We present detailed procedures to produce experimental equilibrium curves of the phase composition as a function of solvent concentration in a solid state system under milling conditions.
The equilibrium outcomes of ball mill grinding can dramatically change as a function of even tiny variations in the experimental conditions such as the presence of very small amounts of added solvent. To reproducibly and accurately capture this sensitivity, the experimentalist needs to carefully consider every single factor that can affect the ball mill grinding reaction under investigation, from ensuring the grinding jars are clean and dry before use, to accurately adding the stoichiometry of the starting materials, to validating that the delivery of solvent volume is accurate, to ensuring that the interaction between the solvent and the powder is well understood and, if necessary, a specific soaking time is added to the procedure. Preliminary kinetic studies are essential to determine the necessary milling time to achieve equilibrium. Only then can exquisite phase composition curves be obtained as a function of the solvent concentration under ball mill liquid assisted grinding (LAG). By using strict and careful procedures analogous to the ones here presented, such milling equilibrium curves can be obtained for virtually all milling systems. The system we use to demonstrate these procedures is a disulfide exchange reaction starting from the equimolar mixture of two homodimers to obtain at equilibrium quantitative heterodimer. The latter is formed by ball mill grinding as two different polymorphs, Form A and Form B. The ratio R = [Form B] / ([Form A] + [Form B]) at milling equilibrium depends on the nature and concentration of the solvent in the milling jar.
Mechanochemistry using manual or ball mill grinding equipment has become increasingly popular in recent years as an attractive and sustainable alternative to traditional solution methods for the synthesis of materials.1 It is attractive because it allows for reaction between solids to be achieved effectively and quantitatively. It is a "green" sustainable technique, requiring little or no solvent. Milling or manual grinding can be performed neat, i.e. with no added solvent, or solvent assisted: in the latter, known as "liquid assisted grinding" (LAG),2,3,4 very small amounts of added liquid can accelerate or even enable otherwise inaccessible mechanochemical reactions between solids. Mechanochemical methods have been used for an ever-increasing number of different chemical reactions and syntheses of inorganic and organic compounds,5,6,7,8,9,11 as well as for the formation of supramolecular architectures such as molecular co-crystals,12,13,14 metalorganic frameworks,15,16,17 and even cages18 and rotaxanes19. It seems that many processes can proceed in the absence of solvent or with solvent present in minimal substoichiometric quantities.2,3,4 The mechanisms and the driving forces involved in the chemical syntheses and supramolecular reactions induced by mechanochemical conditions are subject of debate.1,13,20,21,22,23,24
Our research focuses on the final equilibrium outcomes of the ball mill grinding process and the role of solvent at equilibrium under ball mill LAG conditions. Indeed, after the ball mill grinding reaction reaches completion, thermodynamic equilibrium is achieved in the two systems we have investigated so far in our system, with a stable phase composition.25 The factors that can affect the final equilibrium are numerous and diverse: ball mill jar size and shape and material, ball bearing size and weight and material, milling frequency, temperature, and solvent nature and concentration. This is evidently the case when the thermodynamic outcome of the grinding reaction changes dramatically in response to a change in the solvent volume added, which can be sometime as low as 1µL per 200 mg of total powder.25 Careful and strict experimental procedures have to be tested and followed in order to achieve reproducible precision and accuracy of the experimental results, from reactants and products storage, to pipetting and mixing pre-milling operations. It is difficult to control or even monitor parameters in a milling jar. Therefore, the use of a mechanical mixer mill (also called vibratory mill), which allows for reproducible and controlled milling frequencies and times, and sealed milling jars are essential. Ensuring that all ball mill grinding reactions reach equilibrium requires some preliminary kinetic investigation of the experimental conditions. The mechanical mixer used for the curves we present here was modified. In order to prevent the jars from warming up through the continuous flow of the exhausts of the motor in the sealed chamber over long periods of grinding, the safety cover sealing the front part of the grinder was removed, and an external safety screen was placed in its place.
