the Creative Commons Attribution 4.0 License.
the Creative Commons Attribution 4.0 License.
Low-temperature triple-capillary cryostat for ice crystal growth studies
Brian D. Swanson
Jon Nelson
Ice crystals come in a remarkable variety of shapes and sizes that affect a cloud's radiative properties. To better understand the growth of these crystals, we built an improved capillary cryostat (CC2) designed to reduce potential instrumental artifacts that may have influenced earlier measurements. In CC2, a crystal forms at the end of one, two, or three well-separated, ultrafine capillaries to minimize both potential crystal–crystal and crystal–substrate interaction effects. The crystals can be initiated using several ice-nucleation modes. The cryostat has two vapor-source chambers on either side of the growth chamber, each allowing independent control of the growth chamber supersaturation. Crystals can be grown under a range of air pressures, and the supersaturation conditions in the growth chamber can be rapidly changed by switching between the two vapor-source chambers using a sliding valve. Crystals grow fixed to the capillary in a uniform, stagnant environment, and their orientation can be manipulated to measure the growth rate of each face. The high thermal mass of CC2 increases the stability and uniformity of the thermodynamic conditions surrounding the crystals. Here we describe the new instrument and present several sample observations.
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Ice crystals are important in the radiation balance of the Earth's climate system (Liou and Yang, 2016; Heymsfield et al., 2017). But we still lack knowledge of both the crystal-shape distribution in ice clouds and the processes responsible for the observed variation in crystal shapes. Previous studies have used a variety of techniques to grow ice crystals under simulated tropospheric conditions, but each experiment seems to give different normal growth rates (i.e., rate of face advancement normal to itself), even under similar conditions and using similar techniques. For examples at −15 ∘C, see Beckmann and Lacmann (1982), Lamb and Scott (1972), Sei and Gonda (1989a), Sei and Gonda (1989b), Gonda et al. (1994), and Libbrecht (2003); for examples at −30 ∘C, see Kobayashi (1965), Sei and Gonda (1989a), Gonda and Koike (1983), Gonda et al. (1994), and Libbrecht (2003). What causes this variability?
At low supersaturations, some of the variability is likely due to crystal defects as the ice-nucleation process is expected to leave each crystal facet with a different defect structure. However, as described in Nelson and Knight (1996), the variations may also be caused by potential instrumental artifacts. For example, in growing crystals on a flat substrate (e.g., Shaw and Mason, 1955; Hallett, 1961; Lamb and Scott, 1972; Beckmann and Lacmann, 1982; Sei and Gonda, 1989a), the substrate–crystal edge could be a preferred site for new-layer nucleation that does not exist without the substrate. Such substrates can also have epitaxial-induced strain effects (Cho and Hallett, 1984a, b), and the temperature gradients in the crystal can greatly reduce the growth rates over those predicted assuming equal temperatures of crystal and substrate (Nelson, 1993). Growth on fibers can have smaller, yet still significant, substrate effects. For example, images of small crystals grown on a thin fiber by Kobayashi (1958, 1961) show the fiber often exiting at a crystal corner or edge, which could be showing substrate-induced control over the crystal aspect ratio, but without the capability of rotating the fiber, one cannot rule out the possibility of fiber influence on the other cases as well. Similar questions regarding control of habit by the fiber can be seen in the small crystals in Bailey and Hallett (2004). When the crystals grow away from the fiber, as in the larger crystals in Bailey and Hallett (2004), growth may occur on only one side of the fiber and the crystals may be close enough together to impede each other's growth rates through the vapor-density field (Westbrook et al., 2008). Neither effect typically occurs for cloud crystals as the number density, during the vapor growth phase, typically ranges from 0.1 to 10 crystals per cubic centimeter (Mace et al., 2001; Kärcher and Strom, 2003), so average crystal–crystal separation is typically millimeters (or more) in scale. In addition, many apparatuses have temperature and supersaturation gradients within the chamber that make calculating the precise thermodynamic conditions difficult.
