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Crystallization of calcium carbonate in a large-scale push–pull heat storage test in the Upper Jurassic carbonate aquifer

Crystallization of calcium carbonate in a large-scale push–pull heat storage test in the Upper... martina.ueckert@tum.de Institute of Hydrochemistry, Crystallization of carbonates is a key process affecting the operation of geothermal Technical University facilities and aquifer heat storage systems. The crystals formed in an aquifer heat of Munich, Marchioninistr. 17, 81377 Munich, Germany storage test in the Upper Jurassic carbonate aquifer were investigated at injection Full list of author information ◦ ◦ temperatures of 65 C to 110 C , with varying CO partial pressures, and varying Mg/Ca is available at the end of the ratios. Water samples were directly filtrated, and analyzed by SEM/EDX. Complementary article autoclave experiments were run. In the autoclave experiments with tap water, arago- nite crystals dominated at all temperatures (45–110 C ). In the autoclave experiments with ultra-pure water, calcite crystals dominated at the same temperatures. In the field test, mainly calcite crystals were found up to temperatures of 90 C . Only at very high temperatures of 110 C aragonite crystallization prevailed. CO partial pressure varied especially between injection and production stages. Mg/Ca ratio varied through all stages, and depended on the dissolution of the rock matrix. Together with the auto- clave experiments, this study suggest that temperature and Mg/Ca ratio had no influ- ence on the crystallization, and only supersaturation affected the CaO polymorphs. We further assume that we produced initially injected crystals back during the following production stage. That results in the assumption that existing particles can maintain an equilibrium in the dispersion, and reduce precipitation on surfaces like pipes and heat exchangers. Keywords: CaCO polymorphs, Calcite, Aragonite, Carbonate aquifer, Autoclave experiments Introduction The efficiency of geothermal power generation sites as well as aquifer thermal energy storage in carbonate aquifers is still affected by precipitations of calcium carbonate poly - morphs (Lee 2013; Mundhenk et al. 2013; Ueckert and Baumann 2019). Precipitation of calcium carbonate in geothermal systems is mainly caused by temperature and pressure changes (Baumann et al. 2017). Precipitates of a geothermal or thermal energy storage system are usually investigated by analyzing the occurring scalings (see e.g., Wanner et  al. 2017). On the other hand, there are only very few studies addressing crystallization processes or the particle load of geothermal water (Ueckert 2016; Wolfgramm et al. 2011). As a consequence, little is © The Author(s) 2020. This article is licensed under a Creative Commons Attribution 4.0 International License, which permits use, sharing, adaptation, distribution and reproduction in any medium or format, as long as you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons licence, and indicate if changes were made. The images or other third party material in this article are included in the article’s Creative Commons licence, unless indicated otherwise in a credit line to the material. If material is not included in the article’s Creative Commons licence and your intended use is not permitted by statutory regulation or exceeds the permitted use, you will need to obtain permission directly from the copyright holder. To view a copy of this licence, visit http://creat iveco mmons .org/licen ses/by/4.0/. Ueckert et al. Geotherm Energy (2020) 8:7 Page 2 of 23 known about the crystallization process of the polymorphic forms of calcium carbon- ate in geothermal systems. The crystallization itself has been studied under well-defined laboratory conditions for several years (see e.g., Reddy and Nancollas 1970) and is still a major research topic (see e.g., Schmidt et al. 2019). In classical nucleation theory, crystallization is divided into nucleation and crys- tal growth. While nucleation is depends on the supersaturation of the solution, crys- tal growth is determined by the diffusion of atoms or ions to and on the surface of the nuclei and their following incorporation into the lattice. On the other hand, non- classical crystallization theory was introduced to explain, e.g., the crystallization via amorphous precursors or the formation of mesocrystals (De Yoreo and Vekilov 2003; Meldrum and Cölfen 2008). It is important to explain the crystallization of calcium car- bonate polymorphs, because the (meta)stable forms of calcium carbonate vaterite, cal- cite and aragonite crystallize often via amorphous calcium carbonate (ACC) precursor. The transformation of ACC to the crystalline polymorphs is extremely fast [ < 2 min at 25 C (Rodriguez-Blanco et al. 2011)], and ACC is usually not stable in natural systems. The concept of homogeneous and heterogeneous nucleation was introduced in the lit - erature, and plays an important role in calcium carbonate crystallization. Once a solu- tion reaches a critical supersaturation, a nucleus can spontaneously form, which is called homogeneous nucleation. In heterogeneous nucleation, a surface is already existing, which makes nucleation energetically less demanding (Meldrum and Cölfen 2008). To describe the crystallization of calcite, a diffusion-reaction model was suggested. Here, calcite growth is regulated by two processes: mass transport and surface reac- tion (see e.g., Tai et  al. 2006). Wang et  al. (2013) supported this for calcium carbonate polymorphs experimentally. According to their study, calcite crystallization is favored at high concentration gradients, whereas high temperatures favor aragonite crystalliza- tion. Already Wray and Daniels (1956) reported that aragonite is prevailing over calcite at 45 C . Ahn et al. (2005) postulated that supersaturation of the solution is controlling the growth of the polymorphs and the affinity to crystallize as vaterite, calcite, and arag - onite increases with decreasing supersaturation. Other cations, especially magnesium ions, inhibit crystallization processes of calcite (Chen et  al. 2006; Tai and Chien 1998; Morse et al. 1997; Reddy and Nancollas 1976; Zhang and Dawe 2000), due to their incor- poration into the calcite lattice. However, the presence of magnesium ions is reported to accelerate the crystallization of aragonite (Berner 1975). Furthermore, the availability of magnesium ions inhibits the transformation of vaterite into calcite (Kitamura 2001). Niedermayr et al. (2013) state that the coexisting presence of polyaspartic acid and mag- nesium ions favor the formation of calcite over aragonite and vaterite. Also, the influ - ence of sulfate ions is discussed. Bots et al. (2011) performed laboratory experiments to see the influence of sulfate ions in combination with Mg/Ca ratios on the precipitation of the CaCO polymorphs. Without sulfate or magnesium ions in the solution, calcite crystals prevailed. Without sulfate ions in the solution, aragonite was the dominant pol- ymorph (> 90 % ) at a Mg/Ca ratio of 0.77. As soon as sulfate ions (minimum of 5.1 mM) were added to the solution, aragonite was already at a Mg/Ca ratio of 0.36, dominating the polymorph. The role of other bivalent cations, such as strontium or barium, has been investigated for several years (see e.g., Wray and Daniels 1956), and is still part of the Uecker t et al. Geotherm Energy (2020) 8:7 Page 3 of 23 main research (see e.g., Littlewood et al. 2017). But, according to them, it is likely that it favors aragonite crystallization over calcite. Han et al. (2006) precipitated calcium carbonates by injecting a CO /N -gas mixture 2 2 into a CaCl solution. Vaterite formation is favored at high gas flow rates and low initial CaCl concentrations. An increase from 33 to 66 vol% CO in the injected gas results in 2 2 an increase of vaterite crystals. Aragonite needles were only observed at temperatures of 60 C . It seemed that the bubbling time and the stirring rate are not dominant for the morphology of the carbonates. This experiment seems to be very close to the degas - sing of thermal water in geothermal systems. However, in this experiment CO serves as a source for carbonates, i.e., the equilibria in the solution are controlled by the mass transfer rates of CO from gas phase bubbles into the liquid phase, which at the given experimental conditions result in a net dissolution of CO . In contrast, in geothermal systems in the Upper Jurassic carbonate aquifer in the Bavarian Molasse Basin, no gas phase is present under reservoir conditions with pressures exceeding 200 bar. Inorganic carbon is dissolved and the species distribution is controlled by the carbonic-acid-equi- librium. During production of geothermal water, gas bubbles are formed if the pressure is lower than the sum of the partial pressures of the dissolved gases (bubble point, typi- cally 2–25 bar). In this case, CO is stripped from the geothermal water. Consequently, the carbonic-acid-equilibrium is shifted to higher pH and precipitation of carbonates occurs. In both cases, the presence of the air–water interface at the bubble has to be considered (Baumann 2016; Baumann et al. 2017). As seen in all these well-defined laboratory experiments, the crystallization of cal - cium carbonate polymorphs is very complex, and as soon as one boundary condition is changed, another polymorph might preferentially be formed. Since the knowledge of crystallization processes is indispensable for avoiding cost- intensive shutdowns due to scalings, research focusing on the behavior in complex natural systems is necessary. During a push–pull heat storage test with well-defined boundary conditions, which results are described in Ueckert and Baumann (2019), addi- tionally the crystallization of calcium carbonate polymorphs was analyzed. To support our findings, we performed experiments in a high-temperature autoclave to further reduce the degrees of freedom for the evaluation. Materials and methods Description of the autoclave experiments Experiments were run in an autoclave (Midiclave, Büchi, Switzerland), which has a total volume of 1 L (see Fig  1). The autoclave was filled with 0.5 L of water. The rock matrix (volume of 100 resp. 150 cm ) was put into a stainless steel basket and submersed in water in the center of the reaction vessel. After closing the autoclave, the remaining air was exchanged with argon (99,996 Vol.% purity, Westfalen, Germany). Three different setups were chosen: in the first setup, a rock sample and 500 mL ultra- pure water (= UPW , QPAK 1, Merck) were put into the reaction vessel (see Fig.  3). In the second setup, carbonate tap water (=‘tap water MUC’), was used instead of UPW and a defined initial CO partial pressure (about 5–8 mbar at 20 C and a total pressure of 1.2 bar) was established in the reaction chamber by adding a defined volume of CO . 