The system that we used as a first example is the disulfide exchange reaction between bis-2-nitrophenyldisulfide (named 1-1) and bis-4-chlorophenyldisulfide (named 2-2) in the presence of a small amount of base catalyst 1,8-diazabicyclo[5.4.0]undec-7-ene (dbu) to produce upon ball mill neat grinding (NG) and LAG the compound 4-chlorophenyl-2-nitrophenyl-disulfide (named 1-2).26,27 The latter is formed by ball mill grinding as two different polymorphs, Form A and Form B. For many different LAG solvents, Form A is the thermodynamic product under ball mill NG conditions or when not enough solvent is used in the grinding reaction taken to equilibrium, while Form B is obtained as the thermodynamic product under ball mill LAG conditions at equilibrium when enough solvent is added to the milling jar.Indeed Form A can be obtained from Form B under ball mill NG, while Form B can be obtained from Form A under ball mill LAG. Such direct transformation in milling experiments has been reported before in other systems,28,29 and it has been reported that the nature and concentration of solvent determine the polymorph obtained under LAG conditions.30 Our published experimental results include the investigation of milling equilibrium curves for a range of organic solvents. Here the equilibrium phase composition ratio R = [Form B] / ([Form A] + [Form B]) is plotted against the volume of LAG solvent added for each experiment. The onset of the equilibrium curve and the sharpness of the curve were found to depend on the nature and molar amount of solvent added to the milling jar.
Figure 1: Reaction scheme of the ball mill grinding experiments and key concept of solvent equilibrium curves using the R value.
These equilibrium curves shows graphically the effect of the addition of a few drops of solvent (x axis) on the phase composition of the product (y axis) when ball mill grinding for long enough to achieve equilibrium conditions. The bottom part of the graph accounts for Form A being quantitatively formed, the top part of the graph for Form B being quantitatively formed while a mixture of Form A and Form B is formed for the volume range of the solvent accounting for the sigmoidal part of the graph. This figure has been reprinted with minor changes from the Supplementary information in Chem. Sci., 2016, 7, 6617 (Ref. 25). Please click here to view a larger version of this figure.
Thermodynamic aspects are general and must apply to any given milling system. As a further example to show the generality of our observations, an analogous equilibrium curve was also produced for a second system: the two polymorphs of 1:1 co-crystal of theophylline (tp) with benzamide (bzm), form I and form II, where the outcome depends on the volume of water in the grinding mixture.25 These phase composition versus solvent concentration equilibrium curves are essential for investigating the interaction between the nanocrystal surfaces and the solvent molecules at equilibrium on ball mill grinding reactions. Our results demonstrate that some equilibrium curves are very sharp, showing an "all-or-nothing" behaviour, which is characteristic of particles with a large number of adsorption sites and positive cooperativity of the binding process.31 Shallower equilibrium curves indicate a lower level of cooperativity and suggest the presence of a third phase at equilibrium, possibly an amorphous phase involving the solvent itself. Such milling equilibrium curves have been produced for no other system to our knowledge. We believe this to be partly due to the inherent sensitivity of the solid state system to even very small environmental changes under ball mill LAG conditions.
Preparation of good and reliable solvent concentration curves can only be achieved if the experimentalists carefully validate their pipetting skills with training sets and if they fully understand (i) how pipettes and syringes work and (ii) if the equipment they have selected for delivering accurate and precise volume of a solvent is suitable to perform the intended job. The delivery of an exact volume of solvent can be accomplished with a variety of equipment, this being pipettes or syringes and their choice can depend on availability, user preference and skills, vapor pressure of the solvent used and intended application for the ball mill grinding experiments.