Several support-free methods were developed that reduce the potential for crystal–substrate interaction effects, but they can have other issues. In vertical wind tunnels and cloud chambers (i.e., Yamashita, 1973, 1974; Gonda, 1980; Takahashi and Fukuta, 1988; Takahashi et al., 1991), it is difficult to control the growth conditions precisely. Also here the crystal seeding, which typically occurs near the top of the chamber, leads to crystal fall motions that makes it difficult to continuously monitor the growth of individual crystal faces throughout the experiment. Electrodynamic levitation methods avoid potential crystal–crystal interaction effects, but the rapid motion of the crystals makes high-clarity imaging from a variety of crystal orientations difficult (Swanson et al., 1999; Bacon et al., 2003; Magee et al., 2006; Harrison et al., 2016) . All support-free methods have the potential disadvantage of ventilation factors that can enhance the crystal growth rates of oscillating crystals. Finally, wall-ice formation is a general concern in most laboratory experiments because it can lower the supersaturation (S) in the chamber and be unnoticed by an experimenter without an independent method of following S throughout the experiment.
To observe crystal growth at low temperatures while minimizing such instrumental shortcomings, we built a new instrument called capillary cryostat 2 (CC2). The design is an improvement over the capillary device in Nelson and Knight (1996), hereafter CC1, in which the ice crystal grew at the tip of an ultrafine glass capillary. Like the earlier device, CC2 practically eliminates temperature gradients, greatly reduces substrate effects, and allows all crystal faces to be monitored in a highly controlled, uniform environment. But, in addition, CC2 allows experimenters to follow the growth of, and possible interactions between, several crystals growing under identical conditions. It has two vapor-source chambers for making rapid supersaturation changes and for independent temperature and supersaturation control, and it has an associated vacuum system and gauges for control of the growth chamber air pressure. To date, CC2 has proven useful for studying the formation and behavior of air pockets in ice (Nelson and Swanson, 2019).
The design is basically a box within a box within a box (see Figs. 1 and 2). At the center is the 13 cm ×7.5 cm × 20 cm experimental chamber (EC) with its three chambers – the growth chamber is near the middle with vapor-source chambers both above and below. Figure 2 shows the growth chamber (GC) containing the growing or sublimating crystals of interest. The crystals sit on the ends or sides of three well-separated, pure-silica glass capillaries that extend down about 3 cm from the ceiling of the GC. Individual or multiple ice crystals can be suspended on each capillary. The upper and lower vapor-source chambers (VSCs) control the humidity within the GC. A sliding valve blocks one or the other VSC from the GC. An actuator mechanism attached to the sliding valve allows the experimenter to select which VSC is actively setting the GC humidity. Inside each VSC is a vapor source (VS) mounted on top of a thermoelectric cooler (TEC) module. Each VS is typically filled with frozen high-purity liquid-chromatography (HPLC) water. The supersaturation or subsaturation conditions inside the VSC are controlled by the temperature (TVS) of the VS. Surrounding the EC is an optically clear liquid–cryogenic fluid (typically methanol or a silicone fluid) contained within the bath box. The bath box itself is surrounded by the vacuum-shroud box. A turbomolecular pump typically evacuates the vacuum-shroud box to less than 10−5 Torr to isolate and insulate the EC from the laboratory environment. The EC, bath box, and vacuum-shroud box have silica windows front and back for illumination and imaging of the ice crystals. The imaging is done (at a working distance of about 80 mm) with a choice of back or front illumination and Nikon SLR cameras attached to Leica telemicroscopic zoom lenses. The EC and VS temperatures and pressure are monitored using a LabView data acquisition program, HP switch/multiplexer, and a 5 1/2 digit digital multimeter.
2.1 Instrumental issues addressed by CC2 design
We now describe how the CC2 design addresses several potential instrumental issues and how the capillary method can be used to obtain reliable data sets.
2.1.1 Temperature stability and gradients in the instrumental chamber
Small changes in crystal temperature can have large effects on ice crystal shape. Near liquid-water saturation, a few ∘C change near −8 ∘C changes long columns into thin tabular crystal forms (Takahashi et al., 1991). At low supersaturations, small temperature changes may significantly affect facet-normal growth rates since this rate can depend exponentially on the vapor-source temperature TVS (via its control of supersaturation) when the face is free of new-layer-generating defects (i.e., perfect faces, which were commonly found in CC1).
