CN1170696A - Process for production of purified, synthetic calcium borate - Google Patents
Process for production of purified, synthetic calcium borate Download PDFInfo
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- CN1170696A CN1170696A CN 96107190 CN96107190A CN1170696A CN 1170696 A CN1170696 A CN 1170696A CN 96107190 CN96107190 CN 96107190 CN 96107190 A CN96107190 A CN 96107190A CN 1170696 A CN1170696 A CN 1170696A
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Abstract
A process for the production of calcium borate from boric acid, boric acid, obtained from any source, is reacted with a calcium compound, preferably calcium hydroxide, in an aqueous medium to obtain a suspension of solid calcium borate which is then separated from the residual liquor. Preferably the boric acid is prepared from minerals containing borate salts, in particular, colemanite and howlite; wherein said minerals are ground, reacted with sulfuric acid in an aqueous medium, at high temeperature, to obtain a pulp of solids, including mainly gypsum and clay, in a liquor; said solids are eliminated from the liquor and boric acid is crystallized.
Description
The invention relates to a method for producing calcium borate from borate-containing minerals or boric acid. The calcium borate is mainly used for producing glass fiber, and the glass fiber is mainly used for reinforcing materials and heat insulation materials.
Several methods are known in the art for the preparation of calcium borate from boric acid and from borate-containing minerals, such as ulexite.
The particular method of treatment will depend on the type of mineral used, its purity (impurity content), and "grade" (percentage of borate contained in the mineral), as well as the desired quality of the calcium borate produced.
The basic process for the production of boric acid as disclosed in Kirk Othmer's encyclopedia of chemical technology (second edition, 1964, volume 3, page 615) begins with the reaction of colemanite with sulfuric acid.
Kirk Othmer encyclopedia of chemical technology (second edition, 1964, volume 3, page 649) exemplifies a classic example of boron and calcium forming compounds by reacting boric acid with calcium acetate to form a calcium-boron compound (CaO/B)2O3The molar ratio is 1: 3).
The most common example of a method for producing calcium borate is from ulexite (Na)2O、2CaO、5B2O3.15H2oO) to the same.
One such method is disclosed in U.S. patent 4,270,944 to Ister, assigned to Erwining glass fiber, Inc., wherein high quality ulexite (obtained from Peru Borate, Inc. and having an oxide composition of 6.9% Na) is first formed2O, 9.9% CaO and 41.8% B2O3) Dissolving in hot hydrochloric acid to form a mixture containing undissolved solids; filtering the mixture; adding calcium chloride to the solution to replace all of the sodium in the ulexite; the solution was neutralized with sodium hydroxide at pH 7-9 to form a white calcium borate precipitate, which was filtered off, washed with water and dried at 110 ℃ for 2 or 3 hours. The method can obtain B with content of 46.7% -49%2O3The calcium borate of (1).
Another recent example is us patent 5,268 assigned to bydox dana,154 to boehm et al, to obtain calcium borate and sodium borate. The method comprises adding HBO3And Na2In O solution, under the temperature of 120-200 ℃, the ulexite is separated (de-segregation) to obtain a suspension. Recovering from the suspension by hot filtration to obtain a compound of formula 4CaO.5B2O3.7H2Calcium borate of O. Sodium borate hydrate crystallized from the filtrate at 30 ℃ and was separated from the mother liquor. Sodium hydroxide was added to the mother liquor to maintain H3BO3/N2The weight ratio of O is between 1.8 and 2.7. The mother liquor containing NaOH is recycled as part of the educt liquid.
In the United states of Videl, assigned to the United states department of the navyIn patent 3,332,738(1967) a method for producing synthetic colemanite is disclosed wherein sodium borate or boric acid is mixed with a salt such as Ca (IO)3)2，CaCl2、Ca(C2H3O2)2The compound (2) is reacted for 1 to 8 days.
Other patents relating to the production of boric acid include:
1. U.S. Pat. No. 2,020,57O to Saervaite Siemens, in which colemanite suspended in water and CO are reacted in a high pressure reactor2Carrying out reaction;
2. us patent 4,196,177, wherein an alkali metal borate is reacted with ammonia and ammonium sulfate in the presence of methanol.
