Continuous synthesis of octacalcium phosphate
The continuous synthesis of OCP using controlled reaction parameters addresses the inefficiencies of traditional methods, enabling rapid and pure production of OCP for biomaterials, enhancing bone tissue regeneration and dental restoration applications.
Patent Information
- Application Number
- PCT/IB2025/054651
- Authority / Receiving Office
- WO · WO
- Patent Type
- Applications
- Current Assignee / Owner
- Priority Date
- 2024-05-03
- Filing Date
- 2025-05-03
- Publication Date
- 2025-11-06
AI Technical Summary
Existing methods for the synthesis of octacalcium phosphate (OCP) are time-consuming and lack precise reaction conditions, leading to impurities and inefficiencies in large-scale production, particularly due to rapid flow rates causing the formation of undesirable phases like hydroxyapatite.
A continuous synthesis process using a wet precipitation method with controlled reaction parameters, including separate heating of calcium and phosphate sources, concurrent pumping through pipes, and mixing at specific temperatures and pH, followed by immediate filtration and drying, to produce pure OCP.
Achieves rapid and pure production of OCP with controlled phase purity and morphology, overcoming the limitations of traditional methods by ensuring consistent and uninterrupted flow, resulting in high-quality biomaterials suitable for bone tissue regeneration and dental restoration.
Smart Images

Figure IB2025054651_06112025_PF_FP_ABST
Abstract
Description
[0001] CONTINUOUS SYNTHESIS OF OCTACALCIUM PHOSPHATE
[0002] DESCRIPTION
[0003]
[0001] The invention relates to the field of biomaterials, particularly the method to synthesize octacalcium phosphate (OCP). This process can be applied in the commercial manufacturing of biomaterials for bone tissue regeneration or dental restoration, such as bioinks for 3D printing, calcium phosphate cements, bioceramics, composites and drug delivery systems.
[0004] Background of the art
[0005]
[0002] The biological occurrence of OCP has been reported in calcifying dentine. The presence of OCP in human dentine crystal indicated that the nucleation of non-stoichiometric hydroxyapatite (HAp) crystals as well as OCP occurs simultaneously at the same site of mineralization [1], Thus, OCP is known as a precursor of biological apatite crystals in hard tissues.
[0003] Several bioceramics such as HAp, dicalcium phosphate (DCP), amorphous calcium phosphate (ACP) and octacalcium phosphate (OCP) were implanted in mouse calvaria [2], Amongst all, OCP promoted bone tissue formation within one week whereas DCP, ACP (3 weeks) and HAp (5 weeks) revealed delayed tissue appearance. This confirmed synthetic OCP possesses enhanced bone formation ability.
[0006]
[0004] The most common routes for the synthesis of OCP are precipitation and hydrolysis. It has been reported that the large-scale synthesis of OCP is very challenging [3], The synthesis of OCP is influenced by Gibbs free energy, supersaturation, common ion effect, molarity, pH, temperature, and mixing order / rate. A minor alteration in any of these reaction parameters affects the purity of OCP [4],
[0007]
[0005] A method for the synthesis of OCP is reported. Calcium acetate solution was added dropwise into sodium dihydrogen phosphate solution using a peristaltic pump. The speed of the peristaltic pump was maintained at 58 rpm and the reaction was performed at 67.5 °C for 5 hours. The reaction mixture was stirred at 350 rpm. The resultant precipitate was filtered, washed with double distilled water, and dried for 5 days in an incubator at 55 °C [5], The flow rate of calcium solution into phosphate solution was kept very low which consumed about 5 hours for the synthesis of OCP. As it was identified that a faster dose rate leads to the formation of undesirable phases along with OCP.
[0008]
[0006] The large-scale synthesis of OCP by dropwise addition of calcium solution (0.04 M) into phosphate solution (0.03 M) is known. The calcium solution was added to phosphate solution at a dose rate of 116 mL / min. The reaction was performed at 67.5 °C and the final pH was 4.88. The end product was composed of HAp and OCP mixture [3], The rapid flow rate was found to influence the reaction and compromises the purity of OCP. The faster dose rate of calcium solution assisted in creating a high local concentration in the area of the drop in the phosphate solution. This caused a temporary increase in the Ca / P ratio in this area and resulted in the formation of HAp instead of OCP. Thus, it is recommended to maintain a lower dose rate for a good precipitation reaction large-scale synthesis.
