公开(公告)号：US09423140B2

公开(公告)日：2016-08-23

申请号：US14623881

申请日：2015-02-17

申请人： BE POWER TECH LLC

发明人： Daniel A. Betts ,  Matthew D. Graham ,  John L. Kaufman

IPC分类号： F24F3/14 ,  B01D61/36 ,  B01D53/14 ,  F24F3/147 ,  F24F5/00 ,  F28D7/10 ,  B01D53/26

CPC分类号： B01D53/1425 ,  B01D53/263 ,  B01D61/36 ,  B01D61/364 ,  F24F3/1411 ,  F24F3/1417 ,  F24F3/147 ,  F24F5/0035 ,  F24F2003/1435 ,  F24F2003/1458 ,  F28D7/0058 ,  F28D7/0083 ,  F28D7/026 ,  F28D7/10 ,  F28D7/106 ,  F28D21/0015 ,  F28F1/02 ,  F28F2245/02 ,  F28F2250/02 ,  H01M2250/405

摘要： A liquid desiccant regeneration system and method of liquid desiccant regeneration are described. The liquid desiccant regeneration system includes a liquid desiccant regenerator having an engine producing a heated exit stream, and at least one dehydrating tube comprising a first water vapor permeable wall. A low concentration liquid desiccant stream feeds into the liquid desiccant regenerator, while a high concentration liquid desiccant stream exiting the liquid desiccant regenerator. A carrier stream and the low concentration liquid desiccant are in contact with opposite sides of the first water vapor permeable wall, and the low concentration liquid desiccant stream is heated by heat from the heated exit stream to drive water from the low concentration liquid desiccant stream through the first water vapor permeable wall to the carrier stream to form a humidified carrier stream. As a result, the desiccant concentration in the high concentration liquid desiccant stream is higher than a desiccant concentration in the low concentration liquid desiccant stream.

摘要翻译： 描述了液体干燥剂再生系统和液体干燥剂再生方法。 液体干燥剂再生系统包括具有产生加热出口流的发动机的液体干燥剂再生器和至少一个包含第一水蒸气可渗透壁的脱水管。 低浓度液体干燥剂流进入液体干燥剂再生器，而高浓度液体干燥剂流离开液体干燥剂再生器。 载液流和低浓度液体干燥剂与第一水蒸汽可渗透壁的相对侧接触，低浓度液体干燥剂流由加热出口流的热量加热，以驱动低浓度液体干燥剂流中的水通过 第一水蒸汽渗透壁到载体流以形成加湿载体流。 结果，高浓度液体干燥剂流中的干燥剂浓度高于低浓度液体干燥剂流中的干燥剂浓度。