2 Ueckert et al. Geotherm Energy (2020) 8:7 Page 4 of 23 Fig. 1 Schematic overview of the autoclave experiment. The defined volume of CO is injected by means of a gas syringe In the third setup, only tap water MUC was heated without a rock sample and served as a blank reference. For each setup, five experiments were run at temperatures of 45, 60, 80 and 110 C . The autoclave was heated to the target temperature within 15 min. At temperatures up to 80 C , samples for fluid and particle characterization were taken at the bottom valve of the autoclave immediately after the target temperature had been reached. Samples at higher temperatures were taken after a short cooling period of 10 min to reach 80 C. The experiments with rock sample were performed once with a limestone sample (see lower picture Fig. 3), and once with a dolomite sample (see upper Fig. 3). 12 experiments were run at one rock sample, so 36 samples were taken in total. The reaction vessel was rinsed in two steps after two experiments: first 0.8 L citric acid was heated, and then discarded. Afterwards 1-L ultra-pure water was filled in the auto - clave and then removed. No stirring device was used to simulate the reactions off the main flow paths. The rationale behind that is that most of the heat transfer happens in the karstified layer while reactive surface is necessary for dissolution. Description of the field experiment A detailed description of the heat storage test performed in the Upper Jurassic carbonate aquifer in the North East-Molasse Basin in the city Dingolfing, the operational design and the hydrogeochemical model are given in Bartels et al. (2015) and Ueckert and Bau- mann (2019). The test design at the research borehole was a push–pull test with five injection stages of hot carbonate tap water (injection temperature T = 65 , 80, 90, 110, and 110 C ) into Inj Uecker t et al. Geotherm Energy (2020) 8:7 Page 5 of 23 a carbonate aquifer, each immediately followed by a production stage (see Fig.  2). The flow rate was set to 15 L/s (see Table 1). To prevent precipitates in the heat exchangers, CO was added prior to heating the tap water. The required concentration was calculated using the hydrogeochemical mod - eling software PhreeqC (Parkhurst and Appelo 2013). Taking the reaction rates of cal- cite precipitation and the short residence times (about 0.13 s) in the heat exchanger into account, a saturation index (SI) for calcite between 0.1 and 0.2 was targeted. This slight supersaturation was intended to prevent corrosion effects in the pipes and ground-level facilities. The calculations resulted in CO concentrations between 90  mg/L for T of 2 Inj ◦ ◦ 65 C and 420 mg/L for T of 110 C and a resulting pH of 6.78 and 6.22, respectively. Inj Water samples were taken at a bypass close to the well head. At temperatures exceed- ing 80 C , a cooler was used to maintain safe sampling conditions. Samples were taken during injection (tap water, controlled temperature, controlled CO content) as well as during production (mixture of tap and aquifer water, decreasing temperature (T ), Prod varying CO content), and were filtered immediately. The pressure at the top of the aquifer was constant at 25.3 bar during the production stages. Matrix characterization The upper 20 m of the target aquifer at the test site are built of limestone, layered with dolomitic breccia and dolomites. The rest of the aquifer consists of dolomites and dolo - mitic breccia (about 200  m). Dolomites were formed by dolomitization of limestones. Circulation loss occurred from 297 to 397 m b.s.l., and no cored drilling was possible at that depth. The evaluation of the heat storage test showed that the water is mostly flow - ing in a karstified structure ( = main flow path ), but a smaller amount of water will be transported in the surrounding pores of the rocks (Bartels et al. 2015). Crushed pieces of the core samples were used for the autoclave experiments (see Fig. 3). CT pictures of the rock samples provide data on the accessible surface area, i.e., the area at which reactions can occur under rate-limited conditions. The limestone samples show high contents of ooids and peloids (see lower picture Fig. 3, marked with a green rectangle), and no arag- onite crystals were found (Bartels et al. 2015). Calcium and magnesium ion concentrations of the rock samples were determined by microwave acid digestion, followed by ICP-MS measurements ( n = 3 ). The limestone sample used in the autoclave experiment had a Ca/Mg ratio of 22.1, and the dolomite sample had a ratio of 1.47 (see Table 2). In total, 11 different rock samples from different depths were digested. While all limestone samples had a Ca/Mg ratio > 15 , all dolomite samples had a ratio of 1.47–2.10 (Ueckert 2016). Hydrochemical conditions To assess saturation indices, as well as p(CO ) of the field and autoclave experiments, the software PhreeqC (version 3.4.0-12927, Parkhurst and Appelo 2013), and the database phreeqc.dat was used. Thermodynamic parameters for vaterite were taken from the SIT- database (sit.dat), those for argon and ethane were taken from the Lawrence-Livermore- National-Laboratory database (llnl.dat), and the Peng–Robinson parameters were taken from PREOS.xls (Elliot and Lira 2013). Ueckert et al. Geotherm Energy (2020) 8:7 Page 6 of 23 Fig. 2 Schematic overview of the field experiment. Here, injection stages are shown. During production, arrows point in the opposite direction, and the mixture of tap and aquifer water is discharged after flowing through the bypass Uecker t et al. Geotherm Energy (2020) 8:7 Page 7 of 23 Table 1 Breakdown of the heat storage test. Ueckert and Baumann (2019) Date Time Running time Stage ˙ ˙ Temp. C V L/s V L/s inj. prod. 2014-10-15 22:20 48:00 0 15 65 2014-10-17 22:20 60:00 0 15 2014-11-24 15:15 60:00 1 15 80 2014-11-27 03:15 47:45 1 15 2014-11-29 03:00 48:00 2 15 90 2014-12-01 03:00 36:00 2 15 2014-12-02 15:00 48:10 3 15 110 2014-12-04 15:10 35:50 3 15 2014-12-06 03:00 48:00 4 15 110 2014-12-08 03:00 96:00 4 15 2014-12-12 03:00 End The hydrochemical composition of the used tap waters (MUC and DGF) and of the reservoir water is given in Table 3. The reservoir water contains 922  mg/L total dissolved solids and is described as Na−HCO −Cl-type. The measured Ca/Mg ratio was 1.13, therefore a mainly dolomitic reservoir matrix (Langmuir 1971; Mayrhofer et al. 2014) along the flow paths leading to the borehole can be safely assumed. The isotopic composition of the aquifer water indi - cates significantly lower ambient temperatures compared to recent groundwater, thus putting the reservoir water into a glacial period. A full equilibrium with the matrix can safely be assumed for the reservoir fluids (Baumann et al. 2017). The calculated bubble point for the reservoir water was 2.9 bar, thus we can assume that no gas phase is present under reservoir conditions. The gas with the highest partial pressure is nitrogen (Ueck - ert and Baumann 2019). The injected tap water DGF at the heat storage test contains 525 mg/L total dissolved solids and is characterized as Ca−Mg−HCO -type. Hydrogeochemical modeling with PhreeqC results in a SI for calcite of −0.19 at 20 C . The water is slightly undersaturated, but within the quasi-equilibrium conditions (Merkel and Planer-Friedrich 2002). Heat- ◦ ◦ ing to 65 C results in a slight supersaturation (SI = 0.27 ) and heating to 110 C results in a ninefold supersaturation (SI = 0.95 ) with respect to calcite. The necessary amount of CO to reach a target SI of 0.1–0.2 for calcite in the heat exchanger was calculated for each temperature with PhreeqC and added prior to heating the water from a CO stor- age tank using an injection nozzle. The tap water MUC used in the autoclave experiments was also carbonate tap water, but had a lower magnesium ion concentration and less total dissolved solids (391 mg/L). It is characterized as Ca–Mg–HCO -type. Heating the water to 110 C results in a SI = 1.47. Filtration and particle analysis A custom-made filtration device manufactured in the institute’s workshop (Institute of Hydrochemistry, TUM) was used (see Fig. 4). This device consists of a brass piston to drive the sample gently through a series of up to 5 filters with as little contact to air as possible. All materials in contact with the fluid are made of PTFE, PE, or PMMA, Ueckert et al. Geotherm Energy (2020) 8:7 Page 8 of 23 Fig. 3 Dolomite (left upper picture) and limestone (left lower picture) samples used in the autoclave experiments. Beside the sample, a computed tomography scan is shown. The red circle in the dolomite (upper pictures) marks rhombohedral dolomite crystals, and the green rectangle in the limestone (lower picture) marks a shell. CT images give insights to the reactive surface area which is necessary for dissolution. CT images were taken by Dr. M. Köhne/Prof. Dr. H.J. Vogel, UFZ. The Ca/Mg ratio was determined by acid digestion and ICP-MS analysis Uecker t et al. Geotherm Energy (2020) 8:7 Page 9 of 23 Table 2 Matrix description. Bartels et al. (2015) Sample Description Depth, m b.s.l. Porosity, % Ca/Mg Limestone Microcrystalline grainstone 259 15.7 22.1 Iincl. ooids and peloids Calcite crystals Dolomite Macrocrystalline dolomite 397 4.62 1.47 Mostly idiomorph-hypidiomorph Pores up to 2 cm Dolomite crystals Table 3 Relevant ion concentrations of  the  injected tap (’tap water DGF’) and  aquifer water used in  the  field experiment, and  the  tap water used in  the  autoclave experiments (’tap water MUC’) Parameter Tap water DGF Aquifer water Tap water MUC T, C 13 23 19 pH, - 7.43 7.01 7.61 − − − Redox, mV 253 146 264 TDS,mg/L 525 922 391 0.18 7.7 0.16 Na , mmol/L 0.02 0.40 0.02 K , mmol/L 2+ 1.9 1.1 1.9 Ca , mmol/L 2+ 1.4 0.97 0.75 Mg , mmol/L 2+ 0.0002 0.0017 0.0003 Ba , mmol/L 2+ 0.0018 0.011 0.016 Sr , mmol/L 2+ 0.00001 0.00207 0.00028 Zn , mmol/L Cl , mmol/L 0.40 4.1 0.16 NO , mmol/L 0.25 < 0.0016 0.09 2− 0.13 0.21 0.41 SO , mmol/L HCO , mmol/L 5.7 7.7 4.6 Mg/Ca 0.72 0.88 0.39 p(CO ), bar 0.038 0.035 0.009 SI calcite − 0.19 − 0.19 0.16 SI aragonite − 0.35 − 0.33 0.02 SI vaterite − 0.79 − 0.76 − 0.43 The calculated partial pressures of CO and SI are listed below (tap water for T = 20 C and p = 1 bar ; aquifer water total refers to reservoir conditions) to reduce artifacts and contaminations. In contrast to other filtration devices, the gas composition of the fluid is kept almost untouched, which is very important for samples containing CO . Polycarbonate filters ( d = 47 mm ; pore size: 10, 5, 2, 1, and 0.1μm ) were purchased from Pieper Filters, Germany. The filters were left to dry in PE petri dishes (Greiner Bio-One, Austria) after filtration. The filtered volume for the samples collected in the field experiment was 1  L for 10–1 μm pore size filters and 0.5 L for 0.1μm pore size filters. One sample was ana - lyzed for each injection temperature, while several samples were analyzed during pro- ◦ ◦ duction ( n = 12 at T < 110 C , n = 8 at T = 110 C ). The filtrated volume in the Inj Inj autoclave experiment was 0.5 L, and 25 samples were analyzed in total. Ueckert et al. Geotherm Energy (2020) 8:7 Page 10 of 23 Fig. 4 Sketch of the filtration device used for particle size separation. A PMMA tube allows water filtration with reduced turbulences through PTFE filter holder. A weight pushing down on the water allows faster filtration at smaller pore sizes The description of the particles collected on the filters were determined using SEM/ EDX (Stereoscan 360/Röntec