- Open Access
Preparation and characterization of 10B boric acid with high purity for nuclear industry
© The Author(s) 2016
- Received: 19 February 2016
- Accepted: 9 May 2016
- Published: 28 July 2016
Boric acid is often added into coolant as neutron capture agent for pressurized water reactor, whose amount is influenced by its abundance and purity. Therefore, the preparation of enriched 10B boric acid with high purity is beneficial to nuclear industry. 10B is also used in developing tumor-specific boronated drugs in boron neutron capture therapy. The boronated drug can be administered to patient intravenously, intratumorally, or deposited at tumor site in surgical excision. Thus, enriched 10B boric acid is of practical significance in the field of medicine. Self-made boron trifluoride–methanol-complex solution was selected as one of the experimental reagents, and the preparation of 10B acid was realized by one-step reaction for the complexes with water and calcium chloride. The determination of electrical conductivity in reaction process proves that the optimum reaction time was 16–20 h. Furthermore, the effect of reaction time, ratio of calcium chloride to complex as well as the amount of water on the purity and yield of boric acid was investigated. Finally, the optimum reaction time was 20 h, the optimal solid–liquid ratio (molar ratio) was 3:1, and the amount of water was 1 L of deionized water for each mol of the complex. H2O2 was added in the reaction process to remove Fe2+. After recrystallization, IR spectra of 10B boric acid was measured and compared with standard to verify the product of boric acid. The feasibility of the preparation method was determined by the detection of XRD of boric acid. To observe the morphology by polarizing microscope, crystal structure was obtained. The purity of the final product is 99.95 %, and the yield is 96.47 %. The ion concentration of boric acid accords with the national standard of high purity, which was determined by ICP.
- 10Boron trifluoride–methanol-complex
- 10B boric acid
- Electrical conductivity
Boric acid (“Boric acid that appears in the following text refers to 10B boric acid.”) is widely used in nuclear power plant as coolant (moderator) for reactor to control nuclear reaction rate (Zhang et al. 2014, 2015). The important role of boric acid in nuclear power plant is to control nuclear fission rate and to influence the power generation of nuclear power plant (Odar 2007). Generally speaking, the rate of nuclear fission is controlled by neutron flux, which is released by that process, and boron is an atom that absorbs neutrons with perfect effect. 10B (one of B isotope) has very strong absorption ability, whose neutron absorption cross section of thermal neutron is five times more than boron with natural abundance, 20 times than graphite, and 500 times than traditional protective material of concrete. For that reason, the rate of nuclear fission can be controlled by injecting boric acid into a nuclear power furnace with 10B. Boric acid is prepared in a system consisting of boron and water supply, and enters into chemical volume control system by boron adding loop. The chemical volume control system controls the reactivity of the reactor by controlling boric acid concentration of the loop, and then further controls the power and safety of the reactor (Wootten et al. 1985; Mark 1989; Song and Lee 2003; Staudt et al. 2002).
The main advantages of boric acid solution for controlling water pressure reactor are (Pastina et al. 1999; Hohne et al. 2008): (1) boric acid features the property of dissolving in water. Since this property make boric acid’s effect on the reaction is uniform, and neutron absorption effect is well exerted without additional configuration space, a lot of control rods can be saved. Therefore, core arrangement and pressure vessel structure of the reactor on the top of the heap can be simplified. (2) Boric acid is chemically stable, and cannot react with the material of the loop easily, and its inertia is enhanced with the increase of temperature. Boric acid is neither being deposited itself, nor will be formed on the surface of the compound formed by the chemical composition of the reactor. (3) Boric acid can inhibit corrosion of reactor materials. Significant advantages have been shown by comparing enriched 10B acid with boric acid with natural abundance, since the increase of 10B concentration in reactor’s coolant system and the decrease of whole amount of boric acid can increase the safety and controllability of the reactor and improved, water chemical environment of coolant, and so on. For all the above reasons, the cost is effectively reduced.
