Patent Application
20070092433
The invention relates to the production of polyaluminum hydroxychlorides (PAC) and polyaluminum hydroxychlorosulfates (PACS) suitable for use in water treatment applications and having a wide range of basicities.
Aluminum containing inorganic reagents such as alum (Al2(SO4)3), polyaluminum hydroxychlorides (PAC), and polyaluminum hydroxychlorosulfates (PACS) are commonly used as flocculents and coagulants in municipal and industrial water and wastewater treatment. Although typically more expensive to manufacture than alum, PAC and PACS products are frequently found to work better than alum with regard to floc settling rates, cold water performance, and water pH adjustment. PAC and PACS products are typically described by the empirical formula:
Aln(OH)3n-m-2k(SO4)kClm
where n is the moles of aluminum, k is the moles of sulfate, and m is the moles of chloride in the product. The corresponding basicity of the product is defined as % Basicity={[OH—]/(3[Al3+])}×100, with the basicity calculated as the ratio [(3n-m-2k)/3n]×100. When an alkali metal base or an alkali earth metal base is used to adjust the final basicity of the PAC or PACS product, the empirical formula of the product can be amended in the following manner:
Aln(OH)3n+Zx-m-2k(SO4)kClmYx,
where n is the moles of aluminum, k is the moles of sulfate, m is the moles of chloride, x is the moles of alkali metal or alkali earth metal and Z is the valence of the metal (e.g., 1 for Na+ and 2 for Mg2+). The basicity of the product is typically adjusted in order to account for desired stability, performance, and/or other product characteristics, with the basicity calculated as the ratio [(3n+Zx-n-2k)/3n]×100. In addition, PAC and PACS products are characterized by aluminum and aluminum sulfate polymers consisting of wide degrees of polymerization, with reported values ranging from the ˜1,000 Dalton Al13-mer Keggin-type complex (see, for example, U.S. Pat. Nos. 5,985,234 and 5,997,838) to average molecular weight values of 7,000-35,000 Daltons, as described in U.S. Pat. No. 5,171,453.
A variety of processes have been reported describing methods for producing PAC and PACS chemical reagents for water treatment applications. For example, the above noted U.S. Pat. Nos. 5,985,234 and 5,997,838 describe a process whereby aluminum oxide trihydrate is reacted with hydrochloric acid and sulfuric acid at elevated temperature (115° C.) to form a polyaluminum hydroxychlorosulfate product which can be subsequently reacted with sodium aluminate under high shear mixing (˜1,000 Hz) at temperatures below 60° C. to produce a PACS of 50% -70% basicity and, at temperatures above 60° C., products of greater than 70% basicity. The high shear mixing involved in the process is a necessary component of the reaction. Further, it is described that the formation of significant amounts of smaller aluminum polymers, specifically the Al13-mer Keggin complex, is an important component to the performance of the product. The requirement of high shear mixing is also mentioned in U.S. Pat. No. 4,877,597. The process involves the addition of an alkali metal aluminate to alum between 10° C.-35° C., followed by warming the reaction to 50° C.-90° C. This results in a PACS product with 7% -10% Al2O3, albeit with significant amounts of sodium sulfate by-product.
In addition, U.S. Pat. No. 5,603,912 describes a method of making a 50%-73% basicity PACS via an initial high temperature reaction of aluminum and aluminum chloride or hydrochloric acid, followed by reaction with sulfuric acid and then an alkaline earth carbonate such as calcium carbonate. Important features of the process of that patent include: i) the need to adjust the Al/Cl atomic ratio to 0.70-1.2 prior to sulfate ion addition, ii) initial preparation of the PACS at high temperature, and iii) addition of an alkaline earth carbonate (e.g., CaCO3) at 45° C. Similarly, U.S. Pat. No. 5,246,686 discloses a process whereby an aluminum hydroxychlorosulfate is reacted with an alkaline earth carbonate, although at temperatures ranging from 60° C.-100C., to produce polyaluminum hydroxychlorosulfates with basicities in the range of 45%-70%. However, it is reported that the process results in the undesirable formation of insoluble gypsum.
A method that avoids the formation of gypsum and other alkaline earth sulfates is described in U.S. Pat. No. 5,348,721, requiring the initial production of a PACS of 40%-50% basicity at elevated temperature (140° C.) and pressure (2 bar), which is subsequently reacted with an alkaline metal carbonate (e.g., Na2CO3) or alkaline earth carbonate (e.g., CaCO3) at temperatures in the range of 50° C.-70° C. to form PACS of 65%-75% basicity. Significantly, reaction with the selected base at lower temperatures (e.g., 40° C.), results in a product that is unstable with respect to the formation of a gel.
