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Two-roll laboratory mill

In the case of thermal crosslinking, the corresponding curatives were added to each of the EPDM and CR rubbers on a two-roll laboratory mill at room temperature. A constant friction ratio of 1.2 was maintained between the milling rolls. Approximately 2 mm sheets were drawn out from the mill and cured in a hot press at a pressure of 10 MPa and a temperature of 170°C and 160°C for EPDM and CR, respectively, for their corresponding optimum cure time (f90). [Pg.264]

Sample Preparation. All polymer samples were prepared from commercial general purpose polystyrene (Monsanto HF-77). The additives were incorporated into the polymer by fluxing on a two-roll laboratory mill at about 350°F. Two types of samples were molded from the milled polymer (a) 50-mil plaques, compression molded at 350°F. (b) 1.5-2.5-mil films, compression molded at 390°F. [Pg.304]

As a general rule, most of the reagents were purified carefully (particularly for moisture), and all of the reactions carried out either using vacuum techniques or under pure argon atmosphere. Polymer properties were investigated by standard methods, unless otherwise mentioned. Polymer blending was usually performed for 5 minutes at 190°C on a C.A.M.I.L. two-roll laboratory mill. [Pg.324]

Sample preparation. All ingredients were mixed in an open two-roll laboratory mill at room temperature. The rotors operated at a speed ratio of 1 1.4. Rubber compounds were vulcanized in an electrically heated hydraulic press. The compounds were cured into 0.25 mm thick films at 150 °C for 15 min according to the optimum cure time ( 90) derived from the curing curves previously determined by means of a Rubber Process Analyzer (RPA2000 Alpha Technologies). Rectangularshaped specimens were mechanically cut out from the film samples. [Pg.58]

The compounding of CR with fillers and vulcanization ingredients was done by a laboratory size open two-roll mixing mill. All the weights are given in parts per hundred parts of rubber and the recipe for the CR compounds is given in Table 4. [Pg.101]

Compounding was performed in an open two-roll mixing mill (laboratory size). NR was first masticated on the two-roll mill for about 2 3 min followed by addition of the ingredients. Cure characteristics were analysed using an oscillating disk rheometer (Monsanto R-lOO) at a temperature of 150 °C. The composites were cured at their respective cure times in a hydraulic press under a pressure of about 120 bar at 150 °C. Aged samples were prepared by keeping the samples in a hot air oven at 70 °C for 7 days. ... [Pg.324]

In another study, it was reported that NR gum and CB filled compounds containing nano-ZnO have been prepared on a laboratory size two-roll mixing mill at a friction ratio of 1 1.25 as per ASTM D 3184-89 and the samples were... [Pg.366]

Rubber blends were prepared by means of a two-roll laboratory mixing mill. The vulcanization of rubber blends was carried out with the use of steel molds placed between the shelves of electrically heated hydraulic press. Samples were vulcanized at a temperature of 160 "C, under a pressure of 15 MPa for 30 min. [Pg.176]

Polyethylene can be compounded on any of the standard types of mixing equipment used for visco-elastic materials. For laboratory purposes a two-roll mill is suitable operating temperatures varying from about 90°C to about 140°C according to the type of polymer. On the industrial scale, compounding is undertaken either in internal mixers, or more particularly, extrusion compounders. [Pg.232]

The oldest technology involved in the elastomer blending and vulcanization process is essentially a temperature controlled two roll mill as well as internal mixers followed by an optimum degree of crosslinking in autoclave molds (compression, injection, etc.) in a batch process or in a continuous process such as continuously heated tube or radiated tubes. A few examples of laboratory scale preparation of special purpose elastomeric blends is cited here. [Pg.465]

Processes which melt mix polymer and filler are capable of generating the high shear stresses necessary to cause agglomerate break up, together with re-distribution of the primary filler particles. Since its conception in 1835, the two-roll mill has proved to be an effective means of mixing additives into plastics and rubber and is still in widespread use today, principally for laboratory purposes, but to some extent in large-scale industrial applications. [Pg.190]

Evidence of Interfacial Bonding. In these experiments compounded blends were composed of two elastomer phases that were first mixed with curative ingredients before blending in various ratios. This procedure was adapted to ensure proper initial distribution of the ingredients between the two phases. Blending was accomplished, with one exception, by mill mixing on a small laboratory two-roll mill. After blending, cured specimens in the form of small 0.025-inch thick pads were swollen in a common solvent to observe the over-all state of network... [Pg.85]

