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Standardization of batteries

With this step toward a reasonable standardization of batteries two substantially important aspects for future developments have come into close range ... [Pg.136]

The following committees are in charge of standardization of batteries, that is secondary batteries (accumulators) and primary batteries (dry batteries) at the DKE ... [Pg.363]

The standardization of batteries started in 1912, when a committee of the American Electrochemical Society recommended standard methods of testing dry cells. This eventually led to the first national publication in 1919 issued as an appendix to a circular from the National Bureau of Standards. It further evolved into the present American National Standards Institute (ANSI) Accredited Standards Committee CIS on Portable Cells and Batteries. Since then, other professional societies have developed battery related standards. Many battery standards were also issued by international, national, military, and federal organizations. Manufacturers associations, trade associations, and individual manufacturers have published standards as well. Related application standards, published by the Underwriters Laboratories, the International Electrotechnical Commission, and other organizations that cover battery-operated equipment may also be of interest. [Pg.96]

Fig. 2. Standard potentials of battery (a) negative electrode and (b) positive electrode reactions (13). Potentials are given in volts. Fig. 2. Standard potentials of battery (a) negative electrode and (b) positive electrode reactions (13). Potentials are given in volts.
In Figure 1, the cutaway view of the automotive battery shows the components used in its constmction. An industrial motive power battery, shown in Figure 2 (2), is the type used for lift tmcks, trains, and mine haulage. Both types of batteries have the standard free electrolyte systems and operate only in the vertical position. Although a tubular positive lead—acid battery is shown for industrial appHcations, the dat plate battery constmction (Fig. 1) is also used in a comparable size. [Pg.570]

The main converter, which is located downstream of the EHC, heats to functional temperature much more quickly because of catalytic combustion of exhaust gases that would otherwise pass unconverted through the catalyst during the cold start period. The EHC theoretical power required for a reference case (161) was 1600 watts to heat an EHC to 400°C in 15 s in order to initiate the catalytic reactions and obtain the resultant exotherm of the chemical energy contained in the exhaust. Demonstrations have been made of energy requirements of 15—20 Wh and 2 to 3 kW of power (160,161). Such systems have achieved nonmethane HC emissions below the California ULEV standard of 0.025 g/km. The principal issues of the EHC are system durabihty, battery life, system complexity, and cost (137,162—168). [Pg.494]

Cold crank performance, battery life expectancy, and freedom from maintenance are generally co-affected by the separators, whereas ampere-hour capacity remains largely unaffected at a given separator thickness. The properties of the different leaf and pocket separators are compared in Table 10. These typical separator properties (lines 1-4) are reflected in the electrical results of battery tests (lines 5-8). The data presented here are based on the 12 V starter battery standard DIN 43 539-02 tests based on other standards lead to similar results. [Pg.269]

A standard UPS battery system is capable of running the cooler, allowing us to prepare unexpected electric power failure or to carry the system to a place without power supply. [Pg.377]

The main characteristics of cylindrical AAA size metal-air batteries with PANI/TEG catalysts, as well as standard Zn-Mn02 battery have been gathered in the Table 5. Realization of all types of batteries in the same AAA size gives the possibilities for comparison of above electrochemical systems for some applications. [Pg.123]

STANDARDIZATION OF ANTIGEN RETRIEVAL TECHNIQUES BASED ON THE TEST BATTERY APPROACH... [Pg.3]

Standardization of AR technique should be based on the test battery principle. Achieving the maximal retrieval level of IffC staining intensity is a guideline for standardization. [Pg.20]

Figure 5.1 Diagrammatic explanation of standardization of IHC via AR and test battery to achieve a maximal retrieval level by an optimal protocol of AR. The intensity of IHC (axis y) is inversely correlated with the time of formalin fixation (axis x) as indicated by a reduced slope. Three arrows indicate a potential maximal retrieval level that may equalize the intensity of IHC to a comparable result for routinely processed, paraffin-embedded tissues with various time of fixation. Reproduced with permission from Shi et alHistotechnol. 1999 22 177-192. Figure 5.1 Diagrammatic explanation of standardization of IHC via AR and test battery to achieve a maximal retrieval level by an optimal protocol of AR. The intensity of IHC (axis y) is inversely correlated with the time of formalin fixation (axis x) as indicated by a reduced slope. Three arrows indicate a potential maximal retrieval level that may equalize the intensity of IHC to a comparable result for routinely processed, paraffin-embedded tissues with various time of fixation. Reproduced with permission from Shi et alHistotechnol. 1999 22 177-192.
Additional laser diode technologies recently reported include a continuous-wave rhodamine 700 dye laser with a maximum wavelength output at 758 nm, powered by two laser diodes each operated with two standard AA batteries (RDT E division of the US Naval Command, Control, and Ocean Surveillance Center, San Diego, California), and a tunable laser diode with output laser wavelengths of 650, 780, 850, and 1320 nm (New Focus, Mountain View, California). [Pg.191]

