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Battery simulation

Pearson M. Ballard Power Systems. Power supply and ultracapacitor based battery simulator. US patent 2004/228055. [Pg.467]

E. Barsoukov, J. H. Kim, C. O. Yoon, and H. Lee [1999b] Universal Battery Parameterization to Yield a Non-Linear Equivalent Circuit Valid for Battery Simulation at Arbitrary Load, Power Sources 83, 61-70. [Pg.544]

Figure 25.5 Different mathematical models for lithium-ion battery simulations. Figure 25.5 Different mathematical models for lithium-ion battery simulations.
Funding for this work from ORNL LDRD Predictive Battery Simulation Project is gratefully acknowledged. Discussions with Drs. Jagjit Nanda, Claus Daniel, Jack Wells, and Prof. Egwu Kalu are greatly appreciated. [Pg.870]

The actual flotation phenomenon occurs in flotation cells usually arranged in batteries (12) and in industrial plants and individual cells can be any size from a few to 30 m in volume. Column cells have become popular, particularly in the separation of very fine particles in the minerals industry and coUoidal precipitates in environmental appHcations. Such cells can vary from 3 to 9 m in height and have circular or rectangular cross sections of 0.3 to 1.5 m wide. They essentially simulate a number of conventional cells stacked up on top of one another (Fig. 3). Microbubble flotation is a variant of column flotation, where gas bubbles are consistently in the range of 10—50 p.m. [Pg.41]

Fig. 8. Effect of temperature on relative discharge performance of a fresh "D"-si2e battery for service on simulated ratio use, 25- Q 4-h/d test for (a) an alkaline—manganese battery undergoing 260 h of service, and (b) a carbon—2inc battery undergoing 70 h of service (22). Fig. 8. Effect of temperature on relative discharge performance of a fresh "D"-si2e battery for service on simulated ratio use, 25- Q 4-h/d test for (a) an alkaline—manganese battery undergoing 260 h of service, and (b) a carbon—2inc battery undergoing 70 h of service (22).
A. L. Almerini and S. J. Bartosh, "Simulated Field Tests on Zinc—Air Batteries," Proceedings of the 26th Power Sources Symposium, Adantic City, N.J.,... [Pg.569]

The Na—S system is expected to provide significant iacreases ia energy density for sateUite battery systems (69). In-house testing of Na—S cells designed to simulate midaltitude (MAO) and geosynchronous orbits (GEO) demonstrated over 6450 and over 1400 cycles, respectively. [Pg.586]

Viscosities and specific weights of complexes and the corresponding aqueous phases, with the aim of simulating realistic battery conditions with MEP MEM ratio of 1 1, 3 1 and 6 1 in the electrolyte at 50, 75 and 100% states of charge, were studied in a temperature range between 10 and 50 °C [83], Kinematic viscosities between 5 10 6 and 30 -10 6 m2s of the complex phases were found. MEP-rich ones. [Pg.187]

Research and development into polymer electrolyte battery systems continues, yet many unsolved and controversial issues, particularly relating to the inadequate understanding and control of ion dissociation and the relative mobilities of the ions, remain. Modem computational resources now allow the structures of complex systems such as polymer electrolytes to be simulated and evaluated. Computer simu-... [Pg.520]

The simulated short-circuit test was developed to characterize the response of the separator to a short circuit without the complications of battery electrodes. The separator was spirally wound between lithium foils and placed in an AA-size can. To avoid lithium dendrite formation, an alternating voltage was applied to the cell. The cell current and can temperature were monitored. Figure 6 shows the behavior of Celgard membranes. [Pg.561]

Petard simulating the fire of a battery, used in order to deceive the enemy about the location of gun batteries. Most of these petards consisted of charges of rifle powder enclosed in wood or cardboard boxes, reinforced with cord or wire... [Pg.696]

