ONE-STEP SINGLE HEATER BASED FLOW SYNTHESIS SETUP FOR SYNTHESIS OF INORGANIC PARTICLES IN NEAR AMBIENT CONDITIONS
20200317522 ยท 2020-10-08
Inventors
Cpc classification
C01B25/32
CHEMISTRY; METALLURGY
C01P2002/72
CHEMISTRY; METALLURGY
International classification
Abstract
A flow synthesis system (FSS) based on contamination free PTFE tubing, a pump for pumping requisite solutions and a heater for heating precipitated flow suspensions has been designed. Synthesis, using FSS, eliminates the need for secondary heat-treatments and/or long ageing times required in traditional inorganic synthesis routes. The FSS was used successfully to synthesis calcium phosphates which include phase-pure and ion substituted hydroxyapatite, respectively. Biologically beneficial magnesium, zinc, carbonate and silicon ions were successfully incorporated into hydroxyapatite.
Claims
1. A system comprising: a pump with three feeds; a stainless steel T-piece reactor; and a heater having tubing passing through it, wherein: the pump is connected to the T-piece reactor, the T-piece reactor is connected to the tubing passing through the heater, and the feeds and the tubing are formed of contamination free polytetrafluoroethylene (PTFE).
2. The system of claim 1, wherein a first feed of the pump sends a first solution to the T-piece reactor and a second feed of the pump sends a second solution to the T-piece reactor.
3. The system of claim 2, wherein the third feed of the pump sends a third solution to the T-piece reactor.
4. A method to synthesize at least one of inorganic particles and inorganic nanoparticles, comprising: providing a system comprising: a peristaltic pump with three feeds configured for 30 ml/min flow rates; a stainless steel T-piece or X-piece reactor; and a heater having tubing passing through it, wherein: the pump is connected to the T-piece or X-piece reactor, the T-piece or X-piece reactor is connected to the tubing passing through the heater, and the feeds and the tubing are formed of contamination free polytetrafluoroethylene (PTFE); sending a first solution with a first feed of the pump at a flow rate of 30 ml/min to the T-piece or X-piece reactor; sending a second solution with a second feed of the pump at a flow rate of 30 ml/min to the T-piece or X-piece reactor; and reacting the solutions in the T-piece or X-piece reactor to form a reaction suspension.
5. The method of claim 4, further comprising passing the reaction suspension of the T-piece or X-piece reactor passes through the heater.
6. The method of claim 5, further comprising discharging the suspension from the heater and is collected collecting the suspension in a container in a continuous manner.
7. The method of claim 4, further comprising selecting the first solution and second solution for continuous flow synthesis of grafted and non-grafted inorganic nanoparticles.
8. The method of claim 4, further comprising selecting the first solution and second solution for the synthesis of inorganic particles and nanoparticles.
9. The method of claim 4, further comprising selecting the first solution and second solution for the synthesis of inorganic particles and nanoparticles of a single phase.
10. The method of claim 4, further comprising selecting the first solution and second solution for the synthesis of inorganic particles and nanoparticles belonging to different phases.
11. The method of claim 4, further comprising selecting the first solution and second solution for the synthesis of inorganic particles and nanoparticles grafted with organic groups.
12. The method of claim 4, further comprising selecting the first solution and second solution for synthesis based on variable flow rates.
13. The method of claim 4, further comprising maintaining a same flow rate in all feeds.
14. (canceled)
15. The method of claim 4, further comprising increasing reaction times by increasing a length of the tubing in the heater.
16. The method of claim 4, further comprising using different solution concentrations to influence reaction yield.
17. The method of claim 4, further comprising varying a pH of the feed solutions.
18. The method of claim 4, further comprising independently varying a pH of all feed solutions.
19. The method of claim 4, further comprising synthesizing inorganic particles with varying crystallinity.
20. The method of claim 4, further comprising varying reaction temperatures.
21. The method of claim 4, further comprising varying reaction temperatures to influence phase purity of product.
22. The method of claim 4, further comprising varying reaction temperatures to influence crystallinity.
23. The method of claim 4, further comprising synthesizing grafted and non-grafted inorganic particles and nanoparticles in gram or kilogram level yields.
