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    • 59. 发明授权
    • Process for treating geothermal brine in two phase brine separators
    • 在两相盐水分离器中处理地热盐水的方法
    • US4776961A
    • 1988-10-11
    • US75267
    • 1987-07-17
    • Gregory A. GrittersJohn L. FeatherstoneJessie P. Reverente
    • Gregory A. GrittersJohn L. FeatherstoneJessie P. Reverente
    • B01D3/06B01D9/00C02F1/60B01D17/00B01D21/00
    • C02F1/60B01D3/06B01D9/0022
    • A process for treating hot, pressurized geothermal brine in a liquid-vapor phase separator comprises contacting the brine in the separator with between about 0.2 and about 1.5 parts per million of a defoaming agent so as to substantially reduce the amount of foaming in the separator caused, in part, by steam bubbling through the brine. The preferred defoaming agents are polyglycols having molecular weights between about 1000 and about 2500, those agents having molecular weights below about 1000 being too volatile and those above about 2500 being too difficult to solubilize in the brine. If the separator comprises a draft tube-type flash crystallizer in which silica-rich geothermal brine is contacted with a seed material onto which silica from the brine deposits, the process additionally includes establishing and maintaining a brine level in the crystallizer causing circulation of the brine at a rate substantially reducing the rate of silicious scaling of inner walls of the crystallizer which would result in the absence of brine circulation, the established and maintained brine level being such that in the absence of the defoaming agent, excessive amounts of brine in the form of foam would be carried over into steam discharged from the crystallizer. In preexisting separators in which a design steam production rate cannot be attained because of brine foaming, the addition of a defoaming agent by the present process may enable steam production at a rate greater than the design rate.
    • 用于在液 - 气相分离器中处理热的,加压的地热盐水的方法包括使分离器中的盐水与每百万份消泡剂接触约0.2至约1.5份,以便基本上减少分离器中的起泡量 部分地通过蒸汽通过盐水鼓泡。 优选的消泡剂是分子量在约1000至约2500之间的聚二醇,分子量低于约1000的那些试剂太挥发,而高于约2500的那些试剂太难溶解在盐水中。 如果分离器包括引流管式闪蒸结晶器,其中富含二氧化硅的地热盐水与来自盐水沉积的二氧化硅的种子材料接触,则该方法还包括建立并保持结晶器中的盐水水平,引起盐水循环 以大大降低结晶器内壁的硅质垢的速率,这将导致不存在盐水循环,建立和保持的盐水水平使得在没有消泡剂的情况下,过量的盐水形式 的泡沫将被转移到从结晶器排出的蒸汽中。 在由于盐水发泡而不能实现设计蒸汽生产率的预先存在的分离器中,通过本方法添加消泡剂可以使蒸汽以大于设计速率的速率生产。