首页> 外文会议>14th cryogenics 2017 >PROBLEMS OF BULK STORAGE AND SHIPPING OF LIQUID HYDROGEN IN VOLUMES OF 10,000 TO 100,000 CUBIC METERS AT ONE BAR PRESSURE
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PROBLEMS OF BULK STORAGE AND SHIPPING OF LIQUID HYDROGEN IN VOLUMES OF 10,000 TO 100,000 CUBIC METERS AT ONE BAR PRESSURE

机译:一巴压力下体积为10,000到100,000立方米的液体氢的散装存储和运输问题

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This paper discusses concern about the safety and serious risk assessment of the large scale bulkrnstorage, shipping and handling of liquid hydrogen.rnWhile hydrogen is very attractive as a green fuel and energy store, some of its physical properties providernincreasing problems if the proposed usage increases beyond a limit of, say, 1000 m~3 of liquid hydrogen,rnunder pressures rising to 10 to 15 bar to achieve zero boil-off, in a vacuum insulated container. Cryogenicrntechnology is currently not able to store larger volumes in vacuum insulated tanks under pressure with zerornboil-off, or even at one bar pressure with continuous boil-off. At first sight, the successful shipping andrnstorage of bulk LNG over the past 45 years suggests a satisfactory way forward. In fact, the properties ofrnbulk liquid hydrogen compare unfavourably with those of LNG, and the LNG technology cannot be adaptedrnwith the same degree of safety and economy.rnThe problems start with the large volume of boil-off hydrogen gas produced and its extreme flammabilityrnabove a composition in air of only 4% hydrogen. Safe disposal of this boil-off presents a major problem,rnwhich is enhanced by the fact that the density of LH_2 is 6 times less than that of LNG, and the latent heat ofrnevaporation per unit volume is 7 times less: hence the volume of boil-off hydrogen gas is seven times greaterrnfor the same heat influx.rnFor ship and shore tanks with gas-purged foam insulation, the only safe purge-gas is helium which has arnthermal conductivity k-value 5 times greater than nitrogen or methane purge used for LNG tank insulation.rnThe net boil-off rate of LH_2 using the conventional one metre thickness of foam insulation can therefore bernexpected to be 35 times larger than the working figure of 0.2% per day for stored volumes of LNG.rnThese and other handling problems, together with the associated hazards of disposing of the gas safely, eitherrninto the atmosphere, or flaring it off or re-condensing it, appear to make proposals for bulk liquid hydrogenrnusage not viable for both safety and economic reasons. This paper will review this lack of viability.
机译:本文讨论了对大规模散装储氢,运输和处理液态氢的安全性和严重风险评估的关注。尽管氢作为绿色燃料和能量存储非常有吸引力,但如果提议的使用量增加到超过200万,氢的某些物理性质会增加问题在真空绝热容器中,在压力升至10至15 bar以实现零蒸发的条件下,限制了1000 m〜3的液态氢。低温技术目前无法在零沸腾压力下,甚至在连续蒸发的一巴压力下,在真空绝热罐中存储更大的体积。乍一看,过去45年中散装液化天然气的成功运输和储存表明了令人满意的前进方向。实际上,散装液态氢的性能与LNG相比不利,并且LNG技术不能以相同的安全性和经济性来适应。问题在于产生的大量蒸发氢气及其极易燃性始于组成在空气中只有4%的氢气。安全地处理这种蒸发物是一个主要问题,这是由于LH_2的密度比LNG的密度小6倍,并且单位体积的蒸发潜热少7倍,因此沸腾的体积增加了。对于相同的热量流入,氢气的排放量要大7倍。对于带有气体吹扫泡沫绝缘的船舶和岸上储罐,唯一安全的吹扫气体是氦,其氦气的导热系数k值是氮气或甲烷吹扫使用的5倍LNG储罐的隔热。因此,对于储存的LNG,使用传统的一米厚的泡沫隔热材料所产生的LH_2的净蒸发率因此可以预计是每天0.2%的工作数字的35倍。rn这些和其他处理问题,连同将气体安全地排放到大气中,将其放空或重新冷凝所带来的相关危险,似乎提出了关于散装液态氢废料既不安全又不经济的建议。理由。本文将回顾这种缺乏生存能力的情况。

著录项

  • 来源
    《14th cryogenics 2017》|2017年|140-144|共5页
  • 会议地点
  • 作者

    Scurlock Ralph;

  • 作者单位

    Kryos Technology, Southampton, SO17 1QP, UK. ,scurlock@soton.ac.uk;

  • 会议组织
  • 原文格式 PDF
  • 正文语种 eng
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