Pipettes are commercially available as air displacement or positive displacement covering many solvent ranges. Both types of pipettes are commercially available as manually operated or electronically automated. Automatic pipettes are generally preferred as they are less dependent on the experimentalist skills to be able to aspirate or dispense a solvent evenly at a given speed. The experimentalist must rely on the capability of the pipettes to deliver the exact volume of solvent. This can only happen if the pipettes are accurate to start with, well maintained, serviced and periodically calibrated. Typically, external pipette calibration services will calibrate pipettes to the ISO 8655 standard using water as the solvent. Therefore, for each organic solvent the experimentalist should validate their accuracy and precision of pipetting through accurate weighing experiments over the intended volume range to be dispensed.
The most commonly used solvent delivery equipment is the air displacement pipettes to which a tip needs to be fitted to the syringe barrel. They work on an air-cushion principle; upward movement of the piston produces a partial vacuum in the tip, causing the liquid to be drawn into the tip which is separated from the end of the piston by the air cushion. The vapor phase of the pipetted solvent will start to equilibrate within the air cushion, the extent of evaporation will depend on its vapor pressure. Pre-wetting is crucial when using variable-volume pipettes set at their lowest volume range, since the ratio of airspace to liquid and the potential for evaporation increases dramatically as compared to when the pipette is set at the top of its volume range. The experimentalist will know when this equilibrium is achieved, as the solvent aliquot will be hanging but separated from the end of the piston as from a spring, the solvent at the end of the tip staying firm when the pipette is held in vertical position over a few seconds: the solvent inside the tip should not sag or drip. Air displacement pipettes can be used in two modes; the most generally used is the forward pipetting mode where all the aspirated solvent is quantitatively dispensed by one full movement of the piston. The other mode is the reverse pipetting mode; in this mode a calculated excess of solvent is aspirated by the pipette, and therefore after quantitative dispensing, a residual volume of solvent remain in the pipette tip which needs to be disposed to waste. Reverse pipetting mode can be more suitable for viscous and dispensing very small volume of solvents. However, for high vapor pressure solvents like dichloromethane (DCM) or diethyl ether, equilibration in the air displacement pipette cannot be easily achieved. Positive displacement pipettes or syringes are more suitable in this case.
We propose that equilibrium phase composition versus solvent concentration curves could be obtained for any system under sufficiently well-designed, performed and controlled ball mill LAG conditions.
1. Validation of the precise dispensing of organic solvents
Figure 5: Validation of the accuracy and precision of volume dispensed with electronic air displacement pipette set to reverse pipetting mode, calibrated by weighing experiments. (a,b)
a) Range 10-100µL MeCN; b) expanded narrow range from 20-30 µL MeCN. This figure has been reprinted with minor changes from the Supplementary information in Chem. Sci., 2016, 7, 6617 (Ref. 25). Please click here to view a larger version of this figure.
2. Synthesis of Form A and Form B by ball mill grinding
Figure 2: Rietveld refinement plot example for the equilibrium mixture under milling conditions when using 67 µL methanol.
Experimental pattern (black line), calculated pattern for Form A (blue), calculated pattern for Form B (red), and difference pattern (grey). The refinement converged with Rwp=10.82% and χ2 = 2.65. For this specific example the R ratio was 41%, and crystal size was estimated to be 71 and 86 nm for Form A and Form B respectively. Please click here to view a larger version of this figure.
Figure 3: Kinetic curves obtained for the ball mill neat grinding reaction of 1-1 +2-2 +2%M dbu (a,b).
No fitting was performed – the lines are only a guide to the eye. The graph shows the composition of reactants (1-1 & 2-2) and the heterodimer formed (Form A and Form B) as %M versus grinding time a) HPLC analyses showing chemical composition of the powder at each kinetic point; b) Rietveld refinement of PXRD scans showing phase composition of the powder at each kinetic point. It demonstrates that Form A is exclusively formed while Form B is not formed at any kinetic point. Reprinted with permission from JACS, 2014, 136, 16156 (Ref. 27). Copyright 2014 American Chemical Society. Please click here to view a larger version of this figure.
