THIN FILM PHOTOVOLTAIC SOLAR CELL DEVICE
    1.
    发明申请
    THIN FILM PHOTOVOLTAIC SOLAR CELL DEVICE 审中-公开
    薄膜光伏太阳能电池装置

    公开(公告)号:US20130146133A1

    公开(公告)日:2013-06-13

    申请号:US13324710

    申请日:2011-12-13

    IPC分类号: H01L31/0336 H01L31/18

    摘要: A thin-film photovoltaic solar cell device is disclosed. A transparent conductive oxide (TCO) layer is disposed on a substrate as a front contact. A window layer is disposed on the TCO layer. A metal oxide layer is disposed on the window layer. An absorber layer is disposed on the metal oxide layer. A back contact layer is disposed on the absorber layer. In one embodiment, the device includes a high resistance barrier (HRT) layer interposed between the window layer and the TCO layer.

    摘要翻译: 公开了一种薄膜光伏太阳能电池器件。 透明导电氧化物(TCO)层作为前触点设置在基板上。 窗口层设置在TCO层上。 金属氧化物层设置在窗口层上。 吸收层设置在金属氧化物层上。 背面接触层设置在吸收体层上。 在一个实施例中,该装置包括介于窗口层和TCO层之间的高电阻屏障(HRT)层。

    ACTIVE MAGNETIC REGENERATIVE LIQUEFIER USING PROCESS GAS PRE-COOLING FROM BYPASS FLOW OF HEAT TRANSFER FLUID

    公开(公告)号:US20190390899A1

    公开(公告)日:2019-12-26

    申请号:US16563692

    申请日:2019-09-06

    IPC分类号: F25J1/02 F25J1/00 F25B21/00

    摘要: A process for liquefying a process gas comprising: introducing a heat transfer fluid into an active magnetic regenerative refrigerator apparatus that comprises (i) a high magnetic field section in which the heat transfer fluid flows from a cold side to a hot side through at least one magnetized bed of at least one magnetic refrigerant, (ii) a first no heat transfer fluid flow section in which the bed is demagnetized, (iii) a low magnetic or demagnetized field section in which the heat transfer fluid flows from a hot side to a cold side through the demagnetized bed, and (iv) a second no heat transfer fluid flow section in which the bed is magnetized; continuously diverting a bypass portion of the heat transfer fluid from the cold side of the low magnetic or demagnetized field section into a bypass flow heat exchanger at a first cold inlet temperature; and continuously introducing the process gas into the bypass flow heat exchanger at a first hot inlet temperature and discharging the process gas or liquid from the bypass flow heat exchanger at a first cold exit temperature; wherein the temperature difference between bypass heat transfer first cold inlet temperature and the process gas first cold exit temperature is 1 to 5 K.