3. U.S. patent 3,650,690 to stew chemical company, in which an alkali metal borate is reacted with sulfuric acid, followed by evaporation and recovery of the boric acid with superheated steam.
4. Other patents disclose treatment of boron and calcium or boron and sodium minerals with the following reagents: hydrochloric acid (us patent 2,855,276), phosphoric acid (british patent 423,293), ammonium carbonate (swiss patent 354,760).
5. Patent 2,089,406 assigned to Pacific coast Borax corporation discloses Borax (Na) from the italics2O.2B2O3.4H2O) a process for producing boric acid by reaction with sulfuric acid; and
6. patent 3,103,412 assigned to Sorand, Inc., in which colemanite and/or borosillimanite minerals are reacted with ammonium sulfate.
Furthermore, as described in the introduction to Bulltech University Istanbul (1985, volume 38, page 207-; as described in the journal of colloid science (Vol.13, 386-&396), the journal of crystal growth (Vol.20, 125-&1973), the journal of Canadian chemical society (Vol.36, 1057-&1063, 1958), it is important that a suitable amount of gypsum, which is one of the reaction products of colemanite and sulfuric acid, is formed during the production of boric acid before the production of calcium borate.
As noted above, boric acid can be produced starting from a variety of different boron and calcium and/or boron and sodium minerals and/or compounds using different reactants and conditions.
It has been found in literature that the hard colemanite and/or the borosilcate can be beneficiated either mechanically, e.g., by grinding, milling and separation, or chemically, e.g., by chemical reaction, solvent extraction or sintering. However, colemanite and/or borosillicate contaminated with arsenic, iron, magnesium, strontium, silica, sulfates are not suitable for beneficiation, among other contaminants, because the resulting calcium boron compounds can damage equipment and/or measurement systems under conditions of industrial use.
Examples of methods for beneficiating colemanite and/or borosillicate are found in U.S. Pat. Nos. 4,756,745, 4,756,894 and 4,804,524, assigned to Prefix Margomadagamenna, Inc., of Pullando. In the two former patents, the colemanite and/or borosillimanite minerals are first reacted with sulfuric acid to form a solution depleted of gypsum cake solids, and the remaining solution is reacted with hydrogen sulfide (H)2S) reacting to precipitate the impurities arsenic and iron to obtain selected colemanite or boric acid with a reduced content of impurities. These patents also disclose that it is possible to obtain a calcium ebonite by contacting selected calcium ebonite with Ca (OH)2Reacting to produce calcium borate. In the third patent, use is made of H2S after precipitating the impurities arsenic and iron, the remaining solution is mixed with NH3Reacting to remove impurities Al (OH)3Precipitated and then reacted with sulfuric acid to convert (NH)4)2)SO4Precipitating out to obtain the boric acid.
Since these processes start with colemanite and/or borosilcate of low purity (high impurity content) and low "grade" (low borate content in the minerals), it is often considered necessary to precipitate and remove the impurities arsenic, iron and ammonium sulfate therefrom to obtain an industrially acceptable selected colemanite or boric acid.
In the present invention, the colemanite and/or borosillimanite minerals of low purity and low grade are used without the need to use a catalyst containing a reactive agent such as hydrogen sulfide (H)2S) and ammonia (NH)3) Is treated to remove impurities.
A process is disclosed for producing calcium borate from a low purity and low "grade" colemanite and/or borosilcate mineral, such as gypsum (CaSO)4.2H2O), calcite (CaCO)3) Celestite (SrSO)4) Quartz (SiO)2) Orthoclase(KAlSiO3) And the like, by first reacting said mineral with sulfuric acid to form boric acid, which is crystallized, and then reacting the boric acid with calcium hydroxide in an aqueous medium to produce calcium borate, without intermediate treatment steps of beneficiation. Contrary to the prior art, this new process is not only economically feasible, but also produces calcium borate of high purity and "grade".