Figure 4: Kinetic curves obtained for the ball mill LAG reaction of 1-1 +2-2 +2%M dbu + 50 µL MeCN. (a,b)
No fitting was performed – the lines are only a guide to the eye. The graph shows the composition of reactants (1-1 & 2-2) and the heterodimer formed (Form A and Form B) as %M versus grinding time a) HPLC analyses showing chemical composition of the powder at each kinetic point; b) Rietveld refinement of PXRD scans showing phase composition of the powder at each kinetic point. It demonstrates that Form B is exclusively formed while Form A is not formed at any kinetic point. Reprinted with permission from JACS, 2014, 136, 16156 (Ref. 27). Copyright 2014 American Chemical Society. Please click here to view a larger version of this figure.
3. Preparation of Form A and/or Form B by ball mill LAG using different types and volumes of organic solvents as LAG solvents.
Figure 7: Ball mill LAG of 1-1+2-2+2%M dbu for 3 h at 30 Hz with DMF as LAG solvent. (a-e)
HPLC chromatograms and PXRD scans for 3 examples: at equililbrium, the addition of b) 13µL DMF results in quantitative Form A, c) 30 µL DMF results in quantitative Form B and d)19 µL DMF results in a mixture of Form A and Form B. e) THF equilibration curve is shown for all the 17 experiments performed with DMF, plotting the %R determined versus the µL DMF added to the 200 mg powder. This figure has been reprinted from the Supplementary information in Chem. Sci., 2016, 7, 6617 (Ref. 25). Please click here to view a larger version of this figure.
Figure 6: Solvent equilibrium curves for ball mill grinding reaction of 1-1 + 2-2 + 2%M dbu when using Methanol as the LAG solvent. (a,b)
No fitting was performed – the line is only a guide to the eye. The equilibrium curve (%R versus µL Methanol added to 200 mg powder) in a) gives very poor correlation using experimental Procedure 1 while in b) there is a good correlation when using experimental Procedure 2. This figure has been reprinted from the Supplementary information in Chem. Sci., 2016, 7, 6617 (Ref. 25). Please click here to view a larger version of this figure.
4. Determination of phase composition by PXRD
NOTE: The solid state phase composition of the powder mixtures as obtained at the end of the milling experiment is studied by Rietveld refinement of ex-situ powder diffraction data.32 Some guidelines are here given.
This protocol is always started by the experimentalist validating his or her pipetting skills and inspecting the quality and performance of the pipettes or syringes used. This is best done by performing training sets on pipetting accurate volumes of the specific solvent intended to be used for the ball mill grinding experiments. The accuracy of the dispensed volumes is validated by weighing checks and this validation is repeated until the desired accuracy and precision is achieved. This validation has to be done for each solvent used for the ball mill grinding experiments. Figure 5 shows an example of such a validation of the accurate pipetting with acetonitrile.
HPLC data was collected to obtain the chemical composition and PXRD scans were collected to obtain the phase composition of the powder from ball mill grinding reactions (See Figure 1 for the reaction scheme and the key concept of solvent equilibrium curves). HPLC data quantifies the chemical composition as %M of the 2 homodimers (1-1 and 2-2) and the heterodimer (1-2) in the powder. Rietveld refinement prepared from the PXRD scans is used to quantify the phase composition as %M of the homodimers starting materials (1-1 and 2-2) and the two polymorphs (Form A and Form B) of the heterodimer product 1-2. HPLC can be used therefore to validate the accuracy of the phase composition results obtained by Rietveld refinement on the same samples; the combined concentration of Form A and Form B as %M determined by PXRD should equate with the concentration of 1-2 as %M determined by HPLC, while 1-1 and 2-2 should have the same concentration in %M determined by HPLC and PXRD. This is clearly shown on Figure 3 and Figure 4 where there is a good correlation between the kinetic curves plotting the chemical composition obtained by HPLC analysis and the kinetic curves plotting the phase composition obtained by PXRD analysis.