Leica, Cambridge, UK). Filters were sputtered with gold. Selected samples were cross-checked by Raman microscopy (LabRAM HR, HORIBA Scientific, Japan) to validate the morphological determination by SEM/EDX. The quantification of the particle concentration of the field experiment samples was determined by weighing (Balance ID: L106290, Mettler). Blanks were weighted for each pore size. In total, 50 sample filters were weighted. To determine the elemental composition of the filtered particles the filters were cov - ered by 36% HCl (s.p.) in a reaction vessel and dissolved at 200 C by microwave acid digestion (Berghoff, Germany) and then analyzed by ICP-MS (Elan 6100, Perkin-Elmer, Waltham, USA). For each run, including 12 reaction vessels, we did an acid blank and one filter blank (filter+acid). Results Particle description of the autoclave experiments Autoclave experiments with tap water MUC The p( CO ) varied between 0.008 and 0.019 bar from 45  to  110  C (SI = 0.70−1.47 ) calcite in the tap water experiments with air and between 0.012 and 0.024 bar from 45 to 110  C (SI = 0.52−1.39 ) in the tap water experiments with CO . The Mg/Ca ratio in all calcite 2 experiments was 0.39. The tap water was in quasi-equilibrium with calcium carbonate prior to heating the autoclave, and preexisting crystals were rather unlikely. Figure  5 shows characteristic images of the filters obtained in the tap water experi - ments. At temperatures of 45–80  C wheat-sheaf aragonites were dominating. Also spherical aragonites were found at 80 C . Acicular aragonites were only observed at tem- peratures of 110 C . Single crystals as well as aggregates were found in these experiments. Uecker t et al. Geotherm Energy (2020) 8:7 Page 11 of 23 ◦ ◦ Fig. 5 Crystals on the filter from the experiments with tap water at T = 45 , 60, 80 and 110 C . Pictures show aragonite crystals as dominating calcium carbonate polymorph: wheat-sheaf ( 45 C , ◦ ◦ ◦ 60 C ), spherical ( 80 C ), and acicular aragonite (110 C) Ueckert et al. Geotherm Energy (2020) 8:7 Page 12 of 23 Calcite crystals in a typical rhombohedral habit were not found. The absence of rhom - bohedral calcite crystals is surprising, at least at 45 C . Similar crystals were found in all experimental runs with tap water, regardless of the partial pressures in the gas phase (air vs. argon and CO ) and regardless whether rock samples were present in the vessel or not. The results suggest a formation of aragonite due to the increasing temperature. The higher the temperature, the more pronounced the needle-like structure habit. These setups result in an increase in temperature simultaneously to an increase in supersaturation. Autoclave experiments with ultra‑pure water The p( CO ) varied between 0.0006  and  0.0013 bar from 45  to  110 C , and the water is strongly undersaturated with respect to calcium carbonate. Calcium and magne- sium ion concentrations in the solution after heating (= dissolution of the rock matrix) varied from about 0.22 and 0.04  mmol/L (limestone) to 0.78 and 0.82  mmol/L (dolo- mite), depending on the matrix composition. As a consequence, the Mg/Ca ratio varied between 0.2 and 1. Rhombohedral shaped calcite crystals were found at temperatures from 45  to  110 C (see Fig.  6). Mostly aggregates with a compact habit were built (temperature of ◦ ◦ 45–80 C ), but at a temperature of 110 C micropores were visible. Almost no single crystals were found. Smaller crystals adhered on the surface of bigger ones, and grew there. No aragonite crystals were observed on the filters. The solution is undersaturated with respect to CaCO , and preexisting crystals were rather unlikely. After dissolution of the rock matrix, additional ions are present in the solution. It is likely that some homogeneous nucleation occurred at low, local supersatu- ration in the vicinity of the rock sample. However, the magnesium ion concentration had no impact on the crystal habit of the newly formed crystals. Quantification of the particle concentration The particle mass was below the limit of detection (1 mg/L by weighing) in the labora - tory and the field experiment. Also the elements determined in the supernatant of the digested filters by ICP/MS were below the limit of detection in both experimental set - ups. Thus, a semi-quantitative assessment based on SEM images was applied. The addition of CO to the tap water led to a very low particle concentration of the heated water in the field experiment. The particle size distribution was strongly shifted towards smaller particles on the 0.1μm filters (see Fig.  7, Pictures 1–5). A muddy matrix accumulated on the 0.1μm filter (see Fig. 7, Picture 5 and Fig. 9). The particle concentration increased slightly during production. We assume that this is due to an increase of the concentrations of calcium-, magnesium- and bicarbonate ions due to dissolution of the matrix, followed by particle growth (see Fig. 8). Particle description of the field experiment The p( CO ) varied between 0.26  and  1.1 bar from 65  to  110 C , and the correspond- ◦ ◦ ing saturation index for calcite varied between −0.13 at 65 C and 0.16 at 110 C . The initial Mg/Ca ratio during all injection stages was 0.72, and the median during pro- duction stages was 0.67 (0.44 was the lowest and 1.35 the highest ratio). The ratio Uecker t et al. Geotherm Energy (2020) 8:7 Page 13 of 23 Fig. 6 Crystals on the filters from the experiments with ultra-pure water at T = 45 , 60, 80, and 110 C . Pictures show trigonal rhombohedral calcite crystals as dominating calcium carbonate ◦ ◦ polymorph: mostly as aggregates (45–80 C ) with irregular ion emplacement on the surface. The big crystal at 110 C shows some microporosity from the front view Ueckert et al. Geotherm Energy (2020) 8:7 Page 14 of 23 Fig. 7 Overview of particles collected at the field site (here, at an injection temperature of 90 C ): low particle load on the filters with pore sizes of 10μm to 1μm (see picture 1–4) due to the CO addition. Only filters with 0.1μm pore sizes had a significant particle load (see picture 5). Mostly rounded particles are visible at pore sizes of 1–10μm (see red circles). Pore sizes of 0.1μm showed a muddy matrix, and no crystals can be identified depended on the dissolved reservoir matrix and varied through all stages. All other divalent cations had very low concentrations (< 0.02 mmol/L ). Sulfate ions had low concentrations (between 0.1 - 0.2 mmol/L). The same crystal morphologies were observed during injection (see Figs.  10 and 11, Picture  2) and production stages (see Figs.  10 and 11, Picture  1 and 3). EDX meas- urements show that the particles on the 10–1μm filters mainly consists of calcium carbonate (Fig.  8 Pic. 1–4). No crystals can be identified, but EDX measurements as well as element mapping suggest iron precipitates on the filters with 0.1  μ m pore sizes (Fig.  8, Picture 5). Modeling with PhreeqC and a Pourbaix diagram at the given pH– Eh conditions indicates iron hydroxides (Ueckert 2016). The cracks shown in Fig.  9 likely developed during drying of the filters. Uecker t et al. Geotherm Energy (2020) 8:7 Page 15 of 23 Fig. 8 Typical particle concentration during injection (left picture) and production (right picture) stages. Needle-like aragonites are marked by red ellipses. Spherical particles (here iron and zinc hydroxides) are marked by green circles. The particle concentration clearly increased during production. Here, at T = 110 , aragonite needles were dominating Inj Ueckert et al. Geotherm Energy (2020) 8:7 Page 16 of 23 Fig. 9 SEM picture of the filter cake (left), corresponding mapping (right, top), and EDX spectrum (right, bottom) on the 0.1μm filters, here at T = 110 C during production stage. Iron is the Inj dominant element. Modeling and a Pourbaix diagram indicate iron hydroxides Uecker t et al. Geotherm Energy (2020) 8:7 Page 17 of 23 Fig. 10 Typical carbonate crystals during T = 65 , 80, and 90 C : SEM picture (left) and corresponding EDX Inj ◦ ◦ ◦ spectrum (right). Examples for injection at 80 C (Picture 2) and production at 45 C (Picture 1, T = 65 C ) Inj ◦ ◦ and at 31 C (Picture 3, T = 80 C ). All pictures at these injection temperature indicate irregular calcite Inj crystallization. Still, the morphology suggests rhombohedral calcite crystals. Some of these crystals are magnesium bearing (see Picture 3) According to the SEM measurements, no aragonite crystals could be identified, nei - ther during injection (T = 65  –  90  C ) nor during production. The particles at this injection temperature generally showed a compact rhombohedral habit indicating calcites (Fig. 10), which got partly dissolved (Picture 1), or grew irregularly (Picture 2 and 3). Partly, EDX measurements suggest magnesium bearing particles (see Fig.  10, Picture 3). EDX suggest partly very small amounts of copper. However, once the injection temperature was set to 110 C , acicular aragonite crys- tals prevailed (Fig.  11, Pictures 1–3). Even when the temperature decreased to 37 C , after 92  h of production (see Fig.  11, Picture  1), aragonite crystals were dominating. EDX measurements suggest small peaks of other elements (e.g., copper and zinc), but no magnesium, strontium or barium peaks were measured. Ueckert et al. Geotherm Energy (2020) 8:7 Page 18 of 23 Fig. 11 Typical carbonate crystals during T = 110 C : SEM picture (left) and corresponding EDX spectrum Inj ◦ ◦ resp. mapping (right). Examples for injection (Picture 2) and production at 37 C (Picture 1) 60 C (Picture 3). All pictures at these injection temperatures show acicular aragonite crystals Neither vaterite crystals nor any spherical crystals were detected on any filter sample. Although the filters were analyzed randomly and the content of vaterite is usually sig - CaCO nificantly lower than the stable polymorphic forms of (e.g., Wang et  al. (2013): 8–20  %), the analyses should have identified at least some vaterite spheres, had they been present. Discussion In the laboratory experiments with tap water MUC the SI for calcite was close to equi- librium prior to heating, therefore no (or almost no) concentration gradient was present. Here, temperature predominately controlled the reaction. No difference in the crystal - lization with or without p(CO ) was seen. The influence seemed negligible at low CO 2 2 partial pressures up to 24  mbar (at 110 C , with CO addition). However, within our experimental range, the level of supersaturation strongly depended on the increase of temperature. We saw no influence on the affinity to crystallize as aragonite or calcite Uecker t et al. Geotherm Energy (2020) 8:7 Page 19 of 23 (SI 0.52–1.47), as aragonite crystals were always prevailing. According to the litera- calcite ture (see e.g., Bots et al. 2011), a low Mg/Ca ratio of 0.39, and the low sulfate ion con- centrations of 0.4 mmol/L should not inhibit calcite crystallization. However, aragonite ◦ ◦ crystals prevailed, even at 45 C . For temperatures up to 60 C wheat-sheaf aragonites were seen in the SEM-pictures. At temperatures of 110 C acicular aragonite crystals were predominant (see Fig.  5). Since no aragonite particles were found in the water at 20 C , homogeneous nucleation can be assumed. No macroscopically visible