Method of binding sulfate in a water body, product produced by the method, calcined mixture for use in the method, and use of such a mixture

Abstract

The present invention relates to a method of binding sulfate in a water body comprising sulfate, to a calcined mixture produced by calcining a mixture comprising calcium oxide and a calcium aluminium oxide and / or a calcium aluminate and cooling for sulfate binding in a water body, and to the use of a powder mixture comprising CaO and at least one element of the mayenite supergroup and / or comprising at least one calcium aluminium aluminosilicate and / or at least one calcium aluminosilicate and / or a calcium silicate and / or the calcined mixture for sulfate binding in a water body.

Description

[0001] Process for binding sulfate in a body of water, product produced by the process, calcined mixture for use in the process, and use of such a mixture and a powder mixture comprising CaO and at least one mineral of the mayenite upper group and / or comprising at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or a calcium silicate

[0002] The present invention relates to a method for binding sulfate in a body of water comprising sulfate, a product produced by the method, an annealed mixture produced by annealing a mixture comprising calcium oxide and a calcium aluminum oxide and / or a calcium aluminate and cooling for sulfate binding in a body of water, as well as the use of a powder mixture comprising CaO and at least one mineral of the mayenite upper group and / or comprising at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or a calcium silicate and / or the annealed mixture for sulfate binding in a body of water.

[0003] State of the art

[0004] Sulfate ions are formed in many processes that involve sulfuric acid, including during sulfuric acid production itself. Sulfate ions can also enter nature in other ways, such as through further reaction of sulfur oxides, which can be formed during combustion of fossil fuels, or through fertilization.

[0005] However, sulfate ions are problematic and environmentally harmful in many waters, disrupting the ecological balance. Sulfate ions can also attack buildings and structures. Accordingly, there is a need to reduce excessive sulfate levels.

[0006] The article "Calcium aluminate process for the further precipitation of sulfate and heavy metals" in water, air, and soil, Journal of Environmental Technology, October 10, 1992, discloses the precipitation of sulfate in industrial wastewater using specially formulated calcium aluminate. The removal of sulfates and calcium from wastewater streams with the formation of ettringite can also be found in WO 98 / 55405 A1.

[0007] However, with current sulfate binding and sulfate removal processes, a large amount of sulfate ions still remain in the water. Accordingly, there is a need for processes that can efficiently bind sulfate ions in water bodies.

[0008] Summary of the invention

[0009] It has been found according to the invention that further sulfate binding is possible by adding annealed mixtures which, in addition to calcium aluminate and / or calcium aluminum oxide, also contain CaO.

[0010] A first aspect of the present invention relates to a method for binding sulfate in a body of water comprising sulfate, the method comprising:

[0011] Providing a mixture comprising calcium oxide and a calcium aluminum oxide and / or calcium aluminate;

[0012] Calcining the mixture comprising calcium oxide and calcium aluminum oxide and / or calcium aluminate and cooling the mixture to produce a calcined mixture; and adding the calcined mixture to the body of water comprising sulfate, whereby the sulfate is bound.

[0013] Furthermore, in a second aspect, a method for binding sulfate in a body of water comprising sulfate is disclosed, the method comprising:

[0014] Providing a mixture, in particular a powder mixture, comprising CaO and at least one mineral from the mayenite upper group, preferably comprising mayenite of the empirical formula CaAlyOies (or CaAluOaa), and / or at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or at least one calcium silicate, wherein at least the calcium is present in a mass fraction of 27.0 - 45.0 wt.%, preferably 30.0 - 40.0 wt.%, more preferably 32.0 - 37.0 wt.%, and the aluminum is present in a mass fraction of 20.0 - 28.0 wt.%, preferably 21.0 - 27.5 wt.%, more preferably 21.5 - 25.5 wt.%, based on the mixture, in particular powder mixture, is contained in the mixture, in particular powder mixture (wherein the respective limit values ​​are included); and adding the mixture comprising CaO and at least one mineral of the mayenite upper group and / or comprising at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or a calcium silicate to the body of water comprising sulfate, wherein the sulfate is bound.

