Vol. 46 No. 4 SCIENCE IN CHINA (Series B) August 2003 Effects of magnetic fields on HCFC-141b refrigerant gas hydrate formation LIU Yong ( ), GUO Kaihua (), LIANG Deqing () & FAN Shuanshi ( ) Guangzhou Institute of Energy Conversion, Guangzhou 510070, China Correspondence should be addressed to Liang Deqing (email: liangdq@ms.giec.ac.cn) Received December 20, 2002 Abstract Low-pressure refrigerant gas hydrates have brilliant prospects as a cool storage medium for air-conditioning systems. Intensive effects of some specific magnetic fields on the formation process of HCFC-141b refrigerant gas hydrate are depicted experimentally. Under influence of these specific magnetic fields, the orientation and growth region of gas hydrate are altered; induction time of hydrate crystallization can be shortened extremely, and it can be shortened to 40 min from 9 h; hydrate formation mass can be enhanced considerably, and hydration rate can arrive at 100% in some instances. Meanwhile, the relations of induction time and hydration rate changed with magnetic field intensity are depicted, and some elementary regulations are found. Keywords: magnetic fields, gas hydrate, induction time, hydration rate, cool storage. DOI: 10.1360/02yb0178 Gas hydrates are crystalline compounds formed (usually above 0) by water reacting with some gases or volatile liquids (hydrate former). Guest molecules, such as gas or volatile liquid molecules, are enclosed firmly inside the host cavities and act with water molecules in weak van der Waals force. Gas hydrate usually includes natural gas hydrate, refrigerant gas hydrate and CO2 gas hydrate. Refrigerant hydrates can be formed above 0, and their crystallization is similar to the ordinary ice, so it is also called “warm ice”. Because the phase change temperature of the refrigerant gas hydrate is between 5 and 12 and with a formation heat which is equal to that of ice, it can be a substitute of ice as cool storage medium for air-conditioning systems. The performance and applicability of the gas hydrate cool storage system can have a great superiority to that of the ice[1,2]. To develop a cost-effective cool storage system for air-conditioning, a lowpressure gas hydrate cool storage medium should be employed. Unfortunately, those low-pressure refrigerants, such as those of R11 and HCFC-141b, are comparatively inactive in gas hydrate formation. The diffusing speed of the liquid interface is very slow and the phases are scarcely mixed. Consequently, one has a very long induction time of reaction and a quite slow growth speed, even with surfactants and nucleate seeds added[3 ü5] . Therefore, if refrigerant hydrates are employed as a medium of thermal energy storage in engineering application, a rapid and uniform formation of gas hydrate will be the key for technical success. 408 SCIENCE IN CHINA (Series B) Vol. 46 Electrical and magnetic stationary fields affect significantly the equilibrium formation conditions and growth kinetics of ice from water. Currently, there are no reliable experimental and theoretical data about the effect of these fields on a hydrate formation. Makogon[6] indicated the effect of a stationary magnetic field on density and structure of hydrates. Denser hydrates with a more regular structure formed under the influence of magnetic field. At present, there are no literatures about the effects of magnetic fields on refrigerant gas hydrate formation. In this paper, it is found through a set of experiments that some specific magnetic fields can considerably affect the formation of HCFC-141b refrigerant gas hydrate. 1 Experimental 1.1 Experimental apparatus This experiment was carried out on the experimental system of gas hydrates at a low temperature; and the experimental apparatus is vided in the literature[7,8]. The visualization hydrate reactor in the magnetic field is composed of transparent glass container, airproof lid, magnets, iron wires and stainless steel fixing clip. The schematics of the reactors are shown in fig. 1. Inner diameter of the glass container is 22 mm, and the volume of that is 3.8×10−5 m3. Airproof lid is used to prevent refrigerant from volatilizing and outside impurity dropping into. Iron wires, 2 mm in diameter and 100 mm in length, which are fixed by stainless steel fixing clip, are distributed along the circle whose radius is 7 mm in the glass container. There are two kinds of magnets: one is 20 mm in diameter and 3 mm in thickness; the other is 45 mm in diameter and the thickness of it changes from 5 to 25 mm. The magnet whose diameter is 45 mm was put on the top of the reactor. Magnet, diameter in 20 mm, is firstly put on the bottom of the reactor, and then magnet whose diameter is 45 mm is put below it, and the magnetic intensity is adjusted by changing the thickness of magnet whose diameter is 45 mm. In fig. 1 (a), the bottoms of iron wires are attracted to the South Pole of the magnet. In fig. 1 (b), the bottoms of iron wires are attracted to the North Pole of the magnet. In fig. 1(c), the top of iron wires are attracted to the North Pole of the magnet and the bottom of iron wires are attracted to the South Pole of the magnet. Fig. 1. Schematics of the visualization reactors in the magnetic field. 