The present invention relates to a process for producing calcium borate from boric acid or from minerals containing calcium borate, such as colemanite and colemanite. Unlike U.S. patents 4,804,524 and 4,756,894, which are assigned to pramipexole, McLemmermagdalan, the present invention does not require the inclusion of a compound such as hydrogen sulfide (H)2S) and ammonia (NH)3) The concentrated solution of (a) is treated to remove impurities.
Generally, before the production of calcium borate, the colemanite and/or borosillimanite is washed to reduce the concentration of contaminants therein, such as arsenic sulfide, calcium sulfate and strontium, calcium carbonate and to remove most of the clay hidden in the mineral rock mass and to obtain boric acid.
In this washing step, the minerals were ground to 12.7mm size pieces and then added to a wash tank at 65% solids content with vigorous agitation. The resulting slurry was sieved through a 150 mesh sieve to remove 35% by weight of the finer undersize. The resulting at least washed coarser colemanite and/or colemanite was dried and ground to particles of size 2 mm.
By sieving with a 150 mesh sieve, impurities in colemanite and/or borosillicate are removed, the boron concentration is increased, the consumption of sulfuric acid is reduced, and the filtration time is reduced.
However, the process for producing calcium borate can also start from the original mineral material, such as colemanite and/or colemanite obtained from a mine, without the washing step described.
The washed or virgin mineral substances, such as colemanite and/or calcium silicoborate, are first reacted in a first reactor with sulfuric acid (H) under agitation2SO4) And (4) reacting.
The main reactions carried out in the first reactor are:
consumption of sulfuric acid per ton of H in the reaction3BO3The weight is 0.56-3.0 tons. The sulfuric acid used in the reaction is 20-36 mol. The reaction temperature is 80-100 ℃, and the reaction time is 0.25-2.5 hours. The reaction produces a slurry with a solids content of 25-35%, the slurryThe solids are mainly calcium sulfate, clays and other insoluble compounds in solution, and boric acid. The slurry was filtered and washed with hot water to separate the insoluble soluble material, i.e., "gypsum residue", from the remaining liquid, i.e., "concentrated solution" (strong liq-uor), which was deposited in a tank. The concentrated solution contains 10-18% by weight boric acid in addition to soluble contaminants and water.
The obtained concentrated solution has pH of 0.5-3.0, and contains 0.1-4% sulfuric acid (H)2SO4) Free acid present. The concentrated solution is cooled to a temperature of at most 45 ℃ to obtain boric acid. The resulting mixture containing boric acid is then filtered to separate boric acid (H) from the remaining solution, i.e., the "mother liquor3BO3). It should be noted that in this step, the boric acid obtained by cooling is usually crystallized boric acid. The resulting boric acid is washed to remove impurities that would be adsorbed on the boric acid upon drying. The mother liquor can be recycled in the first reactor, while the obtained boric acid is stirred into the second reactor to obtain an aqueous solution with a boric acid concentration of 16-50 wt%. Then reacting the solution with high-quality calcium hydroxide at 80-100 deg.C for 1-3 hr to obtainTo calcium borate. In the present invention, other calcium compounds than calcium hydroxide, such as calcium oxide, calcium chloride, calcium acetate, calcium iodate, and calcium carbonate, can be used. The resulting calcium borate mixture is filtered and the calcium borate is separated from the remaining solution, which is referred to as the "borate solution". The calcium borate was filtered off in a filter and washed, and then dried in a desiccator at 110 ℃ to obtain calcium borate. The borate solution may be recycled to the first reactor.
The calcium borate produced by the method contains 48 to 61 percent of boron oxide, 19 to 31 percent of calcium oxide, 19 to 23 percent of water and 0 to 1 percent of impurities, and all the percentages are weight percentages.
