Proceedings of the 7th International Conference on Gas Hydrates (ICGH 2011 ), Edinburgh, Scotland, United Kingdom, July 17-21, 2011. EVIDENCE OF A MEMORY EFFECT IN THE FORMATION AND REFORMATION OF CYCLOPENTANE HYDRATE Hami dreza Sefidroodi, Eirin Abrahamsen and Malcolm A. Kelland Department of Mathematics and Natural Science Faculty of Science and Technology Uni versity of Stavanger N-4036 Stavanger NORWAY ABSTRACT While investigating the possibility of testing the performance of low dosage hydrate inhibitors (LDHIs) using cyclopentane hydrates, we noticed that hydrate formation was kinetically very slow with or without any additives even at 0.1 o C and with fast stirring in glass, jacketed beakers. The addition of several solids were able to promote hydrate formation including chalk, barite, sand, clay, ice and cyclopentane hydrate itself. However, to study LDHIs we preferred not to add solids to avoid LDHI-solid interactions which might affect hydrate heteronucleation. Therefore we attempted to use the superheated hydrate or “precursor test method”, pioneered by TOTAL and University of Pau with gas hydrates, in which hydrates are first melted and then reformed. We found that provided the superheating above the equilibrium temperature for cyclopentane hydrates (7.7 o C) was no more than 23 o C, we could obtain hydrates much faster during cooling to 0.0 o C than if hydrates were formed from the liquids for the first time. This is evidence for a so-called memory effect for the formation and reformation of cyclopentane hydrates. Further, it was found that transference of a small amount of water from melted cyclopentane hydrates (made with no more than 2-3 o C superheating) to a much larger amount of fresh water and cyclopentane, with no previous cyclopentane history, initiated cyclopentane hydrate formation significantly faster than using the unspiked fresh water alone. A memory effect has been reported previously for other clathrate hydrates but not Structure II cyclopentane hydrates. This superheated hydrate method has allowed us to study more easily the effect of LDHIs on fluids giving cyclopentane hydrate formation at atmospheric pressure. Keywords: cyclopentane hydrates, memory effect, low dosage hydrate inhibitors NOMENCLATURE CP – cyclopentane CPH – cycleopentane hydrate subcooling KHI – kinetic hydrate inhibitor To – detected onset temperature for hydrate formation t i – induction time Mw - we ight average molecular weight INTRODUCTION The first screening of the performance of low dosage hydrate inhibitors (LDHIs) for use in oilfield applications is normally carried out in small equipment at high pressures with gases that make either Structure I or Structure II clathrate hydrates.1-3 Rocker cells and autoclaves are the most common types of equipment. T etrahydrofuran (THF) hydrate, which makes Corresponding author: Phone: +44 51831823 Fax +47 51831750 E-mail: [email protected] Structure II hydrate, the most common structure encountered in upstream oil and gas operations, has also been investigated for screening LDHIs. This avoids the use of high pressure equipment. However, some researchers have questioned whether the use of THF hydrate is appropriate since THF is very water-soluble but oilfield gas hydrates are formed by gas diffusion into the aqueous phase. (THF hydrate has been useful to measure the growth rate of SII hydrate crystals with various additives). Therefore, we wondered if LDHIs could be screened using cyclopentane hydrates which also would avoid the use of high pressures during testing. Cyclopentane has been reported to form Structure II hydrates at atmospheric pressure without the need for any help gas at equilibrium (dissociation) temperatures usually varying from 7.7-7.9 o C.3-5 Sakemoto and co-workers determined the equilibrium temperature to be 7.0 o C using very small samples and observations with a microscope.3 Even with so-called help gases under pressure cyclopentane still forms SII hydrates.6-9 Figure 1. The complete equipment for the experiments on cyclopentane hydrate. This paper describes attempts to make cyclopentane hydrates by various methods, a redetermination of its equilibrium temperature and an investigation of the memory effect by melting and reforming hydrates. Our studies on the use of cyclopentane hydrates to screen kinetic hydrate inhibitors (KHIs) will be reported in separately. EXPERIMENTAL EQUIPMENT The equipment in which most of the cyclopentane hydrate studies was carried out wa s a parallel series of four previously unused jacketed Pyrex glass beakers coupled to a cooler bath (Figures 13). The beakers have an internal volume of 100ml. Unless otherwise stated experiments were carried out by adding 30ml of distilled water and 10ml of >99% cyclopentane (from Sigma-Aldrich) to each beaker. Each beaker contained a Teflon stirrer bar which wa s stirred by a magnetic stirrer below the beaker at calibrated speeds of 100-660rpm using an oscilloscope. Thus, the only surfaces available to promote cyclopentane hydrate formation from the fluids were Pyrex glass and Teflon, both smooth surfaces. Above each beaker was placed a glass lid which gave a tight fit onto the flat ground glass on the beakers. This lid was used to prevent dust entering the beakers and to avoid evaporation of volatile cyclopentane. Figure 2. The four jacketed and stirred glass beakers for cyclopentane hydrate studies. Figure 3. View from above, as seen by the video camera, of the jacketed beakers. The cooling-heating unit was a Julabo F12 cooling bath with temperature stability ±0.03°C. The cooling fluid wa s a mixture of distilled water and 