1.2 Reagent and apparatus HCFC-141b was bought from AlliedSignal Company, and its purity is 99.5%. Doubly distilled water was used in this paper. Digital magnetic intensity meter was bought from Shanghai 4th Ammeter factory, and its precision is ±1%. Magnetic material is ND-FE-B, and it was manufac- No. 4 EFFECTS OF MAGNETIC FIELDS ON HCFC-141b REFRIGERANT GAS HYDRATE FORMATION 409 tured by Guangzhou Heshun Magnetic Material Factory. Glass container was made from GG17 material by Guangzhou Qianhui Glass Instruments Co., Ltd. Electronical balance was purchased from Beijing Satorius Instruments Co., Ltd., and its precision is 0.01 g. 1.3 Experimental process An important physical characteristic of hydrate, which differs from that of ice, is that it can be formed above 0, therefore, the air bath has been set at 1. 12.5 g HCFC-141b refrigerant and 10 g water were respectively fed into the reactor, and then the reactor was put into the air bath. A continual focus digital video cameraPanasonic NV-DX100ENwas used to observe the HCFC-141b hydrate formation process. Induction time is defined as a period time that system goes through from the equilibrium to appearance of the first visual hydrate, and it is a very ordinary method for studying hydrate formation via visualization in the static state experiments[9]. And hydrate is an ice-like solid, so it can be departed from liquid. According to the practical sense of cool storage for air-conditioning, the mass of hydrate was weighed after it has been put into the air bath for 8 h. 2 HCFC-141b hydrate formation photos 2.1 Morphology of R141b’s formation process under no influence of magnetic field Zhao et al.[7,8] have studied the HCFC-141b hydrate formation under no influence of the magnetic field at 0.5. It is found that the hydrate growth orientation is that hydrate crystals take precedence to grow into the water, and there is almost no hydrate in refrigerant region. In this paper, hydrate formation in no magnetic field is observed when there are only four iron wires and no magnets in the glass container. It is found that the characteristics of hydrate formation are similar to that presented by Zhao et al.[7], as shown in fig. 2. The density of HCFC141b is larger than that of water, thus, water can float on the HCFC-141b liquid, as shown in fig. 2(a). A slim layer of hydrate is firstly formed on the surface of iron wires and interface between Fig. 2. Morphology of R141b’s formation process under no influence of magnetic field. 410 SCIENCE IN CHINA (Series B) Vol. 46 water and refrigerant after about 9 h, then refrigerant molecules diffuse into water to form new hydrate through the formed hydrate layer. Finally, hydrate only grows in water phase in about 16 h, as shown in fig. 2(b)—(d). 2.2 Morphology of R141b’s formation process under influence of magnetic field It is observed through experiments that the hydrate can extend its growth region in the magnetic field, and it can grow not only in water but also in refrigerant region, as shown in fig. 3(a). A slim layer of hydrate is firstly formed on the surface of iron wires and interface between water and refrigerant after an induction time, and the hydrate growth orientation is that it takes precedence to grow into water region. After 1 h 35 min, the formed hydrates have occupied the whole water region in the main. In the later processes, hydrate crystals then continually grow into the refrigerant phase. Because water can diffuse into the refrigerant phase through the hydrate layer, which illuminates that the growth region of hydrate will not be restricted in water phase, and hydrate crystals can also grow in refrigerant phase in the magnetic field. Fig. 3. Morphology of R141b’s formation process under influence of magnetic field. It can be observed from fig. 3(b) that hydrate takes precedence to grow into the refrigerant region after it is firstly