首页> 外国专利> Purification of liquid metal heat exchange fluid for hydrocarbon conversion reactions, involves removing hydrogen from dissolved hydride in drum, at specified temperature and interfacial surface area

Purification of liquid metal heat exchange fluid for hydrocarbon conversion reactions, involves removing hydrogen from dissolved hydride in drum, at specified temperature and interfacial surface area

机译:用于碳氢化合物转化反应的液态金属热交换流体的纯化,包括在规定的温度和界面表面积下,从转鼓中的氢化物中除去氢

摘要

The method involves passing a portion of a circulating liquid metal stream comprising a heat transfer fluid into a drum maintained under vacuum. Sufficient interfacial surface area and sufficient temperature is provided in the drum to release hydrogen from hydride present in a liquid metal stream. The purified liquid stream is recovered and recirculated. The liquid metal stream initially contacts a heat transfer surface that permits permeation of hydrogen into the liquid metal stream and results in the formation of metal hydride. A portion of the circulating stream is withdrawn and passed to the drum maintained under vacuum. Hydrogen released from the drum is vented and removed. The purified liquid metal stream contains a near-equilibrium concentration of the metal hydride and has a reduced concentration of metal hydride relative to the stream separated from the circulating stream. The drum is maintained at a vacuum of 1-10 mm Hg and at 400-550 degrees C. At least a portion of the purified stream passes through an additional hydride removal zone, which comprises a cold trap that removes hydride particles from a cooled liquid metal stream. The cold trap is periodically regenerated by passing a heated liquid metal stream into the trap to dissolve metal hydride particles and produce a regeneration efficient stream comprising liquid metal and the dissolved metal hydride particles. The drum has trays for providing the interfacial surface area. The drum has at least 10 m2 of surface area per m3/hour of liquid passing through the drum. In an alternative method, multiple cold traps are provided either in parallel or serial flow.
机译:该方法包括使一部分包含传热流体的循环液态金属流进入保持在真空下的鼓中。在转鼓中提供足够的界面表面积和足够的温度,以从液态金属流中存在的氢化物释放氢。纯化的液流被回收并再循环。液态金属流最初接触传热表面,该传热表面允许氢渗透到液态金属流中并导致金属氢化物的形成。一部分循环流被抽出并通过保持在真空下的鼓。从鼓中释放的氢气被排出并除去。相对于从循环流分离的流,纯化的液态金属流包含接近平衡浓度的金属氢化物,并且具有降低的金属氢化物浓度。滚筒保持在1-10 mm Hg的真空和400-550摄氏度。至少一部分纯化物流通过附加的氢化物去除区,该区包括一个冷阱,用于从冷却液体中去除氢化物颗粒金属流。通过使加热的液态金属流进入该阱中来周期性地再生该冷阱,以溶解金属氢化物颗粒并产生包含液态金属和溶解的金属氢化物颗粒的高效再生流。鼓具有用于提供界面表面积的托盘。每m3 /小时通过滚筒的液体桶的表面积至少为10 m2。在替代方法中,以并联或串联流动的方式设置多个冷阱。

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