[0009]
[0007] To date, numerous attempts have been made for the synthesis of OCP but no reports are found in the literature about the continuous synthesis of OCP. The methodologies used for the preparation of OCP are time-consuming and the entire reaction process takes from hours to days to complete. Moreover, the findings are unable to report precise reaction conditions for the preparation of OCP (Table 1).
[0010]
[0008] Therefore, there is still a great need for continuous synthesis of OCP for large-scale production and to meet the demands of the biomaterials market.
[0011] Table 1. An Overview of OCP synthesis conditions reported in the literature
[0012] *NA: Information not available
[0013] The object of the invention
[0014]
[0009] An object of the present invention is to develop a method having the ability to produce OCP in continuous process.
[0015]
[0010] Searching for a new synthesis process, we unexpectedly discovered that the use of the wet route in combination with optimum reaction parameters leads to conditions for controlled continuous synthesis of OCP.
[0016] Detailed description of the invention
[0017] [Oi l] OCP is prepared by the wet precipitation method. Stock solutions are prepared separately in deionized water.
[0018]
[0012] The term “stock solution” refers to a solution made from calcium source and phosphate sources.
[0019]
[0013] The term “calcium source” refers to calcium acetate hydrate.
[0020]
[0014] The term “phosphate source” refers to sodium dihydrogen phosphate dihydrate or potassium dihydrogen phosphate.
[0021]
[0015] The term “heated” refers to atemperature of 60 - 80 °C.
[0022]
[0016] The Ca / P ratio for the synthesis of OCP is ranging from 1 to 2, preferably from 1.2 to 1.4 or more preferably 1.3. The calcium source and phosphate source are heated separately. Both sources are pumped separately concurrently continuously using a system (P) providing continuous flow such as a peristaltic pump or automatic liquid dosing system or continuous flow equipment or gravitational flow system, through pipe 1 and pipe 2 respectively, and mixed together in mixing chamber (3) and precipitated OCP suspension is released through pipe (4) as shown in Fig. 1. The volume ratio of both solutions can be 1: 1. The reaction is carried out at a temperature ranging from 60 °C to 80 °C, preferably 60 °C to 70 °C, pH ranging from 4.0 to 6.0, preferably from 4.5 to 5.0.
[0017] Further, from the obtained mixture the precipitate is separated by vacuum fdtration or centrifugation or gravity fdtration. The sample obtained after filtration can be dried in an incubator or lyophilization or hot air oven or at room temperature. The selected reaction conditions assist in obtaining OCP bioceramic.
[0023]
[0018] The term “mixing” refers to any type of mixing of liquids to blend the components evenly throughout the mixture, ensuring uniformity and consistency.
[0024]
[0019] The term “pipes” refers to hollow channels used to transport liquids from one location to another within a system. The pipes can be made of materials such as metal, alloy, plastic, or rubber and are designed to facilitate the efficient and controlled movement of liquids, from a source to a destination.
[0025]
[0020] The term “pumped” refers to the action of using a pump to move or transfer liquid from one point to another. It involves creating a pressure difference, which forces the fluid to move through a system.
[0026]
[0021] The term “separately” refers to the movement or transfer of liquids in a manner where each liquid flows independently, without combining or mixing with each other. This could involve using distinct pipes, tubes, channels, or conduits for each liquid to maintain their individuality throughout the process.
[0027]
[0022] The term “concurrently” refers to the movement or flow of multiple fluids through separate channels in a system or the parallel movement of liquid streams in a netw ork of pipes / tubes.
[0028]
[0023] The term “continuous” refers to the process that occurs without interruption, pause, or break. It describes the reaction that proceeds without stopping.
[0029]
[0024] The term “continuous flow” refers to the uninterrupted movement of liquid. It implies a continuous movement or constant flow of liquid maintaining a consistent rate and direction over time.
[0030]
[0025] The term “peristaltic pump” refers to any pump used to move fluids and operates on the principle of peristalsis. The peristaltic pump maintains precise flow rates of liquids.
[0031]
[0026] The term “automatic liquid dosing system” refers to a system that can precisely dispense liquid substances automatically.
