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Feeder systems

Standard instrument control and pacing signals are generally acceptable for common feeder system operation. Volumetric and gravimetric feeders are usually adaptable to operation from any standard instrument signals. [Pg.95]

MSO is unsuited for treating materials with high inert content, such as asbestos, concrete, soils, and rubble. There is concern over emissions from MSO relating to particulate mercury content and radioactivity. MSO is inappropriate for wastes with high tritium levels. MSO pilot programs have encountered problems with carbon monoxide (CO) emissions. The corrosion of reactor materials by molten salt has remained a concern for the long-term operability of the system. The viscosity and volatility of the melt have to be controlled. There have been problems with material from the melt plugging air exhaust and feeder systems. [Pg.801]

Improved feeder system, scrubber system, and a new power supply to the torch for the PACT-6 (D104585, pp. 17-20). [Pg.876]

The compression zone is located on the back side of the equipment and employs a maximum load force limited by the type of tooling being used. It is of paramount importance to note that, if a load force is applied over the indicated limit, the press unit will not function properly, resulting in premature wear or possible damage to the tooling. The compression set comprises the hopper and feeder system, the die table, the upper and lower compression rollers, the upper and lower turrets, the excess-material scraper, the tablet stripper, the recirculation channel, and the aspiration system. [Pg.1143]

The hopper is usually made of stainless steel and has the shape of a funnel to contain and deliver the product to be compressed. It may be provided with a window for the observation of the product level and may also be provided with low-level sensors that signal an alarm, shut off the engine, or activate the feeding mechanism to deliver the product when it falls below this level. The feeder system usually consists of three sections (in the case of force feeders) and is ideal for press performance at high speed. The first section of a force feeder system is where the hopper is connected and is responsible for the flow of the product from the hopper to the next sections. The second section is where the die cavities are filled to their maximum capacities, and the third section is where the weight control adjustment takes place. These sections contain paddle systems which prevent packing of the product. The... [Pg.1143]

Draper R etal, 1987, High Thermal Conductivity Gas Feeder System. US Patent 4,664,986. [Pg.179]

Chlorine feeders. Chlorine feeders may be categorized as feeders for chlorine gas and feeders for hypochlorite solutions. Schematics of chlorine gas feeder systems are shown in Figures 17.5, 17.6, and 17.7, as well as a drawing of a hypochlorite feeder is shown in Figure 17.8. Hypochlorite feeders are also called hypochlorinators. [Pg.773]

Figure 17.5 is a chlorine gas feeder system that utilizes an evaporator. Evaporation of liqnid chlorine speeds up the dosing delivery process. When dosage rates exceed 680 kg/d, evaporators must be used. Lower dosage rates may also require the use of evaporators when space is limited. [Pg.773]

FIGURE 17.5 Schematic of chlorine feeder system using evaporators and tonne or larger containers. [Pg.773]

A schematic diagram of the process is shown in Figure 1. The feed was chopped to 5-10 cm in a forage harvester and air dried to less than 10% moisture content before use. The feeder system consisted of a funnel-shaped 0.2 m capacity hopper with chain-driven mixer arms, emptying onto a 5 cm diameter screw... [Pg.326]

The process occurring during compaction of particulate matter in roller presses is described and interpreted by different authors in a rather similar way. The feed mechanism is characterized by the pressure caused by gravity or a force feeder system and the friction between the material and roller surface. Compaction between two rolls may be explained by dividing the nip area into two zones the feed zone and the compaction zone. [Pg.263]

The screw feeder system requires testing and development. [Pg.218]

The robot cell layout was designed to minimize the total distance to be covered by the robot in order to assemble onto MID. In addition, the feeder system is movable. As a result, the components can be placed at an optimized position. With this feeder moving system, the placement rate can reach 1800 components/hr (with a stationary feeder the placement rate is up to 1200 components/hr). [Pg.436]

The metal yield is the ratio of the amount of metal melted to the weight of the finished good castings. Five main factors affect metal yield, i.e. quality requirement choice of mould-box size the extent of runner and feeder systems metal shrinkage scrap casting rate. [Pg.139]

The technique results in a minimisation of dust emissions from moulding and finishing, as compared to sand moulding. The emissions of VOC are eliminated as no gas is emitted for the inert ceramic mould. Additionally the amount of waste (dust, metal) is reduced. The reduction of feeder systems results in a higher 5deld of castings per melt. [Pg.202]

The transmission of normal electric power is by a dual feeder system, wherein a feeder is extended from each of the two 2400-volt substation bus sections to each of a number of site load centers. In addition to breaker protection at each end of the feeders, there is a breaker between the feeders at each load center to prevent circulatory power transmission. Thus each load center has in effect a two-section bus. Wherever economy of design and division of processes or facilities has permitted, dual power feed is carried onto.the load so that faulting of one part of the distribution system affects only part of a given load. [Pg.388]

British Materiais Handiing Board (1986) Guidelines for Specifying Weigh Feeder Systems (BMHB, Buckinghamshire, UK). [Pg.162]

All types of asphalt production plants consist of five distinct parts the cold aggregate feeder system, the dryer/heater, the dust collection system, the mixing system and the storage bins. The mixing system is basically the factor that determines their categorisation. [Pg.399]

Figure 40. Exauq)les of alternative Liquid Feeder Systems for overhead... Figure 40. Exauq)les of alternative Liquid Feeder Systems for overhead...
Figure 55. Example of a typical Mate feeder system. Figure 55. Example of a typical Mate feeder system.

See other pages where Feeder systems is mentioned: [Pg.140]    [Pg.605]    [Pg.79]    [Pg.1144]    [Pg.1144]    [Pg.19]    [Pg.511]    [Pg.193]    [Pg.201]    [Pg.274]    [Pg.70]    [Pg.67]    [Pg.270]    [Pg.215]    [Pg.121]    [Pg.150]    [Pg.35]    [Pg.385]    [Pg.280]    [Pg.58]    [Pg.186]    [Pg.193]    [Pg.194]    [Pg.199]    [Pg.273]    [Pg.273]    [Pg.273]    [Pg.307]   
See also in sourсe #XX -- [ Pg.58 ]




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