2257/80
摘要： An adsorption drying apparatus, in particular for drying a compressed gas, includes an adsorption chamber (11) having a plurality of adsorption conduits (101) containing an adsorption material (123), a first feeding line (106) and a first discharging line (109) disposed at a first end (111) of the adsorption chamber (11), and a second feeding line (108) and a second discharging line (107) disposed at a second end (112) of the adsorption chamber (11). The adsorption chamber (11) is rotatable with respect to the feeding and discharging lines (106, 107, 108, 109) so that the adsorption conduits may be fluidically connected in temporal alternation, wherein the gas is dried in a drying sector (102), and the adsorption material (123) is regenerated in the regeneration sector (103). The first feeding line (106) is configured such that the gas stream to be dried may be fed to the regeneration sector (103) as a full flow.
摘要翻译：特别是用于干燥压缩气体的吸附干燥装置包括具有多个吸附管道（101）的吸附室（11），该吸附管道包含吸附材料（123），第一供给管线（106）和第一排出管线 109）设置在吸附室（11）的第一端（111），以及设置在吸附室（11）的第二端（112）的第二供给管线（108）和第二排出管线（107）。吸附室（11）可相对于进料和排出管线（106,107,108,109）旋转，使得吸附管道可以在时间交替中流体连接，其中气体在干燥扇区（102）中干燥，，并且在再生扇区（103）中再生吸附材料（123）。第一供给管线（106）被构造成使得待干燥的气流可以作为全流进给到再生扇区（103）。

5. 发明申请

US20050233040A1 Method and device for homogenizing emulsions 审中-公开
标题翻译：用于均化乳液的方法和装置
公开(公告)号：US20050233040A1
公开(公告)日：2005-10-20
申请号：US10513845
申请日：2003-04-09
申请人： Wolfgang Ehrfeld , Andreas Fredenhagen
发明人： Wolfgang Ehrfeld , Andreas Fredenhagen
IPC分类号： B01F3/08 , B01F5/06 , B01F13/00 , A23P1/00
CPC分类号： B01F5/0682 , B01F3/0807 , B01F13/0059
摘要： Method and device for homogenizing emulsions, especially milk, wherein an emulsion is subjected to a high shearing force in a homoginizer equipped with microstructures.
摘要翻译：用于均化乳液，特别是乳的方法和装置，其中乳液在装有微结构的均质机中经受高剪切力。

6. 发明授权

US5093330A Staurosporine derivatives substituted at methylamino nitrogen 失效
标题翻译：在甲氨基氮取代的星形孢菌衍生物
公开(公告)号：US5093330A
公开(公告)日：1992-03-03
申请号：US673857
申请日：1991-03-21
申请人： Giorgio Caravatti , Andreas Fredenhagen
发明人： Giorgio Caravatti , Andreas Fredenhagen
IPC分类号： C07D498/22
CPC分类号： C07D498/22
摘要： N-substituted derivatives of staurosporine of the general formula[Stau]--N(CH.sub.3)--R (I)in which [Stau] represents a residue of the partial formula ##STR1## and R represents a hydrocarbyl radical R.sup.o or an acyl radical Ac, which radicals preferably have a maximum of 30 carbon atoms, and salts of compounds of the formula I having salt-forming properties, are distinguished as selective inhibitors of proteinkinase C. They are manufactured by conventional alkylation or acylation, respectively, of staurosporine.
摘要翻译：具有通式[Stau] -N（CH 3）-R（I）的星形孢菌素的N-取代衍生物，其中[Stau]表示部分式“IMAGE”的残基，R表示烃基R o或酰基Ac ，这些基团优选具有最多30个碳原子，并且具有成盐性质的式I化合物的盐被区分为蛋白酶C的选择性抑制剂。它们分别通过星形孢菌素的常规烷基化或酰化制备。

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