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Ball-mill oscillation

The second class of grinding equipment is used to prepare dispersions. Typical of this class are ball and pebble mills, ultrasonic mills, and attrition mills. Solids, eg, sulfur, antioxidants, accelerators, and zinc oxide, are generally ground on this equipment (see Size reduction). Ball mill action is assisted in some mills by a combination of dispersion circulation by an external pump and mechanical oscillation of an otherwise fixed nonrotary mill chamber. Where ball mill chambers are rotated it is necessary to experimentally establish an optimum speed of rotation, the size and weight of the ball charge, and ensure the mills do not overheat during the grinding period. [Pg.257]

Oscillating ball mill (MM200 Retsch) with adapter for 2-mL vials. [Pg.207]

Transfer approximately 1 g of a VPG gained by one of the above protocols into a 2mL vial, add 3-5 glass beads (0 1-2 mm) and lOOpL of aqueous medium, e.g. 40 mM phosphate buffer (pH 7.4). Close the vial tightly and set it on an oscillating ball mill. Agitate at maximum speed for 2-3 min. [Pg.210]

Sub-micron milling is not widely used for contaminated soils however, semi-quantitative determination of asbestos may necessitate milling to submicron level. Micronising mills and other ultra-high energy centrifugal, oscillating ball mills or air jet mills are often used for this purpose. [Pg.48]

Figure 7.26 shows the temperature dependence of ESR spectra of PE chain end type of propagating radical tethered to a PTFE surface [27]. The radicals were produced by ball-milling of PTFE with a large amount of ethylene monomer. The dotted spectra at 15 and 30 K were calculated using the site exchange rates of 10 and 56 MHz, respectively. The spectrum observed at 95 K could be simulated by the rotation of the chain end about the chain axis along with the site exchange motion. The oscillation amplitude was also estimated from the values of SPLIT A and B, shown in Fig. 7.26. The ESR spectra of the end type of scission radicals produced by the mechanical fracture of PE were also simulated by the site exchange model between the sites 1 and 2 as described in Fig. 7.50 (in Appendix A7.1). The reason... Figure 7.26 shows the temperature dependence of ESR spectra of PE chain end type of propagating radical tethered to a PTFE surface [27]. The radicals were produced by ball-milling of PTFE with a large amount of ethylene monomer. The dotted spectra at 15 and 30 K were calculated using the site exchange rates of 10 and 56 MHz, respectively. The spectrum observed at 95 K could be simulated by the rotation of the chain end about the chain axis along with the site exchange motion. The oscillation amplitude was also estimated from the values of SPLIT A and B, shown in Fig. 7.26. The ESR spectra of the end type of scission radicals produced by the mechanical fracture of PE were also simulated by the site exchange model between the sites 1 and 2 as described in Fig. 7.50 (in Appendix A7.1). The reason...
Oscillating ball mill, model MM400 (Retsch, Haan, Germany) with steel balls (5-mm diameter)... [Pg.543]

Vibro-energy Mill. Trade-name a VIBRATING BALL MILL (q.v.) designed to oscillate both horizontally and vertically, the vertical motion being of small but sufficient amplitude to prevent the charge from becoming tightly packed. [Pg.346]

Each ground mixture of LOR and P-CD (LOR/P-CD) or LOR and HP-P-CD (LOR/HP-P-CD) with a 1 1 molar ratio was respectively prepared in an oscillatory ball mill (Mixer Mill MM301, Retsch GmbH Co., Germany) with 15 Hz oscillation frequency. About 0.2 g of powder sample was placed in a 25 ml volume stainless steel milling jar containing two 15 mm diameter stainless steel balls, and then oscillated. In the grinding process, the sample was withdrawn at the prescribed intervals for further examination (Lin et al, 2010). [Pg.318]

This review contains an important section about the optimization of mechanochemical reactions. The following parameters were examined (1) type of ball mill (2) rotation/oscillation frequency (v ,t/Vos<) (3) reaction time = milling time (t) (4) type of milling material (density, Qmb) (5) size of milling balls (djviB) number of milling balls (umb). and (6) mode of operation (continuous, cycled). [Pg.135]

The amount of material may range between 25 and 100 mg for a single sample however, it should be noted that (1) a bigger sample is easier to deal with and (2) the volume of solvent used for extraction has to be adjusted accordingly. Homogenization of the plant material should be performed after the addition of steel balls (two per Eppendorf tube) in the oscillating mill (e.g., in Retsch mill MM series). [Pg.543]


See other pages where Ball-mill oscillation is mentioned: [Pg.1840]    [Pg.1850]    [Pg.32]    [Pg.43]    [Pg.257]    [Pg.349]    [Pg.243]    [Pg.32]    [Pg.43]    [Pg.416]    [Pg.348]    [Pg.1599]    [Pg.349]    [Pg.274]    [Pg.2305]    [Pg.171]    [Pg.2288]    [Pg.1844]    [Pg.63]    [Pg.14]    [Pg.220]    [Pg.133]    [Pg.2457]    [Pg.1844]    [Pg.364]    [Pg.1603]    [Pg.1609]    [Pg.50]    [Pg.1848]    [Pg.454]    [Pg.4291]    [Pg.4292]   
See also in sourсe #XX -- [ Pg.20 , Pg.21 , Pg.22 , Pg.23 , Pg.24 , Pg.25 , Pg.26 , Pg.27 , Pg.28 , Pg.29 , Pg.30 , Pg.31 ]




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