24. The method of claim 4, further comprising doping different elements into inorganic particles and nanoparticles.
25. The method of claim 4, further comprising varying resultant particle size is varied.
26. The method of claim 4, further comprising varying dopant levels into inorganic particles and nanoparticles.
27. The method of claim 4, further comprising carrying out reactions based on a water soluble reagent.
28. The method of claim 4, further comprising providing the feeds in the form of suspensions.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0040] The accompanying drawings, which are included to provide a further understanding of the invention and are incorporated in and constitute a part of this specification, illustrate exemplary embodiments of the invention, and together with the description serve to explain the inventive concepts.
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DETAILED DESCRIPTION
[0070] In the following description, for the purposes of explanation, numerous specific details are set forth in order to provide a thorough understanding of various exemplary embodiments or implementations of the invention. As used herein embodiments and implementations are interchangeable words that are non-limiting examples of devices or methods employing one or more of the inventive concepts disclosed herein. It is apparent, however, that various exemplary embodiments may be practiced without these specific details or with one or more equivalent arrangements. In other instances, well-known structures and devices are shown in block diagram form in order to avoid unnecessarily obscuring various exemplary embodiments. Further, various exemplary embodiments may be different, but do not have to be exclusive. For example, specific shapes, configurations, and characteristics of an exemplary embodiment may be used or implemented in another exemplary embodiment without departing from the inventive concepts.
[0071] Unless otherwise specified, the illustrated exemplary embodiments are to be understood as providing exemplary features of varying detail of some ways in which the inventive concepts may be implemented in practice. Therefore, unless otherwise specified, the features, components, modules, layers, films, panels, regions, and/or aspects, etc. (hereinafter individually or collectively referred to as elements), of the various embodiments may be otherwise combined, separated, interchanged, and/or rearranged without departing from the inventive concepts.
[0072] When an element is referred to as being on, connected to, or coupled to another element, it may be directly on, connected to, or coupled to the other element or intervening elements may be present. When, however, an element is referred to as being directly on, directly connected to, or directly coupled to another element, there are no intervening elements present. To this end, the term connected may refer to physical, electrical, and/or fluid connection, with or without intervening elements. Further, the D1-axis, the D2-axis, and the D3-axis are not limited to three axes of a rectangular coordinate system, such as the x, y, and z-axes, and may be interpreted in a broader sense. For example, the D1-axis, the D2-axis, and the D3-axis may be perpendicular to one another, or may represent different directions that are not perpendicular to one another. For the purposes of this disclosure, at least one of X, Y, and Z and at least one selected from the group consisting of X, Y, and Z may be construed as X only, Y only, Z only, or any combination of two or more of X, Y, and Z, such as, for instance, XYZ, XYY, YZ, and ZZ. As used herein, the term and/or includes any and all combinations of one or more of the associated listed items.
[0073] Although the terms first, second, etc. may be used herein to describe various types of elements, these elements should not be limited by these terms. These terms are used to distinguish one element from another element. Thus, a first element discussed below could be termed a second element without departing from the teachings of the disclosure.
[0074] Spatially relative terms, such as beneath, below, under, lower, above, upper, over, higher, side (e.g., as in sidewall), and the like, may be used herein for descriptive purposes, and, thereby, to describe one elements relationship to another element(s) as illustrated in the drawings. Spatially relative terms are intended to encompass different orientations of an apparatus in use, operation, and/or manufacture in addition to the orientation depicted in the drawings. For example, if the apparatus in the drawings is turned over, elements described as below or beneath other elements or features would then be oriented above the other elements or features. Thus, the exemplary term below can encompass both an orientation of above and below. Furthermore, the apparatus may be otherwise oriented (e.g., rotated 90 degrees or at other orientations), and, as such, the spatially relative descriptors used herein interpreted accordingly.
[0075] The terminology used herein is for the purpose of describing particular embodiments and is not intended to be limiting. As used herein, the singular forms, a, an, and the are intended to include the plural forms as well, unless the context clearly indicates otherwise. Moreover, the terms comprises, comprising, includes, and/or including, when used in this specification, specify the presence of stated features, integers, steps, operations, elements, components, and/or groups thereof, but do not preclude the presence or addition of one or more other features, integers, steps, operations, elements, components, and/or groups thereof. It is also noted that, as used herein, the terms substantially, about, and other similar terms, are used as terms of approximation and not as terms of degree, and, as such, are utilized to account for inherent deviations in measured, calculated, and/or provided values that would be recognized by one of ordinary skill in the art.