20% monoethyleneglycol (from VWR) to avoid ice formation in the cooling unit. The distance via the plastic tubing to each of the jacketed beakers wa s the same for each beaker in order to keep the temperature equal in all beakers at any one time. having a thermometer actually placed in the beaker. These values were double-checked by carrying out additional experiments with thermometers in the beakers. It was also found that the temperature at any one time in each of the beakers wa s the same within ±0.05°C irrespective of the cooling bath temperature. To measure the temperature in the fluids in the beakers, and to check that the display for the cooling bath temperature was accurate, we used a digital stick thermometer with accuracy ±0.05°C. The thermometer was removed during actual memory effect experiments to avoid introducing new surfaces and to keep the beaker lids on tight to avoid loss of volatile cyclopentane. A second thermometer with additional real time display was used in the cooling bath to record the actual temperature and to show this display on the video recordings at all times. This gave good control of any temperature in the bath and beakers when left unattended because the video recording could always be checked. The video recording was also critical to judge when cyclopentane hydrate had occurred when no one was present to observe this. The video camera was placed about 1 meter above the cells so that the bottom of all beakers could be seen at the same time. Cyclopentane hydrate formation could be observed to start when the clear stirred solution of cyclopentane and water became cloudy (Figures 4-7). The video camera recording wa s displayed on a PC at all times and the PC coupled to a remote observation system so that experiments could be watched from other PCs via the Internet. INITIAL EXPERIMENTS TO DETERMINE APPROPRIATE CONDITIONS FO R CYCLOPENTANE HYDRATE FORMATION It appears from the literature that making cyclopentane hydrates by simply cooling stirred mixtures of water and cyclopentane, without the addition of a promoter, is not straightforward. One research group added ice crystals to cyclopentane and water at temperatures below 0 o C. Thereafter, the mixture wa s warmed to a temperature above 0 o C to give cyclopentane hydrates.4 Another research group lowered the temperature of cyclopentane-water mixtures to below 0 o C for over 24 hours to obtain cyclopentane hydrates.9 In both cases, it is not clear whether hydrate formation was initiated by ice. Other groups added a small amount of preformed cyclopentane hydrate to a supercooled mixture of cyclopentane and water, or an emulsion, to promote further hydrate formation.10,13 Another method used to make cyclopentane hydrate has been to melt a mixture of ice and cyclopentane above 0.0o C but below the equilibrium temperature of cyclopentane hydrate.14-15 There was a difference in the actual temperature in the beakers and the cooling bath when cooling below room temperature. This difference varied depending on the cooling bath temperature. Therefore, to know the actual temperature in the beakers, experiments were carried out to determine this difference at all temperatures between -0.520.0 o C in the cooling bath. Measurements were made of the beaker temperature, the cooling bath temperature using the video thermometer against the display of the cooling bath temperature. Regression analysis was used and graphs produced so that at all times and all bath temperatures it was possible to know the actual temperature in the beakers by readin g off from the graphs without We also found it difficult to make cyclopentane hydrates without the use of a promoter. For example, by stirring various ratios of cyclopentane and water (or 3.5 wt.% NaCl solution) at 200400rpm at 0.0 o C or 0.1o C (and no lower, to avoid ice formation) for 24 hours gave cyclopentane hydrates in only two tests out of 20 experiments after 190 and 500 minutes. Some of these experiments were continued for 72 hours with still no cyclopentane hydrate formation. This was done in two ways, either by adding the fluids to the beakers at room temperature and then cooling, or by cooling the empty beakers and then adding the fluids. However, if the stirrer bar did not rotate smoothly but rattled around the beaker, which occurred on a few occasions, cyclopentane hydrate wa s often initiated within 24 hours but only after reaching the minimum cooling temperature of 0.0 o C, which took approximately one hour. We also conducted 12 tests at 0.0 o C with only distilled water in the beakers to see if ice formation would occur over 72 hours but no ice was ever formed. THF has been used as a promoter for Structure II gas hydrate formation.16 THF was used because of its high solubility in water. THF has also been used as a promoter for Structure I methane hydrate formation.17 However, in our jacketed beakers, addition of a small amount (0.1 or 1.0 wt.%) of THF to the aqueous phase did not promote any cyclopentane hydrate formation either in 24 hours at 0.1 o C and 200rpm stirring. Accelerated formation of cyclopentane hydrates has been shown to occur using CO2 under pressure mixed with cyclopentane and water.18 To avoid high pressures, which wa s the whole point of the exercise, we tried saturating distilled water with CO2 gas at atmospheric pressure or used a purchased bottle of carbonated mineral water (Farris) as the aqueous phase. Neither method gave cyclopentane hydrates at the same subcooling and stirrer speed as used with THF spiking. We wondered if increasing the interfacial area between the aqueous phase and the upper cyclopentane phase would help promote hydrate formation. Therefore, we emulsified the cyclopentane and water with both a high HLB non-ionic surfactant mixture (a local washing up liquid or polyoxyethylene (20) sorbitan monolaurate (Tween 20) and a low HLB non-ionic surfactant (sorbitan monolaurate (Span 20)) in order to form cyclopentane-in-water and water-incyclopentane emulsions respectively. A concentration of 0.1 wt.