formed on the surface of iron wires and interface between water and refrigerant. Then refrigerant can diffuse into water to form new hydrate through hydrate layer after the formed hydrates have occupied the whole liquid HCFC-141b region in the main, but there is little hydrate in water phase in 8 h. Contrasted to the result of the above-mentioned experiments in this paper and experiment in literature[7], it is found that hydrate growth orientation can be altered under the influence of magnetic field. Crystal growth is a process of discontinuity and nonuniformity in space. Crystallization takes No. 4 EFFECTS OF MAGNETIC FIELDS ON HCFC-141b REFRIGERANT GAS HYDRATE FORMATION 411 place only in interface between solid and liquid. When crystals grow from rich environmental phase, solidification does not take place until the phase change heat is transported from the interface. While crystals grow from the thin environmental phase, the reaction does not proceed until growth element is transported to the interface from other places of the growth system, which is called the transportation effect of crystal growth[10]. There are such characteristics in the hydrate formation, namely crystal nucleuses can be induced only while external molecules dissolved in water is saturated. Refrigerant molecules are not dissolved in water, so hydrate should be usually formed in the interface of water and refrigerant phase (rich environmental phase) where their molecules can sufficiently contact. Clathrate crystallization can be formed while refrigerant molecules are enclosed by water molecules in weak van der Waals force, then refrigerant molecules can diffuse into water to form new hydrate through the lacuna of the formed hydrate. However, it is found through experiments that hydrates do not crystallize in the interface of water and refrigerant (rich environmental phase) at first, and they are firstly formed in the bottom of refrigerant phase in the magnetic field, as shown in fig. 3(c). Water molecules can diffuse into the bottom of the refrigerant in the magnetic field, and hydrates are formed firstly on the surface of the fixing clip and iron wires in the bottom of refrigerant, then hydrates grow along the iron wires. Hydrates are also formed in the interface of the water and refrigerant after about 4 h, then they grow in both water and refrigerant phase, and hydrates in the bottom of refrigerant do not grow obviously at this time. Meanwhile, it is observed that there are the same regulations for the hydrate formation when magnets are distributed according to fig. 1(b). It can be observed from fig. 3(d) that hydrate crystals can be formed not only in the interface but also on surface of iron wires in water and refrigerant phase, and crystal nucleuses manifolded in the latter processes, then these dispersive crystal nucleuses grow continuously on the primary foundation. Although there are many crystal nucleuses, but hydrate formation mass is very little at last, and it can be seen in the hydrate formation curve in the latter of this paper. 3 Effects of magnetic intensity on induction time and hydration rate The chemical reaction relation of water and HCFC-141b refrigerant is that R+17 H2O ↔R17 H2O+∆H (formation heat) Molecular weight of HCFC-141b is 116.95 and that of water is 18, and 12.5 g refrigerant and 10 g water are put into the reactor in each experiment, therefore, the theoretical formation mass of the hydrate is 13.82 g according to the above-mentioned chemical reaction relation. The ratio of practical hydrate formation mass weighed in the experiment and theoretical hydrate formation mass calculated by the above-mentioned chemical relation is defined as the hydration rate. Whereas, the practical hydrate formation mass is a little larger than theoretical hydrate formation mass in very few instances, but the error between them is very small, and the hydration rate is considered as 100% in these instances. 412 SCIENCE IN CHINA (Series B) Vol. 46 If there are no magnets and only four iron wires in the reactor, it can be measured that the induction time is 8 h 47 min, and the hydration rate is 25.11% in 8 h. Meanwhile, the induction time measured by Zhao et al.