[0032]
[0027] The term “continuous flow equipment” refers to equipment used to perform operations continuously, without interruption. Continuous flow7equipment maintains a steady and uninterrupted flow7of liquids resulting in a continuous production of desired material.
[0028] The term "gravitational flow system" refers to the movement of fluids under the influence of gravity. This flow is driven by the potential energy stored in the fluid due to its elevation. When the fluid is allowed to flow freely, it moves from higher elevations to lower elevations, following the path of least resistance.
[0033]
[0029] A method for the synthesis of octacalcium phosphate (OCP) comprises the following steps: a) heating separately calcium and phosphate source; The heating temperature is in the range from 60 to 80 °C; b) pumping continuously, concurrently and separately calcium and phosphate sources through pipes (1,2) using a system (P) providing continuous flow; c) mixing calcium and phosphate source in mixing chamber (3), wherein the Ca / P molar ratio is from 1 to 2, a temperature range is from 60 to 80 °C with pH range from 4.0 to 6.0; The mixing is performed for a duration of less than 5 minutes, preferably less than 3 minutes, or even less than 1 minute. d) releasing the octacalcium phosphate precipitated in step c) through pipe (4); e) drying the octacalcium phosphate obtained in step d).
[0034]
[0030] Temperature plays a key role in controlling the phase purity, morphology, crystallinity, and rate of precipitation of octacalcium phosphate. Heating of reactants before mixing enhances the ion mobility, supersaturation, and decreases the solubility of OCP, leading to the rapid precipitation of OCP within minutes.
[0035]
[0031] Brief description of the drawings:
[0036] Fig.l. System used for the continuous synthesis of OCP: (P- system providing continuous flow; 1- inlet pipe; 2- inlet pipe; 3- mixing chamber; 4- releasing pipe)
[0037] Fig.2. X-ray diffraction pattern (a) and scanning electron microscopy image (b) of sample synthesized at 60 °C
[0038] Fig.3. X-ray diffraction pattern (a) and scanning electron microscopy image (b) of sample synthesized at 70 °C.
[0039] Fig. 4. X-ray diffraction pattern (a) and scanning electron microscopy image (b) of sample synthesized at 60 °C
[0040] Fig.5. X-ray diffraction pattern (a) and scanning electron microscopy image (b) of sample synthesized at 70 °C.
[0041] Examples
[0042]
[0032] The following examples are intended to illustrate certain preferred embodiments of the invention and are not limiting in nature.
[0033] Example 1. Sodium dihydrogen phosphate dihydrate solution (500 mL, 80 mM) and calcium acetate hydrate solution (500 mL, 106.4 mM) was heated separately at 60 °C. Calcium acetate hydrate solution and sodium dihydrogen phosphate dihydrate solution were mixed together using peristaltic pumps as shown in Fig. 1. The speed of the peristaltic pumps is 250 rpm and the reaction was performed at pH 4.7 to 4.9. Both the solutions are mixed simultaneously and the precipitate was fdtrated directly. The resultant precipitate was fdtered using a vacuum fdter, washed with distilled water, frozen in liquid nitrogen, and lyophilized. The sample obtained after lyophilization was analyzed by powder X-ray diffraction (XRD: Panalytical, Aeries, Netherlands) and scanning electron microscope (SEM: Tescan, Bmo, Czech Republic). X-ray diffraction pattern (Fig. 2a.) revealed pure OCP (98 %) phase. The characteristic diffraction maxima observed in XRD pattern matched with the standard octacalcium phosphate ICDD card no. 00-026-1056. This confirmed that the diffraction maxima corresponds only to OCP and no other phases were identified. The scanning electron micrograph (Fig. 2b) showed plate-like morphology.
[0043]
[0034] Example 2. Sodium dihydrogen phosphate dihydrate solution (500 mL, 80 mM) and calcium acetate hydrate solution (500 mL, 106.4 mM) was heated separately at 70 °C. Calcium acetate hydrate solution and sodium dihydrogen phosphate dihydrate solution were mixed together using a peristaltic pumps as shown in Fig. 1. The speed of peristaltic pump is 250 rpm and the reaction was performed at pH 4.7 to 4.9. Both the solutions are mixed simultaneously and the precipitate was filtrated directly. The resultant precipitate was filtered using a vacuum filter, washed with distilled water, frozen in liquid nitrogen and lyophilized. The characterization of the sample obtained after lyophilization was performed as mentioned in Example 1. X-ray diffraction pattern (Fig. 3a.) revealed pure OCP (98%) phase. The characteristic diffraction maxima observed in XRD pattern matched with the standard octacalcium phosphate ICDD card no. 00-026-1056. This confirmed that the diffraction maxima corresponds only to OCP and no other phases were identified. The scanning electron micrograph (Fig. 3b) showed plate-like morphology.