Traditional preparation method of boric acid (Zheng 2000; Zhu et al. 2005; Li and Li 2008) is mostly to get the product with natural abundance and not high purity, whose impurities cannot meet the standard of high purity (Wang et al. 2014; Xue et al. 2015; Duan et al. 2012; Li et al. 2011). 10BF3–methanol complex, prepared by separation device of laboratory boron isotope, was chosen as raw material for preparing boric acid, and calcium chloride and distilled water play the same role. In the reaction process, Fe2+ was oxidized to form precipitation due to the addition of H2O2, and the product of boric acid was purified. Finally, the content of impurity ion was detected by ICP to confirm that final product of boric acid meets the requirement of the national standard of high purity.
- 1.Calcium chloride and deionized water were added into four flasks, being heated and stirred, and a certain amount of complex was weighted in a funnel and placed on the four flasks. The experimental device is shown in Fig. 1. When heating temperature was up to 85 °C, the complex was dropped, and the drop speed was controlled at rate of 0.5–1 drops/s.
After the completion of the complex, a certain amount of H2O2 was added into the same funnel to drop into the same four flasks with the same drop speed.
- 3.After the reaction, the reaction liquid was washed and filtered, and the filtrate was cooled and crystallized. The experimental apparatus of cooling crystallization for boric acid is shown in Fig. 2.
Crystallization products were purified by recrystallization, and then their infrared spectra were determined. At the same time, their crystal morphology was observed by polarized light microscope.
The purity and yield of the final product boric acid were measured and calculated. The content of the impurity ion was detected by ICP, and then the purity of the product was compared with that of the national standard and with the boric acid with high purity produced in foreign countries.
“GB/T 628-2011” is the testing standard for boric acid’s purity in the experiment. Infrared spectrum and XRD were used in analyzing the product of boric acid. Ion concentration of the final product was detected by inductively coupled plasma (ICP).
In the experiment, the preparing process of boric acid by 10BF3–methanol complex, calcium chloride and deionized water as raw materials was studied. The complex and the mixed liquid of a certain amount of water and calcium chloride underwent heating reaction, and then were filtered through filter, dehydrated and dried, then boric acid solid was acquired. The effect of reaction time, raw material ratio and the amount of water on the yield and purity of boric acid was investigated. Optimum technological conditions were obtained.
Determination of optimum reaction time and its effect on the purity and yield of boric acid
By the graph, the reaction conductivity decreased with the increase of reaction time. At the beginning of the reaction, HF, HBF3OH, HBF2(OH)2 and HBF(OH)3 were generated, and the electrical conductivity was higher. As the reaction went on, boric acid was gradually formed, meanwhile HF, HBF3OH, HBF2(OH)2 and HBF(OH)3 gradually reacted completely. The electrical conductivity of boric acid is relatively low because it is a weak acid. With the increase of reaction time, the electrical conductivity of the system decreased. The change of the system’s electrical conductivity is basically flat after the reaction time was longer than 16 h, which has no change when it lasted for more than 20 h. Therefore, optimal reaction time was about 20 h.
The effect of reaction time on the purity and yield of boric acid was investigated in 16–24 h.
Effect of solid–liquid ratio of reaction on the purity and yield of boric acid
The yield and purity of boric acid increased with the increase of the ratio of n(CaCl2):n(10BF3–methanol complex). When the ratio reached 3:1, the yield and purity of boric acid tended to balance, which basically did not increase even though the proportion of raw materials continued to increase. Accordingly, the ratio of n(CaCl2):n(10BF3–methanol complex) = 3:1 was appropriate.