The stability of two temperatures, that of the experimental chamber TEC and that of the ambient air surrounding the crystal Ta, is important. The temperature stability of the EC is set by (1) the cryogenic refrigerant temperature control from a Neslab ULT-80 bath-circulator unit (temperature stability exceeds 0.1 ∘C over a 3 h period), (2) the room temperature stability, and (3) the large thermal mass of the EC (which smooths short-term temperature fluctuations via its roughly 15 min response time). Specifically, the EC was milled from a single block of tellurium copper and then nickel plated on the outside and gold plated inside for surface uniformity and to reduce the potential for oxide formation and contamination. Temperature variations in Ta will be due to temperature fluctuations and gradients in the internal walls of the GC. A time-series measurement of the 12 thermistors buried in the walls of the EC shows that the maximum fluctuation of the EC block is less than 50 mK over a 1 d period. We worried that the TECs might induce small gradients in the EC temperature but find no measurable additional thermal gradient in the GC when the TEC current ITEC<0.5 A – a value much larger than is needed for growth or sublimation conditions in a cold cloud. For a typical 11 h period, the maximum gradient across the EC block was less than 10 mK. So we are comfortable assuming that TEC=Ta to within a few millikelvin.
2.1.2 Precise control and stability of supersaturation around the crystal
While chamber temperature is relatively straightforward to measure and control, precise supersaturation measurement within a chamber along with measurement and control near the surface of a growing crystal is much more difficult. In any experiment we are concerned with both spatial and temporal gradients in the growth chamber supersaturation SGC. The gold standard for crystal-growth experiments involves two parts: a stable, controlled, and gradient-free SGC within the experimental chamber, and the measurement of the supersaturation near the surface of the growing (or sublimating) crystal, Sa, at the same time the crystals are growing (or sublimating). No ice crystal growth rate experiment to date satisfies these two conditions, but the method used in CC2, although not yet at the gold standard level, has enhanced thermal stability and a relative gradient-free nature that is a large improvement over previous methods.
Within CC2 all crystals grow simultaneously within an approximately 1 cm3 volume near the center of the GC. Simultaneous growth in a chamber without gradients means all crystals experience the same thermodynamic conditions. Sequential growth experiments cannot claim all crystals experienced the same thermodynamic conditions without a direct, local measurement of Sa. Previous experiments have assumed gradient-free conditions and in this case the ambient supersaturation at the crystal surface given in percent by
where Neq is the equilibrium vapor density in molecules per cubic meter (molecules m−3) and Ta is the temperature at the crystal surface. It is possible that other factors affect Sa, so in future experiments we will test the use of this equation. Other than the effect of thermal gradients within the EC (which are minimal as discussed above), the possible gradients in SGC within the GC can come from three potential sources: (a) thermal instability of TVS, (b) gradients within the VS itself, and (c) the presence of other ice crystals within the EC.
- a.
Thermal stability of TVS. The numerator in Eq. (1) is to first order proportional to the ice surface-temperature elevation . Thus, the relative uncertainty in supersaturation . With feedback TEC temperature control the VS temperature standard deviation ΔT is typically about 3 mK (the variation observed over several hours). This gives an estimated uncertainty in Sa of about 0.03 %. To understand the meaning of 0.03 % supersaturation, consider that an ice crystal growing at the maximum possible rate at −30 ∘C at this supersaturation is about 60 µm h−1 in a pure vapor (from the Hertz–Knudsen equation, e.g., Eq. 1, of Holyst et al., 2015; this equation assumes a rough surface, or α=1), then we expect the uncertainty to add about 0.2 µm h−1 additional growth to a 100 µm diameter spherical crystal in an atmosphere of air (Maxwell's expression or Hertz–Knudsen divided by the vapor-diffusion impedance). This uncertainty is less than the measurement resolution over several hours growth.
- b.