In a preferred embodiment of the invention, colemanite and/or colemanite are stirred together with sulfuric acid in a first reactor and the liquid is circulated at 95 ℃ to obtain a slurry, which is filtered and washed with hot water (95 ℃) to separate the insoluble matter, i.e. "gypsum residue", from the remaining liquid, i.e. "concentrated solution". Depositing the concentrated solution in a tank, cooling at a temperature of up to 30 deg.C under vacuum, crystallizing to obtain boric acid crystal, H3BO3. The resulting mixture is filtered to separate the boric acid crystals from the remaining liquid, i.e., the "mother liquor". The boric acid crystals are filtered in a filter and washed. The mother liquor was circulated to the first reactor, and the resulting boric acid crystals were charged into the second reactor and stirred to form a 35% by weight aqueous solution of boric acid. The aqueous solution is then reacted with a high level of calcium hydroxide under the following conditions: reacting 5 parts by weight of boric acid with 1 part by weight of lime or 6 moles of boron with 1 mole of calcium at 90 ℃ for 1 to 3 hours to obtain a mixture containing calcium borate, wherein the molecular formula of the calcium borate is CaO.3B2O3.5H2And O. The mixture containing the calcium borate is filtered and the calcium borate is separated from the remaining solution, the "mother liquor". Washing calcium borate in a filter and drying at 110 deg.C in a dryer to obtain CaO.3B2O3.4H2Calcium borate of O containing 60-61% of B2O3. At a drying temperature of 140 ℃ and 800 ℃, it is possible to obtainWater contentLower calcium borate. The calcium borate solution has a pH of 6 to 7 and is recycled to the first reactor.
In this preferred embodiment, the weight of the calcium compound used is such that the molar ratio of boron to calcium is maintained at 6 moles of boron to 1 mole of calcium.
By this process, calcium boron compounds of unusual purity can be obtained, containing about 61% by weight of boron oxide, about 18.5% by weight of calcium oxide, about 20% by weight of water and about 0.5% by weight of impurities.
Examples
The following are some examples of the process of the invention carried out in the laboratory and pilot plant of the company McLemmermardanrnen, McLeibei. Example 1
10 g of a mixture containing 39% of B2O3With 60 g of circulating liquid (H)3BO35.8%) were mixed at 95 ℃ and reacted with 2 g of 100% sulfuric acid at the stated temperature for 2 hours. The gypsum cake was washed and filtered to give a concentrated solution containing 16% boric acid. The temperature was reduced from 95 ℃ to 30 ℃ to give boric acid crystals, which were separated from the mother liquor by filtration. The mother liquor is recycled. After washing the crystals, they were mixed with 6.9 g of water at 95 ℃ and reacted with 2.5 g of calcium oxide (in the form of calcium hydroxide) at 95 ℃ to 100 ℃ for 3 hours. The product was filtered and washed, the borate solution was recycled and the calcium borate was dried at 110 ℃. And (3) analysis results:
B2O3＝46％；CaO＝30％；L.O.I＝24％
the results of the product analysis in the main step are as follows:product weight (g)% B2O3B2O3Distributed% mineral 10.039.0 circulating solution 60.03.9100.0 concentrated solution 60.09.0 gypsum cake 10.01.22.0 boric acid 3.756.2 mother liquor 54.03.330.3 borate solution 15.03.69.2 calcium borate 7.446.057.9 example 2
2 kg of a mixture containing 14% of B2O3Is added to 4.8 kg of a 95 ℃ circulating solution. It was reacted with 0.53 kg of 100% sulfuric acid for 2 hours; the pH of the mixture was 1.5. The gypsum cake was filtered and washed, and its wet weight was 2.5 kg (dried at 50 ℃). The concentrated solution was crystallized in vacuo (17% water evaporated), the temperature was reduced from 95 ℃ to 30 ℃, the resulting thick liquid was filtered and washed, the mother liquor was recycled, thus obtaining 0.49 kg of boric acid; it is then mixed with 0.92 kg of water at 95 ℃ and finally the boric acid is reacted with 0.098 kg of technical grade calcium hydroxide at 95 ℃ to 100 ℃ for 3 hours. The reaction pH was 6.4. After filtration and washing with water at 90 ℃ a borate solution was obtained which was recycled and the calcium borate was dried at 110 ℃ to obtain 0.415 kg of calcium borate.