% or 1.0 wt.% surfactant wa s used based on the aqueous phase. Neither emulsion gave hydrate formation in 20 hours when stirred at 0.1 o C at 200-400rpm, even when 1 wt.% THF was added to the aqueous phase. The same result was obtained with 1 wt.% of the ionic surfactants, sodium dodecyl sulphate (SDS) or tetradecyltrimethylammonium chloride. However, as with other groups’ studies discussed earlier, we found we could promote cyclopentane hydrates by adding a small quantity of ice to the water phase at 0.1o C. The ice slowly melted but gave cyclopentane hydrate formation in less than 5 minutes with stirring at 200rpm. In this and all subsequent experiments reported herein we used 10ml of cyclopentane and 30ml of distilled water in each jacketed glass beaker. In our 100ml beakers and with stirring at 200rpm the cyclopentane is partially dispersed as large, clear drops in the aqueous phase (Figure 4). When hydrate formation starts the droplets become cloudy and cyclopentane hydrates grow around the edges of the droplets (Figure 5-7). After several minutes the droplets become more and more white with hydrates and the walls become coated with hydrates due to the centrifugal force from the fast stirring. Figure 4. Clear, stirred fluids before the start of cyclopentane hydrate formation seen from the top of a glass cell. Cyclopentane hydrate formation in our jacketed glass beakers is clearly much slower than experiments we have conducted with natural gas hydrates in 23ml sapphire cells at 40-150 bar pressure at equivalent stirring rates (200-400rpm) and subcoolings.19-24 With natural gases (either methane to form SI or a C1-C4 gas mixture forming SII hydrates), nucleation of gas hydrates occurs in a maximum of a few minutes at 7.67.7 o C subcooling in our e quipment. Once gas hydrate formation is initiated further hydrate formation is very rapid, leading to a plug of hydrate and stopping of the stirrer within a few minutes. In contrast, cyclopentane hydrates are much harder to nucleate without a promoter in either our jacketed, glass beakers or the sapphire cells despite the cells having additional steel surfaces. In addition, once cyclopentane hydrate formation has been initiated in either equipment, further hydrate formation is relatively slow, compared to gas hydrate formation, taking up to 20-30 minutes to form sufficient hydrates to stop the rotation of the stirrer. We speculate that the slower nucleation and growth rates of cyclopentane hydrates is due to cyclopentane being less soluble in water at atmospheric pressure than natural gases at high pressure. example, at 0.1 o C and 200rpm with 10ml cyclopentane and 30ml distilled water in the jacketed beakers, addition of 20mg of the following solids initiated cyclopentane hydrate formation within 2-20 minutes in all cases after first stirring without the addition of solids for 20 hours: Rust from corroded iron Rust-free iron metal powder Calcium carbonate powder (outcrop chalk sourced from Denmark) Barium sulphate powder (from a deposited scale sample) Powdered sandstone Powdered Bentonite clay (aluminosilicatebased) However, we did not want to use the addition of solids for studying the relative performance of KHIs in case the primary hydrate inhibition mechanism became absorption of the KHIs onto the solid surface thereby inhibiting initiation of hydrate formation. This included cyclopentane hydrates itself since one would then be studying primarily crystal growth inhibition rather than nucleation inhibition of hydrates. Figures 5-7. Views from above glass cells showing chronological stages of CPH formation. Besides ice and cyclopentane hydrate, we found that addition of various other solids, that could be found in actively producing oilfields, could also initiate cyclopentane hydrate formation significantly faster than with no solids present. For Von Solms and co-workers have used silica particles to initiate gas hydrate formation in studies of some KHIs and have found that hydrate formation is less stochastic giving more reproducible induction times than if no silica was added.25 A second method this research group used to improve the reproducibility of the induction time to gas hydrate formation was the superheated hydrate or so-called “precursor KHI test method” first introduced by TOTAL oil company and the University of Pau.26-27 In this method, gas hydrates are formed, melted and reformed, all in the presence of a KHI. The second formation of hydrates is more reproducible because, as the authors propose, the aqueous phase contains some residual structure or precursors (polyhedral clustering or embryos) from the melted hydrates which promotes hydrate reformation when cooled again.28 Both constant cooling experiments and isothermal experiments were carried out. Residual structure or precursors in the aqueous phase has been proposed as the mechanism for the so-called “memory effect”. Thus a system that has formed hydrates and then been melted will reform hydrates at a higher and more reproducible temperature when re-cooled than a system with no hydrate history. The reformed hydrates will still melt at the same dissociation temperature. This memory effect for clathrate hydrates is a type of hysteresis.29 However, rather