[0015] A third aspect of the invention relates to a calcined mixture for sulfate binding in a body of water, prepared by providing a mixture comprising calcium oxide and a calcium aluminum oxide and / or a calcium aluminate; and

[0016] Annealing the mixture comprising calcium oxide and a calcium aluminum oxide and / or a calcium aluminate and cooling the mixture to produce an annealed mixture for sulfate binding in a body of water.

[0017] In a fourth aspect, a product produced by a process according to the invention comprising bound sulfate is directed.

[0018] Also disclosed is the use of a powder mixture comprising CaO and at least one mineral of the mayenite upper group and / or comprising at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or a calcium silicate and / or an annealed mixture according to the invention for sulfate binding in a body of water.

[0019] Further aspects of the present invention can be found in the dependent claims and the detailed description. Description of the figures

[0020] The accompanying drawings are intended to illustrate embodiments of the present invention and to provide a further understanding thereof. Together with the description, they serve to explain concepts and principles of the invention. Other embodiments and many of the noted advantages will become apparent upon review of the drawings. The elements of the drawings are not necessarily drawn to scale. Identical, functionally equivalent, and acting elements, features, and components are designated by the same reference numerals throughout the figures of the drawings, unless otherwise noted.

[0021] Figure 1 shows schematically a method according to the invention of the first aspect, and Figure 2 shows schematically a method according to the invention of the second aspect.

[0022] Detailed description of the invention

[0023] Definitions

[0024] Unless otherwise defined, technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which the invention pertains.

[0025] For the purposes of the present invention, bodies of water or waters are understood to mean all bodies of water or waters, such as ponds, lakes, rivers, dams, coastal waters, fjords, brackish water lakes, sea bays, seawater, breeding stations for fish and other marine animals, aquariums, water in storage systems for agriculture or drinking water reservoirs, and groundwater aquifers, whereby the aforementioned bodies of water may also contain soils, sediments and / or sludge as well as suspended and settling solids. For the purposes of the present invention, sediments are understood to mean solids present in bodies of water, such as in ponds, lakes, and rivers. The sludge can originate, for example, from sewage treatment plants, wastewater filters, etc. and / or be found at the bottom of bodies of water. Preferred bodies of water are freshwaters with sediments and / or sludge deposits, such as ponds, lakes, etc., which have suboxic and / or anoxic zones and can quickly deteriorate, but which can be effectively treated with the present processes. The present processes are particularly suitable for waters with lower sulfate concentrations, for example, up to 2.5 g / L. Sulfate removal is also beneficial in seawater desalination to prevent the formation of gypsum and thus save energy during desalination by reducing membrane stress.

[0026] When identifying and naming calcium aluminum oxide and / or calcium aluminate, overlaps in the definition may occur within the scope of the invention. Scientifically, the terms calcium aluminum oxide and calcium aluminate have not yet been clearly distinguished from one another, so that there is also practical overlap between the two (see, for example, A. Intiso et al., "The fascinating world of mayenite (Ca^AluOss) and its derivatives," Rendiconti Lincei. Scienze Fisiche e Naturali, 2021, 32, 699,708, where mayenite is referred to as mesoporous calcium aluminum oxide in the abstract and as mesoporous calcium aluminate in section 1). For example, the mineral krotite is also referred to alternatively as calcium aluminum oxide with the chemical formula CaAbO4 or as calcium aluminate with the chemical formula CaO-AbOs. Accordingly, both terms are used here both alternatively and synonymously, since a clear scientific distinction is not possible.In addition to monocalcium aluminate, found as a mineral in the form of the aforementioned krotite and dmitryivanovite (CaO-AbOs (CA)), other calcium aluminates include tricalcium aluminate (3CaO-AbO3 (C3A)), dodecacalcium heptaaluminate, also known as mayenite (12CaO-7AbO3 (C12A7)), monocalcium dialuminate (CaO-2AbO3 (CA2)), found as a mineral in the form of grossite, and monocalcium aluminate (CaO-6AbO3 (CAe)), found as a mineral in the form of hibonite. Synthetic or exotic calcium aluminates such as brownmillerite should also be mentioned.