[0076] Unless otherwise defined, all terms (including technical and scientific terms) used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this disclosure is a part. Terms, such as those defined in commonly used dictionaries, should be interpreted as having a meaning that is consistent with their meaning in the context of the relevant art and should not be interpreted in an idealized or overly formal sense, unless expressly so defined herein.
[0077] As illustrated in
[0078] Calcium hydroxide solution and Diammonium hydrogen phosphate with the concentrations shown in Table 1 were pumped using a peristaltic pump at a flow rate of 30 ml/min with the exit temperature at 70 C. (controlled using adjusting set temperature of Heater H1). Resulting suspension was collected immediately after exit. The suspension was then centrifuged followed by washing (2 times) using deionized water. Synthesized samples were then freeze dried using an Alpha 1-2 LD plus freeze dryer.
TABLE-US-00001 TABLE 1 Concentrations and volumes of precursors used for synthesis of 2 samples of hydroxyapatite (A, B) in this study. Volume Volume Reactions Concentration (mL) Concentration (mL) ID Diammonium hydrogen phosphate Calcium Hydroxide Sample A 0.3M 250 0.5M 250 Sample B 0.3M 250 0.3M 250
[0079] X-ray Diffraction: XRD analysis confirmed samples to be phase pure hydroxyapatite when compared to ICDD Pattern #09-432 as no other peak was observed in the spectrum (please see
[0080] Scanning Electron Microscopy: SEM was performed to analyze morphology and particle size of the samples synthesized. The average particle size was calculated at 1000 and 5000 magnifications about 4 m as seen in image (a) of
[0081] Synthesis of Hydroxyapatite Using Calcium Nitrate Tetrahydrate & Diammonium Hydrogen Phosphate
[0082] Phase pure HA: Similarly, reactions were carried out with Diammonium hydrogen phosphate solution and Calcium nitrate tetrahydrate solution with the different concentrations as shown in Table 2 were pumped at a flow rate 30 ml/min with the exit temperature 70 C. The pH was maintained 10 with 3 ml of ammonium hydroxide solution. Then the mixture was centrifuged and filtered and washed twice by de-ionized water.
TABLE-US-00002 TABLE 2 Concentrations and volumes of precursors used for synthesis of 4 samples of hydroxyapatite (A, B, C and D) in this study. Volume Volume Concentration (mL) Concentration (mL) Reactions Diammonium Calcium nitrate ID hydrogen phosphate tetra hydrate Sample A 0.3M 200 0.5M 200 Sample B 0.3M 200 0.6M 200 Sample C 0.3M 200 0.3M 200 Sample D 0.3M 200 0.6M 200
[0083] X-ray Diffraction: confirms the synthesis of Hydroxyapatite when compared to ICDD Pattern #09-432. But another peak was observed in the spectrum near 30 Theta, which was possibly due to unreacted Calcium Hydroxide, as shown in images (a)-(e) of
[0084] Ion Substituted Hydroxyapatite: Substituted reactions were carried out with Diammonium hydrogen phosphate solution and Calcium nitrate tetrahydrate solution with the different concentrations as shown in Table 3 were pumped at a flow rate 30 ml/min with the exit temperature 70 C. The pH was maintained 10 with 3 ml of ammonium hydroxide solution. Then the mixture was centrifuged and filtered and washed twice by de-ionized water.
