摘要:
Provided is a sealing structure of a photoelectric conversion element in which the open side end section of the photoelectric conversion element can be surely and continuously sealed by a simple structure with high durability, and also the problem of insufficient sealing of the extraction electrode can be solved. A sealing structure 10 of a dye-sensitized solar cell as an example of the photoelectric conversion element is configured by a cylindrical dye-sensitized solar cell main body 12 and sealing sections 14a and 14b which respectively seal both ends of the dye-sensitized solar cell main body 12. Lid bodies 26a and 26b, each of which is formed of a conductive metal member, are respectively provided at both end sections of a transparent glass tube 16, so as to seal the dye-sensitized solar cell main body 12, and are also respectively electrically connected to a pair of electrode sections of the dye-sensitized solar cell main body 12, so as to be used as a pair of extraction electrodes.
摘要:
This invention relates to a method for removing unreacted monomers and other volatile matters from a polymer solution composition produced from a mixture containing an aromatic vinyl monomer, utilizes two or more flash devolatilizing vessels, and effects the removal by adjusting the solid content of the polymer solution composition at the outlet of the devolitilizer before the last-stage devolitilizer to a level in excess of 97%, adding 0.5-4 parts by weight of a foaming agent to the total polymer solution composition, passing the polymer solution composition through the last-stage devolitilizer while maintaining the pressure of the polymer solution at 10 kg/cm2 or more by means of a pressure controller and the temperature in the range 190-260° C., introducing the polymer solution composition to a vapor-liquid separation vessel maintained at a vacuum of 20 Torr or less, and allowing the composition to foam.
摘要翻译:本发明涉及从由含有芳香族乙烯基单体的混合物制备的聚合物溶液组合物中除去未反应的单体和其它挥发物的方法,利用两个或更多个闪蒸脱挥发容器,并通过调节聚合物溶液的固体含量 在最后阶段脱挥发酵剂之前的脱挥发剂的出口处的组成达到超过97%的水平,向总的聚合物溶液组合物中加入0.5-4重量份的发泡剂,使聚合物溶液组合物通过最后阶段 通过压力控制器和190-260℃的温度将聚合物溶液的压力保持在10kg / cm 2或更高的压力下,将聚合物溶液组合物引入保持在 真空度为20托或更低,并使组合物发泡。