[0027] Quantities within the scope of the present invention refer to wt.%, unless otherwise stated or apparent from the context.

[0028] The standard pressure is 101325 Pa = 1.01325 bar. A first aspect of the present invention relates to a method for binding sulfate in a body of water comprising sulfate, the method comprising:

[0029] Providing a mixture comprising calcium oxide and a calcium aluminum oxide and / or calcium aluminate;

[0030] Calcining the mixture comprising calcium oxide and calcium aluminum oxide and / or calcium aluminate and cooling the mixture to produce a calcined mixture; and adding the calcined mixture to the body of water comprising sulfate, whereby the sulfate is bound.

[0031] In the process, the provision of a mixture comprising calcium oxide and a calcium aluminum oxide and / or calcium aluminate is not particularly limited.

[0032] The mixture comprising calcium oxide and a calcium aluminum oxide and / or calcium aluminate is not particularly limited according to the invention, as long as it contains calcium oxide and additionally at least one calcium aluminum oxide, at least one calcium aluminate, or at least one of both. In addition, according to certain embodiments, the mixture also contains at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or at least one silicate, for example gehlenite (Ca2Al((AlSi)Oy)) and / or calcio-olivine (Ca2(SiO4)).

[0033] There are no particular restrictions on the calcium oxide. It can be added to the mixture in any suitable way, for example, in the form of a technically pure or pure compound, or as burnt lime or quicklime.

[0034] The calcium aluminum oxide and / or calcium aluminate are also not particularly limited. The mixture can also contain more than one calcium aluminum oxide and / or calcium aluminate. According to certain embodiments, the calcium aluminum oxide and / or calcium aluminate is provided as a mineral mixture - for example, a natural, for example mined - comprising calcium aluminum oxide and / or calcium aluminate, which is then mixed with calcium oxide in a manner suitable for producing the mixture. According to certain embodiments, the mineral mixture and accordingly the mixture contains at least krotite and grossite and, according to certain embodiments, mayenite, wherein mayenite is preferably present in an amount of, for example, <0 wt.% and less than 7 wt.%, preferably less than 4 wt.% and more preferably less than 2 wt.%, based on the mineral mixture. The mineral mixture orAccording to certain preferred embodiments, the mixture also comprises at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or at least one calcium aluminum silicate, in particular gehlenite (C2AS, Ca2AlffAISiJOy)) and / or calcio-olivine (C2S, Ca2(SiC>4)).

[0035] According to certain embodiments, at least the calcium is present in the mineral mixture in a mass fraction of 20.0-29.0 wt.%, preferably 23.0-26.0 wt.%, more preferably 24.0-25.8 wt.%, and the aluminum in a mass fraction of 27.0-35.0 wt.%, preferably 27.2-30.5 wt.%, more preferably 27.5-29.5 wt.%, based on the mineral mixture (the respective limit values ​​being included). This allows preferred phases for sulfate bonding to be achieved during annealing.

[0036] According to certain embodiments, the mixture contains calcium oxide and a mineral mixture comprising calcium aluminum oxide and / or calcium aluminate. According to certain embodiments, the mixture comprising calcium oxide and a mineral mixture comprising calcium aluminum oxide and / or calcium aluminate contains the calcium oxide and the mineral mixture comprising calcium aluminum oxide and / or calcium aluminate in a ratio (w / w) of 5:95 to 50:50, preferably 10:90 to 30:70. This means that the calcium oxide is present in the mixture at 5 to 50 parts by weight, preferably 10 to 30 parts by weight, relative to the calcium aluminum oxide, calcium aluminate, or both (if both are considered present according to the nomenclature) at 50 to 95 parts by weight, preferably 70 to 90 parts by weight. Sulfate binding can be further improved by appropriate adjustment. The mineral mixture can be, for example, as described above, a natural one, e.g.mined, mineral mixture.