TABLE-US-00003 TABLE 3 Concentrations and volumes of precursors used for synthesis of 4 samples of Substituted hydroxyapatite (A, B, C and D) in this study. Volume Volume Reactions ID Concentration (mL) Concentration (mL) Sample A Zinc Substituted HA 0.15M 200 0.3M 200 Sample B Magnesium substituted HA 0.15M 200 0.3M 200 Sample C Silicone Substituted HA 0.15M 200 0.3M 200 Sample D Carbonated HA 0.15M 200 0.3M 200
[0085] Zinc Substituted Hydroxyapatite (Zn-HA)
[0086] X-ray Diffraction: It is clearly seen from XRD pattern (a) of
[0087] Scanning Electron Microscopy: SEM was performed to analyze morphology and particle size of the samples synthesized in this study. Images (a) and (b) of
[0088] Magnesium Substituted Hydroxyapatite (Mg-HA)
[0089] X-ray Diffraction: It is clearly seen from the XRD pattern (a) of
[0090] Scanning Electron Microscopy: Scanning Electron Microscopy was performed for morphological analysis of Mg-HA in this study. Images (a) and (b) of
[0091] Silicone Substituted Hydroxyapatite (Si-HA)
[0092] X-Ray Diffraction: The XRD pattern (a) in
[0093] Scanning Electron Microscopy: images (a) and (b) of
[0094] Carbonate Substituted Hydroxyapatite (CO.sub.3-HA)
[0095] X-Ray Diffraction: The XRD pattern (a) of CO.sub.3-HA (Sample D) in
[0096] Scanning Electron Microscopy: images (a) and (b) of
[0097] Synthesis of Zinc Phosphates
[0098] For the synthesis of zinc phosphates, stock solutions of 0.15M zinc nitrate and 0.1M di ammonium hydrogen phosphase were prepared in deionized water respectively. For first reaction (Sample A), 250 ml each solution was used and pumped at a flow rate of 30 ml/min. In this reaction no pH was adjusted and no heating was involved.
[0099] In a second reaction (Sample B) 250 ml of each solution were pumped at same flow rate but pH was adjusted by adding 3 ml of ammonia solution in the original reagent solutions. The third reaction (Sample C) was again done at same flow rate but no pH adjusted but heating was involved up to 70 C. In the fourth reaction (Sample D), again we used 250 ml of each solution but in this reaction no heating and pH adjustment were involved as shown in Table 4. After collection the suspensions were filtered followed by washing with deionized water (2 times). All the samples were dried in drying oven at 80 C. for 24 hours.
[0100] Table: 4 shows the reactions IDs, reaction parameters, concentrations and volumes of precursors used for synthesis of zinc phosphates in this embodiment.
TABLE-US-00004 Volume Volume Reactions Concentration (mL) Concentration (mL) ID Parameters Diammonium Hydroxide Zinc Nitrate tetra hydrate Sample A No Heating, No pH 0.1M 250 0.15M 250 Sample B Heating, pH adjusted 0.1M 250 0.15M 250 Sample C Heating, No pH 0.1M 250 0.15M 250 Sample D No Heating, pH adjusted 0.1M 250 0.15M 250
[0101] X-ray Diffraction: When no heating was used without any pH adjustment Zn.sub.3 (PO.sub.4).sub.2.2H.sub.2O phase was observed for Sample A in pattern (a) of
[0102] Scanning Electron Microscopy: SEM analysis reveals image (a) of
[0103] Synthesis of Phase Pure and Ion Substituted Oxides
[0104] Phase Pure Zinc Oxide
[0105] Zinc oxide was synthesized using the 0.3M Zn(NO.sub.3).sub.2.6H.sub.2O and 0.6M NaOH solutions with a flow rate of 30 ml/min with exit temperature of 70 C. The synthesized samples were then freeze dried for 24 hours to obtain phase pure ZnO.
[0106] X-ray Diffraction: pattern (a) of
[0107] Scanning Electron Microscopy: images (a) and (b) of
[0108] Ion Doped Zinc Oxides
[0109] To synthesize doped-Zinc oxides, pre-weighed dopant sources [Ce(NO.sub.3).sub.3.6H.sub.2O, KNO.sub.3, Ca(NO.sub.3).sub.2.4H.sub.2O, Mg(NO.sub.3).sub.2.6H.sub.2O, & Fe(NO.sub.3).sub.3.9H.sub.2O] were added to Zinc Nitrate solution.
[0110] Cerium, Potassium, Magnesium, Calcium and Iron ions were doped in Zinc Oxide in varying (theoretical) concentrations (0.5 mole %, 1 mole % & 2 mole %). Please see Table 5 for details.
[0111] Table: 5 shows the amounts of dopant ion sources added to Zinc Nitrate precursor solution.