than there being partial clusters of hydrates (precursors), molecular modeling work has shown that there may be a persistent higher-than-equilibrium concentration of methane in the water phase after melting methane hydrate that could cause the memory effect.30-31 Several groups have observed a memory effect from experiments with gas hydrates at temperatures well above the normal melting point of ice.3,32-38 The first observation of memory effect in a semi-clathrate hydrate system has been reported for tetragonal tetra-n-butyl ammonium bromide semi-clathrate hydrate.39 Recrystallization was shown to occur in the vicinity of the place where the last piece of initial crystal was dissociated. The authors state that this implies that a small amount of residual structures remain in the dissociated water, but they could not confirm this with Raman micro-spectroscopy. One group has reported results on THF hydrate stating that no memory effect exists.40-41 However, in this study THF hydrates were melted at a minimum of 6.5 o C above the equilibrium temperature which may have destroyed any significant residual hydrate structures and thus the memory effect may have been lost. Cooling rates were fast and nucleation observed to occur on the wa lls of the vessel. Others have reported that if hydrates are melted we ll above the equilibrium temperature and/or for very long periods the memory effect is lost.3,26,37,41 There was observed no residual structure from a neutron diffraction study on melted methane hydrates, i.e. there was no difference in the water structure before hydrate formation and after melting the hydrates.42 The researchers speculate that it is possible that other studies, where it was implied that there is a memory effect, may have not reached equilibrium as melting was only 2 hrs usually.17,43 Thus, there may have been microscopic hydrate crystals still present. Very recently, a molecular simulation study on a hydrate former “M”, akin to CH4 or CO2 , has been reported.44 On warming the hydrate above the equilibrium temperature the hydrate was observed to melt from the periphery outwards leaving a hydrate core. The researchers speculate that the whole hydrate including the core takes time to fully melt away, and thus the core remnants can be sites for reforming hydrates on recooling. High pressure autoclave experiments carried out by Dicharry’s group showed that the repeatability of KHI performance tests diminished rapidly when the hydrates were melted at a temperature more than 2-4 o C above the equilibrium temperature for 2 hours.26 It was speculated that the residual hydrate structures are destroyed under these conditions (i.e. loss of memory effect) and therefore the process reverts to being strongly stochastic again, as if hydrates had never been preformed at all with these fluids. We have also carried out a comprehensive study of the superheated hydrate KHI test method with natural gas hydrates in high pressure sapphire and steel cells. We also obtained better reproducibility of hold times using this test method compared to more common non-superheated hydrate methods.45 The superheated hydrate test method seemed a suitable method to test KHIs with cyclopentane hydrate systems. The reason is that the hydrates can be formed and melted at a given temperature at atmospheric pressure, and then the KHI can be added. Using this method, the amount of residual hydrate structure in the aqueous phase (i.e. the intensity of the memory effect) is kept constant for all KHIs. This is important as it is known that KHIs can affect the dissociation temperature of gas hydrate to different degrees.1-3,46-50 For example, 5000ppm of poly(N-vinylcaprolactam), originally based on the water phase, can raise the dissociation temperature of Structure II gas hydrates by several degrees Celsius at a range of pressures. Poly(N-vinylpyrrolidone), a poorer KHI, has a much weaker effect on the dissociation temperature. Therefore, if you dose the KHI to the water phase first, make gas hydrates and melt them for a short time period at 1-4o C above the true equilibrium temperature, the amount of residual hydrate structure will vary depending on the structure of the KHI. In some cases, such as with poly(N-vinylcaprolactam), you may not even get complete macroscopic melting of the gas hydrates. Therefore, as the University of Pau suggested in a later research paper, it may be best to measure the dissociation temperature for each system with its added KHI and superheat to the same degree above these measured dissociation temperatures for each KHI separately. This can be a fairly timeconsuming experimental procedure. With cyclopentane hydrates one can avoid the problem of measuring individual dissociation temperatures for each KHI. This is because the KHI can be easily added to the aqueous phase after melting the hydrates because the experiment is conducted at atmospheric pressure. In our case, this involves simply lifting a glass lid off the beaker and injecting the required amount of a concentrated solution of the KHI in water. Adding the KHI to a system under high pressure is not so easy and would require some kind of pressurized injection equipment. Work carried out by the University of Pau with natural gas hydrates suggests that gas hydrates melted about 4 o C above the equilibrium temperature for a few hours lose their memory effect. Therefore, in order to screen KHIs with cyclopentane hydrates we wanted to be sure that there was indeed a memory effect operating and at which temperature above the equilibrium temperature the memory effect began to disappear. This led us to conduct a