Figure 2. Cellulose synthesis by Rut-NG14 in a 6% cellulose fermentation. (Data from M. Mandels, U.S. Army Laboratories, Natick, Mass.) (O—O) Residual dry weight, (A—A) FP units/mh (42), ( — ) soluble protein, (A—A) mycelial protein. Substrate 6% two-roll milled cotton Mandels (42) basic salts medium without urea inoculum 20% v/v of a 3-day-old shake flask mycelium pH > 3, continuous addition of NH OH. Figure 2. Cellulose synthesis by Rut-NG14 in a 6% cellulose fermentation. (Data from M. Mandels, U.S. Army Laboratories, Natick, Mass.) (O—O) Residual dry weight, (A—A) FP units/mh (42), ( — ) soluble protein, (A—A) mycelial protein. Substrate 6% two-roll milled cotton Mandels (42) basic salts medium without urea inoculum 20% v/v of a 3-day-old shake flask mycelium pH > 3, continuous addition of NH OH.
Fig. 8.49 is another schematic representation, published by one of the manufacturers (CPM), showing the typical design of a pellet mill with cylindrical die and two internal press rollers. The execution suggested by Fig. 6.4b.5 (Chapter 6), 8.40, and 8.41 with one press roller is only used in laboratory and small production machines. For structural and process reasons, the perforated concave die can not be very wide (Fig. 8.50). Therefore, to increase the capacity of a given press and more uniformly distribute the forces acting on the ring, up to three rollers (see below. Fig. 8.52) are installed. With two rollers (Fig. 8.49) the capacity of a machine doubles as compared with a single roll pellet mill and triples with three rollers from a ring loading point of view, the latter also results in the best distribution of the pressing forces. Fig. 8.49 is another schematic representation, published by one of the manufacturers (CPM), showing the typical design of a pellet mill with cylindrical die and two internal press rollers. The execution suggested by Fig. 6.4b.5 (Chapter 6), 8.40, and 8.41 with one press roller is only used in laboratory and small production machines. For structural and process reasons, the perforated concave die can not be very wide (Fig. 8.50). Therefore, to increase the capacity of a given press and more uniformly distribute the forces acting on the ring, up to three rollers (see below. Fig. 8.52) are installed. With two rollers (Fig. 8.49) the capacity of a machine doubles as compared with a single roll pellet mill and triples with three rollers from a ring loading point of view, the latter also results in the best distribution of the pressing forces.
Da Costa et al. investigated the influences of rice husk ash loadings on the mechanical properties of NR composites. Table 19.3 shows the physical characterization of black rice husk ash (BRHA) and white rice husk ash (WRHA). The compounds were carried out using a laboratory-sized two-roll mill. [Pg.582]

Following the trend of using PVC as matrix, research on the use of EFB as composite in PVC matrix was also reported. Bakar et at [37] used the EFB as filler in unplasticized poly(vinyl chloride) (PVC-U). They studied the effects of extracted EFB on the processability, impact and flexural properties of EFB/PVC-U composites. PVC-U resin, EFB and other additives were first dry-blended using a heavy-duty laboratory mixer and then milled into sheets on a two-roll mill before being hot-pressed and cut into impact and flexural test specimens. There were two kinds of EFB used in this experiment, which were extracted and xmextracted. The FTIR showed that the unextracted EFB contained oil residue, while the extracted one contained less oil residue. The results showed that both extracted and unextracted EFB decreased the fusion time and melt viscosity. However, the fusion time increased with the increase of extracted EFB content. Meanwhile, there was no significant difference in both the impact and flexural properties of extracted and xmextracted EFB. [Pg.48]

Prep Mill, Laboratory two-roll mill, Brabender, C. W., Instruments, Inc. [Pg.929]

Color labs are outfitted with laboratory size equipment that simulates the larger machines used for production internally and by their customers. Typical processing equipment found in the lab are small extruders, two-roll mills, ban-burry mills, and media mills. Small rotational, injection and blow molding machines are used to duplicate the customers process. Instruments and computers are required for testing physical properties and color. Most labs have a computer-controlled color measuring system and a light booth to evaluate color. The spectrophotometer with computer is initially used to assist in colorant formulation and later as a quality control (QC) tool to provide certification of the quahty of match to standard. The light booth provides a standardized set of conditions to visually observe color and appearance. [Pg.1589]

Particle size in water and paraffin oil were measured with Zetasizemano S90 (Malvern Instruments). Cure characteristics were measured at 160°C using a Monsanto rheometer. The robber mixes were prepared on a laboratory two-roll mill at about 30°C, with roll dimensions of D = 200 mm and L - 450 mm. The rotational speed of a front roll (Vp) was 2s ... [Pg.147]

The rubbers were compounded according to the formulations described in Section 8.3.1.1, using a laboratory 15.2 cm two-roll mill. All masterbatches were masticated on a two-... [Pg.222]

As a result of these limitations, two-roll mills in the plastics industry tend to be used only for laboratory scale activities. The mill consists of a pair of contra-rotating rolls, the typical laboratory mill having rolls around 300 mm wide and 200 mm diameter. [Pg.18]

As it is very costly to run commercial scale equipment, initially the effects of a newly developed lubricant system on the properties of a rPVC compound are measured using laboratory scale equipment such as rheometers, dynamic two-roll mills and small scale molders and extruders. An example of the effect of various lubricants on output in a laboratory extruder is shown in Figure 2. [Pg.457]

In laboratory tests on a two-roll mill, compounding of LSFR additive was much easier than compounding of the other synergists because LSFR acted as a processing aid, providing external lubrication. [Pg.58]

On a laboratory scale, the small two-roll mill is the most convenient compounding equipment it was previously commonly used in industry, too. [Pg.862]


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See also in sourсe #XX -- [ Pg.260 ]




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