[0044]
[0035] Example 3. Potassium dihydrogen phosphate solution (500 mL, 80 mM) and calcium acetate hydrate solution (500 mL, 106.4 mM) was heated separately at 60 °C. Calcium acetate hydrate solution and potassium dihydrogen phosphate solution were mixed together using a peristaltic pumps as shown in Fig. 1. The speed of peristaltic pump is 250 rpm and the reaction was performed at pH 4.7 to 4.9. Both the solutions are mixed simultaneously and the precipitate was filtrated directly. The resultant precipitate was filtered using a vacuum filter, washed with distilled water, frozen in liquid nitrogen and lyophilized. The characterization of the sample obtained after lyophilization was performed as mentioned in Example 1 . X-ray diffraction pattern (Fig. 4a.) revealed pure OCP (98 %) phase. The characteristic diffraction maxima observed in XRD patern matched with the standard octacalcium phosphate ICDD card no. 00-026-1056. This confirmed that the diffraction maxima corresponds only to OCP and no other phases were identified. The scanning electron micrograph (Fig. 4b) showed plate-like morphology.
[0045]
[0036] Example 4. Potassium dihydrogen phosphate solution (500 mL, 80 mM) and calcium acetate hydrate solution (500 mL, 106.4 mM) was heated separately at 70 °C. Calcium acetate hydrate solution and potassium dihydrogen phosphate solution were mixed together using a peristaltic pumps as shown in Fig. 1. The speed of peristaltic pump is 250 rpm and the reaction was performed at pH 4.7 to 4.9. Both the solutions are mixed simultaneously and the precipitate was filtrated directly. The resultant precipitate was filtered using a vacuum filter, washed with distilled water, frozen in liquid nitrogen and lyophilized. The characterization of the sample obtained after lyophilization was performed as mentioned in Example 1 . X-ray diffraction patern (Fig. 5a.) revealed pure OCP (98 %) phase. The characteristic diffraction maxima observed in XRD patern matched with the standard octacalcium phosphate ICDD card no. 00-026-1056. This confirmed that the diffraction maxima corresponds only to OCP and no other phases were identified. The scanning electron micrograph (Fig. 5b) showed plate-like morphology.
[0046] References
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[0055]
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[0056]
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[0057]
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[0058]
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[0060]
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[0061]
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[0062]
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[0063]
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[0064]
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[0065]
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[0066]
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[0067]
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Claims
CLAIMS1. A method for the synthesis of octacalcium phosphate (OCP) comprises the following steps: a) heating both phosphate and calcium source separately in a range from 60 to 80 °C; b) pumping continuously, concurrently and separately calcium and phosphate sources through pipes (1,2) using a system (P) providing continuous flow; c) mixing calcium and phosphate source in a mixing chamber (3), wherein the mixing is performed for a duration of less than 5 minutes, wherein the Ca / P molar ratio is from 1 to 2, a temperature range is from 60 to 80 °C with pH range from 4.0 to 6.0; d) releasing the octacalcium phosphate precipitated in step c) through pipe (4).
2. The method according to Claim 1, wherein the mixing in step c) is performed for a duration, preferably, of less than 3 minutes, or even less than 1 minute.
3. The method according to Claim 1 wherein the calcium source is calcium acetate hydrate.
4. The method according to Claim 1 wherein the phosphate source is selected from the group consisting of sodium dihydrogen phosphate dihydrate or potassium dihydrogen phosphate.
5. The method according to Claim 1 wherein the system (P) of step b) is selected from a peristaltic pump or automatic liquid dosing system or continuous flow equipment or gravitational flow system.
6. The method according to Claim 1 wherein the pH of step c) is in the range from 4.5 to 5.0.
7. The method according to Claim 1 wherein the Ca / P ratio of step c) is in the range from 1.2 to 1.4.
8. The method according to any of the previous Claims wherein the OCP obtained in step d) is dried.