Para boric acid (H)3BO3) And calcium borate (CaO.3B)2O3.4H2O) were analyzed.
CaO.3B2O.4H2O H3BO3
％B2O361.0 56.200
％CaO 18.0 0.005
％H2O 20.1＜0.100
ppm As ＜1 ＜1
％Fe2O30.06 0.010
％SO30.29 ＜0.010
％SiO20.30 ＜0.010
％MgO 0.06 0.008
δ 2.10 1.480Product quantity (Kg)% B2O3B2O3Distribution% ofMaterial 2.00014.0 circulating solution 4.8003.7100.0 gypsum cake 1.9001.25.0 concentrated solution 4.8009.0 boric acid 0.49056.3 mother liquor 3.4003.8 borate solution 1.3503.811.20 calcium borate 0.41561.055.32 example 3
10 g of a mixture containing 15% of B2O3Is mixed with 30 grams of a 95 c circulating solution containing 3.7% boric acid. It was reacted with 3 g of sulfuric acid at a pH of 1.5 for 1.5 hours with continuous stirring.
The resulting slurry was filtered and washed with water at 95 ℃. 13 g of wet cake and 30 g of concentrated solution with a pH of 1.8 are obtained. It was crystallized by concentrating 8 grams of water and reducing its temperature from 95 ℃ to 30 ℃. The boric acid slurry was washed and filtered to give 18.7 g of mother liquor. The wet boric acid, having a weight of 4.1 grams, was dried and mixed with 4.94 grams of water at 95 ℃, 2.66 grams of calcium hydroxide was added and reacted at 95 ℃ to 100 ℃ for 2 hours, then filtered and washed with water at 95 ℃ to give 3 grams of borate solution and 9.42 grams of wet calcium borate, which was dried at 110 ℃ and the analytical results were as follows:
B2O336 percent; CaO 39%; l.o.i. ═ 25%. Amount of product (g)% B2O3B2O3Distribution% colemanite 10.015. O circulating solution 30.02.1100.0 Gypsum cake 10.00.803.75 concentrated solution 30.07.10 boric acid 2.6656.30 calcium borate 3.9536.0066.70 borate solution 3.000.100.14 mother liquor 18.7013.3529.40Example 4
506 g of H2O and 31 g boric acid (reaction grade) were mixed at 85 ℃. 200 g of a mixture containing 17.4% of B2O3To which colemanite and/or borosillicate is addedThe mixture was then reacted with 63 g of 100% sulfuric acid at 90 ℃ to 95 ℃ and a pH of 2.3 for 2 hours. The resulting slurry was filtered and washed with water at 95 ℃. 288 g of a wet gypsum cake and 600 g of boric acid (H) were obtained3BO3) Concentrated solution with concentration of 17.8% and free sulfuric acid concentration of 0.08%. It was concentrated by evaporation in vacuo to yield 295 g of water. The resulting liquid containing 35% boric acid was reacted with 21.3 g of high purity calcium hydroxide at 95 ℃ to 100 ℃ for 2 hours. The resulting mixture was filtered and washed with water at 95 ℃ to give 230 g of borate solution and 140 g of an orange-colored wet solid, which was dried at 110 ℃. Amount of Compound (g)% B2O3B2O3Distribution% mineral 200.017.40 synthetic solution 537.03.25100.0 Gypsum cake 201.01.806.9 concentrated solution 600.010.00 Borate solution 230.03.5015.4 calcium Borate 73.655.0077.5
The main steps were chemically analyzed, mainly to emphasize the borate solution and borate obtained from the concentrated solution.
B2O3(％) As(ppm) Fe2O3(％) MgO(％) SO3(%) CaO (%) mineral 17.419213.0905.047.5821.800 concentrated solution 10.02800.6980.311.430.026 calcium borate 55.020325.4701.408.7016.500 borate solution 3.5800.0680.360.950.100
In this example, calcium hydroxide was added to a concentrated solution (containing boric acid) to obtain calciumborate which was highly contaminated. If the boric acid crystals are separated from the mother liquor and then reacted with lime, high purity (low contamination level) calcium borate can be obtained.
