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Electric energy, costs

A.nnual energy and fuel costs electric energy costs chiller or compressor pumps chilled water heating water condenser or tower water weE water... [Pg.363]

Because the peroxodisulfate salts are all made electrochemicaHy, the electrical energy cost is a significant part of thek manufacturing cost. The 1994 world capacity for peroxodisulfate salts was about 75,000 metric tons, valued at about 30 x 10 . The principal appHcations are in polymerization catalysis and the market broadly tracks the plastics business. The Caro s acid business is difficult to quantify because the product itself is not commercial but made on-site from purchased hydrogen peroxide. [Pg.99]

Since the electric energy cost is 0.04/kWhr, then... [Pg.33]

The operating cost for air compression is basically the electric utility needed ftir ihe isentropic compression. Electric energy needed to compress air may be calculated using Eq. (2.29). The isentropic efficiency of the compressor is taken as 60% and the electric energy cost is 0.06/kWhr,... [Pg.40]

Barlow, S., Reducing Electrical Energy Costs for Extrusion Processes, SPE ANTEC Tech. Papers, 55, 1157 (2009)... [Pg.475]

Take a careful look at your next electric bill. Note that you " pay for electrical energy in units of kilowatt-hours. A kilowatt-hour (kWh) is the amount of energy consumed in 1 hour at a rate of 1 kilowatt (1000 joules per second). Therefore, if electrical energy costs 15 cents per kilowatt-hour, a lightbult that has a power rating of 100 watts (0.1 kilowatt) can be run for 10 hours at a cost of 15 cents. [Pg.639]

Anions. Predominantly chloride Electrical energy cost. 1.0 cent/kw.-hr. [Pg.247]

Moreover, the performance of the two-compartment cell can be enhanced by the introduction of a third chamber. For example, the multichamber cation cell now uses two CEMs [23]. In operation the salt solution is first fed to the chamber between the two CEMs and then passes to the acid compartment. This gives a salt/acid stream with a higher concentration of acid than the standard two-compartment cell. The multichamber anion cell is used in a similar way to that of the cation cell. Clearly, this multicell arrangement incurs a greater electrical energy cost due to the higher cell voltage than that needed in the two-compartment cell. [Pg.588]

Annual Electric Energy Cost Final Tube Thickness m Weight kg Fixed Cost Annualized Cost hr W/m K T °C... [Pg.861]

Figure 10-6. Electric energy cost of syngas production as function of [0] [C] ratio. Figure 10-6. Electric energy cost of syngas production as function of [0] [C] ratio.
Figure 10-12. Energy cost of the plasma-chemical pyrolysis of methane as a function of the specific plasma energy input upper curve, total energy cost of the process with respect to the total produced hydrogen lower curve, electrical energy cost with respect to additional hydrogen produced by the discharge. Figure 10-12. Energy cost of the plasma-chemical pyrolysis of methane as a function of the specific plasma energy input upper curve, total energy cost of the process with respect to the total produced hydrogen lower curve, electrical energy cost with respect to additional hydrogen produced by the discharge.
Figure 10-14. Plasma (electric) energy cost of syngas production during plasma conversion of kerosene as function of specific energy input in the system (1) partial oxidation (2) steam-oxygen conversion with preheating of air (3) steam-oxygen conversion with excess water, (4) steam-conversion in low-temperature regime (5) steam conversion in high temperature regime. Figure 10-14. Plasma (electric) energy cost of syngas production during plasma conversion of kerosene as function of specific energy input in the system (1) partial oxidation (2) steam-oxygen conversion with preheating of air (3) steam-oxygen conversion with excess water, (4) steam-conversion in low-temperature regime (5) steam conversion in high temperature regime.
Electric energy cost is one of the cracial factors characterizing the plasma treatment HVLC VOC exhausts. To analyze the energy cost of VOC treatment in non-thermal plasma, we should point out that the mechanism of plasma oxidation of hydrocarbons can be generally... [Pg.830]

For this optimal removal with the application of both conditioning liquids, the energy consumption was calculated to be 28.4kWh/m of mixed contaminated soil. Assuming in Canadian dollar (CAD) that CAD 0.03/kWh is the unitary cost, the electrical energy cost for soil remediation would be CAD 0.85 perm The lowest energy cost (beside control cell) of CAD 0.65/m was observed when a surfactant... [Pg.327]

As a purely indicative example, an electrolysis plant based on three-compartment cells is considered, having a capacity of3000 t/a of sodium sulfate (100 % basis) fed to the cells as a 20 % solution The investment for a doubleeffect evaporation unit represents about 10-15% of the total investment for the complete plant, comprising cells, rectifier, pretreatment unit, evaporation, and construction. The cost of steam amounts to about 50% of the total electric energy cost. [Pg.150]

Thermal and electrical energy costs are reduced by over 90% by the efficient use of natural gas and the production of a small amount of electricity used elsewhere in the plant. [Pg.345]


See other pages where Electric energy, costs is mentioned: [Pg.364]    [Pg.422]    [Pg.117]    [Pg.29]    [Pg.391]    [Pg.28]    [Pg.155]    [Pg.350]    [Pg.256]    [Pg.54]    [Pg.33]    [Pg.267]    [Pg.364]    [Pg.745]    [Pg.224]    [Pg.548]    [Pg.858]    [Pg.364]    [Pg.25]    [Pg.176]    [Pg.178]    [Pg.54]    [Pg.10]    [Pg.681]    [Pg.682]    [Pg.698]    [Pg.698]    [Pg.845]    [Pg.151]    [Pg.152]    [Pg.83]   
See also in sourсe #XX -- [ Pg.175 ]




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