TABLE-US-00005 Element 0.5 mole % 1 mole % 2 mole % Cerium (CeNO.sub.36H.sub.2O) 0.1620 g 0.3250 g 0.6510 g Potassium (KNO.sub.3) 0.0379 g 0.0700 g 0.1500 g Calcium (Ca(NO.sub.3).sub.24H.sub.2O) 0.0886 g 0.1170 g 0.3540 g Iron (Fe(NO.sub.3).sub.39H.sub.2O) 0.1500 g 0.3000 g 0.6060 g Magnesium (Mg(NO.sub.3).sub.26H.sub.2O) 0.0960 g 0.1900 g 0.3800 g
[0112] Elemental Analysis (using SEM-EDS): An EDS detector attached to the SEM was used to verify the dopant ions presence in synthesized oxides. The spectra revealed no additional impurities. The results are summarized in Table 6 below. It was observed that the measured dopant amount was generally lesser than the added dopant amount. This difference may be attributed to the high diffusivity of the flow process which provides less (hence quick) residence times. These results elucidate that successful doping was achieved.
TABLE-US-00006 TABLE 6 Dopant amounts (mole %) added to precursor solution (theoretical) and the measured dopants amounts (mole %) Mole % Average Weight % Element (Theoretical) (Evaluated) Cerium 0.50 0.45 1.00 2.10 2.00 2.64 Potassium 0.50 0.03 1.00 0.05 2.00 0.12 Calcium 0.50 0.01 1.00 0.04 2.00 0.09 Iron 0.50 0.40 1.00 0.64 2.00 1.41 Magnesium 0.50 0.33 1.00 0.36 2.00 0.57
[0113] X-Ray Diffraction: patterns (a)-(d) of
[0114] Furthermore, it was observed that the sharpness of the peak reduces along with shift as the dopant concentration increases. It can be inferred that the dopant affects decreases the crystallinity due to ZnO lattice distortion.
[0115] Coupled with the confirmation of doping from EDS elemental analysis, the shift in peaks confirms the incorporation of dopant ions in the ZnO lattice. In all the cases, the observed samples were found to be phase-pure (i.e. no other oxides were detected). It is evident that the dopants have broadened the spectra which depicts change in particle size; which were then validated by SEM results.
[0116] Scanning Electron Microscopy: Scanning Electron Microscopy was used to investigate the effect of dopant concentrations on particle morphology and aggregation.
[0117] Images (a) and (b) of
[0118] At lower concentration of potassium i.e. 0.5 mole %, the nanoparticles were clustered together and formed agglomerates, the high magnification images (a) and (b) of
[0119] The calcium doping at 0.5 mole % resulted in agglomeration of nanoparticles. The image (a) at low magnification of
[0120] 0.5 mole % Fe doped ZnO depicted very small independent features of about 33.194 nm to 126.399 nm at low magnification. However, at high magnification the fused entities were spotted (72.05812 nm), as shown in images (a) and (b) of
[0121] Similarly, the doping of Mg to ZnO lead to particle growth when the dopant concentration was increased to 2%, as shown in images (e) and (f) of
[0122] Phase Pure Cerium Oxide Synthesis
[0123] Cerium oxide was synthesized using the reagents cerium nitrate tetra hydrate (0.1M in 250 ml water) and sodium hydroxide (1M in 250 ml water) at a flow rate of 30 ml/min. The synthesized sample was freeze dried at 4000 rpm followed by twice washing.
[0124] X-Ray Diffraction: XRD pattern shown in
[0125] Scanning Electron Microscopy: Scanning Electron Microscopy of CeO.sub.2 was performed to analyze particle size and morphology.
[0126] Grafted Oxides
[0127] Surface modification using the flow synthesis system was carried out. A monomer urethane dimethacrylate (UDMA) was grafted onto ZnO particles by utilizing a third stream in the pumps.
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[0129] Although certain exemplary embodiments and implementations have been described herein, other embodiments and modifications will be apparent from this description. Accordingly, the inventive concepts are not limited to such embodiments, but rather to the broader scope of the appended claims and various obvious modifications and equivalent arrangements as would be apparent to a person of ordinary skill in the art.