[7] is 8 h 45 min.Whereas, under the influence of magnetic field, it is found that the induction time can be shortened to about 40 min and the hydration rate can arrive at 100% in many instances. The relations that induction time and hydration rate changed with magnetic intensity are shown in fig. 4. And No. 1, No. 2 and No. 3 curves represent that magnets are put onto the reactor respectively according to fig. 1(a), (b) and (c). Magnetic field intensities on the bottom of the reactor all change from 32.0×10−2 to 55.0×10−2, and that on the top of reactor in fig. 1(c) is always 31.2×10−2. And there are four iron wires fixuped by fixing clip in the reactor. Fig. 4. Effects of magnetic intensity on the induction time and hydration rate. (a) Effects on induction time; (b) effects on hydration rate. No. 1, No. 2 and No. 3 curves: Magnets are distributed according to fig. 1(a), (b) and (c) respectively. Relations that induction time changes with the magnetic field intensity are shown in fig. 4(a). It can be found from No.1 and No.2 curves in fig. 4(a) that regulations that induction time changes with the magnetic field intensity are the same although different magnetic poles are put on the bottom of the reactor. The induction time decreases with the increasing of magnetic intensity while magnetic intensity is less than 36.5×10−2 T, then it changes evenly when the magnetic intensity is between 36.5×10−2 and 52.0×10−2 T, and it will increase when the magnetic field intensity is larger than 52.0×10−2 T. The less induction time should be better for the hydrate formation. Therefore, magnetic intensity should not be larger or smaller. Meanwhile, it can be observed from the curves in fig. 4(a) that the induction time of each point in No. 1 curve is much smaller than that in No.2 curve, which shows that the South Pole of magnet has better effects on the hydrate formation than the North Pole. And it can be seen from No. 3 curve that the induction time on the first point of the curve is relatively large, but that on other points of curve always fluctuate between 40 min and 70 min, which shows that it will have better effects on the hydrate formation while magnets are put onto both ends of the reactor. The relations that hydration rate changes with the magnetic field intensity are shown in fig. 4(b). No. 2 curve shows that the hydration rate decreases with increasing of the magnetic intensity No. 4 EFFECTS OF MAGNETIC FIELDS ON HCFC-141b REFRIGERANT GAS HYDRATE FORMATION 413 when the North Pole of magnet is put on the bottom of the reactor. By contrasting No. 1 curve to No. 2 curve, it can be seen that the hydration rate of each point in No. 1 curve is much larger than that in No. 2 curve, which shows that the South Pole of magnet has better effects on the hydrate formation than the North Pole. Meanwhile, it can be seen that the hydration rate of each point in No. 3 curve is much larger than that in No. 1 and No. 2 curves, which illustrates that magnets put on both ends of the reactor have better effects on the formation process of hydrate than that put on the bottom of the reactor. According to the practical sense of cool storage for air conditioning, induction time should be shorter and the hydration rate should be much more. It can be observed from fig. 4 (a) and (b) that if magnets are put on both ends of the reactor, they have better effects on both induction time and hydration rate; and the South Pole of magnet has better effects on the hydrate formation than the North Pole. Relations that the induction time and hydration rate change with the number of iron wires are shown in fig. 5. No. 1 and No. 2 curves represent that magnets are put onto the reactor according to fig. 1(a). And No. 3 curve represents that magnets are put onto the reactor according to fig.1(c). Magnetic intensity is 41.0×10−2 T in No. 1 curve, that is 52.0×10−2 T in No. 2 curve, and that on the top and bottom of the reactor is respectively 31.2×10−2 and 52.0×10−2 T in No. 3 curve. In the above conditions, we can find the relations that induction time and hydration rate change with the number of iron wires while the magnetic intensity is invariable. Fig. 5. Effects of the number of iron wires on the induction time and hydrate formation mass. (a) Effects on induction time, (b) effects on hydrate formation mass. No. 1: Magnets are distributed according to fig. 1(a), and its intensity is 41.0×10−2 T; No. 2: magnets are distributed according to fig. 1(a), and its intensity is 52.0×10−2 T; No. 3: magnets are distributed according to fig. 1(c), and its intensity on the top and bottom of the reactor is respectively 31.2×10−2 and 52.0×10−2 T. It can be seen from No. 1 and No. 2 curves in fig. 5(a) that the induction time fluctuates with the increasing of the number of iron wires according to the same regulation although the magnetic intensity on the bottom of reactor is different. And the induction