precipitates were found on the rock samples or in the reaction vessel. In contrast to the tap water experiments, temperature increase did not come not along with supersaturation in the ultra-pure water experiments. The solution was strongly undersaturated with respect to calcium carbonate. Therefore, a concentration gradi - ent between rock sample and ultra-pure water existed. Once the solution was heated, matrix got dissolved, and a low local supersaturation occurred. Here, only calcite crys- tallized and no aragonite crystals were observed, even at temperatures of 110 C . This might have been linked to the strong concentration gradient, which favors the crystal- lization of calcite over aragonite, or by the low supersaturation (Wang et al. 2013). Cal- cite crystallization should be inhibited by magnesium ion concentrations (Chen et  al. 2006; Reddy and Nancollas 1976). The dissolution of the rock matrix changed the Mg/Ca ratio from 0.2 to 1, but no influence on the crystallization of the CaCO polymorphs was seen. At least at these low ion concentrations of maximum 0.78  mmol/L calcium ions and 0.82 mmol/L magnesium ions, no inhibition of the calcite crystallization was seen. No nuclei were initially present in the solution, and homogeneous nucleation occurred. However, most crystals existed as aggregates which suggest a subsequent growth on the initial crystals. In summary, no influence of foreign ions and temperature on the crystallization of CaCO polymorphs was seen in the autoclave experiments. We assume that the level of supersaturation strongly influenced the crystallization of the CaCO polymorphs. Cal- cite crystals were dominant at low supersaturation, and aragonite crystals at saturation indices above 0.50. The autoclave experiments at very well-defined conditions served as a benchmark for the processes and the models. However, they were never intended to mimic the field conditions, which is not necessary if the underlying conceptual framework can be tested with that experiment. During the field experiment, we produced 15  L/s, 11 C cold carbonate tap water at atmospheric conditions which was in quasi-equilibrium with calcite. Prior to heating, CO was added to the water and the water was strongly undersaturated with respect to calcium carbonate. Heating in the plate heat exchangers brought the SI for calcite to 0.1–0.2 (slight supersaturation). Since the injection temperatures were high, and we had foreign ions, especially magnesium ions, in the solution we expected to find mainly aragonite particles. Surprisingly, calcite crystals prevailed at injection temperatures of ◦ ◦ 65  - 90 C , and aragonites were only present at injection temperatures of 110  C . The non-ideal crystallization of calcites during injection stages can be explained by low supersaturation of the tap water due to CO addition, and by undirected growth which points to turbulent flow. Due to the results of the autoclave experiments, we assume that the low supersaturation inhibited aragonite crystallization. The pressure was with 25 bar Ueckert et al. Geotherm Energy (2020) 8:7 Page 20 of 23 above bubble pressure (2.9 bar). Sharp pressure drops that occur in submersible pumps are absent in our setup. Thus degassing was rather unlikely. We had turbulent flow in the pipe ( Re = 120, 000 , at 20 C and 15 L/s), and we can also safely assume turbulences in the karstic system close to the borehole where flow velocities were high. We can there - fore assume that no diffusion-limited conditions were existent. Once the injected tap water reached the aquifer, a thermal equilibrium was established by mixing with the water in the reservoir and heat exchange with the matrix. The initial sharp temperature drop was followed by a slower decrease as the injected water propa- gates into the matrix. The decrease of the temperature caused a sharp decrease of the SI for calcite. The water became undersaturated with respect to calcite, and dissolved the carbonate matrix (Ueckert and Baumann 2019). Crystal nuclei and crystals in the water should also have been dissolved. After fast dissolution of carbonates in the aquifer to reach equilibrium with the rock matrix, the water became supersaturated during pro- duction, which caused crystal nuclei to grow irregularly under turbulent flow conditions (Han et al. 2004). Interestingly, we did not see differences in the crystal habit during production, com - pared to the injection stages. At injection temperatures of 65–90 C , and the following production stages, far from ideal rhombohedral calcites were characterized. At injection temperatures of 110 C , and the following production stages, acicular aragonite crystals were detected, even after a production time of 92  h, when the water had a minimum temperature of 37 C . The crystals at the corresponding production stage showed the same polymorphism. If detrital mobilization had occurred, one would not expect single crystals or varying polymorphs at different temperatures. We further assume that we had some homogeneous nucleation, but based on our data we are not able to distinguish if we had additionally heterogenous nucleation, e.g., on tiny iron hydroxide crystals. Calcite crystallization was favored in the autoclave experiments with ultra-pure water, and in the field experiment up to temperatures of 90 C , because of the low supersat- uration (Wang et  al. 2013). These calcites in the field experiment grew irregularly and mostly as compact single crystals. Even if aragonite crystals were suddenly dominating at 110 C , it is surprising that aragonites were stable for at least 92 h at a minimum tem- perature of 37 C . This is counter-intuitive because the strong undersaturation should lead to dissolution or at least shrinking size. Since the crystals of the injection and pro- duction stages were similar, although the boundary conditions changed, we assume that the dissolution of the crystals in the injected tap water was slow, and crystal nuclei were stable through the dissolution of the aquifer matrix. During production, these nuclei grew by additional ions in the solution. This hypothesis results in the assumption that crystal nuclei and crystals will be trans - ported between the wells of an operating system. That might be favorable for operation because it reduces precipitates at the wall of the pipes and the heat exchangers, as long as they are kept in solution. Conclusion Increasing temperature from 45 to 110  C , Mg/Ca ratios up to 1, as well as low p(CO ) (up to 24  mbar) had no influence on the crystallization of the CaCO polymorphs in the autoclave experiments. It seems that supersaturation controlled the CaCO 3 Uecker t et al. Geotherm Energy (2020) 8:7 Page 21 of 23 polymorphs. Only aragonite crystals were morphologically identified in the tap water experiments. Lower temperatures up to 60 C resulted in wheat–sheaf structures, and the higher the temperature the more acicular aragonites prevailed. A strong concen- tration gradient and undersaturation in the ultra-pure water experiments resulted in exclusive calcite crystallization, even at high temperatures of 110 C , and high Mg/Ca ratios of 1. The push–pull heat storage test was in line with the results of the laboratory tests showing that varying Mg/Ca ratios, and p(CO ) had no influence on the crystallization of the CaCO polymorphs. The low supersaturation within the quasi-equilibrium up to 90 C resulted in calcite crystallization. Turbulent flow was the reaction-controlling pro - cess, and inhibited the crystallization due to irregular growth. Aragonite crystals pre- vailed at injection temperatures of 110 C. Surprisingly, CaCO polymorphs were similar between injection and the following production stage. Based on these observations, we assume that nuclei and crystals were already injected during the injection stages. Once the water reached the aquifer and was cooling, dissolution of the aquifer matrix occurred and more calcium and magnesium ions were available in the water. As a consequence, existing nuclei were able to grow and were produced during production stages in their injected polymorphic form. Even if the solubility products of aragonite and calcite are related, it is necessary to establish a sound knowledge of the crystallization of the calcium carbonate polymorphs in natural systems to avoid precipitations. In our experiments, we have shown the first results, and possible explanations of the crystallization of CaCO in geothermal sys- tems. The next step should be an investigation of CaCO polymorphs by in situ experi- ments. The conditions in a full-scale aquifer heat storage system are very similar to the push–pull test, except that the cooling of the water takes place in heat exchangers above ground and the dissolution is occurring at the cold well. We expect that crystals are transported between the wells, which is favorable for the operation, because this reduces precipitation at the walls of pipes and heat exchangers. These particles should therefore be kept in solution, rather than removing them by filters. Abbreviations DGF: Sample name: tap water in the field experiment; ICP-MS: Inductively coupled plasma mass spectrometry; MUC: Sample name: tap water in the autoclave experiment; UPW: Ultra-pure water; SEM/EDX: Scanning electron microscope/ energy-dispersive X-ray spectroscopy; SI: Saturation Index; TDS: Total dissolved solids; T : Injection temperature of the Inj tap water at the field experiment; T : Production temperature of the tap water at the field experiment; PE: Polyethyl- Prod ene; PMMA: Polymethylmethacrylate; PTFE: Polytetrafluoroethylene. Acknowledgements The financial support by the Bayerisches Staatsministerium für Wirtschaft und Medien, Energie und Technologie and the BMW Group is gratefully acknowledged. We would like to thank our colleagues Sebastian Wieseman and Roland Hoppe for technical improvements of the autoclave and constructing the filtration device. Christine Benning is gratefully acknowledged for SEM/EDX and ICP-MS measurements. Thank you, Philipp Anger, for Raman microscopy measurements. We would like to thank our cooperation partners Daniel Bohnsack and Dr. Kai Zosseder, Chair of Hydrogeology at TUM, for providing us data of the rock properties. Last but not least, we want to thank Prof. Dr. Hans-Jörg Vogel and PD Dr. Maximilian Köhne, Chair of Soil System Science at the UFZ Halle, for the CT images! Authors’ contributions MU planned, organized, and performed the field experiments and evaluation, planned and evaluated the autoclave experiments and did the graphical representation. CW organized and performed the autoclave experiments. TB had the idea, designed and implemented the evaluation routines of the field test. All authors read and approved the final manuscript. Funding This work was partially funded by the Bavarian Ministry of Economic Affairs, Energy and Technology and the BMW Group. Ueckert et al. 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Mineralneubildungen und Partikeltransport im Thermalwasserkreislauf geother- mischer Anlagen Deutschlands In: Zeitschrift geol. Wissenschaften 2011. Wray JL, Daniels F. Precipitation of calcite and aragonite. J Am Chem Soc. 1956;79(9):2031–4. 2+ Zhang Y, Dawe R. Influence of Mg on the kinetics of calcite precipitation and calcite crystal morphology. Chem Geol. 2000;163:129–38. https ://doi.org/10.1016/S0009 -2541(99)00097 -2. Publisher’s Note Springer Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations. http://www.deepdyve.com/assets/images/DeepDyve-Logo-lg.png Geothermal Energy Springer Journals