thorough investigation in which cyclopentane hydrates were melted at various temperatures and then reformed on cooling again. It is this work that is discussed in the rest of this paper. MEMORY EFFEC T EXPERIMENTAL METHOD The preparation of the cyclopentane hydrate in each beaker in all memory effect experiments was carried out as follows. The beakers were cooled to 0.0 o C before the addition of any fluids. Then 10ml cyclopentane and 30ml distilled water was added. After stirring at 200rpm for 10 minutes, to bring the fluid temperature to 0.0 o C, a small crystal of cyclopentane hydrate, made earlier and kept in a refrigerator at 3-4 o C, was added to each beaker. The time to the observation of the formation of further cyclopentane hydrate was less than 2 minutes in all experiments. Then, before the actual memory tests were started, the temperature in the beakers wa s adjusted to 9.2 o C 30 or 60 minutes after nucleation of cyclopentane hydrates began. After complete melting of the hydrates to give a clear mixture of fluids the beakers were cooled again to 0.0 o C at a constant rate in all experiments (this requires setting the cooling bath to a temperature of 0.4 o C). Hydrate formation occurred almost at the same time in each beaker in each experiment. The start of the hydrate formation time was determined as the time when hydrate formation occurred in the last beaker. After a designated hydrate formation time, the temperature in the beakers was increased to 0.3 o C below the hydrate equilibrium temperature, i.e. 7.4 o C and held for 5 minutes before further increasing the temperature more slowly to a designated melting temperature. This was done to avoid overheating the contents of the beakers if the melting temperature only had been programmed into the heating unit. After holding the beakers at the melting temperature for a designated time period the beakers were again cooled to 0.0 o C at a constant rate in all experiments. The onset temperature (To) for cyclopentane hydrate formation was recorded based on visual observations. If hydrate formation occurred in any beaker after the beaker temperature reached 0.0 o C the induction time to formation of hydrate formation at 0.0 o C (t i) was recorded. If no hydrate wa s observed to form within 20 hours the experimental result was recorded as “no hydrate” (NH). T h is memory test procedure avoids the possibility that the added cyclopentane hydrate crystal might be the last hydrate particle to melt and was the main initiator of hydrate formation in the second cycle. It also avoided any suspicion that ice may be nucleating hydrate formation. Any data from experiments in which the stirrer bar did not rotate smoothly in the centre of the beaker but rattled around the beaker were ignored. As discussed earlier, this behavior occurred on a few occasions and accelerated cyclopentane hydrate formation. After each memory test, hot water (50-60 o C) was added to the beakers to melt the hydrates. The fluids were removed and the same hot water wa shing procedure repeated at least three times. The beakers were then cleaned with paper towels, wa shed again with hot water and then rinsed thoroughly with distilled water. The magnetic stirrer bars were also washed well in hot tap water and rinsed in distilled water. The same stirrer bar wa s kept in the same beaker throughout the whole study. The glass lids were also washed the same way after each experiment and kept to the same beaker. Blank tests were carried intermittently to check that no hydrates formed from cyclopentane and water at 0.0 o C within at least 20 hours using fresh water with no previous cyclopentane hydrate history. This made sure that our washing procedure for the cells was adequate. CYCLOPENTANE HYDRATE EQ UILIBRIUM TES T METHOD AND RESULTS To determine the cyclopentane hydrate equilibrium temperature, the same preparation of the fluids in the cells (beakers) was carried out as done for the memory effect experiments. This made sure that the conditions in the four cells wa s very similar before further experimental work. After cyclopentane hydrate formation at 0.0 o C, the beakers were warmed over to 7.3 o C over approximately 5 minutes, then heated stepwise 0.1 o C at a time holding at each step for at least 30 minutes. The temperature at which the fluids became totally clear and no longer cloudy with no visible sign of hydrate particles wa s taken as the dissociation (equilibrium) temperature. This wa s found to be 7.7 o C in all experiments, which other groups have also observed.10 It was sometimes necessary to hold the beaker at this temperature for much longer than 30 minutes to see complete dissociation of hydrates (i.e. back to a clear solution), sometimes for up to 18 hours. RESULTS AND DISCUSSION OF MEMORY EFFEC T EXPERIMENTS Three sets of experiments were carried out which are summarized in Figures 8-11 and Table 1. In the first set of experiments, cyclopentane hydrates were melted at various set temperatures for 20 minutes. In the second set of experiments the melting period was 2 hours and in the third set it wa s 24 hours. Figures 6-8 show data for the onset temperatures (To) of cyclopentane hydrate formation at melting temperatures that always gave cyclopentane hydrate formation before reaching the minimum temperature of 0 o C. This graphical data is supplemented by Table 1 which contains data for experiments in which cyclopentane hydrate formation did not always occur before reaching the minimum temperature of 0 o C. This tabulated data is either the onset temperature before reaching 0.0 o C or the time after reaching 0.0 o C at which hydrate