Effect of water amount on the purity and yield of boric acid
Water plays three important roles in the reaction process. Firstly, water is a kind of reactant, whose amount will affect whether the reaction is complete. Secondly, water, as dispersion medium, can make the formation of suspension with calcium chloride be dispersed in it. If water amount is in shortage, calcium chloride cannot be dispersed evenly. Lastly, water is a solvent for the production of boric acid. Once water amount is not enough, the product of boric acid will precipitate and mix with nonreacted calcium chloride, which might cause that it is hard to acquire pure boric acid. Water’s three roles testify that water amount should not be too less. However, there should not be too much water too. Otherwise, boric acid will be volatile with water in the concentration process of boric acid, reducing the yield of boric acid. At the same time, it will produce more liquid waste, which makes it more difficult to follow up.
As can be seen from Fig. 6, the yield and purity of boric acid increases with the increase of water amount, and they keep unchanged even though it is more than 500 g. Under the circumstance, calcium chloride can be dispersed evenly and boric acid can be completely dissolved. Since theoretical molar ratio of calcium chloride and water is 1:1.5, this water amount is fully able to meet the needs of the reaction. Therefore, 500 g of water amount is appropriate for the experiment.
Effect of added amount of H2O2 on the concentration of Fe2+ in boric acid
Ksp(Fe(OH)2) = 4.86 × 10−17, Ksp(Fe(OH)3) = 2.8 × 10−39. Fe2+ will be converted to Fe3+ by oxidation and Fe3+ in the solution was completely precipitated. When c(Fe3+) ≤10−5 mol/L, pH ≥3.2 (Wang et al. 2009), oxidation products precipitated by changing pH, which was 4–5 in boric acid solution, and impurities were removed by thermal filtration. The amount of added H2O2 was 3 % of the solution volume, which can effectively reduce the concentration of Fe2+ in the product of boric acid. Specific numerical analysis was carried out for the impurity ion in boric acid.
IR spectra analysis of boric acid
The stretching vibration of intermolecular hydrogen bond (O–H) is between 3500 and 3200 cm−1, characteristic peaks of B–O bond is between 1430 and 1355 cm−1, the stretching vibration of C–O is between 1300 and 1000 cm−1, and surface curvature of O–H is between 769 and 659 cm−1. Upon comprehensive analysis and comparison with standard spectra, the product obtained was boric acid.
Analysis of X-ray powder diffraction
Crystal structure diagram of boric acid
Detection of the concentration of the impurity ion in boric acid
Ion concentration detection of optimum product and the results of comparison
Sample in this study/10−6
Analytical purity sample/10−6
High purity sample of GB/T 628-2011/10−6
High purity sample of E. Merck/10−6
5.4 (without adding H2O2)
The standard of main ion concentration of boric acid is much higher than that of national analytical reagent, which meets the requirement of national high purity.
With adding H2O2, the concentration of Fe2+ in the solution is significantly reduced. It can be clearly seen from the data that the addition of H2O2 make the products meet the requirements of the national analytical reagent. The advantage of adding H2O2 is obviously.
Compared with the standard of boric acid with high purity produced by foreign companies, domestic production technology is still to be improved, which has a certain gap with the world’s leading boric acid production technology, requiring developing more advanced technology of boric acid purification.
The optimum reaction condition for preparing boric acid with 10BF3–methanol complex, deionized water and calcium chloride as raw materials are as follows: optimum reaction time is 20 h, the ratio of n(calcium chloride) and n(10BF3–methanol complex) is 3:1, and water amount is 1 L deionized water per mol complex. Under this condition, the purity of 10B boric acid can reach 99.95 % and the yield reaches 96.47 %.
It is proved that the product is boric acid and the production is feasible by the analysis of IR and XRD. The crystal structure of boric acid is observed and the experimental results are real and reliable.
The addition amount of H2O2 is 3 % of the solution volume, which can effectively reduce the concentration of Fe2+ in the product of boric acid.
The concentration of the impurity ion in the product of boric acid meets the requirement of national high purity standard by detection of ICP after purification by recrystallization, which can be used in nuclear industry.