[0037] According to the invention, the mixture comprising calcium oxide and calcium aluminum oxide can be blended and ground prior to calcination. The blending and grinding is not particularly limited and can be carried out in any suitable manner, for example, using a suitable grinding device, preferably a ball mill. Blending and grinding can produce a powder that, upon calcination of the mixture, leads to advantageous phase formation for efficient sulfate binding in the process.

[0038] According to certain embodiments, the mixing and grinding takes place to a particle size of > 0.0 to less than or equal to 20.0 mm, preferably to a particle size of > 0.0 to less than or equal to 10.0 mm, more preferably to a particle size of > 0.0 to less than or equal to 5.0 mm, even more preferably to a particle size of > 0.0 to less than or equal to 1.0 mm, e.g. to a particle size of > 0.0 to less than or equal to 0.5 mm. According to certain embodiments, the particle size is determined by sieving the mixed and ground mixture.

[0039] After preparation and possible mixing, grinding and sieving, the mixture can then be annealed.

[0040] Annealing the mixture comprising calcium oxide and calcium aluminum oxide and / or calcium aluminate and cooling the mixture to produce an annealed mixture is also not particularly limited. It can be carried out, for example, in a suitable furnace.

[0041] According to certain embodiments, the annealing is carried out at a temperature of 800 to 1500°C, preferably at a temperature of 900 to 1450°C, more preferably at a temperature of 950 to 1400°C. At such a temperature, a beneficial phase transformation of the mixture occurs, which allows for further improved sulfate binding in the process. The duration of the annealing is also not particularly limited and is carried out, for example, for 1 to 12 hours, e.g., 3 to 8 hours, e.g., 6 hours.

[0042] Furthermore, the cooling is not particularly limited and usually takes place at room temperature (18-25°C), for example by natural cooling, for example in a desiccator or under ambient conditions. Furthermore, the addition of the calcined mixture to the body of water comprising sulfate, whereby the sulfate is bound, is not particularly limited. According to certain embodiments, the addition of the calcined mixture to the body of water comprising sulfate takes place by distributing the calcined mixture into the body of water, and / or after the addition, natural and / or artificially induced mixing takes place. The distribution is not particularly limited and can, for example, comprise scattering. A homogeneous distribution is preferred here. Natural and / or artificially induced mixing can be achieved, for example, by introducing it into a natural current and / or creating an artificial current.Through distribution and / or mixing, the calcined mixture can contribute more quickly to sulfate reduction and side reactions can be better avoided.

[0043] According to certain embodiments, mixing after addition is carried out for at least 30 minutes, preferably at least 1 hour, preferably at least 2 hours. Longer mixing can promote sulfate binding.

[0044] According to certain embodiments, the addition takes place at a temperature of 20 to 40°C, preferably 23 to 37°C, more preferably 27 to 33°C. Accordingly, for example, introduction into natural waters is preferred in the summer months.

[0045] Before adding the calcined mixture to the water, according to certain embodiments, the water can be brought to a suitable pH, for example, in a pH range of 6.0 to 13.0, for example 7.0 to 12.5, preferably 10.0 to 12.0, for example approximately 11.0. If necessary, the pH can be suitably adjusted using, for example, CaO and / or NaOH and / or milk of lime.

[0046] After sulfate binding, a product formed can be suitably separated from the water according to certain embodiments, i.e., the product can be separated with the bound sulfate. There are no particular restrictions on the separation method.

[0047] A corresponding method according to the invention of the first aspect is shown schematically in Figure 1. Providing a mixture comprising calcium oxide and a calcium aluminum oxide and / or calcium aluminate in step 1 is followed by calcining the mixture comprising calcium oxide and calcium aluminum oxide and / or calcium aluminate and cooling the mixture to produce a calcined mixture in step 2 and adding the calcined mixture to the body of water comprising sulfate in step 3, whereby the sulfate is bound.