Thermal gradients within the VS. Each VS consists of a gold-plated copper disc, machined such that the top portion forms a cup shape that holds up to 2 g of water. Each VS has an exposed surface area of about 6 cm2. As the typical grown crystal is less than 0.05 cm across, the VS surface area is usually more than 1000 times larger than the crystal being studied, and, in the absence of other crystals or wall ice, Sa=SVS. This supersaturation is determined by the vapor-source temperature, which is controlled by setting ITEC. The design improves upon that used in CC1 (Nelson and Knight, 1996), which used the solute method alone, although solutes can be used in the VSC as well.
Consider now the temperature difference between the thermistors imbedded in the VS cup TVS and the surface of the VS ice TVSS. In general, we need this difference to be much less than ΔT, the set temperature rise of the VS cup over that of the environment; otherwise, our inferred supersaturation will be too high. To estimate , assume a steady state in which the rate of latent-heat loss at the source-ice surface (during a crystal-growth experiment) equals the sum of the (i) rate of heat conduction through the VS ice plus (ii) the heat loss from the surface to the surroundings. Consider just (i) first. Assuming that the number of molecules of water leaving the VS ice per second equals the number depositing on the observed crystal on a capillary (i.e., steady state), and using the Clausius–Clapeyron equation, this ratio can be shown to equal , where R is the surface-averaged normal growth rate of the crystal (i.e., normal to the surface), L is the average thickness of the VS ice, Ar is the ratio of areas between the observed crystal and the VS ice, kB is Boltzmann's constant, β is the latent heat per molecule normalized by kBT, Ω is the volume per molecule in solid ice, and λ is the thermal conductivity of ice. This last factor in parenthesis involves only material properties and equals about 1×108 s m−3. Using R=5 µm h−1, Sa=0.01 (1 %), L=1 cm, and , this ratio is 10−4. As these are roughly maximum values, we can generally assume the temperature offset to be negligible. (Also, as the factor depends on L∕λ, the influence of temperature gradients in the vapor-source cup itself should be negligible due to the tellurium copper having a thermal conductivity nearly 200 times larger than that of ice (and L being smaller)).
Concerning (ii), the heat loss to the surroundings, there are four to consider: conductive loss from the ice to the air, conductive loss from the VS cup to the cup holder, convective loss to the air, and radiative loss to the walls. For the conductive loss to the air, we can estimate the effect by equating the heat flow through the ice to the heat flow through the air via conduction. The resulting temperature shift in the ice divided by (TVSS−Ta) (i.e., ΔT less the temperature shift in the ice) will equal the ratio of the conduction distances times the inverse ratio of the thermal conductivities. The first factor is about 1∕3, and the second is about 0.015∕2.1. Thus, this temperature shift is only about 1∕300 of that of ΔT and can be ignored. The conductive loss from the VS cup to the cup holder would create gradients in the cup holder. However, the thermal conductivity of the Te-Cu cup is about 4000× that of the rubber O-ring holding it in place and nearly 40 000× that of the air gap. Thus, even though this gap is small, we can neglect the resulting thermal gradients in the cup.
The heat loss can also be convective if the vapor source is heated for growth experiments and requires a critical temperature difference between the ice surface and the top wall of the VSC. (If we instead use solute, as was done in CC1, then the issue cannot arise.) For growth experiments the resulting convection may significantly cool the ice surface, so our aim is to stay below the critical temperature. If we assume that the onset of convection occurs with a Rayleigh number of about 1500 (following Saxena et al., 2018, where this number is proportional to the cube of the chamber height, the temperature difference between wall and source, and properties of the air), then, for our chamber and operating temperature, staying below this Rayleigh number requires that the ice surface lies within about 0.5 K of the wall temperature. Finally, the influence of the radiative heat flux is considered in Sect. 2.1.4 below.
- c.