The success of the preparation of accurate and precise solvent equilibrium curves for the ball mill grinding reaction relies on 3 factors: a) accurate and precise pipetting by the experimentalist; b) knowing when the ball mill grinding reaction has achieved equilibrium, which can be learned by performing the relevant kinetic studies as shown in Figure 3 and Figure 4; and c) by using the right experimental procedure for each solvent. The equilibrium curve in Figure 7 demonstrates good correlation between %R and the µL of DMF added to the grinding reaction when using experimental procedure 1. However, experimental procedure 1 gives very poor correlation between %R and the µL of methanol added to the grinding reaction as shown in Figure 6a, while the use of experimental procedure 2 for methanol gives good correlation as shown in Figure 6b. Figure 8 shows individually and combined how different solvents (MeCN, Acetone, THF, EtOAc, DMF, CHCl3, DCM, MeOH, EtOH, IPA and DMSO) results in different solvent equilibrium curves for the ball mill LAG reactions. Figure 8 demonstrate that good correlation between %R and the amount of solvent added to the ball mill grinding reaction can be achieved if care and good experimental design is applied when performing these experiments.
While most of the literature on mechanochemistry focuses either on pragmatic outcomes or on reaction mechanisms, this paper addresses the thermodynamic end point of ball mill grinding. From this perspective, kinetic studies are a necessary step to the definition of the final equilibrium plateaus. Through our kinetic and final equilibrium studies, we know that the ball mill grinding reactions here discussed are driven by thermodynamics, resulting in the most stable polymorph composition under the given milling conditions. This is also the first time to our knowledge that experimental preparation methods – such as pipetting methods and milling jar setup – for mechanochemical experiments are presented and discussed in detail.
It is critical to the successful outcome of the ball mill LAG experiments that a preliminary kinetic study is undertaken to establish for how long the ball mill grinding experiment needs to run to reach equilibrium. Under thermodynamic conditions ball mill grinding reactions can present three scenarios discussed in this manuscript; a) adding not enough volume of the given solvent for the ball mill grinding reaction, in which case the outcome is the quantitative formation of Form A; b) using at least enough volume of the given solvent, which results in the quantitative formation of Form B; c) the third case is in the gap between both extremes, where the skills, care and experimental design of the experimentalist become most important. The successful experimentalist will be able to demonstrate that the concentration of Form B increases with increased added solvent volume of the given solvent in a sigmoidal way until enough solvent is added to result in quantitative formation of Form B in a ball mill LAG reaction. For some solvents this change is so sharp that a difference of just 1 µL suffices to obtain quantitatively either Form A or Form B, as in the case of acetonitrile and acetone. Figure 8 summarizes this discussion.
Figure 8: Individual and combined solvent milling equilibrium curves plotted as solvent concentration versus %R index.
No fitting was performed – the lines are only a guide to the eye. Solvent investigated are: MeCN, acetone, THF, DMF, EtOAc, CHCl3, DCM, DMSO, MeOH, EtOH, IPA and water. Water does not lead to the formation of Form B. The dispensing of DCM as LAG solvent was performed with a gas tight glass syringe. This figure has been reprinted from the Supplementary information in Chem. Sci., 2016, 7, 6617 (Ref. 25). Please click here to view a larger version of this figure.
Since thermodynamic concepts are general, milling equilibria as a function of solvent concentration under ball mill LAG conditions should be amenable to study for virtually for any given system setting up analogous procedures. There is therefore the potential to explore and discover new polymorphs by variation of added solvent, which may have practical implications in various industrial settings, and this includes most organic and inorganic reactions, as well as supramolecular compounds.