A low temperature process for the preparation of PACS is reported in U.S. Pat. No. 5,124,139 whereby aluminum trichloride is blended with alum at temperatures between 35° C.-50° C., followed by addition of a calcium base such as calcium carbonate, calcium oxide, or calcium hydroxide. However, in contrast to the process of the present invention, it was noted that products above 60% basicity made via the process of that patent are unstable and tend to solidify. In addition, reaction mixtures containing amounts of AlCl3 and Al2(SO4)3 such that initially prepared solutions with Al2O3 contents greater than 8.5% were reported to solidify even prior to addition of base. Finally, no example is given of a product made via the method of that patent containing concentrations of aluminum greater than 10% Al2O3.
The invention involves the production of polyaluminum hydroxychlorosulfates (PACS) suitable for effective use as flocculants and coagulants in water treatment. The resulting product is a fluid, clear solution that is stable with respect to precipitation and gelling for extended periods of time. Key features of the process include: i) the production of a PACS solution of about 12%-16% Al2O3 and about 40%-60% basicity at moderate temperatures (50° C.-60° C.) using a zerovalent aluminum source, such as aluminum powder; ii) the addition of an alkali metal or alkali earth metal base at low temperatures (20° C.-45° C.) to produce PACS products ranging from 9-12% Al2O3 with basicities ranging from 70%-80%; iii) the addition of a soluble alkali metal or alkaline earth metal base at low temperatures without the use of high shear mixing to the aforementioned PACS solution to produce PACS products ranging from 9%-12% Al2O3 with basicities ranging from 70%-80%; iv) the production of a PACS solution of about 9-12% Al2O3 and about 60%-80% basicity at moderate temperatures (50° C.-60° C.) using a zerovalent aluminum source, such as aluminum powder, and without the use of a soluble alkali metal or alkaline earth metal base; v) the formation of an efficacious PACS product that does not contain significant amounts of the Al13-mer Keggin complex (<15%), as determined by tandem size exclusion chromatography (SEC)/multi-angle laser light scattering (MALLS); vi) the formation of PACS solutions with greater than 80%-95% of the aluminum polymers distributed in the range of 20,000-40,000 Daltons and in the range of 135-750 Daltons; and vii) the formation a PACS whereby greater than 95% of the sulfate is bound to aluminum and greater than 95% of the sulfate is contained in the aluminum polymers distributed in the range of 20,000-40,000 Daltons, as determined by tandem size exclusion chromatography (SEC)/inductively coupled plasma (ICP) analytical techniques.
In the preferred embodiment of the invention, aluminum chloride is mixed with water and a sulfate source according to the desired concentration. The sulfate source may include, but is not limited to, sulfuric acid or alum. Further, the amount of the sulfate source used is chosen so as to produce a solution such that the final sulfate concentration is in the range of 0.5%-4%, more preferably 1%-3%, most preferably 1.5%-2.5%. The reaction mixture is warmed to a temperature of about 50° C.-60° C. and a zerovalent aluminum source such as, but not limited to, aluminum nuggets, comminuted aluminum metal, shredded metal sheeting and preferably aluminum powder is added such that an initial product of about 12%-16% Al2O3 is produced and the final product will contain an alumina (Al2O3) concentration of 9%-12%, more preferably 10%-12%, most preferably 10%-11%. The Al/Cl ratio is maintained in the range of 0.6-1.0, preferably 0.7-0.9, and most preferably 0.75-0.85. The mixture is then allowed to react for about 4-24 hours until the desired concentration is reached. This produces a PACS product with a basicity in the range of 40%-60%.
Subsequent to the production of the PACS, enhanced stability and performance can be imparted to the product by increasing the basicity of the product to 60%-85%, more preferably 65%-80%, and most preferably 70%-75%. In contrast to other known prior art, which typically require elevated temperatures and/or high shear mixing in order to maintain the stability of the system upon increasing the basicity, the present invention involves an effective and efficient process to increase the basicity and performance of the PACS by cooling the solution to 30° C. or below, followed by addition of an alkali metal base including, but not limited to, a soluble alkali metal carbonate, alkali metal bicarbonate, alkali earth-metal and mixtures thereof, preferred carbonates including sodium carbonate or sodium bicarbonate, as a solid, slurry, or solution. The resulting clear solution is adjusted with water to the desired % Al2O3 concentration and then filtered. Overall, the process provides a convenient means of producing a high basicity PACS product that is stable with respect to precipitation and gelling, does not result in the production and disposal of excess sulfate salts, and is of sufficiently low viscosity so as to simplify the production of PACS.