A question of practical interest is the amount of electrolyte adsorbed into nanostructures and how this depends on various surface and solution parameters. The equilibrium concentration of ions inside porous structures will affect the applications, such as ion exchange resins and membranes, containment of nuclear wastes [67], and battery materials [68]. Experimental studies of electrosorption studies on a single planar electrode were reported [69]. Studies on porous structures are difficult, since most structures are ill defined with a wide distribution of pore sizes and surface charges. Only rough estimates of the average number of fixed charges and pore sizes were reported [70-73]. Molecular simulations of nonelectrolyte adsorption into nanopores were widely reported [58]. The confinement effect can lead to abnormalities of lowered critical points and compressed two-phase envelope [74]. [Pg.632]

This capacity limit for a given cell size has been determined as a result of computer simulation by GP Battery Technologies, as referenced from J. Fan and D. Magnuson, in Rechargeable Lithium Batteries K.M. Abraham, E.S. Takeuchi, M. Doyle eds., PV 2000-21, the Electrochemical Proceedings Series, Pennington, NJ (2000). [Pg.309]

Leaching of chemicals from complex materials or matrices is a complicated phenomenon in which many factors may influence the release of the specific organic compounds and inorganic ions. Important factors include major element chemistry, pH, redox, complexation, liquid to solid ratio, contact time, and biological activity. To describe fully the leaching of SWMs/COMs under field conditions, a battery of leaching tests was specifically designed to simulate various physical and chemical release mechanisms. [Pg.221]

NN applications, perhaps more important, is process control. Processes that are poorly understood or ill defined can hardly be simulated by empirical methods. The problem of particular importance for this review is the use of NN in chemical engineering to model nonlinear steady-state solvent extraction processes in extraction columns [112] or in batteries of counter-current mixer-settlers [113]. It has been shown on the example of zirconium/ hafnium separation that the knowledge acquired by the network in the learning process may be used for accurate prediction of the response of dependent process variables to a change of the independent variables in the extraction plant. If implemented in the real process, the NN would alert the operator to deviations from the nominal values and would predict the expected value if no corrective action was taken. As a processing time of a trained NN is short, less than a second, the NN can be used as a real-time sensor [113]. [Pg.706]

The useful life of a practical primary battery is determined principally by the nature of its discharge pattern. Thus the best way of assessing a system for some particular application is to subject it to a discharge which simulates the service conditions. Tests have therefore been developed which recognize the principal function of various types of battery and specify the generation of intermittent or continuous currents of appropriate levels. Such procedures have been standardized for batteries of uniform size and cell configuration by bodies such as the International Electrotechnical Commission (IEC) and the American National Standards Institute (ANSI). New test routines are continually being devised to keep pace... [Pg.60]

Zebra batteries have been subjected to a series of tests to demonstrate their ruggedness and safety. These include overcharge, short circuit, overheating and vibration and shock. Drop testing to simulate the effect of a... [Pg.271]

Figure 14.3. Representation of countercurrent extraction batteries, (a) A battery of mixers and settlers (or separators), (b) Schematic of a three-stage countercurrent battery, (c) Simulation of the performance of a three-stage continuous countercurrent extraction battery with a series of batch extractions in separatory funnels which are designated by circles on the sketch. The numbers in the circles are those of the stages. Constant amounts of feed F and solvent S are mixed at the indicated points. As the number of operations is increased horizontally, the terminal compositions Et and R3 approach asymptotically the values obtained in continuous countercurrent extraction (Treybal, 1963, p. 360). Figure 14.3. Representation of countercurrent extraction batteries, (a) A battery of mixers and settlers (or separators), (b) Schematic of a three-stage countercurrent battery, (c) Simulation of the performance of a three-stage continuous countercurrent extraction battery with a series of batch extractions in separatory funnels which are designated by circles on the sketch. The numbers in the circles are those of the stages. Constant amounts of feed F and solvent S are mixed at the indicated points. As the number of operations is increased horizontally, the terminal compositions Et and R3 approach asymptotically the values obtained in continuous countercurrent extraction (Treybal, 1963, p. 360).
Another application for silver-cadmium batteries is propulsion power for submarine simulator-target drones,... [Pg.188]


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See also in sourсe #XX -- [ Pg.789 , Pg.790 ]




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