Crystallization of calcium carbonate in a large-scale push–pull heat storage test in the Upper Jurassic carbonate aquifer

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Abstract

martina.ueckert@tum.de Institute of Hydrochemistry, Crystallization of carbonates is a key process affecting the operation of geothermal Technical University facilities and aquifer heat storage systems. The crystals formed in an aquifer heat of Munich, Marchioninistr. 17, 81377 Munich, Germany storage test in the Upper Jurassic carbonate aquifer were investigated at injection Full list of author information ◦ ◦ temperatures of 65 C to 110 C , with varying CO partial pressures, and varying Mg/Ca is available at the end of the ratios. Water samples were directly filtrated, and analyzed by SEM/EDX. Complementary article autoclave experiments were run. In the autoclave experiments with tap water, arago- nite crystals dominated at all temperatures (45–110 C ). In the autoclave experiments with ultra-pure water, calcite crystals dominated at the same temperatures. In the field test, mainly calcite crystals were found up to temperatures of 90 C . Only at very high temperatures of 110 C aragonite crystallization prevailed. CO partial pressure varied especially between injection and production stages. Mg/Ca ratio varied through all stages, and depended on the dissolution of the rock matrix. Together with the auto- clave experiments, this study suggest that temperature and Mg/Ca ratio had no influ- ence on the crystallization, and only supersaturation affected the CaO polymorphs. We further assume that we produced initially injected crystals back during the following production stage. That results in the assumption that existing particles can maintain an equilibrium in the dispersion, and reduce precipitation on surfaces like pipes and heat exchangers. Keywords: CaCO polymorphs, Calcite, Aragonite, Carbonate aquifer, Autoclave experiments Introduction The efficiency of geothermal power generation sites as well as aquifer thermal energy storage in carbonate aquifers is still affected by precipitations of calcium carbonate poly - morphs (Lee 2013; Mundhenk et al. 2013; Ueckert and Baumann 2019). Precipitation of calcium carbonate in geothermal systems is mainly caused by temperature and pressure changes (Baumann et al. 2017). Precipitates of a geothermal or thermal energy storage system are usually investigated by analyzing the occurring scalings (see e.g., Wanner et  al. 2017). On the other hand, there are only very few studies addressing crystallization processes or the particle load of geothermal water (Ueckert 2016; Wolfgramm et al. 2011). As a consequence, little is © The Author(s) 2020. This article is licensed under a Creative Commons Attribution 4.0 International License, which permits use, sharing, adaptation, distribution and reproduction in any medium or format, as long as you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons licence, and indicate if changes were made. The images or other third party material in this article are included in the article’s Creative Commons licence, unless indicated otherwise in a credit line to the material. If material is not included in the article’s Creative Commons licence and your intended use is not permitted by statutory regulation or exceeds the permitted use, you will need to obtain permission directly from the copyright holder. To view a copy of this licence, visit http://creat iveco mmons .org/licen ses/by/4.0/. Ueckert et al. Geotherm Energy (2020) 8:7 Page 2 of 23 known about the crystallization process of the polymorphic forms of calcium carbon- ate in geothermal systems. The crystallization itself has been studied under well-defined laboratory conditions for several years (see e.g., Reddy and Nancollas 1970) and is still a major research topic (see e.g., Schmidt et al. 2019). In classical nucleation theory, crystallization is divided into nucleation and crys- tal growth. While nucleation is depends on the supersaturation of the solution, crys- tal growth is determined by the diffusion of atoms or ions to and on the surface of the nuclei and their following incorporation into the lattice. On the other hand, non- classical crystallization theory was introduced to explain, e.g., the crystallization via amorphous precursors or the formation of mesocrystals (De Yoreo and Vekilov 2003; Meldrum and Cölfen 2008). It is important to explain the crystallization of calcium car- bonate polymorphs, because the (meta)stable forms of calcium carbonate vaterite, cal- cite and aragonite crystallize often via amorphous calcium carbonate (ACC) precursor. The transformation of ACC to the crystalline polymorphs is extremely fast [ < 2 min at 25 C (Rodriguez-Blanco et al. 2011)], and ACC is usually not stable in natural systems. The concept of homogeneous and heterogeneous nucleation was introduced in the lit - erature, and plays an important role in calcium carbonate crystallization. Once a solu- tion reaches a critical supersaturation, a nucleus can spontaneously form, which is called homogeneous nucleation. In heterogeneous nucleation, a surface is already existing, which makes nucleation energetically less demanding (Meldrum and Cölfen 2008). To describe the crystallization of calcite, a diffusion-reaction model was suggested. Here, calcite growth is regulated by two processes: mass transport and surface reac- tion (see e.g., Tai et  al. 2006). Wang et  al. (2013) supported this for calcium carbonate polymorphs experimentally. According to their study, calcite crystallization is favored at high concentration gradients, whereas high temperatures favor aragonite crystalliza- tion. Already Wray and Daniels (1956) reported that aragonite is prevailing over calcite at 45 C . Ahn et al. (2005) postulated that supersaturation of the solution is controlling the growth of the polymorphs and the affinity to crystallize as vaterite, calcite, and arag - onite increases with decreasing supersaturation. Other cations, especially magnesium ions, inhibit crystallization processes of calcite (Chen et  al. 2006; Tai and Chien 1998; Morse et al. 1997; Reddy and Nancollas 1976; Zhang and Dawe 2000), due to their incor- poration into the calcite lattice. However, the presence of magnesium ions is reported to accelerate the crystallization of aragonite (Berner 1975). Furthermore, the availability of magnesium ions inhibits the transformation of vaterite into calcite (Kitamura 2001). Niedermayr et al. (2013) state that the coexisting presence of polyaspartic acid and mag- nesium ions favor the formation of calcite over aragonite and vaterite. Also, the influ - ence of sulfate ions is discussed. Bots et al. (2011) performed laboratory experiments to see the influence of sulfate ions in combination with Mg/Ca ratios on the precipitation of the CaCO polymorphs. Without sulfate or magnesium ions in the solution, calcite crystals prevailed. Without sulfate ions in the solution, aragonite was the dominant pol- ymorph (> 90 % ) at a Mg/Ca ratio of 0.77. As soon as sulfate ions (minimum of 5.1 mM) were added to the solution, aragonite was already at a Mg/Ca ratio of 0.36, dominating the polymorph. The role of other bivalent cations, such as strontium or barium, has been investigated for several years (see e.g., Wray and Daniels 1956), and is still part of the Uecker t et al. Geotherm Energy (2020) 8:7 Page 3 of 23 main research (see e.g., Littlewood et al. 2017). But, according to them, it is likely that it favors aragonite crystallization over calcite. Han et al. (2006) precipitated calcium carbonates by injecting a CO /N -gas mixture 2 2 into a CaCl solution. Vaterite formation is favored at high gas flow rates and low initial CaCl concentrations. An increase from 33 to 66 vol% CO in the injected gas results in 2 2 an increase of vaterite crystals. Aragonite needles were only observed at temperatures of 60 C . It seemed that the bubbling time and the stirring rate are not dominant for the morphology of the carbonates. This experiment seems to be very close to the degas - sing of thermal water in geothermal systems. However, in this experiment CO serves as a source for carbonates, i.e., the equilibria in the solution are controlled by the mass transfer rates of CO from gas phase bubbles into the liquid phase, which at the given experimental conditions result in a net dissolution of CO . In contrast, in geothermal systems in the Upper Jurassic carbonate aquifer in the Bavarian Molasse Basin, no gas phase is present under reservoir conditions with pressures exceeding 200 bar. Inorganic carbon is dissolved and the species distribution is controlled by the carbonic-acid-equi- librium. During production of geothermal water, gas bubbles are formed if the pressure is lower than the sum of the partial pressures of the dissolved gases (bubble point, typi- cally 2–25 bar). In this case, CO is stripped from the geothermal water. Consequently, the carbonic-acid-equilibrium is shifted to higher pH and precipitation of carbonates occurs. In both cases, the presence of the air–water interface at the bubble has to be considered (Baumann 2016; Baumann et al. 2017). As seen in all these well-defined laboratory experiments, the crystallization of cal - cium carbonate polymorphs is very complex, and as soon as one boundary condition is changed, another polymorph might preferentially be formed. Since the knowledge of crystallization processes is indispensable for avoiding cost- intensive shutdowns due to scalings, research focusing on the behavior in complex natural systems is necessary. During a push–pull heat storage test with well-defined boundary conditions, which results are described in Ueckert and Baumann (2019), addi- tionally the crystallization of calcium carbonate polymorphs was analyzed. To support our findings, we performed experiments in a high-temperature autoclave to further reduce the degrees of freedom for the evaluation. Materials and methods Description of the autoclave experiments Experiments were run in an autoclave (Midiclave, Büchi, Switzerland), which has a total volume of 1 L (see Fig  1). The autoclave was filled with 0.5 L of water. The rock matrix (volume of 100 resp. 150 cm ) was put into a stainless steel basket and submersed in water in the center of the reaction vessel. After closing the autoclave, the remaining air was exchanged with argon (99,996 Vol.% purity, Westfalen, Germany). Three different setups were chosen: in the first setup, a rock sample and 500 mL ultra- pure water (= UPW , QPAK 1, Merck) were put into the reaction vessel (see Fig.  3). In the second setup, carbonate tap water (=‘tap water MUC’), was used instead of UPW and a defined initial CO partial pressure (about 5–8 mbar at 20 C and a total pressure of 1.2 bar) was established in the reaction chamber by adding a defined volume of CO . 