The presence of other crystals. We consider two cases separately: a few crystals very near the monitored crystal of interest and a large number of crystals on the wall as frost. The later case is discussed in Sect. 2.1.3 below; here we focus on the former. When other crystals are nearby a crystal of interest then Sa can be less than SVS even when the area of the VS ice surface greatly exceeds that of any other ice in the system. In the case of the simultaneous growth of several observed crystals, the supersaturation near an observed crystal may be reduced due to the proximity to other crystals. Westbrook et al. (2008) estimate a 3-fold reduction in growth rate for close crystals along a fiber, a situation that was simulated in Bailey and Hallett (2004). At larger crystal separations, the effect has not been determined, but the 1∕r dependence of the vapor-diffusion field away from a crystal suggests that, to ensure a crystal-proximity effect of less than 10 %, the crystals should be separated by nearly 10× their mean dimension. We find (result reported elsewhere; Swanson, 2019) about a 30 % reduction in the facet-normal growth rate (caused by the vapor uptake by the neighboring polycrystal crystallites) for a prismatic crystal growing on top of a polycrystal as compared with similar prismatic crystals growing and separated by hundreds of micrometers.
In CC2, the three capillaries are on nonparallel axes, and thus their separations are adjustable, allowing measurement of the proximity effect. They are easily set to be several centimeters apart, which is more than 100× their typical dimension of about 100 µm. For the growth of three ice crystals each less than 500 µm in size and separated by least 5 mm, then we can assume Sa=SVS to within 10 % of SVS.
2.1.3 Frost formation on the experimental chamber walls
Frost can form on chamber walls and, if the area is large, can uptake a significant fraction of the source vapor. A highly controlled vapor-source supersaturation, SVS, does not necessarily set the ambient supersaturation, Sa, at the center of the chamber where the crystals are growing if there is frost or condensate growing on the wall. Such frost is a particular problem when growing crystals sequentially because any measured difference in their rate or habit may not be inherent but instead be due to their being affected more or less by frost. To reduce this issue, the CC2 windows allow observation of all surfaces inside the GC and VSC. But it is possible that this ice is so thin as to make it nearly invisible to the eye. An important factor is the relative surface area of the frost versus that of the VS ice. If their areas and thicknesses are the same, then the vapor density in the EC would be midway between the equilibrium values for the VS ice and the chamber walls. However, the effect in practice would likely be worse because the frost layers would likely be much thinner than the VS ice, pushing the vapor density closer to the equilibrium value for the walls due to the temperature-gradient effect in Sect. 3.1.2 above.
The windows on the sides of the VSC provide for easy detection of large frost crystals and, once noticed, that chamber can be immediately sealed off. In practice, we find that when frost crystals first appear, they are in the VSC, relatively close to the source ice. For the experiments described here, the VSC and GC internal walls were continuously monitored for frost. If frost began to form in the attached VSC, then the sliding valve was changed to disconnect the VSC from the GC, and the TEC in the other VSC was set to maintain the desired humidity in the GC. The ability to isolate one VSC from the GC when frost first occurs and to switch to a frost-free VSC allows us to continue to grow the crystals for long periods at near-constant Sa conditions. To clear the frost off the walls of a VSC, we first evacuate the VSC and set its TVS to at least 10 ∘C below Ta. The frost typically left the walls within about 30 min under these conditions. For the conditions of the experiments described here, typically no frost was observed on VSC walls for at least 6 h. The data set here was collected before frost started to form in the GC walls.
In a future paper, Swanson and Nelson (2019), we report results from droplet evaporation measurements done simultaneous with the crystal growth measurements. Measuring the evaporation rate of pure water droplets during crystal growth does give a direct and independent measure of Sa near the growing crystals surface. For these experiments one capillary is used to hold the evaporating droplet while the other two hold the growing or sublimating crystals. Results from these experiments demonstrate that accurately predicting Sa at a chamber center requires careful calibration. For the results reported here we are concerned with facet-normal growth rate differences for crystals growing simultaneously under the same thermodynamic conditions. In these experiments the ice crystal surface area is small compared with that of the VS and no wall ice was present. We continuously measure TGC and TVS and the enhanced thermal stability, and control within CC2 gives us confidence that, within the variations caused by the measured temperature gradient across the EC, Sa is to good approximation SVS within that 1 cm3 volume that contains the capillary tips. In future experiments, where a detailed comparison with crystal growth models is the goal, Sa calibration measurements will be made along with the growth rate measurements.