Claims (67)
1. A process for producing calcium borate from boric acid wherein said boric acid is formed into a 30 to 40 weight percent boric acid solution and reacted with a calcium compound in a molar ratio of about 6 moles of boron to 1 mole of calcium to provide calcium borate.
2. The method of claim 1, wherein the solution is reacted with the calcium compound at 80 ℃ to 100 ℃ for a time.
3. The method of claim 1, wherein the reaction of the boric acid solution with the calcium compound is carried out for 1 to 3 hours.
4. The method of claim 1 wherein the solution is reacted with the calcium compound at about 90 ℃ for 1 to 3 hours.
5. The method of claim 1, wherein said solution is an aqueous solution.
6. The method of claim 1, wherein the calcium compound is at least one compound selected from the group consisting of calcium hydroxide, calcium oxide, calcium sulfate, calcium chloride, calcium acetate, a mixture of calcium acetate and calcium hydroxide, calcium carbonate of calcium iodate.
7. The method of claim 1 wherein the calcium compound is calcium hydroxide.
8. The method of claim 1 wherein the calcium compound is calcium oxide.
9. The method of claim 1 wherein said calcium compounds are calcium hydroxide and calcium oxide.
10. The method of claim 1, wherein the solution is a 33-37% boric acid solution.
11. The method of claim 1, wherein the solution is an about 35% boric acid solution.
12. A process for producing calcium borate from at least one mineral containing borate, wherein said mineral is reacted with sulfuric acid at a reaction temperature to produce a slurry of solids and a first boric acid solution; separating the solids in the slurry from the first solution; crystallizing boric acid from the first solution to obtain boric acid crystals; forming a second boric acid solution in an amount of 30-40% by weight; and reacting the second diboronic acid solution with a calcium compound in a molar ratio of about 6 moles of boron to 1 mole of calcium.
13. The process of claim 12 wherein the reaction of the mineral matter with sulfuric acid is carried out under agitation.
14. The process of claim 12, wherein the reaction of the mineral substance with sulfuric acid is carried out at a temperature of 90 ℃ to 100 ℃.
15. The method of claim 12, wherein the reaction of the mineral substance with sulfuric acid is carried out for 0.25 to 2.5 hours.
16. The method of claim 12, wherein crystallizing boric acid from the first solution is performed by cooling the solution to a temperature below 45 ℃.
17. The method of claim 12, wherein crystallizing boric acid from the first solution is performed by cooling the solution to about 30 ℃.
18. The method of claim 12, wherein crystallizing boric acid from the first solution is performed under vacuum.
19. The method of claim 12, wherein the reaction of the second solution with the calcium compound is performed at a temperature of 80 ℃ to 100 ℃.
20. The method of claim 12, wherein the second solution is reacted with the calcium compound for 1 to 3 hours to obtain calcium borate.
21. The method of claim 12 wherein said second solution is reacted with said calcium compound at about 90 ℃ for 1 to 3 hours.
22. The method of claim 12, wherein the resulting calcium borate is filtered and dried at 110 ℃.
23. The process of claim 12 wherein the molar concentration of sulfuric acid is from 20 to 36.
24. The method of claim 12, wherein the mineral is colemanite, or a mixture of both.
25. The method of claim 12, wherein the second solution is an aqueous solution.
26. The method of claim 12, wherein the calcium compound is at least one compound selected from the group consisting of calcium hydroxide, calcium oxide, calcium sulfate,calcium chloride, calcium acetate, a mixture of calcium acetate and calcium hydroxide, calcium iodate, and calcium carbonate.