2 Ueckert et al. Geotherm Energy (2020) 8:7 Page 4 of 23 Fig. 1 Schematic overview of the autoclave experiment. The defined volume of CO is injected by means of a gas syringe In the third setup, only tap water MUC was heated without a rock sample and served as a blank reference. For each setup, five experiments were run at temperatures of 45, 60, 80 and 110 C . The autoclave was heated to the target temperature within 15 min. At temperatures up to 80 C , samples for fluid and particle characterization were taken at the bottom valve of the autoclave immediately after the target temperature had been reached. Samples at higher temperatures were taken after a short cooling period of 10 min to reach 80 C. The experiments with rock sample were performed once with a limestone sample (see lower picture Fig. 3), and once with a dolomite sample (see upper Fig. 3). 12 experiments were run at one rock sample, so 36 samples were taken in total. The reaction vessel was rinsed in two steps after two experiments: first 0.8 L citric acid was heated, and then discarded. Afterwards 1-L ultra-pure water was filled in the auto - clave and then removed. No stirring device was used to simulate the reactions off the main flow paths. The rationale behind that is that most of the heat transfer happens in the karstified layer while reactive surface is necessary for dissolution. Description of the field experiment A detailed description of the heat storage test performed in the Upper Jurassic carbonate aquifer in the North East-Molasse Basin in the city Dingolfing, the operational design and the hydrogeochemical model are given in Bartels et al. (2015) and Ueckert and Bau- mann (2019). The test design at the research borehole was a push–pull test with five injection stages of hot carbonate tap water (injection temperature T = 65 , 80, 90, 110, and 110 C ) into Inj Uecker t et al. Geotherm Energy (2020) 8:7 Page 5 of 23 a carbonate aquifer, each immediately followed by a production stage (see Fig.  2). The flow rate was set to 15 L/s (see Table 1). To prevent precipitates in the heat exchangers, CO was added prior to heating the tap water. The required concentration was calculated using the hydrogeochemical mod - eling software PhreeqC (Parkhurst and Appelo 2013). Taking the reaction rates of cal- cite precipitation and the short residence times (about 0.13 s) in the heat exchanger into account, a saturation index (SI) for calcite between 0.1 and 0.2 was targeted. This slight supersaturation was intended to prevent corrosion effects in the pipes and ground-level facilities. The calculations resulted in CO concentrations between 90  mg/L for T of 2 Inj ◦ ◦ 65 C and 420 mg/L for T of 110 C and a resulting pH of 6.78 and 6.22, respectively. Inj Water samples were taken at a bypass close to the well head. At temperatures exceed- ing 80 C , a cooler was used to maintain safe sampling conditions. Samples were taken during injection (tap water, controlled temperature, controlled CO content) as well as during production (mixture of tap and aquifer water, decreasing temperature (T ), Prod varying CO content), and were filtered immediately. The pressure at the top of the aquifer was constant at 25.3 bar during the production stages. Matrix characterization The upper 20 m of the target aquifer at the test site are built of limestone, layered with dolomitic breccia and dolomites. The rest of the aquifer consists of dolomites and dolo - mitic breccia (about 200  m). Dolomites were formed by dolomitization of limestones. Circulation loss occurred from 297 to 397 m b.s.l., and no cored drilling was possible at that depth. The evaluation of the heat storage test showed that the water is mostly flow - ing in a karstified structure ( = main flow path ), but a smaller amount of water will be transported in the surrounding pores of the rocks (Bartels et al. 2015). Crushed pieces of the core samples were used for the autoclave experiments (see Fig. 3). CT pictures of the rock samples provide data on the accessible surface area, i.e., the area at which reactions can occur under rate-limited conditions. The limestone samples show high contents of ooids and peloids (see lower picture Fig. 3, marked with a green rectangle), and no arag- onite crystals were found (Bartels et al. 2015). Calcium and magnesium ion concentrations of the rock samples were determined by microwave acid digestion, followed by ICP-MS measurements ( n = 3 ). The limestone sample used in the autoclave experiment had a Ca/Mg ratio of 22.1, and the dolomite sample had a ratio of 1.47 (see Table 2). In total, 11 different rock samples from different depths were digested. While all limestone samples had a Ca/Mg ratio > 15 , all dolomite samples had a ratio of 1.47–2.10 (Ueckert 2016). Hydrochemical conditions To assess saturation indices, as well as p(CO ) of the field and autoclave experiments, the software PhreeqC (version 3.4.0-12927, Parkhurst and Appelo 2013), and the database phreeqc.dat was used. Thermodynamic parameters for vaterite were taken from the SIT- database (sit.dat), those for argon and ethane were taken from the Lawrence-Livermore- National-Laboratory database (llnl.dat), and the Peng–Robinson parameters were taken from PREOS.xls (Elliot and Lira 2013). Ueckert et al. Geotherm Energy (2020) 8:7 Page 6 of 23 Fig. 2 Schematic overview of the field experiment. Here, injection stages are shown. During production, arrows point in the opposite direction, and the mixture of tap and aquifer water is discharged after flowing through the bypass Uecker t et al. Geotherm Energy (2020) 8:7 Page 7 of 23 Table 1 Breakdown of the heat storage test. Ueckert and Baumann (2019) Date Time Running time Stage ˙ ˙ Temp. C V L/s V L/s inj. prod. 2014-10-15 22:20 48:00 0 15 65 2014-10-17 22:20 60:00 0 15 2014-11-24 15:15 60:00 1 15 80 2014-11-27 03:15 47:45 1 15 2014-11-29 03:00 48:00 2 15 90 2014-12-01 03:00 36:00 2 15 2014-12-02 15:00 48:10 3 15 110 2014-12-04 15:10 35:50 3 15 2014-12-06 03:00 48:00 4 15 110 2014-12-08 03:00 96:00 4 15 2014-12-12 03:00 End The hydrochemical composition of the used tap waters (MUC and DGF) and of the reservoir water is given in Table 3. The reservoir water contains 922  mg/L total dissolved solids and is described as Na−HCO −Cl-type. The measured Ca/Mg ratio was 1.13, therefore a mainly dolomitic reservoir matrix (Langmuir 1971; Mayrhofer et al. 2014) along the flow paths leading to the borehole can be safely assumed. The isotopic composition of the aquifer water indi - cates significantly lower ambient temperatures compared to recent groundwater, thus putting the reservoir water into a glacial period. A full equilibrium with the matrix can safely be assumed for the reservoir fluids (Baumann et al. 2017). The calculated bubble point for the reservoir water was 2.9 bar, thus we can assume that no gas phase is present under reservoir conditions. The gas with the highest partial pressure is nitrogen (Ueck - ert and Baumann 2019). The injected tap water DGF at the heat storage test contains 525 mg/L total dissolved solids and is characterized as Ca−Mg−HCO -type. Hydrogeochemical modeling with PhreeqC results in a SI for calcite of −0.19 at 20 C . The water is slightly undersaturated, but within the quasi-equilibrium conditions (Merkel and Planer-Friedrich 2002). Heat- ◦ ◦ ing to 65 C results in a slight supersaturation (SI = 0.27 ) and heating to 110 C results in a ninefold supersaturation (SI = 0.95 ) with respect to calcite. The necessary amount of CO to reach a target SI of 0.1–0.2 for calcite in the heat exchanger was calculated for each temperature with PhreeqC and added prior to heating the water from a CO stor- age tank using an injection nozzle. The tap water MUC used in the autoclave experiments was also carbonate tap water, but had a lower magnesium ion concentration and less total dissolved solids (391 mg/L). It is characterized as Ca–Mg–HCO -type. Heating the water to 110 C results in a SI = 1.47. Filtration and particle analysis A custom-made filtration device manufactured in the institute’s workshop (Institute of Hydrochemistry, TUM) was used (see Fig. 4). This device consists of a brass piston to drive the sample gently through a series of up to 5 filters with as little contact to air as possible. All materials in contact with the fluid are made of PTFE, PE, or PMMA, Ueckert et al. Geotherm Energy (2020) 8:7 Page 8 of 23 Fig. 3 Dolomite (left upper picture) and limestone (left lower picture) samples used in the autoclave experiments. Beside the sample, a computed tomography scan is shown. The red circle in the dolomite (upper pictures) marks rhombohedral dolomite crystals, and the green rectangle in the limestone (lower picture) marks a shell. CT images give insights to the reactive surface area which is necessary for dissolution. CT images were taken by Dr. M. Köhne/Prof. Dr. H.J. Vogel, UFZ. The Ca/Mg ratio was determined by acid digestion and ICP-MS analysis Uecker t et al. Geotherm Energy (2020) 8:7 Page 9 of 23 Table 2 Matrix description. Bartels et al. (2015) Sample Description Depth, m b.s.l. Porosity, % Ca/Mg Limestone Microcrystalline grainstone 259 15.7 22.1 Iincl. ooids and peloids Calcite crystals Dolomite Macrocrystalline dolomite 397 4.62 1.47 Mostly idiomorph-hypidiomorph Pores up to 2 cm Dolomite crystals Table 3 Relevant ion concentrations of  the  injected tap (’tap water DGF’) and  aquifer water used in  the  field experiment, and  the  tap water used in  the  autoclave experiments (’tap water MUC’) Parameter Tap water DGF Aquifer water Tap water MUC T, C 13 23 19 pH, - 7.43 7.01 7.61 − − − Redox, mV 253 146 264 TDS,mg/L 525 922 391 0.18 7.7 0.16 Na , mmol/L 0.02 0.40 0.02 K , mmol/L 2+ 1.9 1.1 1.9 Ca , mmol/L 2+ 1.4 0.97 0.75 Mg , mmol/L 2+ 0.0002 0.0017 0.0003 Ba , mmol/L 2+ 0.0018 0.011 0.016 Sr , mmol/L 2+ 0.00001 0.00207 0.00028 Zn , mmol/L Cl , mmol/L 0.40 4.1 0.16 NO , mmol/L 0.25 < 0.0016 0.09 2− 0.13 0.21 0.41 SO , mmol/L HCO , mmol/L 5.7 7.7 4.6 Mg/Ca 0.72 0.88 0.39 p(CO ), bar 0.038 0.035 0.009 SI calcite − 0.19 − 0.19 0.16 SI aragonite − 0.35 − 0.33 0.02 SI vaterite − 0.79 − 0.76 − 0.43 The calculated partial pressures of CO and SI are listed below (tap water for T = 20 C and p = 1 bar ; aquifer water total refers to reservoir conditions) to reduce artifacts and contaminations. In contrast to other filtration devices, the gas composition of the fluid is kept almost untouched, which is very important for samples containing CO . Polycarbonate filters ( d = 47 mm ; pore size: 10, 5, 2, 1, and 0.1μm ) were purchased from Pieper Filters, Germany. The filters were left to dry in PE petri dishes (Greiner Bio-One, Austria) after filtration. The filtered volume for the samples collected in the field experiment was 1  L for 10–1 μm pore size filters and 0.5 L for 0.1μm pore size filters. One sample was ana - lyzed for each injection temperature, while several samples were analyzed during pro- ◦ ◦ duction ( n = 12 at T < 110 C , n = 8 at T = 110 C ). The filtrated volume in the Inj Inj autoclave experiment was 0.5 L, and 25 samples were analyzed in total. Ueckert et al. Geotherm Energy (2020) 8:7 Page 10 of 23 Fig. 4 Sketch of the filtration device used for particle size separation. A PMMA tube allows water filtration