formation did occur. An experimental result of “NH” is given in each case when no hydrates formed in 24 hours at the minimum temperature. Figure 8. Onset temperature results of memory effect experiments with a melting time of 20 minutes at melting temperatures that always gave cyclopentane hydrate formation before reaching the minimum temperature of 0 o C. Figure 9. Onset temperature results of memory effect experiments with a melting time of 2 hours at melting temperatures that always gave cyclopentane hydrate formation before reaching the minimum temperature of 0 o C. superheated to higher temperatures or kept for 20hrs at 9 o C or more the solution was clear (Figure 13). Table 1. Summary of the data for melting temperatures that did not always give cyclopentane hydrate formation before cooling to the minimum temperature of 0.0o C. (NH means no hydrates observed in 20 hours). Figure 10. Onset temperature results of memory effect experiments with a melting time of 20 hours at melting temperatures that always gave cyclopentane hydrate formation before reaching the minimum temperature of 0 o C. Figure 11. Onset temperature results of memory effect experiments with all three melting times at melting temperatures that always gave cyclopentane hydrate formation before reaching the minimum temperature of 0o C. Lines of best fit are also shown. The turbidity of the fluids when cyclopentane hydrates had been melted wa s dependent on the superheating and the length of time the fluids were kept at this temperature. If cyclopentane hydrates were melted a t 8 o r 9o C for 20mins or 2hrs the fluid was still cloudy but no particles could be observed visibly in the cells (Figure 12). If Melt Temp o ( C). Melt Time (hours) Expts that o gave To ( C) Expts that o gave ti ( C) or NH after o reaching 0 C 13.1 0.33 0.4, 0.4, 0.0 15, 105, NH, 25, 33, 961 14.1 0.33 0.3, 1.3, 2.0 NH, NH, 43, 7, NH, 7, NH, NH 15.1 0.33 0.2, 1.7 NH, NH, NH, NH, NH 16.1 0.33 11.1 2 2.0, 0.9, 0.6, 2.8, 1.7, 0.5, 0.3, 1.5 12, 53, 3, NH 12.1 2 0,3, 0.0, 1.6, 0.7, 0.4, 0.4, 1163, 1, >1 (final time not recorded), 1034, NH, NH, 12, 3, 22 13.1 2 0.7 161, 383, NH, NH, NH 14.1 2 10.2 20 1.4 146, 12, 9, 5 11.1 20 1.4 56, 26, 79, 6, 16 12.1 20 609, 79, NH, 305, 14, NH 13.1 20 NH, NH, NH, NH, NH, NH NH, NH, 11, 36, NH, NH, NH, NH NH, NH, NH, NH, NH, NH over 1 hour. It should also be pointed out that no beaker gave constantly worse results than any another beaker, i.e. there was no trend that any one beaker was different from another. Even with the limited number of experiments carried out in this study, these data are clear, statistically significant evidence of some kind of memory effect in the beakers which promotes reformation of cyclopentane hydrates at an earlier time and/or higher onset temperature in the cooling cycle. Figure 12. Cloudy solution cyclopentane hydrates. after melting Figure 13. Clear solution after melting cyclopentane hydrates for a sufficiently long period or with sufficient superheating. From the figures and tables it is clear that cyclopentane hydrate formation can occur much earlier when the fluids have a history of previously forming hydrates and the superheating and melting time period are low. As discussed earlier, for fresh fluids with no previous cyclopentane hydrate history, we only observed cyclopentane hydrate formation in 2 out of 20 experiments after at least 24 hours at 0.0 o C. In these 2 experiments hydrates formed after 190 and 500 minutes after reaching the minimum temperature of 0.0 o C. Using fluids with previous cyclopentane history we could obtain hydrates well before reaching the minimum temperature and up to onset temperatures of about 4 o C with the cooling rate used. For example, to cool from 9.2 o C to 0.0 o C took consistently just In addition, the data in Figures 8-10 show a trend by which longer melting temperatures cause a loss of the memory effect. This trend is graphically displayed in Figure 11 where lines of best fit through the three sets of data at 0.33, 2 and 20 hours melting times have been added. For example, using a melting temperature of 12.1 o C for 0.33 hours gave onset temperatures from reformation of cyclopentane hydrates of in the range 0.5-2.4 o C whereas with 24 hours melting time at the same temperature hydrates always formed after reaching the minimum temperature of 0 o C or not all within the 24 hour experimental period. However, when the melting period gets longer and/or the melting temperature increased the results become more random and the probability of getting no hydrate formation in 24 hours increases. For example, with 20 hours melting time, hydrates always formed during the cooling period before reaching 0 o C when the first hydrates were melted at 8.3 o C, whereas when melted at 13.1 o C for the same time period no hydrates were reformed after 24 hours in all the 6 experiments carried out. The number of experiments at any one particular melting temperature or melting time period is not very large but enough to see a trend, and certainly with all the data as a whole the trend is even more evident and statistically significant. A further 8 experiments (i.e. 32 beakers), were also carried out with 95 minutes melting time at various melting temperatures and these also fit with the observed trends discussed herein. For example at a melting temperature of 9.2 o C all beakers gave cyclopentane hydrate formation at an onset temperature of 2.8o C. At a melting temperature of 12.1o C hydrates formed at 0.11.4 o C in 5 beakers and at 32-386 minutes after reaching 0.0 o C in 3 other beakers. Another point to mention from the results in Figures 