2.1.4 Radiative heating effects
Radiative heating can occur in two places. First, consider thermal radiation between the VS surface and the VSC wall. The VS–GC temperature difference is typically less than 3.5 ∘C – the value needed to achieve liquid-water saturation at −40 ∘C. Due to the relatively small temperature differences involved, and also the very low emissivity of the gold plating of all interior walls, such a radiative heat transfer has a negligible influence on the VS surface temperature. Second, consider thermal radiation between the ice crystals and sources outside the windows. The ice crystals sit at Ta, but the thermal link is weak due to the crystal being surrounded by air. Considering the different materials viewed by the crystal (windows, walls, and circulating fluid), determining the influence of radiative heating on ice-crystal temperature is best handled as an experimental issue. We examine this issue by monitoring the crystals in the growth chamber under controlled conditions in which the windows are alternately exposed or covered with low-IR-emissive material. When we have tried this test, we observed no IR heating effects on the normal growth rates.
2.1.5 The effect of the capillary on crystal growth
The capillary holds the crystal steady, allowing clear imaging and viewing from several angles. Also, as the crystal starts at the capillary tip (typical case), one can usually measure the advance of all parts of the crystal with respect to the fixed capillary tip. Although these features are advantages of the method, the capillary can promote growth on one, two, or three faces.
Consider the examples in Fig. 3. The images show two crystals nucleated and grown at the same time but on different capillaries – Fig. 3a and b show the front capillary Cf and Fig. 3c–f show the back capillary Cb. The crystal on the left (Fig. 3a and b) is nearly a hexagonal prism, but, by measuring the distance from the capillary tip along the surface normal, one finds that the top right prism face has grown about 25 % faster than the others. The capillary is seen exiting the crystal at the vertex between this face and the top left prism. Subsequent images (not shown here) show the crystal growing larger but the capillary remaining at this vertex. As the vertex stays at the capillary, these observations show that the capillary determines the relative normal growth rates of these two faces. The rotated view in Fig. 3b shows that the two basal faces have nearly equal normal growth rate, and neither is contacted by the capillary. Thus, the basal faces appear unaffected by the capillary. So, of the eight crystal faces, two are directly compromised by the capillary, but six are not directly influenced. In using data from this crystal, we must consider the influence that the faster growth on the top two prism faces has on the vapor-diffusion field near the other faces and the crystal temperature. In this way, the influence of the capillary may be overcome by crystal-growth modeling. The exact method will be described in a later publication.
The crystal on the back capillary, in Fig. 3c–f, shows further limitations and features. In this case, we cannot see the location of the capillary inside the crystal and must instead estimate its location by examining the growth sequence starting from nucleation (not shown). Nevertheless, the basal-side views in Fig. 3c and f show that the capillary does not contact the basal faces (except possibly from the ice interior), yet one basal face grew faster than the other. Moreover, the views in Fig. 3d and e show that this crystal has two opposite prism faces that are much larger in area and thus have much lower growth rates. The overall shape is similar to that proposed for crystals that generate the Parry arc (Westbrook, 2011).
Finally, consider the crystal in Fig. 4. In this case, the capillary exits at a corner, thus contacting one basal face and two prisms. As in other cases like this observed during both the CC2 and CC1 experiments, the crystal does not start this way, but once the corner reaches the capillary it always remains there (at least under constant conditions). Why does this occur? Clearly, the introduction of an interior glass-ice corner should promote new-layer nucleation. If such a site is the most active on a given face, then that site will increase the normal growth rate of the face. Moreover, if this capillary is tilted towards a neighboring face, then the relative increase in growth rate over that neighboring face will bring the edge between the two faces closer to the capillary. Once the edge reaches the capillary, it will stay there because the same promotion of layer nucleation will occur on the neighboring face. In three dimensions, if the capillary also tilts towards a third face, this process will bring that face to the capillary until the capillary exits at the common corner. However, if the layer-nucleation-promotion effect is relatively weak, then supersaturation gradients or a surface defect site may produce more rapid layer nucleation elsewhere, such as at a nearby crystal corner. Thus, there are cases where, despite such promotion of layer nucleation, the face growth is controlled by a more active site, making the capillary influence irrelevant. For example, if the capillary exits the crystal from near the face middle, it will likely lie at a lower-supersaturation region, with the more active step-generation site instead being at the corner. In such a case, the capillary may have a small local influence but not influence the normal growth rates of the faces. These considerations also apply to crystals grown not at the tip but midway along a capillary or any fiber. This explains why, for example, in previous high-supersaturation experiments, the rapid-growing parts of the crystal are away from the fiber (e.g., Nakaya, 1954; Kobayashi, 1958; Bailey and Hallett, 2012).
