公开(公告)号：US20160090658A1

公开(公告)日：2016-03-31

申请号：US14865875

申请日：2015-09-25

申请人： Richard Diver ,  Gregory Scott Duncan ,  Michal Korenko ,  Carol Larson ,  Shahin Nudehi ,  Robert Palumbo ,  Jonathan Schoer ,  Luke Venstrom

发明人： Richard Diver ,  Gregory Scott Duncan ,  Michal Korenko ,  Carol Larson ,  Shahin Nudehi ,  Robert Palumbo ,  Jonathan Schoer ,  Luke Venstrom

IPC分类号： C25C7/00 ,  C25C3/04

CPC分类号： C25C7/005 ,  C25C3/04

摘要： Systems, methods, and other embodiments associated with thermal electrolytic production. According to one embodiment, a system includes a tower having an active reflux evaporator and a condenser system. The active reflux evaporator having a distributor pump assembly and an absorber. The distributor pump assembly pumps a heat pipe liquid metal to a distributor. The absorber receives the liquid metal from the distributor. The absorber facilitates evaporation of the liquid metal to form an evaporated metal. The condenser system includes a thermal load and a liquid pump assembly. The thermal load condenses the evaporated metal back to the liquid metal. The liquid pump assembly actively pumps the liquid metal to the distributor pump assembly.

摘要翻译： 与热电解生产相关的系统，方法和其他实施方案。 根据一个实施例，系统包括具有主动回流蒸发器和冷凝器系统的塔架。 主动回流蒸发器具有分配器泵组件和吸收器。 分配器泵组件将热管液体金属泵送到分配器。 吸收器从分配器接收液态金属。 吸收剂促进液体金属的蒸发以形成蒸发的金属。 冷凝器系统包括热负荷和液体泵组件。 热负荷将蒸发的金属冷凝回液态金属。 液体泵组件主动将液体金属泵送到分配器泵组件。

公开(公告)号：US20060216826A1

公开(公告)日：2006-09-28

申请号：US11386911

申请日：2006-03-22

申请人： Gerald Marek ,  Shahin Nudehi

发明人： Gerald Marek ,  Shahin Nudehi

IPC分类号： G01N21/64

CPC分类号： G01N15/0272 ,  G01F25/0007 ,  G01N1/2252 ,  G01N5/02 ,  G01N35/00693 ,  G01N2001/2223 ,  G01N2001/225 ,  Y10T436/10

摘要： A particulate sampler system includes a diluted exhaust mass flow controller that receives flow from a dilution mass flow controller and a laminar flow element (LFE). The dilution mass flow controller and LFE are fluidly arranged parallel to one another. A controller communicates with the mass flow controllers and the LFE to determine the flow through these devices, command valves in the mass flow controllers and generate data for determining calibration coefficients and correction factors. The diluted exhaust mass flow controller is calibrated and calibration coefficients are generated using a first to fourth order curve fit. Similarly, initial calibration coefficients are generated for the dilution mass flow controller. The diluted exhaust mass flow controller is set at a desired flow point. The dilution mass flow controller is varied between set points corresponding to different dilution ratios at the common, desired set point. The data obtained is used to determine a correction factor for example, by performing a linear curve fit of the data. The correction factor is applied to the calibration coefficients associated with the mass flow controllers.