27. The method of claim 12 wherein the calcium compound is calcium hydroxide.
28. The method of claim 12 wherein the calcium compound is calcium oxide.
29. The method of claim 12 wherein said calcium compounds are calcium hydroxide and calcium oxide.
30. The method of claim 12, wherein the solution is a 33-37% boric acid solution.
31. The method of claim 12, wherein the solution is a 35% boric acid solution.
32. Contains 48-61% of boron oxide, 19-31% of calcium oxide, 19-23% of water and 0-1% of calcium borate as impurity.
33. Calcium borate is produced by a process in which at least one borate-containing mineral is reacted with sulfuric acid at 90 ℃ to 100 ℃ for 0.25 to 2.5 hours with agitation to produce a slurry of solids and a first boric acid solution; separating the solids in the slurry from the first solution; cooling the first solution to a temperature lower than 45 ℃ to obtain boric acid crystals; the boric acid crystals are stirred to dissolve to obtain 30-40 wt% of a second boric acid solution and reacted with a calcium compound at a molar ratio of about 6 moles of boron to 1 mole of calcium at 80-100 ℃ for 1-3 hours to obtain the calcium borate.
34. The calcium borate of claim 33, wherein the crystals obtained in said processare obtained by crystallization.
35. The calcium borate of claim 33, wherein the crystals obtained in said process are obtained by vacuum crystallization.
36. The calcium borate of claim 33, wherein the resulting calcium borate is filtered and dried at 110 ℃.
37. The calcium borate of claim 33, wherein the sulfuric acid has a molar concentration of 20 to 36.
38. The calcium borate of claim 33, wherein the mineral is colemanite, colemanite or a mixture of both.
39. The calcium borate of claim 33 wherein the first solution is cooled to about 30 ℃.
40. The calcium borate of claim 33 wherein the second solution is an aqueous solution.
41. The calcium borate of claim 33, wherein the calcium compound is at least one compound selected from the group consisting of calcium hydroxide, calcium oxide, calcium sulfate, calcium chloride, calcium acetate, a mixture of calcium acetate and calcium hydroxide, calcium iodate, and calcium carbonate.
42. The calcium borate of claim 33 wherein the calcium compound is calcium hydroxide.
43. The calcium borate of claim 33 wherein the calcium compound is calcium oxide.
44. The calcium borate of claim 33 wherein the calcium compound is calcium hydroxide and calcium oxide.
45. The calcium borate of claim 33 wherein the solution is a 33-37% boric acid solution.
46. The calcium borate of claim 33 wherein the solution is an about 35% boric acid solution.
47. The calcium borate of claim 33, wherein the resulting calcium borate is filtered and dried at 110 ℃.
48. The calcium borate of claim 33, wherein the calcium borate is a compound comprising 48% to 61% boron oxide, 19% to 31% calcium oxide, 19% to 23% water, and 0% to 1% impurities.
49. Calcium borate is produced by a process in which at least one borate-containing mineral is reacted with sulfuric acid at 90 ℃ to 100 ℃ for 0.25 to 2.5 hours with agitation to produce a slurry of solids and a first boric acid solution; separating the solids in the slurry from the first solution; cooling the first solution to be lower than 45 ℃ in vacuum to obtain boric acid crystals; stirring and dissolving the boric acid crystal to obtain 30-40 wt% of second boric acid solution, and reacting the second boric acid solution with a calcium compound at 80-100 ℃ for 1-3 hours to obtain the calcium borate.
50. Calcium borate is obtained by a method in which boric acid is dissolved to give a boric acid solution of 30 to 40% by weight and reacted with a calcium compound at a molar ratio of 6 moles of boron to 1 mole of calcium.
51. The calcium borate of claim 50 wherein the solution is an aqueous solution.
52. The calcium borate of claim 50 wherein the calcium compound is at least one compound selected from the group consisting of calcium hydroxide, calcium oxide, calcium sulfate, calcium chloride, calcium acetate, a mixture of calcium acetate and calcium hydroxide, calcium iodate, and calcium carbonate.
53. The calcium borate of claim 50 wherein the calcium compound is calcium hydroxide.
54. The calcium borate of claim 50 wherein the calcium compound is calcium oxide.
55. The calcium borate of claim 50 wherein the calcium compound is calcium hydroxide and calcium oxide.
56. The calcium borate of claim 50 wherein the solution is a 33-37% boric acid solution.
57. The calcium borate of claim 50 wherein the solution is an about 35% boric acid solution.
58. The calcium borate of claim 50 wherein the resulting calcium borate is filtered and dried at 110 ℃.
59. The calcium borate of claim 50 wherein the calcium borate is a compound comprising 48% to 61% boron oxide, 19% to 31% calcium oxide, 19% to 23% water, and 0% to 1% impurities.