Occasionally, we observe indications of different influences from the capillary. For example, the crystal can appear to avoid contact with the capillary. This appears to be a vapor-shielding effect because it only occurs when the crystal size is within a few diameters of the capillary tip and only occurs where the crystal contacts the capillary. Other parts of the crystal are unaffected, and the effect vanishes when the crystal grows larger. Another effect that can occur is rapid growth up the capillary in which the growth appears as smaller crystals of the same orientation. It is possible that this crystallization may be a result of thin-film crystallization on the glass capillary after a crystal nucleates at the tip. Both of these influences should be smaller with smaller-diameter capillaries and may also be reduced with suitable coatings. Finally, within the ice just adjacent to the capillary (within a few capillary diameters), the interface may create strain effects in the ice. To date, we have not seen evidence of such effects, but they remain a possibility.
Thus, the capillary influence on new-layer production can be irrelevant in some cases and may be overcome using modeling in other cases but should always be examined. Acknowledging this influence has two additional benefits. One, we may use it to study the nucleation process itself. Two, we can recognize the effect in other studies and realize that the resulting data may not be reliable. In future experiments, we plan to research these effects and develop strategies for quantifying their influence.
Finally, we describe a case in which we nucleated crystals using a Snomax–water solution1 and grew them for several days at low temperature and low supersaturation. Before insertion of the crystals the GC was prepared as follows. (a) The internal GC walls were washed with acetone, ethanol, and finally with HPLC water. (b) After window cleaning and reassembly, the GC was flushed for over an hour with dry nitrogen and then the cooling began with the ULT-80 set to 0 ∘C. (c) The VS cups were loaded with HPLC water and each TEC was set such that TVS remained about −10 ∘C below Ta. (d) A slow cooldown was then initiated to the experimental temperature. Keeping the VS frozen with the above procedure avoided fogging of the GC windows and reduced the possibility of ice forming on the inside walls of the EC. Once the desired Ta was established, then TVS was set to produce the desired supersaturation SVS and the capillaries were inserted into CC2. Unlike the nucleation method used for the previous crystals, this one produced several crystals along each capillary. We report just on the ones at the ends of capillary Cf and Cr.
All crystals began the experiment as near-identical ∼20 µm diameter liquid droplets of a Snomax-HPLC water solution. The 5 µm diameter capillaries were dipped into a Snomax solution made similar to Wood et al. (2002) and then inserted into CC2. The experiment was broken into two phases: part A (which lasted 45 h; h to t=0) directly followed by part B (which lasted 47 h; t=0 to t=47 h). For the entire 92 h the growth chamber temperature Ta was held at −29.8 ∘C. During part A, the crystals grew from the 20 µm frozen droplets into a variety of crystal shapes. During part A the crystals grew for 28.5 h with SVS∼5 %, followed by 9.5 h of no growth with % (after which some facet edge rounding was observed) and by a 7 h growth period with SVS∼2 %. During part B SVS was maintained such that ∘C, resulting in SVS=5 %.
Figure 5 shows the crystals at both t=0 and t=47 h. The images have been magnified and crystal sizes are shown in Fig. 6. We define a(t) as the growth normal to the prism face and c(t) as the growth normal to the basal face. The value of a and c are diameters in these two normal directions. (Thus, they include measurements normal to faces potentially influenced by the capillary as discussed above.) The aspect ratio . In the lower image of crystal Cf, we see that the upper basal face, which is contacted by the capillary, grew faster than the lower facet. But for crystal Cr, the lower image shows the two basal faces to have nearly the same normal growth rate, and neither is contacted by the capillary. Thus, for the basal faces, Cf has one that is possibly affected by the capillary, but Cr appears unaffected by the capillary.