Laboratory environment (temperature, atmospheric pressure, humidity) during sample preparation and experiments can affect the kinetics and equilibrium end point of the milling process – see Tumanov et al. (2017)37 as an example. In our experience, even small variations in size and shape of the milling jar and ball bearings – as well as the material they are made of – and total amount of powder can significantly affect the reaction rate and final equilibrium of the milling experiments. The experimentalist needs to take great care in the design and performance of these experiments, considering: (i) what pipetting technique has to be adopted for a specific solvent; (ii) how compounds have to be added to the milling jar and mixed; (iii) the size and shape of the milling jar and ball bearings; (iv) whether a stainless steel or a transparent material – which is necessary for in-situ techniques such as Raman21,38 – should be adopted for the milling jar and ball bearings. Perspex jars are easily damaged by many solvent used with LAG and solvents used for cleaning the jars. 3D printing of transparent jars from polylactic acid (PLA) allows more intricate design of the external geometry of jars, which show good mechanical and chemical resistance compared with Perspex, and are therefore more suitable for ball-milling experiments.39 Equilibrium experiments must be performed as consistently as possible, both in the experimental procedure and hardware, i.e. using identical preparation methods, jars, ball bearings and total amount of powder.
Care must be taken not to overgrind unnecessarily as decomposition can occur. For our disulfide system, decomposition products can be observed for example by HPLC analysis or NMR. If this happens, a decomposition kinetic study is necessary. Ball mill grinding must be performed for the shortest time that leads to equilibrium.
The current experimental approach has limitations in that we are not controlling macroscopic temperature efficiently and do not know local temperatures within the steel reaction vessel. We are also currently unable to monitor the evolution of crystallinity, which refers to the degree of structural order in a crystalline solid and crystal morphology during the course of grinding. In a nanocrystalline powder, crystallinity is mostly related to the average crystal size, which can crucially affect the polymorph stabilities.25 Improvements in these areas would greatly enhance our ability to explore and understand underlying processes.
The authors have nothing to disclose.
AMB and JKMS are grateful to the EPSRC for financial support. We thank C. A. Bland for the design and the mechanical setup and P. Donnelly for the software design of the automation of the grinders for repeat grinding. We thank Richard Nightingale, Ollie Norris and Simon Dowe from the mechanical workshop for the manufacture of the grinding jars, and the Solenoid holder for the "Push a Button" setup and Keith Parmenter from the glass workshop at the Department of Chemistry for the manufacture of the glass sample PXRD slides. We thank C. A. Bland for the maintenance and repair of the screw closure grinding jars. We thank Professor Bill Jones for the use of the PXRD equipment at the Department of Chemistry and Professor Chris Hunter for the use of his laboratory facilities. We thank the Department of Earth Sciences (GIL) for general support.
Bis(2-nitrophenyl) disulfide named 1-1 | Aldrich | 215228-25G | [1155-00-6] (98%) |
Bis(4-chlorophenyl) disulfide named 2-2 | TCI | D0360 | [1142-19-4] (98+%) |
1,8-Diazabicyclo [5.4.0]undec-7-ene (dbu) | Acros Organics | 160610250 | [6674-22-2] (>97.5 % by GC) |
2-nitrophenyl-4-chlorophenyl-disulfide named 1-2 | in house synthesis | Synthesised by ball mill grinding: 1:1 of 1-1 + 2-2 + 2%M dbu | |
Form A | in house synthesis | Polymorph of 1-2 prepared by ball mill neat grinding | |
Form B | in house synthesis | Polymorph of 1-2 prepared by ball mill liquid assisted grinding | |