with reduced turbulences through PTFE filter holder. A weight pushing down on the water allows faster filtration at smaller pore sizes The description of the particles collected on the filters were determined using SEM/ EDX (Stereoscan 360/Röntec Leica, Cambridge, UK). Filters were sputtered with gold. Selected samples were cross-checked by Raman microscopy (LabRAM HR, HORIBA Scientific, Japan) to validate the morphological determination by SEM/EDX. The quantification of the particle concentration of the field experiment samples was determined by weighing (Balance ID: L106290, Mettler). Blanks were weighted for each pore size. In total, 50 sample filters were weighted. To determine the elemental composition of the filtered particles the filters were cov - ered by 36% HCl (s.p.) in a reaction vessel and dissolved at 200 C by microwave acid digestion (Berghoff, Germany) and then analyzed by ICP-MS (Elan 6100, Perkin-Elmer, Waltham, USA). For each run, including 12 reaction vessels, we did an acid blank and one filter blank (filter+acid). Results Particle description of the autoclave experiments Autoclave experiments with tap water MUC The p( CO ) varied between 0.008 and 0.019 bar from 45  to  110  C (SI = 0.70−1.47 ) calcite in the tap water experiments with air and between 0.012 and 0.024 bar from 45 to 110  C (SI = 0.52−1.39 ) in the tap water experiments with CO . The Mg/Ca ratio in all calcite 2 experiments was 0.39. The tap water was in quasi-equilibrium with calcium carbonate prior to heating the autoclave, and preexisting crystals were rather unlikely. Figure  5 shows characteristic images of the filters obtained in the tap water experi - ments. At temperatures of 45–80  C wheat-sheaf aragonites were dominating. Also spherical aragonites were found at 80 C . Acicular aragonites were only observed at tem- peratures of 110 C . Single crystals as well as aggregates were found in these experiments. Uecker t et al. Geotherm Energy (2020) 8:7 Page 11 of 23 ◦ ◦ Fig. 5 Crystals on the filter from the experiments with tap water at T = 45 , 60, 80 and 110 C . Pictures show aragonite crystals as dominating calcium carbonate polymorph: wheat-sheaf ( 45 C , ◦ ◦ ◦ 60 C ), spherical ( 80 C ), and acicular aragonite (110 C) Ueckert et al. Geotherm Energy (2020) 8:7 Page 12 of 23 Calcite crystals in a typical rhombohedral habit were not found. The absence of rhom - bohedral calcite crystals is surprising, at least at 45 C . Similar crystals were found in all experimental runs with tap water, regardless of the partial pressures in the gas phase (air vs. argon and CO ) and regardless whether rock samples were present in the vessel or not. The results suggest a formation of aragonite due to the increasing temperature. The higher the temperature, the more pronounced the needle-like structure habit. These setups result in an increase in temperature simultaneously to an increase in supersaturation. Autoclave experiments with ultra‑pure water The p( CO ) varied between 0.0006  and  0.0013 bar from 45  to  110 C , and the water is strongly undersaturated with respect to calcium carbonate. Calcium and magne- sium ion concentrations in the solution after heating (= dissolution of the rock matrix) varied from about 0.22 and 0.04  mmol/L (limestone) to 0.78 and 0.82  mmol/L (dolo- mite), depending on the matrix composition. As a consequence, the Mg/Ca ratio varied between 0.2 and 1. Rhombohedral shaped calcite crystals were found at temperatures from 45  to  110 C (see Fig.  6). Mostly aggregates with a compact habit were built (temperature of ◦ ◦ 45–80 C ), but at a temperature of 110 C micropores were visible. Almost no single crystals were found. Smaller crystals adhered on the surface of bigger ones, and grew there. No aragonite crystals were observed on the filters. The solution is undersaturated with respect to CaCO , and preexisting crystals were rather unlikely. After dissolution of the rock matrix, additional ions are present in the solution. It is likely that some homogeneous nucleation occurred at low, local supersatu- ration in the vicinity of the rock sample. However, the magnesium ion concentration had no impact on the crystal habit of the newly formed crystals. Quantification of the particle concentration The particle mass was below the limit of detection (1 mg/L by weighing) in the labora - tory and the field experiment. Also the elements determined in the supernatant of the digested filters by ICP/MS were below the limit of detection in both experimental set - ups. Thus, a semi-quantitative assessment based on SEM images was applied. The addition of CO to the tap water led to a very low particle concentration of the heated water in the field experiment. The particle size distribution was strongly shifted towards smaller particles on the 0.1μm filters (see Fig.  7, Pictures 1–5). A muddy matrix accumulated on the 0.1μm filter (see Fig. 7, Picture 5 and Fig. 9). The particle concentration increased slightly during production. We assume that this is due to an increase of the concentrations of calcium-, magnesium- and bicarbonate ions due to dissolution of the matrix, followed by particle growth (see Fig. 8). Particle description of the field experiment The p( CO ) varied between 0.26  and  1.1 bar from 65  to  110 C , and the correspond- ◦ ◦ ing saturation index for calcite varied between −0.13 at 65 C and 0.16 at 110 C . The initial Mg/Ca ratio during all injection stages was 0.72, and the median during pro- duction stages was 0.67 (0.44 was the lowest and 1.35 the highest ratio). The ratio Uecker t et al. Geotherm Energy (2020) 8:7 Page 13 of 23 Fig. 6 Crystals on the filters from the experiments with ultra-pure water at T = 45 , 60, 80, and 110 C . Pictures show trigonal rhombohedral calcite crystals as dominating calcium carbonate ◦ ◦ polymorph: mostly as aggregates (45–80 C ) with irregular ion emplacement on the surface. The big crystal at 110 C shows some microporosity from the front view Ueckert et al. Geotherm Energy (2020) 8:7 Page 14 of 23 Fig. 7 Overview of particles collected at the field site (here, at an injection temperature of 90 C ): low particle load on the filters with pore sizes of 10μm to 1μm (see picture 1–4) due to the CO addition. Only filters with 0.1μm pore sizes had a significant particle load (see picture 5). Mostly rounded particles are visible at pore sizes of 1–10μm (see red circles). Pore sizes of 0.1μm showed a muddy matrix, and no crystals can be identified depended on the dissolved reservoir matrix and varied through all stages. All other divalent cations had very low concentrations (< 0.02 mmol/L ). Sulfate ions had low concentrations (between 0.1 - 0.2 mmol/L). The same crystal morphologies were observed during injection (see Figs.  10 and 11, Picture  2) and production stages (see Figs.  10 and 11, Picture  1 and 3). EDX meas- urements show that the particles on the 10–1μm filters mainly consists of calcium carbonate (Fig.  8 Pic. 1–4). No crystals can be identified, but EDX measurements as well as element mapping suggest iron precipitates on the filters with 0.1  μ m pore sizes (Fig.  8, Picture 5). Modeling with PhreeqC and a Pourbaix diagram at the given pH– Eh conditions indicates iron hydroxides (Ueckert 2016). The cracks shown in Fig.  9 likely developed during drying of the filters. Uecker t et al. Geotherm Energy (2020) 8:7 Page 15 of 23 Fig. 8 Typical particle concentration during injection (left picture) and production (right picture) stages. Needle-like aragonites are marked by red ellipses. Spherical particles (here iron and zinc hydroxides) are marked by green circles. The particle concentration clearly increased during production. Here, at T = 110 , aragonite needles were dominating Inj Ueckert et al. Geotherm Energy (2020) 8:7 Page 16 of 23 Fig. 9 SEM picture of the filter cake (left), corresponding mapping (right, top), and EDX spectrum (right, bottom) on the 0.1μm filters, here at T = 110 C during production stage. Iron is the Inj dominant element. Modeling and a Pourbaix diagram indicate iron hydroxides Uecker t et al. Geotherm Energy (2020) 8:7 Page 17 of 23 Fig. 10 Typical carbonate crystals during T = 65 , 80, and 90 C : SEM picture (left) and corresponding EDX Inj ◦ ◦ ◦ spectrum (right). Examples for injection at 80 C (Picture 2) and production at 45 C (Picture 1, T = 65 C ) Inj ◦ ◦ and at 31 C (Picture 3, T = 80 C ). All pictures at these injection temperature indicate irregular calcite Inj crystallization. Still, the morphology suggests rhombohedral calcite crystals. Some of these crystals are magnesium bearing (see Picture 3) According to the SEM measurements, no aragonite crystals could be identified, nei - ther during injection (T = 65  –  90  C ) nor during production. The particles at this injection temperature generally showed a compact rhombohedral habit indicating calcites (Fig. 10), which got partly dissolved (Picture 1), or grew irregularly (Picture 2 and 3). Partly, EDX measurements suggest magnesium bearing particles (see Fig.  10, Picture 3). EDX suggest partly very small amounts of copper. However, once the injection temperature was set to 110 C , acicular aragonite crys- tals prevailed (Fig.  11, Pictures 1–3). Even when the temperature decreased to 37 C , after 92  h of production (see Fig.  11, Picture  1), aragonite crystals were dominating. EDX measurements suggest small peaks of other elements (e.g., copper and zinc), but no magnesium, strontium or barium peaks were measured. Ueckert et al. Geotherm Energy (2020) 8:7 Page 18 of 23 Fig. 11 Typical carbonate crystals during T = 110 C : SEM picture (left) and corresponding EDX spectrum Inj ◦ ◦ resp. mapping (right). Examples for injection (Picture 2) and production at 37 C (Picture 1) 60 C (Picture 3). All pictures at these injection temperatures show acicular aragonite crystals Neither vaterite crystals nor any spherical crystals were detected on any filter sample. Although the filters were analyzed randomly and the content of vaterite is usually sig - CaCO nificantly lower than the stable polymorphic forms of (e.g., Wang et  al. (2013): 8–20  %), the analyses should have identified at least some vaterite spheres, had they been present. Discussion In the laboratory experiments with tap water MUC the SI for calcite was close to equi- librium prior to heating, therefore no (or almost no) concentration gradient was present. Here, temperature predominately controlled the reaction. No difference in the crystal - lization with or without p(CO ) was seen. The influence seemed negligible at low CO 2 2 partial pressures up to 24  mbar (at 110 C , with CO addition). However, within our experimental range, the level of supersaturation strongly depended on the increase of temperature. We saw no influence on the affinity to crystallize as aragonite or calcite Uecker t et al. Geotherm Energy (2020) 8:7 Page 19 of 23 (SI 0.52–1.47), as aragonite crystals were always prevailing. According to the litera- calcite ture (see e.g., Bots et al. 2011), a low Mg/Ca ratio of 0.39, and the low sulfate ion con- centrations of 0.4 mmol/L should not inhibit calcite crystallization. However, aragonite ◦ ◦ crystals prevailed, even at 45 C . For temperatures up to 60 C wheat-sheaf