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A terminal plant and method for storing and regasifying a hydrocarbon product

机译:用于储存和再气化碳氢化合物产品的码头设备和方法

摘要

A terminal plant and a method for storing and subsequent regasification of a hydrocarbon product, in particular a hydrocarbon product having a high content of gaseous hydrate. The plant comprises at least one storage tank (1) in which the hydrocarbon product is stored until the regasification shall take place, and where the storage tank (1), which may be dimensioned to endure only a relatively low storage pressure (of for instance approximately 1 bar), is adapted to have a low storage temperature so that the gaseous hydrate remains stable during the complete storage period. The terminal plant also comprises at least one smaller dissociation tank (40) which are dimensioned to endure a regasification pressure much higher than the storage pressure. The dissociation tank or tanks (40) are connected to: a heating system (41; 47) adapted to heat the contents within the dissociation tank or tanks (40) up to the regasification temperature; to transport means (30; 17-23, 48) preferably being pressure equalizing and adapted to transfer the gaseous hydrate from the storage tank or tanks (1) in which the storage pressure prevails; and also to separate outputs (42, 45) for gaseous- and liquid components.
机译:一种用于储存和随后再气化烃产物,特别是气态水合物含量高的烃产物的终端设备和方法。该设备包括至少一个储罐(1),碳氢化合物产品将一直存储在该储罐中,直至进行再气化;储罐(1)的尺寸可设置为仅承受相对较低的存储压力(例如大约1巴),具有较低的存储温度,以使气态水合物在整个存储期间保持稳定。终端设备还包括至少一个较小的离解罐(40),其尺寸设计成能承受比储存压力高得多的再气化压力。一个或多个离解罐(40)连接到:加热系统(41; 47),其适于将一个或多个离解罐(40)中的内容物加热到再气化温度;输送至输送装置(30; 17-23、48),该输送装置优选地是压力均等的并且适于从存在储存压力的一个或多个储存罐(1)中转移气态水合物;并分离出气态和液态成分的输出(42、45)。

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