[0048] Furthermore, a method for binding sulfate in a body of water comprising sulfate is disclosed, the method comprising:

[0049] Providing a mixture, in particular a powder mixture, comprising CaO and at least one mineral of the mayenite upper group, preferably comprising mayenite of the empirical formula CaAlyOies (or CaAluOaa), and / or at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or at least one calcium silicate, wherein at least the calcium is contained in a mass fraction of 27.0 - 45.0 wt.%, preferably 30.0 - 40.0 wt.%, more preferably 32.0 - 37.0 wt.%, and the aluminum is contained in a mass fraction of 20.0 - 28.0 wt.%, preferably 21.0 - 27.5 wt.%, more preferably 21.5 - 25.5 wt.%, based on the mixture, in particular the powder mixture; and

[0050] Addition of the mixture comprising CaO and at least one mineral of the mayenite upper group and / or comprising at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or a calcium silicate to the water comprising sulfate, wherein the sulfate is bound.

[0051] The provision of the mixture, in particular powder mixture, comprising CaO and at least one mineral from the mayenite upper group, preferably comprising mayenite of the empirical formula CaagAlyOies (or CaizAluOss), and / or at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or at least one calcium silicate is not particularly restricted. The mixture, in particular powder mixture, comprises at least CaO (calcium oxide) and at least one mineral from the mayenite upper group, preferably comprising mayenite of the empirical formula CaagAlyOies (or CaizAluOss), and / or at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or at least one calcium silicate. According to certain embodiments, the mixture, in particular powder mixture, comprises at least CaO and a mineral from the mayenite upper group, preferably mayenite.According to certain embodiments, the mixture, in particular a powder mixture, comprises at least CaO, mayenite, and a calcium silicate such as alite (CasSiOs). Preferably, mayenite is the main component in the powder mixture, accounting for more than 50 wt.%, preferably more than 80 wt.%, more preferably more than 85 wt.%, based on the powder mixture (i.e., 100 wt.% powder mixture). A corresponding mixture, in particular a powder mixture, can be obtained in particular by annealing, as described in the method of the first aspect.

[0052] In the mixture, in particular the powder mixture, at least the calcium is present in a mass fraction of 27.0-45.0 wt.%, preferably 30.0-40.0 wt.%, more preferably 32.0-37.0 wt.%, and the aluminum is present in a mass fraction of 20.0-28.0 wt.%, preferably 21.0-<27.5 wt.%, more preferably 21.5-25.5 wt.%, based on the mixture, in particular the powder mixture. Adjusting the proportions accordingly results in more efficient sulfate binding.

[0053] According to certain embodiments, the mixture is a powder mixture. According to certain embodiments, the powder mixture comprises particles with a particle size of > 0.0 to less than or equal to 20.0 mm, preferably with a particle size of > 0.0 to less than or equal to 10.0 mm, more preferably with a particle size of > 0.0 to less than or equal to 5.0 mm, even more preferably with a particle size of > 0.0 to less than or equal to 1.0 mm, e.g. with a particle size of > 0.0 to less than or equal to 0.5 mm, or preferably consists of such particles. The particle size is determined according to certain embodiments by sieving the powder mixture.According to certain embodiments, the addition of the mixture, in particular powder mixture, comprising CaO and at least one mineral from the mayenite upper group and / or comprising at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or a calcium silicate to the body of water comprising sulfate takes place by distributing the calcined mixture into the body of water and / or by natural and / or artificially induced mixing after the addition, wherein the mixing preferably takes place for at least 30 minutes, preferably at least 1 hour, preferably at least 2 hours after the addition. The distribution is not particularly limited and can, for example, comprise scattering. A homogeneous distribution is preferred here. Natural and / or artificially induced mixing can be achieved, for example, by introducing it into a natural current and / or creating an artificial current.Through distribution and / or mixing, the calcined mixture can contribute more quickly to sulfate reduction, and side reactions can be better avoided. Longer mixing promotes sulfate binding.