WZ carried out the main influence factors on the purity and yield of boric acid, participated in the measurement and recording of experimental data and drafted the manuscript. TL conceived of the research process and put forward to join H2O2 on the reducing concentration of Fe2+ in boric acid as innovation point, and helped to draft the manuscript. JX carried out multiple detection and analyzing results. All authors read and approved the final manuscript.
The authors declare that they have no competing interests.
Open AccessThis article is distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution, and reproduction in any medium, provided you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license, and indicate if changes were made.
- Duan SJ, He XW, Chen LX, Zhang YK (2012) 4-mercapto-phenylboronic acid functionalized quartz crystal microbalances sensor for the determination of sialic acid. Chem J Chin Univ 33:464–469Google Scholar
- Hohne T, Kliem S, Rohde U et al (2008) Boron dilution transients during natural circulation flow in PWR—experiments and CFD simulations. Nucl Eng Des 238:1987–1995View ArticleGoogle Scholar
- Li SS, Li H (2008) New technology of extracting boric acid from salt lake brine. J Salt Chem Ind 1:1–3Google Scholar
- Li GQ, Yu JS, Li GW (2011) Novel fluorescent vesicular sensor for saccharides based on boronic acid–diol interaction. Chem J Chin Univ 32:793–796Google Scholar
- Mark L (1989) Enriched boric acid promises greater flexibility for PWR operators. Water Chem Nucl Eng Int 34:47Google Scholar
- Ministry of Chemical Industry (1995) Chemical reagent standard. Chemical Industry Press, BeijingGoogle Scholar
- Odar S (2007) Fundamental aspects of water chemistry in the primary system of PWRs. In: Water chemistry seminar, Suzhou, ChinaGoogle Scholar
- Pastina B, Isabey J, Hickel B (1999) The influence of water chemistry on the radiolysis of the primary coolant water in pressurized water reactors. J Nucl Mater 264:309–318View ArticleGoogle Scholar
- Song MC, Lee KJ (2003) The evaluation of radioactive corrosion product at PWR as change of primary coolant chemistry for long-term fuel cycle. Ann Nucl Energy 30:1231–1246View ArticleGoogle Scholar
- Staudt U, Odar S, Stuzmann A et al (2002) Water chemistry operation experience and steam generator maintenance measures in PWRs. In: Proceedings of the international conference on water chemistry in nuclear reactors systems, Avignon, pp 1–18Google Scholar
- Wang T, Shi JY, Zheng YJ (2009) Experimental study on removal of iron and arsenic by oxidation method from smelted copper sulfate. Met World 1:41–47Google Scholar
- Wang YP, Liu MZ, Zhang YX et al (2014) Synthesis and properties of a novel boron-containing and its application in the preparation of azo poly. Chem J Chin Univ 35:1086–1092Google Scholar
- Wootten MJ, Wolfe CR, Hermer RE (1985) Boric acid inhibition of steam generator materials corrosion. Trans Am Nucl Soc USA 49:64–65Google Scholar
- Xue YN, Li JY, Hao ZJ et al (2015) Synthesis, thermal decomposition mechanism and kinetic equation of polyhedral boron hydride compound [(C2H5)4N]2B10H10 with high enthalpy of combustion. Chem J Chin Univ 36:375–380Google Scholar
- Zhang L, Zhang WJ, Xu J et al (2014) Synthesis of enriched 10B boric acid of nuclear grade. Trans Tianjin Univ 20:458–462View ArticleGoogle Scholar
- Zhang L, Zhang WJ, Xu J et al (2015) Preparation of boric-10 acid applied in nuclear industry. Trans Tianjin Univ 21:172–177View ArticleGoogle Scholar
- Zheng XJ (2000) Review of domestic and foreign boric acid production technology. Liaoning Chem Ind 29:276–278Google Scholar
- Zhu JH, Wei XM, Ma SF (2005) Advances in boron resources and their processing. Mod Chem Ind 25:26–31Google Scholar