aragonites were seen in the SEM-pictures. At temperatures of 110 C acicular aragonite crystals were predominant (see Fig.  5). Since no aragonite particles were found in the water at 20 C , homogeneous nucleation can be assumed. No macroscopically visible precipitates were found on the rock samples or in the reaction vessel. In contrast to the tap water experiments, temperature increase did not come not along with supersaturation in the ultra-pure water experiments. The solution was strongly undersaturated with respect to calcium carbonate. Therefore, a concentration gradi - ent between rock sample and ultra-pure water existed. Once the solution was heated, matrix got dissolved, and a low local supersaturation occurred. Here, only calcite crys- tallized and no aragonite crystals were observed, even at temperatures of 110 C . This might have been linked to the strong concentration gradient, which favors the crystal- lization of calcite over aragonite, or by the low supersaturation (Wang et al. 2013). Cal- cite crystallization should be inhibited by magnesium ion concentrations (Chen et  al. 2006; Reddy and Nancollas 1976). The dissolution of the rock matrix changed the Mg/Ca ratio from 0.2 to 1, but no influence on the crystallization of the CaCO polymorphs was seen. At least at these low ion concentrations of maximum 0.78  mmol/L calcium ions and 0.82 mmol/L magnesium ions, no inhibition of the calcite crystallization was seen. No nuclei were initially present in the solution, and homogeneous nucleation occurred. However, most crystals existed as aggregates which suggest a subsequent growth on the initial crystals. In summary, no influence of foreign ions and temperature on the crystallization of CaCO polymorphs was seen in the autoclave experiments. We assume that the level of supersaturation strongly influenced the crystallization of the CaCO polymorphs. Cal- cite crystals were dominant at low supersaturation, and aragonite crystals at saturation indices above 0.50. The autoclave experiments at very well-defined conditions served as a benchmark for the processes and the models. However, they were never intended to mimic the field conditions, which is not necessary if the underlying conceptual framework can be tested with that experiment. During the field experiment, we produced 15  L/s, 11 C cold carbonate tap water at atmospheric conditions which was in quasi-equilibrium with calcite. Prior to heating, CO was added to the water and the water was strongly undersaturated with respect to calcium carbonate. Heating in the plate heat exchangers brought the SI for calcite to 0.1–0.2 (slight supersaturation). Since the injection temperatures were high, and we had foreign ions, especially magnesium ions, in the solution we expected to find mainly aragonite particles. Surprisingly, calcite crystals prevailed at injection temperatures of ◦ ◦ 65  - 90 C , and aragonites were only present at injection temperatures of 110  C . The non-ideal crystallization of calcites during injection stages can be explained by low supersaturation of the tap water due to CO addition, and by undirected growth which points to turbulent flow. Due to the results of the autoclave experiments, we assume that the low supersaturation inhibited aragonite crystallization. The pressure was with 25 bar Ueckert et al. Geotherm Energy (2020) 8:7 Page 20 of 23 above bubble pressure (2.9 bar). Sharp pressure drops that occur in submersible pumps are absent in our setup. Thus degassing was rather unlikely. We had turbulent flow in the pipe ( Re = 120, 000 , at 20 C and 15 L/s), and we can also safely assume turbulences in the karstic system close to the borehole where flow velocities were high. We can there - fore assume that no diffusion-limited conditions were existent. Once the injected tap water reached the aquifer, a thermal equilibrium was established by mixing with the water in the reservoir and heat exchange with the matrix. The initial sharp temperature drop was followed by a slower decrease as the injected water propa- gates into the matrix. The decrease of the temperature caused a sharp decrease of the SI for calcite. The water became undersaturated with respect to calcite, and dissolved the carbonate matrix (Ueckert and Baumann 2019). Crystal nuclei and crystals in the water should also have been dissolved. After fast dissolution of carbonates in the aquifer to reach equilibrium with the rock matrix, the water became supersaturated during pro- duction, which caused crystal nuclei to grow irregularly under turbulent flow conditions (Han et al. 2004). Interestingly, we did not see differences in the crystal habit during production, com - pared to the injection stages. At injection temperatures of 65–90 C , and the following production stages, far from ideal rhombohedral calcites were characterized. At injection temperatures of 110 C , and the following production stages, acicular aragonite crystals were detected, even after a production time of 92  h, when the water had a minimum temperature of 37 C . The crystals at the corresponding production stage showed the same polymorphism. If detrital mobilization had occurred, one would not expect single crystals or varying polymorphs at different temperatures. We further assume that we had some homogeneous nucleation, but based on our data we are not able to distinguish if we had additionally heterogenous nucleation, e.g., on tiny iron hydroxide crystals. Calcite crystallization was favored in the autoclave experiments with ultra-pure water, and in the field experiment up to temperatures of 90 C , because of the low supersat- uration (Wang et  al. 2013). These calcites in the field experiment grew irregularly and mostly as compact single crystals. Even if aragonite crystals were suddenly dominating at 110 C , it is surprising that aragonites were stable for at least 92 h at a minimum tem- perature of 37 C . This is counter-intuitive because the strong undersaturation should lead to dissolution or at least shrinking size. Since the crystals of the injection and pro- duction stages were similar, although the boundary conditions changed, we assume that the dissolution of the crystals in the injected tap water was slow, and crystal nuclei were stable through the dissolution of the aquifer matrix. During production, these nuclei grew by additional ions in the solution. This hypothesis results in the assumption that crystal nuclei and crystals will be trans - ported between the wells of an operating system. That might be favorable for operation because it reduces precipitates at the wall of the pipes and the heat exchangers, as long as they are kept in solution. Conclusion Increasing temperature from 45 to 110  C , Mg/Ca ratios up to 1, as well as low p(CO ) (up to 24  mbar) had no influence on the crystallization of the CaCO polymorphs in the autoclave experiments. It seems that supersaturation controlled the CaCO 3 Uecker t et al. Geotherm Energy (2020) 8:7 Page 21 of 23 polymorphs. Only aragonite crystals were morphologically identified in the tap water experiments. Lower temperatures up to 60 C resulted in wheat–sheaf structures, and the higher the temperature the more acicular aragonites prevailed. A strong concen- tration gradient and undersaturation in the ultra-pure water experiments resulted in exclusive calcite crystallization, even at high temperatures of 110 C , and high Mg/Ca ratios of 1. The push–pull heat storage test was in line with the results of the laboratory tests showing that varying Mg/Ca ratios, and p(CO ) had no influence on the crystallization of the CaCO polymorphs. The low supersaturation within the quasi-equilibrium up to 90 C resulted in calcite crystallization. Turbulent flow was the reaction-controlling pro - cess, and inhibited the crystallization due to irregular growth. Aragonite crystals pre- vailed at injection temperatures of 110 C. Surprisingly, CaCO polymorphs were similar between injection and the following production stage. Based on these observations, we assume that nuclei and crystals were already injected during the injection stages. Once the water reached the aquifer and was cooling, dissolution of the aquifer matrix occurred and more calcium and magnesium ions were available in the water. As a consequence, existing nuclei were able to grow and were produced during production stages in their injected polymorphic form. Even if the solubility products of aragonite and calcite are related, it is necessary to establish a sound knowledge of the crystallization of the calcium carbonate polymorphs in natural systems to avoid precipitations. In our experiments, we have shown the first results, and possible explanations of the crystallization of CaCO in geothermal sys- tems. The next step should be an investigation of CaCO polymorphs by in situ experi- ments. The conditions in a full-scale aquifer heat storage system are very similar to the push–pull test, except that the cooling of the water takes place in heat exchangers above ground and the dissolution is occurring at the cold well. We expect that crystals are transported between the wells, which is favorable for the operation, because this reduces precipitation at the walls of pipes and heat exchangers. These particles should therefore be kept in solution, rather than removing them by filters. Abbreviations DGF: Sample name: tap water in the field experiment; ICP-MS: Inductively coupled plasma mass spectrometry; MUC: Sample name: tap water in the autoclave experiment; UPW: Ultra-pure water; SEM/EDX: Scanning electron microscope/ energy-dispersive X-ray spectroscopy; SI: Saturation Index; TDS: Total dissolved solids; T : Injection temperature of the Inj tap water at the field experiment; T : Production temperature of the tap water at the field experiment; PE: Polyethyl- Prod ene; PMMA: Polymethylmethacrylate; PTFE: Polytetrafluoroethylene. Acknowledgements The financial support by the Bayerisches Staatsministerium für Wirtschaft und Medien, Energie und Technologie and the BMW Group is gratefully acknowledged. We would like to thank our colleagues Sebastian Wieseman and Roland Hoppe for technical improvements of the autoclave and constructing the filtration device. Christine Benning is gratefully acknowledged for SEM/EDX and ICP-MS measurements. Thank you, Philipp Anger, for Raman microscopy measurements. We would like to thank our cooperation partners Daniel Bohnsack and Dr. Kai Zosseder, Chair of Hydrogeology at TUM, for providing us data of the rock properties. Last but not least, we want to thank Prof. Dr. Hans-Jörg Vogel and PD Dr. Maximilian Köhne, Chair of Soil System Science at the UFZ Halle, for the CT images! Authors’ contributions MU planned, organized, and performed the field experiments and evaluation, planned and evaluated the autoclave experiments and did the graphical representation. CW organized and performed the autoclave experiments. TB had the idea, designed and implemented the evaluation routines of the field test. All authors read and approved the final manuscript. Funding This work was partially funded by the Bavarian Ministry of Economic Affairs, Energy and Technology and the BMW Group. Ueckert et al. 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