time at each point of No. 3 curve is obviously shorter and fluctuates evenly with the increasing of number of the iron wires contrasting to that of No. 1 and No. 2 curves. It can be observed from three curves in fig. 5(b) that the hydration rate increases with the increasing of the number of the iron wires. And hydration rate at each point of No. 3 curve is much more than that of No. 1 and No. 2 curves. It can be seen from the contrast of three curves in fig. 5 that there are more effects on both the induction time and hydration rate when magnets are dis- 414 SCIENCE IN CHINA (Series B) Vol. 46 tributed according to fig. 1(c), and the induction time will be shorter and hydration rate will be much more. 4 Effects of other magnetic fields on the hydrate formation Other different magnetic fields are imposed to the reactor and their schematics are respectively shown in fig. 6. There are only magnets on both ends of the reactor, as shown in fig. 6(a). Crushed magnets are put into the reactor, as shown in fig. 6(b). Magnets are put vertically onto the interface of water and refrigerant, as shown in fig. 6(c). Schematic of annular magnet is shown in fig. 6(d), and the reactor is put into the inner of a set of annular magnets. There are only four pieces of iron wires in the reactor, as shown in fig. 6(e). There are four pieces of brass wires in the reactor and magnets are imposed to both ends of the reactor, as shown in fig. 6(f). It is found through a set of experiments that the hydrate cannot be formed in 8 h under the effects of these magnetic fields. Magnetic fields in fig. 6(a)—(d) illustrate that magnetic fields cannot affect the formation process in all conditions. Magnetic fields in fig. 6(e)—(f) show that there is little effect on the hydrate formation although iron wires and brass wires can be served as the inducing nucleation factor. Meanwhile, magnets are put onto the reactor according to fig. 1, but when there is only a kind of magnet whose diameter is 45 mm on the bottom of the reactor, and iron wires are put into the reactor, it is found that the hydrate can be formed in few instances in 8 h and experiments cannot be repeated basically. At present, it has been tested that only when magnets on the bottom of the reactor are combination of different diameter magnets and then iron wires are magnetized by them in the reactor, the hydrate formation can be affected intensively. Maybe HCFC-141b molecules and water molecules are both pole molecules, and the specific magnetic field can be formed when iron wires are magnetized by magnets, which can affect the formation process of HCFC-141b gas hydrate intensively. Fig. 6. Schematics of other magnetic fields on the reactor. No. 4 EFFECTS OF MAGNETIC FIELDS ON HCFC-141b REFRIGERANT GAS HYDRATE FORMATION 415 5 Conclusions (i) In the specific magnetic field, hydrate growth orientation can be altered; growth region can be extended into both water and refrigerant phases; hydrate can be formed firstly in the bottom of refrigerant phase. (ii) The induction time of hydrate crystallization can be shortened extremely to 40 min from 9 h in the magnetic field. Meanwhile, magnetic pole, magnetic intensity and the number of iron wires all can affect the hydrate formation. (iii) The hydrate formation mass can be enhanced considerably in the magnetic field, and the hydration rate can arrive at 100% in some instances. Meanwhile, magnetic pole, magnetic intensity and the number of iron wires all can affect the hydration rate. (iv) Magnetic fields cannot affect the formation process of gas hydrate in all conditions. Specific magnetic field, which is formed when iron wires are magnetized by magnets, can affect the hydrate formation. Acknowledgements This work was supported by the National Natural Science Foundation of China (Grant No. 59836230), the Major State Basic Research Program (Grant No. G2000026306) and Superintendent Fund of Guangzhou Institute of Energy Conversion, the Chinese Academy of Sciences (Grant No. 07-20406). References 1. Guo, K. H., Gas hydrate and advanced uses in cool storage systems, Refrigeration (in Chinese), 1994, 47(2): 22ü28. 2. Guo, K. H., Shu, B. F., Yang, W. J., Advanced and applications of gas hydrate in thermal energy storage technology, in Proc. 1st Trabzon Int. Energy and Environment Symp., Vol.1 (ed. Ayhan, T.), Trabzon: Karadeniz Technical University 3. Isobe, F., Mori, Y. H., Formation of gas hydrate or ice by direct-contact evaporation of CFC alternatives, Int. J. Refrig., 4. 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