Since at least the publication of Gonda and Koike (1983), we have known that prismatic crystal aspect ratios can be different for similar growth conditions. The case here is consistent with this finding. In particular, we also find that the crystals in Fig. 5 responded to Ta and Sa in different ways. Comparing crystal shape at the beginning (AR0) and end (AR47) of part B, we find that for Cf, , while for Cr, . This illustrates that, under the same conditions, a crystal can grow more plate-like at the same time another crystal is growing more column-like. (Concerning the capillary influence, the potential promotion of growth on one basal for Cf and one or two prisms for Cr oppose this trend. Thus, it is likely that this finding is not due to a capillary influence.) The relative growth rates shown in Fig. 6 for the two crystals are also quite different. Both crystals ended part A of the experiment with tabular habits. But the thinner plate (Cr with AR0=0.46) grew during part B to be more columnar, while the thicker plate (Cf with AR0=0.72) grew to be more tabular. This behavior is also clear from the relative growth rates (indicated generally by the slope of the curves) in the and directions. The curves in Fig. 6 are from a simple two-parameter fit to the data set. We see here that a simple t1∕2 parameterization (where t is the time) for both c(t) and a(t) fits well. With or without capillary influence the growth of both crystals is well described by a similar parabolic growth model as has been found for spherical droplets (Fukuta and Walter, 1970). A more detail discussion of these results is reported elsewhere (Swanson, 2019).
Crystals in previous experiments were often grown sequentially, making it difficult to ensure the exact same conditions were reproduced. Moreover, in many cases, experimenters were unable to follow the development of each crystal, and each crystal face, throughout the growth process. In our experiments, several well-separated crystals can be grown simultaneously and experience the same thermodynamic conditions. The crystals remain prismatic during the multiday growth period, but large variations in AR and growth rate in the and directions are observed. Such variations in AR turn out to be typical for prismatic crystals (Bacon et al., 2003; Swanson, 2019) and show control of growth shape is likely via defect-driven surface processes. By using CC2 to measure the growth of individual crystal faces for a wide range of conditions, we will be able to quantify the variability of facet-normal growth rates.
We have built a new instrument to measure high-precision growth rates of ice crystals and droplets at temperatures down to −60 ∘C. Preliminary observations have shown the advantage of following individual faces of multiple crystals in the CC2 apparatus. With CC2, thermodynamic control is much tighter than has been reported for previous instruments. The ability to grow multiple crystals under identical thermodynamic conditions, starting from their nucleation and following each face over long time periods, as well as being able to track and remove frost during the experiment, gives us confidence that differences in observed behavior can be distinguished from instrumental effects. We expect the method will be complementary to our substrate-free electrodynamic balance methods (Bacon et al., 2003). To check these results, future experiments that combine both techniques are planned.
Data are available upon request.
BS and JN designed and assembled the new instrument. BS and JN designed the experiments and carried them out. BS developed the LabView data acquisition code, made the figures, and prepared the manuscript with contributions from JN.
The authors declare that they have no conflict of interest.
We thank Chris Foreman at Foreman CNC Machining Ltd.; Dave Shatford at Met-All-Fab in Sidney, BC, Canada; and Glenn Ryan at Limited Productions Inc. Bellevue, WA, for assistance with the fabrication of the instrument. We thank Hawk Ridge Systems for providing a copy of SolidWorks CAD software. We thank Mary Laucks for helpful comments on this paper.
This research has been supported by the National Science Foundation grant AGS-1348238 and by the Laucks Foundation, which kindly supplied research funds, equipment, and laboratory space.
This paper was edited by Murray Hamilton and reviewed by three anonymous referees.
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Snomax is a common ice nucleant used for making artificial snow at ski resorts and is a product of York International, Victor, New York 14564.