8-11 is that the reproducibility in the onset temperatures is good (i.e. scattering of To in the range of about 1 o C), only with 2 hours or less melting time and superheating of less than about 2 o C. In comparison, Dicharry and co-workers found that good reproducibility in onset temperatures (or induction times at constant temperature) was lost if the superheating was more than 3-4o C for 2 hours using natural gas hydrate systems.26 Another interesting set of tests that we carried out wa s to see if cyclopentane hydrate formation could be accelerated by transferring some of the melted water from cyclopentane hydrates to a fresh mixture of water and cyclopentane with no cyclopentane hydrate history in another beaker that was the cooled. The procedure was as follows: 10ml cyclopentane and 30ml distilled water were added to one of the 4 beakers (the other 3 were empty), cooled to 0.0 o C and a crystal of cyclopentane hydrate from the refrigerator added. After 30 minutes of hydrate formation the temperature in the beakers was raised to 9.3 o C for 1 hour to fully melt the hydrates and then cooled again to 0.0 o C for 30 minutes. Hydrates formed again and the beaker warmed to 7.7 o C for 20 hours to give a totally clear mixture of water and cyclopentane. 30ml distilled water with no hydrate history and 10ml cyclopentane was then added to the other 3 empty beakers and left for 1 hour to cool the fluids to 7.7 o C. Using a pipette pre-cooled in a refrigerator, 3ml of the melted cyclopentane hydrate water in the first beaker was transferred quickly to each of the other three beakers. All 4 beakers were then cooled to 0.0 o C which took about 50 minutes. Cyclopentane hydrate formation occurred at 1.0, 1.6 and 3.6 o C in the three beakers with the spiked fresh solutions and at 1.9 o C in the original beaker with previous hydrate history. A repeat experiment also gave the same result, i.e. hydrate formation in all four beakers before reaching 0.0 o C. In other experiments, one or two of the beakers was not spiked with melted cyclopentane hydrates and only these beakers did not give hydrate formation when cooled to 0.0 o C for 24 hours. In another experiment 1ml of melted hydrate water from 3 beakers wa s added to the fourth beaker with fresh water and cyclopentane and cooled to 0.0 o C. Cyclopentane hydrate formation occurred at 3.4 o C in the fourth beaker and at 1.7, 3.4 and 3.4o C in the other three beakers. These experiments indicate that the memory effect is located in the aqueous phase and that it can be transferred from one solution to a fresh aqueous solution with no previous hydrate history. CONCLUSION Our experiments show that it can be difficult to form cyclopentane hydrates at 0.0o C in stirrer glass beakers even at 7.7 o C subcooling without the aid of a promoter. Examples of promoters include cyclopentane hydrate or ice crystals as we ll as powdered iron metal, rust, chalk, barite or Bentonite clay. The final cyclopentane hydrate promoter investigated wa s residual hydrate structure, or so-called precursors, in the water phase from melting cyclopentane hydrates a maximum of a few degrees Celsius (preferably <23 o C) for short time periods above the equilibrium temperature. The equilibrium temperature wa s determined to be approximately 7.7 o C. Thus, we found that provided the superheating above the equilibrium temperature was no more than 3-4 o C for short time periods, we could obtain hydrates much faster during cooling to 0.0 o C than if hydrates were formed from the liquids for the first time. Even after 20 hours superheating at 9.2 o C or less. T he residual structure appeared to persist since hydrate formation was still greatly accelerated compared to fluids with no hydrate history. These results are evidence for a so-called memory effect for the formation and reformation of cyclopentane hydrates. Further, it was found that transference of a small amount of water from melted cyclopentane hydrates (made with no more than 2-3o C superheating) to a much larger amount of fresh water and cyclopentane, with no previous cyclopentane history, initiated cyclopentane hydrate formation significantly faster than using the fresh water alone. A memory effect has been reported previously for other clathrate hydrates but not Structure II cyclopentane hydrates. This superheated hydrate test method has allowed us to study the effect of LDHIs on fluids giving cyclopentane hydrate formation at atmospheric pressure.51 REFERENCES [1] Kelland MA.; Energy & Fuels, 2006: 20(3): 825-847. [2] Kelland MA., Production Chemicals for the Oil and Gas Industry, Boca Raton, FL, CRC Press, Taylor & Francis Group, (2009). [3] Dendy SE; Koh AC; Clathrate Hydrates of Natural Gases, Third Edition. Boca Raton, Fl: CRC Press, 2008. [4] Joseph W. Nicholas, Laura E. Dieker, E. Dendy Sloan, Carolyn A. Koh. (2009). J. Coll. Interf. Sci. 331, 322. [5] Nakajima, Masahiro, Ohmura, Ryo & Mori, Yasubiko H., (2008), Ind. Eng. Chem. Res., 47, 8933-8939. [6] Mohammadi, Amir H. & Richon, Dominiqe, (2009), Ind. Eng. Chem. Res., 48, 9045-9048. [7] Ripmeester, J. A.; Ratcliffe, C. I.; Mclaurin, G. E. The Role of Heavier Hydrocarbons in Hydrate Formation, AIChE Spring Meeting, Session 44, Hydrates in the Gas Industry, April 1991. [8] Ripmeester, J. A.; Ratcliffe, C. I. J. Phys. Chem. 1990, 94, 8773-8776. [9] Sun, Z- G.; Fan, S- S.; Guo, K-H.; Shi, L.; Guo, Y-K.; Wang, R-Z, J. Chem. Eng. Data, 2002, 47, 313. [10] Fan, S.S., Liang, D.Q., Gou, K.H., (2001), J. Chem. Eng. Data, 46, 930-932. [11] Nakajima, Masahiro, Ohmura, Ryo & Mori, Yasubiko H., (2008), Ind. Eng. Chem. Res., 47, 