[0054] Before adding the mixture, in particular a powder mixture, comprising CaO and at least one mineral from the mayenite upper group and / or comprising at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or a calcium silicate to the body of water, the body of water can, according to certain embodiments, be brought to a suitable pH, for example in a pH range of 6.0 to 13.0, for example 7.0 to 12.5, preferably 10.0 to 12.0, for example approximately 11.0. If necessary, the pH can be suitably adjusted using, for example, CaO and / or NaOH and / or milk of lime.

[0055] After sulfate binding, a product formed can be suitably separated from the water according to certain embodiments, i.e., the product can be separated with the bound sulfate. There are no particular restrictions on the separation method.

[0056] An exemplary method of the second aspect is shown schematically in Figure 2. Providing a mixture, in particular a powder mixture, comprising CaO and at least one mineral of the mayenite upper group, preferably comprising mayenite of the empirical formula CaAlyOies (or CaAluOss), and / or at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or at least one calcium silicate, wherein at least the calcium is present in a mass fraction of 27.0 - 45.0 wt.%, preferably 30.0 - 40.0 wt.%, more preferably 32.0 - 37.0 wt.%, and the aluminum is present in a mass fraction of 20.0 - 28.0 wt.%, preferably 21.0 - <27.5 wt.%, more preferably 21.5 - 25.5 wt.%, based on the powder mixture contained in the powder mixture, in step 2 a, the mixture comprising CaO and at least one mineral of the mayenite upper group and / or comprising at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or a calcium silicate is added to the water comprising sulfate in step 3a, wherein the sulfate is bound.

[0057] Furthermore, a calcined mixture for sulfate binding in a body of water is disclosed, prepared by providing a mixture comprising calcium oxide and a calcium-aluminum oxide and / or a calcium aluminate; and

[0058] Annealing the mixture comprising calcium oxide and a calcium aluminum oxide and / or a calcium aluminate and cooling the mixture to produce an annealed mixture for sulfate binding in a body of water. The annealed mixture is obtained in particular using a method according to the first aspect and is accordingly outstandingly suitable for sulfate binding. The annealed mixture preferably contains at least mayenite and a calcium silicate such as alite (Ca3SiO5). Mayenite is preferably the main component in the powder mixture, accounting for more than 50 wt.%, preferably more than 80 wt.%, more preferably more than 85 wt.%, based on the powder mixture (i.e., 100 wt.% powder mixture).

[0059] Annealing is preferably carried out at a temperature of 800 to 1500°C, more preferably at a temperature of 900 to 1450°C, even more preferably at a temperature of 950 to 1400°C, and is not particularly restricted, nor is cooling. These can be carried out as described in the first aspect. The starting material here corresponds in particular to that described in the first aspect. Accordingly, the aspects described there can also be applied to the annealed mixture for sulfate binding. Furthermore, a product comprising bound sulfate is disclosed, which is produced by a process according to the invention according to the first or second aspect.This particularly includes the sulfate bound as ettringite (CaAlz SC OHj x 26 H2O), although other sulfate-containing compounds such as Orscha Hit (Cas SCbh SC XHzOjiz) and / or other compounds such as calcite (CaCCX) and / or bayerite (Al OHX) may also be present in the product and are preferably included. The product also preferably exhibits an excellent particle size distribution due to the starting compound and is therefore ideally suited for further use, for example, as an aggregate in concrete and / or cement production, or in the production of plaster or mortar.

[0060] Also disclosed is the use of a mixture, in particular a powder mixture, comprising CaO and at least one mineral from the mayenite upper group and / or comprising at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or a calcium silicate and / or an annealed mixture according to the invention for sulfate binding in a body of water. As explained above, this powder mixture and / or annealed mixture is particularly suitable for sulfate binding in certain bodies of water with a lower sulfate content, for example, bodies of water that are not industrial wastewater.

[0061] The above embodiments, refinements, and developments can be combined with one another as desired, where appropriate. Further possible embodiments, refinements, and implementations of the invention also include combinations of features of the invention not explicitly mentioned above or described below with respect to the exemplary embodiments. In particular, those skilled in the art will also add individual aspects as improvements or additions to the respective basic form of the present invention.

