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Recovery capacity

The C02 gas quality has significant impact on the capture cost by this technology, and uncertainties on the future regulatory requirements of C02 quality for its transport and storage has influence on the process configuration of the oxy-combustion plant, gas cleaning unit performance, overall C02 recovery capacity and on the energy requirements for C02 compression and purification. [Pg.88]

The advantage of either rope or belt skimmers is that they do not require significant operational attention. They can be left unattended (except for routine maintenance) for extended periods of time. Also, either unit can recover thin layers of floating product without sophisticated instrumentation. The primary disadvantage is that the recovery capacity is limited to a few hundred gallons per day per unit. Higher-viscosity oils attach more effectively to the oleophilic materials. Less-viscous products are recovered less effectively. [Pg.231]

Development and testing of these specialized sorbents is usually a lengthy process. The reaction must first be shown to proceed on the sorbent, in addition to recovery, capacity, and storage stability tests. The procedure for preparation of the sorbent must be shown to be consistent with several batches of prepared sorbent. [Pg.188]

Table I presents a refinery sulfur recovery capacity forecast made by the National Petroleum Council (NPC). The top portion of the table represents the initial conditions based on current crude input and refinery product slates the bottom indicates additional capacity required for each of three, non-additive, scenarios. As the NPC study shows that sulfur production, as a percent of capacity, in 1982 is expected to be 60% in district I, 54% in district II, 71% in district III, 72% in district IV, and 49% in district V... Table I presents a refinery sulfur recovery capacity forecast made by the National Petroleum Council (NPC). The top portion of the table represents the initial conditions based on current crude input and refinery product slates the bottom indicates additional capacity required for each of three, non-additive, scenarios. As the NPC study shows that sulfur production, as a percent of capacity, in 1982 is expected to be 60% in district I, 54% in district II, 71% in district III, 72% in district IV, and 49% in district V...
Source control is most effective for TTD and MNT. TTD has been usurped to minimize human impact on the environment. Its mediocre effect is obliterated by associated secondary pollution and consumption rise. Net damage to the environment still exceeds nature s recovery capacity [31-33]. Using TDBT to meet climbing material demand rendered further environmental damage inevitable and sustainability impossible. MNT s revolutionary production processes promise eventual total elimination of all pollution sources, not to mention control, treatment or abatement. [Pg.215]

Economy is a very complex issue. In commercial production the time to market can override issues such as optimisation for recovery, capacity or speed. Robustness and reliability are also of great concern since a batch failure can have major consequences. [Pg.14]

As noted previously, flue gas is the largest potential source of CO2. However, recovery costs must be sufficiently low to allow for acceptable end product values. The recovery of CO2 from flue gases is accomplished with aqueous solutions of MEA. An analysis of the cost of proprietary technologies for recovery of a CO2 generation plant with a CO2 recovery capacity of 1000 tons/day reveal a net cost of producing CO2 to be... [Pg.6]

Nevertheless, the assumptions were conservative in the sense that the predictions based on them likely represent an upper limit for the impact on the lead-acid battery recycling industry. The mass of lead in scrap EV batteries is projected to increase as shown in Figure 9, reaching about 16,000 metric tons in 2005. This can be compared to Figure 10, which shows the amount of lead from battery scrap and the total amount of lead recovered from scrap in the U.S. through the year 1995 from U.S. Bureau of Mines data. Total secondary lead is nearing IM metric tons per year. The predicted EV battery lead mass in 2005 is only about 1.5% of the secondary lead recovery capacity in 1996 and will actually be less than that in 2005 once the future growth in secondary lead recovery is included. Clearly EV battery waste will remain a very small portion of secondary lead production well beyond 2005. [Pg.312]

Fig. 10. Lead from Battery Scrap, Total Lead Scrap, Secondary Lead Recovery Capacity, and Lead Scrap Export in the U.S. Fig. 10. Lead from Battery Scrap, Total Lead Scrap, Secondary Lead Recovery Capacity, and Lead Scrap Export in the U.S.
Normal Recovery Capacity - A characteristic appiied to domestic water heaters that is the amount of gailons raised 100 degrees Fahrenheit per hour (or minute) under a specified thermal efficiency. [Pg.384]

The ammonia-recovery MGA installation is designed for ammonia-removal efficiencies >99%. That this goal has been met is clear from Figure 4.13, which shows the ammonia-removal efficiency as a function of the air flow rate through the MGA installation. The MGA installation has an ammonia-recovery capacity of 83 tonnes/year. [Pg.67]

Solvents are recovered by distillation in four rectification and stripping columns with a total recovery capacity of 700 litres per hour and a range of 12-27 theoretical plates. Rhodium is recovered by a process which has been patented, and returned to the original manufacturer for refining and transformation into catalyst quality. Some 80% rhodium is recovered. Triphenyl phosphine is recovered as its oxide and can be reconverted for reuse. [Pg.46]

The use of oxygen-enriched air and the partial bypassing of the first stage condenser and reheat exchanger resulted in a combined capacity increase of 24%. However, these two operating parameters were only used during periods of limited sulfur recovery capacity. [Pg.341]

The average reduction approximated 0.5 mol% which represented a 5% gain of sulfur recovery capacity. [Pg.342]

Reducing the water vapor content of acid gas to a minimum also increased Claus capacity. During periods when one of the two sulfur trains was out of service, the amine regenerator reflux drum temperature was reduced from 135°F to 110 F. This was achieved by spraying treated water on the exterior of the amine regenerators overhead fin fan tube bundles. This reduced the water content of the acid gas from 10% to 5% and thus increased sulfur recovery capacity by 2%. [Pg.342]

The fuel and electricity are used to power large pieces of equipment with the capacity to transform and transfer a lot of energy to do a great deal of work. When this energy is misdirected, it can harm people and equipment. As any emergency room physician can attest, the human body has marvelous recovery capacity. The troublesome tradeoff is that it is easy to injure the human body. For example, it only takes 5 seconds of exposure for water at 140°F to cause a full thickness bum to adult skin (Withers 1984). If the bum area is relatively small, full recovery is a reasonable expectation. [Pg.44]


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See also in sourсe #XX -- [ Pg.75 ]




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