An alternate form of the process involves the preparation of the PACS of the present invention without the use of a soluble alkali metal or alkali earth metal base to achieve basicities greater than 70%. In such preparations, aluminum chloride is mixed with water and a sulfate source according to the desired concentration. The sulfate source may include, but is not limited to, sulfuric acid or alum. Further, the amount of the sulfate source used is chosen so as to produce a solution such that the final sulfate concentration is in the range of 0.5%-4%, more preferably 1%-3%, most preferably 1.5%-2.5%. The reaction mixture is warmed to a temperature of about 50° C.-60° C. and a zerovalent aluminum source such as, but not limited to, aluminum nuggets, comminuted aluminum metal, shredded metal sheeting and preferably aluminum powder is added such that the final product will contain an alumina (Al2O3) concentration of 9%-12%, preferably 10%-12%, and more preferably 10%-11%. The Al/Cl ratio is maintained in the range of 0.6-2.0, preferably 0.7-1.9, and more preferably 1.4-1.75. The mixture is then allowed to react for about 4-24 hours until the desired concentration is reached. This produces a PACS product with a basicity in the range of 40%-80%, preferably 65%-80%, and more preferably 70%-80%.
The polyaluminum hydroxychlorosulfates produced in accordance with the invention are characterized via high performance liquid chromatography (HPLC) using size exclusion chromatography (SEC) and multi-angle laser light scattering (MALLS). In SEC, polymers are separated on a column according to their relative average molecular weights and detected via a UV, refractive index, light scattering, and/or ICP detector. The identification and separation of aluminum polymers is well known, particularly in the antiperspirant industry (see, for example, U.S. Pat. Nos. 5,330,751, 5,356,612 and 5,356,609). Further, the use of light scattering techniques allows for the absolute determination of the average molecular weights of polymers in solution and can be combined with chromatographic separation in order to determine the molecular weights of different polymers in a particular matrix (see Wyatt, P. J., Analytica ChimicaActa 1993, 272, pp. 1-40).
Known reports of the aluminum polymer distribution in PACS products include the aforementioned U.S. Pat. Nos. 5,985,234 and 5,997,838, which indicate that a polymer of approximately 1,000 Daltons, known as the Al13-mer Keggin complex, is a key component to the overall performance of the product. Other prior art indicate that this species is a key component for efficient performance polyaluminum hydroxychloride and polyaluminum hydroxychlorosulfate water treatment chemicals (see, for example, the above mentioned U.S. Pat. No. 5,348,721; van Benschoten, J. E.; Edzwald, J. K., Wat. Res. 1990, 24, pp. 1519-1526; and Gao, B.; Ue, Q.; Wang, B., Chemosphere 2002, 46, pp. 809-813). This polymer and polymers of similar molecular weight are readily observed via size exclusion high performance liquid chromatography. Hence, SEC/MALLS analysis of the PACS produced according to the present invention indicates that less than 5% of the aluminum polymers are in this molecular weight range. Rather, the product of the present invention typically contains 35%-50% of the aluminum polymers in the molecular weight range of 20,000-40,000 Daltons while 45%-60% of the polymers have molecular weights of 135-750 Daltons (
Analysis via SEC/ICP studies indicate that no free sulfate (<5%) exists in solution and that all of the sulfate is associated with aluminum polymers in the molecular weight range of 20,000-40,000 Daltons (
The following examples show the physical properties and characteristics of the PACS produced according to the method of the invention. These examples are intended as illustrative and should not be construed as placing a limitation on the scope of the invention.
188 g of aluminum chloride is mixed with 120 g of water and 11 g of sulfuric acid (98%) at ambient temperature. The reaction mixture is heated to 50° C.-60° C. and 12 g of aluminum powder is added over a period of 2 hours. The reaction is continued for an additional 4 hours and then cooled to 25° C. 125 g of sodium carbonate solution (11.74% w/w) and 44 g of sodium bicarbonate were added over a 2 hour period. The mixture is stirred and filtered after dissolution of suspended material, resulting in a clear solution containing 10.65% Al2O3, 9.70% Cl, 1.97% SO4, and a 70.5% basicity.