8933-8939. [12] Whitman, C.A.; Mysyk, R.; White, M.A.; J. Chem. Phys., 2008, 129, 174502. [13] Lo, C.; Zhang, J.S., Somasundaran, P.; Lu, S.; Couzis, A.; Lee, J.W.; Langmuir, 2008, 24, 12723. [14] Zhang, Y.; Debenedeti, P.G.; Prud’homme, R.K.; Pethica, B.A.; J. Phys. Chem. B, 2004, 108, 16717. [15] Aspenes, G., Dieker, L.E., Aman, Z.M., Høiland, S., Sum, A.K., Koh, C.A., Sloan, E.D., (2010), J. Coll. Interf. Sci., 343, 529-536. [16] York, J. D., and Firoozabadi, A., Energy & Fuels (2009) 23, 2937–2946. [17] N. Zhengfu, Z. Shixi, Z. Sh uangyi and C. Guangjin, Petroleum Science, 2007, 4(1), 61. [18] Zhang, Junshe & Lee, Jae W., (2009), Ind. Eng. Chem. Res. 48, 4703-4709. [19] M.A. Kelland, T.M. Svartaas and L.A. Dybvik, Control of Hydrate Formation by Surfactants and Polymers, Paper SPE 28506, Proceedings of the SPE Annual Technical Conference, New Orleans, September 1994. [20] M.A. Kelland, T.M. Svartaas, L.A. Dybvik, A New Generation of Gas Hydrate Inhibitors, Paper SPE 30695, Proceedings of the SPE Annual Technical Conference, Dallas, October 22-25, 1995. [21] L. Del Villano, Malcolm A. Kelland, Garret M. Miyake and Eugene Y.-X. Chen, Energy Fuels, 2010, 24(4), 2554. [22] L. Del Villano, R. Kommedal, R. Hoogenboom, M.W.M. Fijten and M.A. Kelland, Energy Fuels, 2009, 23, 3665. [23] L. Del Villano, R. Kommedal and M.A. Kelland, Energy & Fuels, 2008, 22(5), 3143. [24] L. Del Villano and M.A. Kelland, Chem. Eng. Sc i., 2010: 65: 5366. [25] Jensen L; Ramløy H, Thomsen K; von Solms N; Ind. Eng. Chem. Res., 2010: 49: 1486. [26] Duchateau, Christophe, Peytavy, Jean-Louis, Glènat, Philippe, Pou, Tong-Eak, Hidalgo, Manuel, Dicharry, Christophe. (2009). Energy & Fuels, 23, 962. [27] Duchateau, Christophe, Peytavy, Jean-Louis, Glènat, Philippe, Pou, Tong-Eak, Hidalgo, Manuel, Dicharry, Christophe. (2009). Energy & Fuels, 24, 616. [28] Koga,T.; Wong, J.; Endoh, M.K.; Mahajan, D.; Gutt, C.; Satija, S.K.; Langmuir, 2010, 26, 4627. [29] Ni, X., Brown, C.J., (2009), Chemical Engineering Journal, 157, 131-139. [30] Rodger, M., in Proc. Ga s Hydrates: Challenges for the future, (Holder, G.D., Bishnoi, P.R., eds), Ann. N.Y. Acad. Sci., 912, 474 (2000). [31] Rodger PM. Methane Hydrate Melting and Memory. Ann. N. Y. Acad. Sci. 2000; 912: 474482. [32] Makogon, Y. F., Hydrates of Natural Ga s, Moscow, Nedra, Izadatelstro, PennWell Books, Tulsa, Oklahoma, p.237 in Russian (1981 English) (1974). [33] Lederhos, J. P., Long J. P., Sum, A., Chistiansen, R. L., Sloan E. D. Chem. Eng. Sci., 51, 1221 (1996). [34] Takeya, S., Hori, A., Hondoh, T., Uchida, T. J. Phys. Chem. B, 104, 4164 (2000). [35] Parent, JS, Bishnoi P.R., Chem. Eng. Commun., 1996 144, 51. [36] Lee JD, Susilo R, Englezos, P, Proceedings of the 5 th International Conference on Gas Hydrates: Volume 1, 13-15 June 2005, Trondheim, Norway, pp 221-230. [37] Ohmura R., Ogawa, M, Yasuja K, Mori YH, J. Phys. Chem. B. 2003, 107, 5289. [38] Zeng, H., Wilson, L. D., Walker, V. K. and J. A. Ripmeester. 2006, J. Am. Chem. Soc., 9, 128, 2850. [39] Motoi Oshima, Wataru Shimada, Sh unsuke Hashimoto, Atsushi Tani and Kazunari Ohgaki, Chem. Eng. Sci., 2010, 20, 5442. [40] P.W. Wilson and A.D.J. Haymet, Chem. Eng. J., 2010, 161, 146. [41] Wilson, P.W., Lester, Daniel, Haymet, A.D.J., (2005), Heterogeneous nucleation of clathrates from supercooled THF/water mixtures, and the effect of an added catalyst, Chem. Eng. Sci., 60, 2937-2941. [42] Buchanan, Piers, Soper, Alan K., Thompson Helen, Westacott, Robin E., Creek, Jefferson L., Hobson, Greg, Koh, Carolyn A. (2005). J. Chem. Phys., 123, 164507. [43] Gao, S; Chapman, W; House, W, Proceedings of the 5 th International Conference on Gas Hydrates, Vol. 1 Kinetics and Transport Phenomena, (Tapir Academic), Trondheim, Norway, 13-15 June, 2005. [44] Jacobson, C.L.; Waldemar, H.; Molinero, V.; J. Am. Chem. Soc., 2010, 132, 11806. [45] An Investigation Into The Laboratory Method For The Evaluation Of The Performance Of Kinetic Hydrate Inhibitors Using Superheated Gas Hydrates, L. Del Villano and M.A. Kelland, Chem. Eng. Sci., 2011, 66, 1973. [46] Gulbrandsen, A.C., Svartaas, T.M.; Influence of Formation Temperature and Inhibitor Concentration on Dissociation Temperature for Hydrates Formed with Polyvinylcaprolactam, Proceedings of the 6 th International Conference on Ga s Hydrates (ICGH-6, 2008), Vancouver, British Columbia, Canada, July 6-10, 2008, Editors: Peter Englezos and John Ripmeester. [47] Gulbrandsen, A.C., Svartaas, T.M.; Influence of the Melting Rate on the Dissociation of Hydrates where the Kinetic Inhibitor PVCap is Present; Proceedings of the 6 th International Conference on Gas Hydrates (ICGH-6, 2008), Vancouver, British Columbia, Canada, July 6-10, 2008, Editors: Peter Englezos and John Ripmeester. [48] Habetinova, E., A. Lund, and R. Larsen. Hydrate Dissociation under the Influence of LowDosage Kinetic Inhibitors, in 4 th International Conference on Natural Gas Hydrates. 2002. Yokohama, Japan 2002. [49] Lee, J.D. and P. Englezos, Unusual kinetic inhibition effects on gas hydrate formation, Chemical Engineering Science, 2006. 61: p. 13681376. [50] Vebenstad, A., R. Larsen, and A. Lund. Ga s Hydrate Behaviour under the Influence of Low Dosage Hydrate Inhibitors (LDHIs), in 11 th international conference MULTIPHASE '03. 2003. San Remo, Italy. [51] Erik Gisle Dirdal, Chandrakala Arulanantham, Hamidreza Sefidroodi And Malcolm A. Kelland; Can Cyclopentane Hydrate Formation Be Used To Rank The Performance Of Kinetic Hydrate Inhibitors?, Proceedings Of The 7th International Conference On Gas Hydrates (ICGH 2011), Edinburgh, Scotland, United Kingdom, July 17-21, 2011.
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