Under Guideline S2B, the following standard test battery is recommended (1) a test for gene mutation in bacteria, (2) an in vitro test with cytogenetic evaluation of chromosomal damage with mammalian cells or an in vitro mouse lymphoma thymidine kinase (TK) assay, and (3) an in vivo test for chromosomal damage using rodent hematopoietic cells. [Pg.306]

A calculation of the power requirements of the smart dust mote underscores our point that the present generation of batteries cannot effectively power this device. Thin-film batteries are among the most advanced of the lithium battery systems, with a capability to scale down to dimensions on the same order of magnitude as the cubic millimeter of the dust mote. 3 The energy density for the thin-film system is 2 J mm , which matches or exceeds standard lithium ion systems, such as those that power laptop computers. A key design requirement for the smart dust mote is that the power consumption cannot exceed 10 juW. If the dust mote uses this power continuously over a day, it will consume 1 J. [Pg.226]

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]

Anhydrous perchloric acid is not sold commercially, Aqueous solutions of perchloric acid are sold at low concentrations foi analytical standard applications and at concentrations up to 70%. The price for 70% perchloric acid varies and starts at 2.70/kg, depending on the quantity and level of impurities. The U.S. domestic capacity of ammonium perchlorate is roughly estimated at 31,250 t/yr. The actual production vanes, based on the requirements for solid propellants. Environmental effects of the decomposition products, which result from using solid rocket motors based on ammonium perchlorate-containing propellants, are expected to keep increasing public pressure until consumption is reduced and alternatives are developed. Approximately 450 t/yr of NH+ClCXt-equivalent cell liquor is sold to produce magnesium and lithium perchlorate for use in the production of batteries. [Pg.1223]

Thus far, quality objectives for chemical substances are derived from the most sensitive organisms in acute and chronic toxicity test batteries that determine NOEC values for different trophic levels. The pT-method similarly determines specific sample dilution levels that are devoid of adverse effects toward (micro)organisms of a standardized test battery. Common to both approaches is the more frequent use of water-column test organisms as opposed to benthic-dwelling organism that reflect more intimate contact with sediment. This practice is primarily based on the fact that standardized bioassays capable of appraising sediment porewaters and elutriates are presently more numerous than solid-phase tests for whole-sediment assessment. As more of these latter tests become developed and standardized (see Chapters 12 and 13, volume 1 of this book on amphipod and chironomid tests), their more frequent use will contribute to a better understand of the toxic effects of sediment-bound contaminants. [Pg.298]

Suppose a battery-powered device requires a minimum voltage of 9.0 V to run. How many lead-acid cells would be needed to run the device (Remember that a standard automobile battery contains six lead-acid cells connected in one package.) The overall reaction of a lead-acid cell is... [Pg.34]

The manufacturing process for biomolecules intended for therapeutic use must include extensive quality control measures to insure the production of a safe and effective product which meets rigorous standards of quality and batch-to-batch consistency. While this requirement applies to both small molecules and proteins, the manufacturing and structural complexity of proteins dictates the use of a much more extensive battery of analytical tests, many of which are quite complex and not routinely conducted in conventional analytical laboratories. [Pg.113]

In modem commercial lithium-ion batteries, a variety of graphite powder and fibers, as well as carbon black, can be found as conductive additive in the positive electrode. Due to the variety of different battery formulations and chemistries which are applied, so far no standardization of materials has occurred. Every individual active electrode material and electrode formulation imposes special requirements on the conductive additive for an optimum battery performance. In addition, varying battery manufacturing processes implement differences in the electrode formulations. In this context, it is noteworthy that electrodes of lithium-ion batteries with a gelled or polymer electrolyte require the use of carbon black to attach the electrolyte to the active electrode materials.49-54 In the following, the characteristic material and battery-related properties of graphite, carbon black, and other specific carbon conductive additives are described. [Pg.269]


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See also in sourсe #XX -- [ Pg.2 , Pg.3 , Pg.4 , Pg.22 ]




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Batteries standardization

STANDARDIZATION OF ANTIGEN RETRIEVAL TECHNIQUES BASED ON THE TEST BATTERY APPROACH

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