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Feed capacity

Filter selection, based on the feed capacity, m /h, to be handled, varies from 1 to 45 m /h in the many sizes available. A permanent magnetic filter is shown in Figure 11. [Pg.427]

Table No. Feed Feed size Feed capacity, tons/hr Speed, rpm Stroke, in Water with feed, gakmin Dressing water, gakmin Size of deck... Table No. Feed Feed size Feed capacity, tons/hr Speed, rpm Stroke, in Water with feed, gakmin Dressing water, gakmin Size of deck...
Feed capacity is limited by putting a given amount of feed (RHS) in a feed capacity tank. The other type of limit is that necessary to keep flows from accumulating or stacking in the middle of the plant in one of the intermediate tanks (rows). To inhibit this stacking, high prices are placed on any material accumulation. These are called slack prices (SPRICES). [Pg.347]

If 90% of the reactant A is converted to products in a reactor, and if one obtains a second reactor that is one half the size of the first, determine the increase in feed capacity that results from the following types of operation. [Pg.306]

After extensive research and several tests, the option selected was recycling hypochlorite to the feed brine of the electrolysis cells. For this purpose, hypochlorite feed pipes were manufactured and the hydrochloric acid feed capacity to the brine degassing tanks was enlarged. [Pg.192]

The second adsorbent characteristic is capacity. Capacity is defined as the quantity of desired component for example normal paraffins adsorbed from the feed while the adsorbent is exposed to the feed. Capacity is reported either as a weight or volume of the desired component retained by the adsorbent per volume or weight of adsorbent. It is desirable to have capacity values as great as physically practical. Capacity, just like selectivity, is measured using the pulse test apparatus. [Pg.251]

With the conversion to a mechanical feed system, they expect to double their tdf feed capacity and run 4 tons per hour. This should result in a considerable fuel cost savings, because they can obtain tdf for about 1 per million Btu, whereas they would otherwise be burning more coal which costs about 2 per million Btu. With the new configuration they could obtain 10 percent of their heating value from tdf, 10 percent from natural gas, and 80 percent from coal. Both their old and new configurations utilize 2-inch by 2-inch pieces of tdf. With the new capacity Arizona Portland could increase its capacity to over 3 million scrap tires per year. In 1990, Arizona Portland utilized approximately 1 million scrap tires (54). [Pg.63]

The feed capacity depends on the free screw volume (channel depth, number of threads), the pitch, the screw speed, and the bulk density of the product. The product can only be conveyed if there is friction between the product and the cylinder wall. [Pg.60]

An increase in the free cross-section and hence a 10 to 15% increase in the resulting maximum feed capacity is possible by using (non-self-wiping) pushing flight elements. [Pg.60]

For simple melt conveying, screw elements with a pitch of 1 D are commonly used. If other components are to be added, e.g., via a side feeder, the pitch should be 1.5 D in order to increase the feed capacity. [Pg.65]

Packings also offer easy trade-off between capacity and separatum. Going to smaller packings converts spare capacity in the tower into separation stages. Larger packings can overcome capacity bottlenecks at the expense of loss in separation. If both of these can be performed in different sections of the same column, and assuming no pinch neer the feed, capacity or separation or both can be improved with little... [Pg.518]

Economics The process is designed to function at a much higher level of conversion per pass. This high conversion minimizes the size of the BT columns, and the size of Tatoray process unit, as well as the utility consumption of all of these units. Estimated ISBL costs based on a unit processing feed capacity of 355,000 mtpy (US Gulf Coast site in 2003) ... [Pg.114]

This is a fluid-bed cracking process. It was first tested in 1990s. This pilot plant has a 400 tonne per year feed capacity, but runs continuously on a 50 Kg/h scale as it has limited product storage. The next steps in the development process to follow are optimization and scale-up. [Pg.367]

Anthony, K. R. N. (2000). Enhanced particle-feeding capacity of corals on turbid reefs (Great Barrier Reef, Australia). Coral Reefs. 19, 59-67. [Pg.976]

Designing of a commercial membrane system for feed capacity of 8 m /day of 10% NaSCN solution... [Pg.1113]

Feed capacity Feed concentration Feed pressure Feed temperature Number of stages Initial feed dilution ratio Subsequent dilution ratios Total feed quantity per stage Stage cut... [Pg.1120]

Optimized Five-Stage Process Scheme for Feed Capacity of 8 m /day (Second Cycle of Operation Onwards [Steady State])... [Pg.1121]


See other pages where Feed capacity is mentioned: [Pg.156]    [Pg.415]    [Pg.1226]    [Pg.994]    [Pg.82]    [Pg.298]    [Pg.156]    [Pg.415]    [Pg.306]    [Pg.591]    [Pg.734]    [Pg.163]    [Pg.188]    [Pg.200]    [Pg.576]    [Pg.30]    [Pg.79]    [Pg.381]    [Pg.1049]    [Pg.591]    [Pg.735]    [Pg.624]    [Pg.792]    [Pg.1113]    [Pg.1123]    [Pg.145]    [Pg.146]    [Pg.591]    [Pg.735]   
See also in sourсe #XX -- [ Pg.60 ]




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