[0062] The invention will be explained in more detail below with reference to various examples. However, the invention is not limited to these examples. Examples

[0063] Reference example 1

[0064] A natural mineral mixture containing as main phases gehlenite, krotite, grossite, calcio-olivine and mayenite, determined by X-ray diffraction (XRD) such that a weight fraction of Ca was 25.5 wt.% and a weight fraction of Al was 27.5 wt.%, was ground by ball mill and the fraction with a grain size of less than 0.5 mm was sieved from the ground mineral mixture and used for further experiments.

[0065] The XRD measurement was performed according to DIN EN 13925-1, -2:2003, -3:2005, and DIN EN 1330-11:2007 using Bragg-Brentano geometry in reflection mode with a PANalytical "AERIS research" diffractometer using Cu Koc radiation at 1.5418 angstroms.

[0066] The resulting ground mineral mixture was designated as reference mixture “V1”.

[0067] A portion of the mineral mixture was mixed with CaO (calcium oxide powder; CAS 1305-78-8; >96%; Product: 22645.360, VWR Chemicals) in a mass ratio of 80:20 (w / w) and calcined at 1000°C for 6 h in a ceramic crucible in a muffle furnace. The prepared mixture was then allowed to cool to room temperature in a desiccator. The mass loss during calcination was 4.23 wt.%. The resulting mixture was designated as example mixture "B1." The calcined mixture B1 was also analyzed by XRD as above, revealing a Ca weight fraction of 34.7 wt.% and an Al weight fraction of 23.8 wt.%, with the main phases being mayenite, alite, portlandite, and katoite.

[0068] In addition, a portion of the comparative mixture V1 was calcined at 1000°C in a ceramic crucible in a muffle furnace, corresponding to the example mixture B1, for 6 hours. The correspondingly prepared mixture was then allowed to cool to room temperature in a desiccator. The loss on ignition was 0.68 wt.%. The resulting mixture is referred to as comparative mixture "V2." Examples 1 and 2 and Comparative Examples 1 to 4

[0069] An artificial sulfate-containing water was prepared by weighing sodium sulfate (NazSC ) and adding and dissolving it in tap water at a concentration of 0.2 g / L and the pH was adjusted to 11.0 with CaO and / or Na OH and / or milk of lime.

[0070] The reference mixtures V1 and V2, as well as CaO itself and the example mixture B1, were added to corresponding sample quantities of the sulfate-containing tap water at the temperatures specified in Table 1 to a final concentration of 10 g / L of V1, V2, CaO, and B1, respectively. The samples thus prepared were stirred for 24 h using a magnetic stirrer at 250 revolutions per minute. Sediment partially formed, and the supernatant was filtered through a calcium acetate filter with a pore size of 0.45 pm, or 0.25 pm for Example 1.

[0071] The sulfate content was determined using a Metrohm ion chromatograph (IC Metrohm 881). The mobile phase consisted of 5.2995 g Na2CO3 and 0.168 g NaHCO3 per 1000 ml of ultrapure water. Sulfate was calibrated using a multi-element standard to obtain a calibration curve with an r 2of 0.998 between 1 - 50 mg / L sulfate. The results of the sulfate reduction compared to the original sulfate content are given as a percentage in Table 1.

[0072] Table 1 : Results of sulfate reduction In Example 1, an additional sample was taken after 3 h and filtered accordingly.

[0073] The sulfate reduction (w / w) was already 96.0% and was thus already above the values ​​of comparative examples 2 and 3 after 24 h of stirring.

[0074] It is evident that increased sulfate reduction can be achieved through longer mixing. However, the temperature also plays a role in the sulfate reduction, although this has less of an impact with mixture B1 than with mixture V1, which did not achieve sulfate reduction at low temperatures, nor does CaO alone in general. However, even at an elevated temperature of 31°C, the inventive mixture B1 was unexpectedly superior to the comparative mixture V2 in terms of sulfate removal, which can be attributed to the additional presence of the extra CaO during annealing (reduction of 99.3% compared to 95.2%), with the annealed mixture V2 being only slightly superior to the unannealed mixture V1.

