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An experimental study of evaporation waves in a superheated liquid

机译:过热液体中蒸发波的实验研究

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NOTE: Text or symbols not renderable in plain ASCII are indicated by [...]. Abstract is included in .pdf document.\ud\udEvaporation waves in superheated liquids are studied using a rapid-depressurization facility consisting of a vertical glass test cell situated beneath a large, low-pressure reservoir. The objective of this study is to learn more about the physical mechanisms of explosive boiling (of which an evaporation wave is a specific example), as well as properties of the flow it produces.\ud\udThe test cell is initially sealed from the reservoir by a foil diaphragm, and is partially filled with a volatile liquid (Refrigerant 12 or 114). An experiment is initiated by rupturing the diaphragm via a pneumatically driven cutter. The instrumentation consists of fast-response pressure measurements, high-speed motion pictures, and spark-illuminated still photographs. The liquid temperature is typically 20°C; the liquid superheat is controlled by setting the reservoir pressure to values between vacuum and 1 atm. The pressures subsequent to depressurization are very much less than the critical pressure, and the initial temperatures are sufficiently low that, although the test liquid is highly superheated, the superheat limit is not approached. Evaporation waves in which bubble nucleation within the liquid column is suppressed entirely are considered almost exclusively.\ud\udWhen the diaphragm is ruptured, the liquid pressure drops to virtually the reservoir value within a few milliseconds. Provided that the liquid superheat so obtained is sufficiently high, the free surface then erupts in a process known as explosive boiling, which is characterized by violent, fine-scale fragmentation of the superheated liquid and extremely rapid evaporation. The explosive boiling process proceeds as a "wavefront" into the liquid column, producing a highspeed, two-phase flow that travels upward into the low-pressure reservoir, emptying the test cell in a few hundred milliseconds. The speed of the wavefront varies between 0.2 and 0.6 m/s, depending on run conditions; the corresponding two-phase flow varies between about 5 and 35 m/s.\ud\udIn the highest superheat case for the more volatile liquid (Refrigerant 12), explosive boiling usually initiates by the rapid formation of nucleation sites at random spots on the liquid free surface and at the glass/free-surface contact line. Boiling spreads to the remaining surface within 160 [...]. In the highest superheat case for the less volatile liquid (Refrigerant 114), nucleation begins only at the glass/free-surface contact line. Boiling then spreads radially inward toward the center. In the lower superheated cases for both liquids, nucleation begins at one or more sites on the glass/free-surface contact line, and propagates across the free surface.\ud\udAt the higher superheats, explosive boiling initiates within a few milliseconds from diaphragm burst, the same time scale as that of liquid depressurization. No distinction is made between the onset of nucleation and that of explosive boiling. However, if the reservoir pressure is raised above a certain approximate value, the onset of explosive boiling is delayed. During the delay period, relatively slow bubbling (initiated at one or more nucleation sites at the glass/free-surface contact line) occurs, and a cluster of bubbles forms in the vicinity of the initial site. The bubble cluster then "explodes," marking the transition to explosive boiling. The delay period increases significantly as the reservoir pressure is raised slightly further. Reservoir pressures corresponding to a delay period of order 100 ms define an approximate self-start threshold pressure, above which the transition to explosive boiling does not occur. \ud\udWithin about 10 ms of initiation, the wave reaches a quasi-steady condition in which the average wave speed, two-phase flow speed, and base and exit pressures are constant. However, the instantaneous propagation rate and the mechanisms that generate the mean flow are observed to be highly nonsteady. The wavefront appears to propagate by heterogeneous bubble nucleation at its leading edge, and any given region of the wavefront tends to propagate in surges associated with new nucleation and/or very fine-scale surface perturbations. Measurements of the instantaneous position of the upstream tip of the wavefront indicate that local velocity fluctuations are the same order as the mean velocity. The leading-edge bubble lifetimes and diameters are statistically distributed; mean values are of order 1 ms and 1 mm, respectively. The leading-edge bubbles are fragmented in violent "bursts" of aerosol. Bursts have a tendency to sweep over the leading-edge bubble layer in a wavelike manner: They are "large-scale structures" associated with the fragmentation of many bubbles.