160 g of aluminum chloride is mixed with 95 g of water and 8.2 g of sulfuric acid (98%) at ambient temperature. The reaction mixture is heated to 50° C.-60° C. and 13 g of aluminum powder is added over a period of 1 hour. The reaction is continued for an additional 12 hours and then cooled to 30° C. 104 g of sodium carbonate solution (22.0% w/w) is added over a 1.5 hour period. The mixture is stirred and filtered after dissolution of suspended material, resulting in a clear solution containing 10.91% Al2O3, 9.55% Cl, 2.10% SO4, and a 68.8% basicity.
160 g of aluminum chloride is mixed with 49 g of water and 8.2 g of sulfuric acid (98%) at ambient temperature. The reaction mixture is heated to 50-60° C. and 13 g of aluminum powder is added over a period of 1 hour. The reaction is continued for an additional 12 hours and then cooled to 30° C. 15 g of water is added, followed by 171 g of sodium carbonate solution (22.0% w/w) over a 2.5 hour period. The mixture is stirred and filtered after dissolution of suspended material, resulting in a clear solution containing 10.0% Al2O3, 8.81% Cl, 1.92% SO4, and a 80.0% basicity.
In order to illustrate the significance of the lower temperatures in the process of the present invention and the enhanced performance imparted thereby, an analogous polyaluminum hydroxychlorosulfate was prepared at high temperatures. 188 g of aluminum chloride is mixed with 120 g of water and 11 g of sulfuric acid (98%) at ambient temperature. The reaction mixture is heated to 80° C.-90° C. and 12 g of aluminum powder is added over a period of 2 hours. The reaction is continued for an additional 3 hours and then 125 g of sodium carbonate solution (11.74% w/w) and 44 g of sodium bicarbonate over a 2 hour period. The mixture is stirred and filtered after dissolution of suspended material, resulting in a clear solution containing 10.82% Al2O3, 9.27% Cl, 2.06% SO4, and a 72.7% basicity.
119 g of aluminum chloride is mixed with 100 g of water and 6.42 g of alum at ambient temperature. The reaction mixture is heated to 50-60° C. and 9.75 g of aluminum powder is added. The reaction is continued for an additional 22 hours and then cooled to 30° C. 65 g of sodium carbonate solution (27.6% w/w) over a 2 hour period. The mixture is stirred and filtered after dissolution of suspended material, resulting in a clear solution containing 10.76% Al2O3, 9.36% Cl, 1.95% SO4, and a 78.2% basicity.
200 g of aluminum chloride is mixed with 137 g of water and 11.0 g of sulfuric acid at ambient temperature. The reaction mixture is heated to 50-60° C. and 16 g of aluminum powder is added. The reaction is continued for an additional 15 hours and then cooled to 30° C. 136 g of a magnesium carbonate slurry (21.3% w/w) over a 2 hour period. The mixture is stirred and filtered after dissolution of suspended material, resulting in a clear solution containing 10.28%Al2O3, 9.06% Cl, 2.11% SO4, and a 73.2% basicity.
This examples illustrates the preparation of the product according to the process of this invention without the use of a soluble metal carbonate base. 91 g of aluminum chloride is mixed with 283 g of water and 8.52 g of sulfuric acid (98%) at ambient temperature. The reaction mixture is heated to 50-60° C. and 17 g of aluminum powder is added over a 1-2 hour period. The reaction is continued for an additional 21 hours and then cooled to ambient temperature. The mixture is filtered, resulting in a clear solution containing 10.5% Al2O3, 4.49% Cl, 2.09% SO4, and a 72.5% basicity.
The following table summarizes the aluminum polymer distribution within the product of the present invention.
The following table illustrates the use of the polyaluminum hydroxychlorosulfate of the present invention as an effective water treatment chemical. Jar tests were conducted on an equal % Al2O3 basis and involved rapid agitation (220 rpm) of the test water for ˜1 second after coagulant addition, followed by slow mixing (40 rpm) for 15 minutes and 20 minutes for floc settling.
The following table illustrates the stability of the PACS produced according to the present invention in terms of solution turbidity.
The invention has been described in terms of particular embodiments. However, it would be apparent to those skilled in the art that various alternatives and substitutes may be applied from the disclosure herein provided. It will be understood, accordingly, that the invention is not to be limited to the details described herein, unless so required by the scope of the appended claims.