Claims

Patent claims 1. A method for binding sulfate in a body of water comprising sulfate, the method comprising: Providing a mixture comprising calcium oxide and a calcium aluminum oxide and / or calcium aluminate; Calcining the mixture comprising calcium oxide and calcium aluminum oxide and / or calcium aluminate and cooling the mixture to produce a calcined mixture; and adding the calcined mixture to the body of water comprising sulfate, whereby the sulfate is bound.

2. The method according to claim 1, wherein the annealing is carried out at a temperature of 800 to 1500°C, preferably at a temperature of 900 to 1450°C, more preferably at a temperature of 950 to 1400°C.

3. The method according to claim 1 or 2, wherein the mixture contains calcium oxide and a mineral mixture comprising calcium aluminum oxide and / or calcium aluminate, wherein the mixture comprising calcium oxide and a mineral mixture comprising calcium aluminum oxide and / or calcium aluminate contains the calcium oxide and the mineral mixture comprising calcium aluminum oxide and / or calcium aluminate in a ratio (w / w) of 5:95 to 50:50, preferably 10:90 to 30:

70.

4. A process according to any one of the preceding claims, wherein the mixture comprising calcium oxide and calcium aluminum oxide is mixed and ground before annealing, preferably with a ball mill.

5. The method according to claim 4, wherein the mixing and grinding takes place to a particle size of > 0.0 to less than or equal to 20.0 mm, preferably to a particle size of > 0.0 to less than or equal to 10.0 mm, more preferably to a particle size of > 0.0 to less than or equal to 5.0 mm, even more preferably to a particle size of > 0.0 to less than or equal to 1.0 mm.

6. Method according to one of the preceding claims, wherein the addition of the calcined mixture to the body of water comprising sulfate is carried out by distributing the calcined mixture into the body of water and / or natural and / or artificially induced mixing takes place after the addition.

7. The method according to claim 6, wherein the mixing after the addition takes place for at least 30 minutes, preferably at least 1 hour, preferably at least 2 hours.

8. A method for binding sulfate in a body of water comprising sulfate, the method comprising: Providing a mixture, in particular a powder mixture, comprising CaO and at least one mineral of the mayenite upper group, preferably comprising mayenite of the empirical formula CaOAlOies, and / or at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or at least one calcium silicate, wherein at least the calcium is contained in a mass fraction of 27.0 - 45.0 wt.%, preferably 30.0 - 40.0 wt.%, more preferably 32.0 - 37.0 wt.%, and the aluminum is contained in a mass fraction of 20.0 - 28.0 wt.%, preferably 21.0 - <27.5 wt.%, more preferably 21.5 - 25.5 wt.%, based on the mixture, in particular the powder mixture; and Addition of the mixture comprising CaO and at least one mineral of the mayenite upper group and / or comprising at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or a calcium silicate to the water comprising sulfate, wherein the sulfate is bound.

9. The method according to claim 8, wherein the addition of the powder mixture comprising CaO and at least one mineral of the mayenite upper group and / or comprising at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or a calcium silicate to the body of water comprising sulfate takes place by distributing the calcined mixture into the body of water and / or after the addition a natural and / or artificially induced mixing takes place, preferably wherein the mixing takes place after the addition for at least 30 min, preferably at least 1 h, preferably at least 2 h.

10. An annealed mixture for sulfate binding in a body of water, prepared by providing a mixture comprising calcium oxide and a calcium aluminum oxide and / or a calcium aluminate; and Annealing the mixture comprising calcium oxide and a calcium aluminum oxide and / or a calcium aluminate and cooling the mixture to produce an annealed mixture for sulfate binding in a body of water.

11. A product comprising bound sulfate, prepared according to any one of claims 1 to 9.

12. Use of a mixture, in particular a powder mixture, comprising CaO and at least one mineral of the mayenite upper group and / or comprising at least one calcium aluminum aluminosilicate and / or at least one calcium aluminosilicate and / or a calcium silicate and / or a calcined mixture according to claim 10 for sulfate binding in a body of water.

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