60. Calcium borate is produced by a process in which at least one borate-containing mineral is reacted with sulfuric acid at 90 ℃ to 100 ℃ for 0.25 to 2.5 hours with agitation to produce a slurry of solids and a first boric acid solution; separatingthe solids in the slurry from the first solution; cooling said first solution to about 30 ℃ to obtain boric acid crystals; the boric acid crystals are dissolved with stirring to provide a second boric acid solution of about 35% by weight and reacted with a calcium compound at a molar ratio of about 6 moles of boron to 1 mole of calcium at about 90 ℃ for 1-3 hours to provide the calcium borate.
61. The calcium borate of claim 60 wherein the resulting calcium borate is filtered and dried at 110 ℃.
62. The calcium borate of claim 60 wherein the calcium borate is a compound comprising 48% to 61% boron oxide, 19% to 31% calcium oxide, 19% to 23% water, and 0% to 1% impurities.
63. The calcium borate of claim 60 wherein the calcium borate is a compound comprising about 61% boron oxide, about 18.5% calcium oxide, about 20% water, and about 0.5% impurities.
64. Calcium borate is produced by forming boric acid from any source into a second boric acid solution of about 35% by weight and reacting with a calcium compound at a molar ratio of about 6 moles boron to 1 mole calcium at about 90 ℃ for 1 to 3 hours to obtain said calcium borate.
65. The calcium borate of claim 64 wherein the resulting calcium borate is filtered and dried at 110 ℃.
66. The calcium borate of claim 64 wherein the calcium borate is a compound comprising 48% to 61% boron oxide, 19% to 31% calcium oxide, 19% to 23% water, and 0% to 1% impurities.
67. The calcium borate of claim 64wherein the calcium borate is a compound comprising about 61% boron oxide, about 18.5% calcium oxide, about 20% water, and about 0.5% impurities.
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|---|---|---|---|
| CN96107190A CN1099375C (en) | 1996-07-11 | 1996-07-11 | Process for production of purified, synthetic calcium borate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96107190A CN1099375C (en) | 1996-07-11 | 1996-07-11 | Process for production of purified, synthetic calcium borate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1170696A true CN1170696A (en) | 1998-01-21 |
| CN1099375C CN1099375C (en) | 2003-01-22 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN96107190A Expired - Lifetime CN1099375C (en) | 1996-07-11 | 1996-07-11 | Process for production of purified, synthetic calcium borate |
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| Country | Link |
|---|---|
| CN (1) | CN1099375C (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1315727C (en) * | 2004-12-23 | 2007-05-16 | 大连理工大学 | Manufacturing method of calcium borate by dissociating ulexite in limebase prooess |
| CN103601208A (en) * | 2013-11-25 | 2014-02-26 | 武汉大学 | Preparation method of boron and calcium composite oxide with micro-nano structure |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4270944A (en) * | 1980-01-11 | 1981-06-02 | Owens-Corning Fiberglas Corporation | Method for producing calcium borates |
| CN1033799C (en) * | 1992-09-17 | 1997-01-15 | 雷振玺 | Method for prepn. of calcium borate from boride ore |
-
1996
- 1996-07-11 CN CN96107190A patent/CN1099375C/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1315727C (en) * | 2004-12-23 | 2007-05-16 | 大连理工大学 | Manufacturing method of calcium borate by dissociating ulexite in limebase prooess |
| CN103601208A (en) * | 2013-11-25 | 2014-02-26 | 武汉大学 | Preparation method of boron and calcium composite oxide with micro-nano structure |
| CN103601208B (en) * | 2013-11-25 | 2015-11-18 | 武汉大学 | The preparation method of micro-nano structure boron calcium composite oxides |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1099375C (en) | 2003-01-22 |
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