\ud\udFragmentation, rapid evaporation, flow acceleration, and pressure drop occur primarily within about 1 cm of the leading edge. Downstream of this region, the average speed and appearance of the flow are virtually constant. This developed flow is a highly nonuniform, two-phase spray containing streaklike structures. Its liquid phase is composed of drops (with a maximum diameter of about 100 [...]), as well as clusters and chains of bubbles (with a diameter of a few hundred microns). A thin liquid layer begins climbing the wall upon wave initiation. Its speed is a few m/s-significantly slower than that of the two-phase flow through the center. Exit pressure measurements indicate that the flow chokes for sufficiently low reservoir pressure; at higher reservoir pressures the flow is unchoked.\ud\udThe self-start threshold is not a propagation threshold, as waves are observed to propagate at somewhat lower superheats if started artificially. This is accomplished in Refrigerant 114 by "jump-starting" the wave, using the more volatile Refrigerant 12. For sufficiently high reservoir pressures, an "absolute" threshold is reached at which the quasi-steady rapid evaporation processes break down.\ud\udPossible mechanisms for explosive boiling are discussed in light of the present results. While neither of the two previous schools of thought (interfacial instability hypotheses and the secondary nucleation hypothesis) are alone adequate to explain the observed behavior, there is evidence that both may play a role. It is here proposed that the bursting phenomenon and bubble nucleation at the wavefront leading edge are mutually interactive processes-bursting occurring as the violent breakup of interstitial bubble liquid, and nucleation (and fine-scale perturbations) being caused by burst-generated aerosol striking the leading-edge surface. It is not understood what role interfacial instability may play in the bursting process.\ud\udAn evaporation wave is analogous to a premixed flame in that both are classified as "weak deflagration" waves in gasdynamic theory. It is shown that using several approximations that are valid for the type of evaporation waves studied, the conservation equations (jump conditions) can be reduced to a single, simple expression in terms of readily measured and inferred properties.\ud
机译:注意:用[...]表示无法用纯ASCII呈现的文本或符号。摘要包含在.pdf文件中。\ ud \ ud使用快速降压设备研究过热液体中的蒸发波,该设备由位于大型低压储罐下方的垂直玻璃测试室组成。这项研究的目的是更多地了解爆炸沸腾的物理机理(其中蒸发波就是一个具体例子)及其产生的流动特性。\ ud \ ud最初将测试池与储层密封通过箔膜隔膜,并部分地充满挥发性液体(制冷剂12或114)。通过经由气动切割机使隔膜破裂来开始实验。仪器包括快速响应的压力测量,高速运动图像和火花照亮的静态照片。液体温度通常为20°C;通过将储罐压力设置为真空到1个大气压之间的值来控制液体过热。降压后的压力远远小于临界压力,并且初始温度足够低,以至于尽管测试液体高度过热,但仍未达到过热极限。几乎完全认为其中完全抑制了液柱内气泡成核的蒸发波。\ ud \ ud当隔膜破裂时,液体压力实际上在几毫秒内下降到储层值。只要如此获得的液体过热度足够高,自由表面就会以称为爆炸沸腾的过程喷发,该过程的特征是过热液体发生剧烈的细碎并迅速蒸发。爆炸性沸腾过程以“波阵面”的形式进入液柱,产生高速的两相流,向上流向低压储罐,在几百毫秒内将测试单元排空。波前的速度在0.2到0.6 m / s之间变化,具体取决于运行条件。相应的两相流大约在5到35 m / s之间变化。\ ud \ ud在挥发性最高的液体(制冷剂12)的最高过热情况下,爆炸沸腾通常是通过快速形成晶核在随机点上形成而引起的。无液体表面和玻璃/自由表面接触线。沸腾扩散到160 [...]内的剩余表面。在挥发性较低的液体(制冷剂114)过热程度最高的情况下,成核仅在玻璃/自由表面接触线上开始。然后沸腾向内径向向内扩散。在两种液体的过热度较低的情况下,成核始于玻璃/自由表面接触线上的一个或多个位置,并在整个自由表面上传播。\ ud \ ud在较高的过热度下,爆炸沸腾在距隔膜几毫秒的范围内开始爆裂,与液体减压的时间尺度相同。在成核的开始和爆炸沸腾之间没有区别。但是,如果储层压力升高到某个近似值以上,炸药沸腾的发生就会延迟。在延迟期间,发生相对较慢的起泡(在玻璃/自由表面接触线处的一个或多个成核位置处开始),并且在初始位置附近形成一簇气泡。然后,气泡簇“爆炸”,标志着向爆炸沸腾的过渡。随着储层压力的进一步升高,延迟时间将显着增加。对应于约100 ms的延迟时间的储层压力定义了一个近似的自启动阈值压力,在该压力之上不会发生向爆炸沸腾的过渡。 \ ud \ ud在大约10 ms的开始时间内,波达到准稳态条件,在该条件下,平均波速,两相流速以及基本压力和出口压力是恒定的。但是,观察到瞬时传播速率和产生平均流量的机制非常不稳定。波前似乎通过其前缘的异质气泡形核传播,波前的任何给定区域都倾向于在与新形核和/或非常精细的表面扰动相关的浪涌中传播。对波前上游尖端的瞬时位置的测量表明,局部速度波动与平均速度的阶次相同。前沿气泡的寿命和直径是统计分布的;平均值分别为1 ms和1 mm。前沿气泡在强烈的气溶胶“破裂”中破碎。爆炸倾向于以波状方式掠过前沿气泡层:它们是与许多气泡破碎相关的“大型结构”。\ ud \ ud破碎,快速蒸发,流动加速,并且压降主要发生在前缘的大约1 cm之内。在此区域的下游,平均速度和流的外观实际上是恒定的。产生的气流是高度不均匀的两相喷雾,包含条纹状结构。它的液相由液滴(最大直径约为100)以及气泡的簇和链(直径为几百微米)组成。波浪开始时,薄薄的液体层开始爬壁。它的速度比通过中心的两相流的速度慢几m / s。出口压力测量表明,对于足够低的油藏压力,流量阻塞了。在较高的储层压力下,水流不会阻塞。\ ud \ ud自启动阈值不是传播阈值,因为如果人为启动,则观察到波在较低的过热度下传播。在制冷剂114中,这是通过使用挥发性更高的制冷剂12“跳跃”波浪来实现的。对于足够高的储层压力,达到了“绝对”阈值,在该阈值处准稳态快速蒸发过程破裂。根据目前的结果讨论了爆炸沸腾的可能机理。尽管先前的两个学派(界面不稳定性假说和次生成核假说)都不足以解释所观察到的行为,但有证据表明两者都可能起作用。在此提出,波阵面前沿的破裂现象和气泡成核是相互相互作用的过程-爆裂是由于间隙气泡液体的剧烈破裂而发生的,而成核(和小尺度的扰动)则是由破裂产生的气溶胶撞击到玻璃表面而引起的。前缘表面。尚不了解界面不稳定性在破裂过程中可能起什么作用。\ ud \ ud蒸发波类似于预混火焰,因为在气体动力学理论中两者都被归类为“弱爆燃”波。结果表明,使用对研究的蒸发波类型有效的几种近似值,守恒方程(跳跃条件)可以根据易于测量和推断的性质简化为一个简单的表达式。

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    Hill, Larry Glenn;

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  • 年度 1991
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