Formic Acid | Scientific Laboratory Supplies | 56302-50ML | [64-18-6] Mass spectrometry grade |
Trifluoroacetic acid (TFA) | ThermoFisher | 85183 | [76-05-1] Reagent-Plus 99% |
Water (H2O) | Rathburn | W/0106/PB17 | [7732-18-5] HPLC gradient analysis grade used also for HPLC analysis |
Acetonitrile (MeCN), | Merck | 160610250 | [75-05-8] Hypergrade for LCMS grade LiChrosolv used also for HPLC analysis |
Acetone | Fisher Scientific | A/0606/17 | [67-64-1] HPLC grade |
Methanol (MeOH) | Fisher Scientific | M/4062/17 | [67-56-1] LCMS grade |
Ethanol (EtOH) | Sigma Aldrich | 15727-5L | [64-17-5] laboratory reagent, absolute, |
isopropanol (IPA) | Fisher Scientific | P/7508/17 | [67-63-0] HPLC grade |
Tetrahydrofurane (THF) | Acros Organics | 268290010 | [109-99-9] For HPLC; 99%8, unstabilised |
Ethyl acetate (EtOAc) | Fisher Scientific | E/0906/15 | [141-78-6] |
Chloroform (CHCl3,) | Fisher Scientific | C/4966/17 | [67-66-3] HPLC grade, stabilised with amylene |
Dichloromethane (DCM) | Fisher Scientific | D/1857/17 | [75-09-2] HPLC grade, unstabilised |
Dimethylformamide (DMF) | Alfa Aesar | 22915 | [68-12-2] very toxic HPLC grade 99+% pure |
Dimethylsulfoxide (DMSO) | Alfa Aesar | 36480 | [67-68-5] very toxic ACS, 99.9% min |
Cyclohexane | Fisher Scientific | C/8936/15 | [110-82-7] HPLC grade, 99.8+% |
Toluene | Fisher Scientific Ltd | T/2306/15 | [108-88-3] HPLC grade |
Benzene | Sigma Aldrich | 401765 | [71-43-2] puriss pa reagent |
5 -120 mL automatic pipette | Sartorius | Picus eLine | systematic error in specification: for 120mL is ±0.48 mL, for 60 mL is ±0.36 mL, for 12 mL is ±0.24 mL |
VIAL screw clear 1.5ml + CAP bakelite solid screw PTFE lined for 10mm vial | Jaytee Biosciences | JW41110 + JW43927 |
Capped vial used for validating accuracy and precision of dispensed solvent |
Crystal Structural Database | The Cambridge Crystallogra-phic Data Centre (CCDC) | Cambridge Structural Database (CSD) | Containing over 900,000 entries from x-ray and neutron diffraction analyses |
powder X-ray diffractometer | Panalytical | X-Pert PRO MPD | Equipped with an X’Celerator detector with Cu Kα radiation |
powder X-ray diffractometer data Collector software | Panalytical | X’Pert HighScore Plus v3.0 | solftware package used to adquire the PXRD data |
Rietveld refinement software including Scherrer equation | BRUKER | Version 6 of TOPAS-Academic | To prepare phase composition and crystal size from PXRD scans |
HPLC equipment | Agilent | HP1200 Series modular HPLC system | HPLC high pressure binary pump, autosampler, Peltier type column oven with 6 µL heat exchanger and Diode Array Detector with a semi-micro flow cell (1.6uL, 6mm pathlength). |
HPLC column | Agilent | 1.8mm Zorbax XDB C18, | (4.6mm ID × 50 mm length) |
Ball mill grinder | Retsch | MM400 | modified: replaced safety cover for external safety screen |
14 mL snap closure stainless steel jars | In house | manuctured from 316 stainless steel | |
14 mL screw closure stainless steel jars | In house | manuctured from 316 stainless steel – contains a PTFE washer |
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Stainless steel ball bearings: | Dejay Distribution Ltd | 7.0 mm (1.37g) | Stainless Steel Balls A.I.S.I. 420 Carbon (0.25/0.35%) & Chromium (12/14%) |
"Push a Button" software | Developed at Department of Chemistry | Written in Visual Basic. It activates an electronically controlled switch (relay). | |
"Push a Button" Solenoid | Magnet Schultz | Type 609RP 12 Volt DC |
609RP (RP stands for) R – for spring-return P – for push-rod |
"Push a Button" Solenoid holder |
Department of Chemistry | To hold solenoid over START button on the MM400 | |
"Push a Button" Relay | KM Tronic | USB one relay | USB Relay Controller – One Channel – HyperTerminal ASCII commands. Connection to a PC's USB port using VCP (Virtual COM port). |
re-usable adhesive putty | Bostik | Blu-Tack | Used to hold the jar fixed on the bench. |