Saft SBL Скачать руководство пользователя страница 23

22

8.4

Charge efficiency

The charge efficiency of the battery is
dependent on the state of charge 
of the battery and the temperature.
For much of its charge profile, it 
is recharged at a high level of
efficiency.

In general, at states of charge less
than 80 % the charge efficiency
remains high, but as the battery
approaches a fully charged condition,
the charging efficiency falls off. This is
illustrated graphically in Figure 7.

8.5

Temperature effects

As the temperature increases, 
the electrochemical behavior becomes
more active, and so, for the same
floating voltage, the current increases.
As the temperature is reduced then
the reverse occurs. Increasing the
current increases the water loss, and
reducing the current creates the risk
that the cell will not be sufficiently
charged. Thus, as it is clearly
advantageous to maintain the same
current through the cell, it is necessary
to modify the floating voltage as the

temperature changes. The
recommended change in voltage
required, or “temperature
compensation”, is -3 mV/ °C, starting
from an ambient temperature of 
+ 20°C to + 25°C.

8.6

Commissioning charge

It is recommended that a good first
charge should be given to the battery.
This is a once, only operation, and is
essential to prepare the battery for its
long service life. It is also important
for discharged and empty cells which
have been filled, as they will be in 
a totally discharged state.

A constant current first charge is
preferable and this should be such 
as to supply 300 % of the rated
capacity of the cell. Thus, a 250 Ah
cell will require 750 ampere hours
input, e.g. 50 amperes for 15 hours.

Cells which have been stored for less
than one year should be charged for
15 hours at the recommended charge
current* before being placed in
service.

Cells that have been stored for more
than one year, or have been supplied
empty and have been filled, should
be charged for 15 hours at the
recommended charge current *
discharged to 1.0 volts per cell and
then charged for 10 hours at the
recommended charge current*. 

In cases where it is not possible to
provide constant current charging, 
it is possible to achieve this with a
constant voltage by using a high
voltage level, e.g. 1.65 voltage limit
may be used for 20 to 30 hours, if 
the current limit is approximately
equivalent to the 5 hour charge
current*. If the current rating is lower,
then the charge time should be
increased accordingly.

When the charger maximum voltage
setting is too low to supply constant
current charging, divide the battery
into two parts to be charged
individually at a high voltage.

The battery can now be put into
service.

*Please refer to the installation and
operation instruction sheet.

Figure 7 - Charge efficiency as a function of state of charge

110 %

100 %

90 %

80 %

70 %

60 %

50 %

40 %

30 %

20 %

10 %

0 %

0 20 40 60 80 100 120 140

Percentage

charge efficiency

Charge input (% Rated Capacity)

capacity charged

Charge at Constant Current

(current 0.2 C

5

A)

BlockBat  3/11/98  10:12  Page 27

Home       Back     

Home       Back     

Home       Back     

Home

Back

Contents

Содержание SBL

Страница 1: ...Nickel cadmium block battery Technical manual...

Страница 2: ...lly safe 4 2 13 Low life cycle cost 4 3 Electrochemistry of nickel cadmium batteries 5 4 Construction features of the block battery 6 4 1 Plate assembly 7 4 2 Separation 8 4 3 Electrolyte 8 4 4 Termin...

Страница 3: ...technical manuals are available which address the particular characteristics of these ranges 6 7 Cycling 14 6 8 Effect of temperature on lifetime 14 6 9 Water consumption and gas evolution 16 7 Batter...

Страница 4: ...nd operating characteristics of the Saft Nife pocket plate block battery to enable a successful battery system to be achieved A battery which while retaining all the advantages arising from nearly 100...

Страница 5: ...see section 9 2 Mechanical abuse 2 8 High resistance to electrical abuse The block battery will survive abuse which would destroy a lead acid battery for example overcharging deep discharging and high...

Страница 6: ...in the electrochemistry of the process and are naturally corroded during the life of the battery The charge discharge reaction is as follows During discharge the trivalent nickel hydroxide is reduced...

Страница 7: ...blocks of 1 10 cells depending on the cell size Plate group bus Connects the plate tabs with the terminal post Plate tabs and terminal post are projection welded to the plate group bus Separating grid...

Страница 8: ...ssembly The nickel cadmium cell consists of two groups of plates the positive containing nickel hydroxide and the negative containing cadmium hydroxide The active materials of the Saft Nife pocket pla...

Страница 9: ...n the cell plates irrespective of the charge level In most applications the electrolyte will retain its effectiveness for the life of the battery and will never need replacing However under certain co...

Страница 10: ...d 4 They can be recognized from the block dimensions as follows Block width mm Block height mm Plate module 123 194 1 123 264 2 195 349 3 195 405 4 Table 1 Correlation between block dimensions and pla...

Страница 11: ...e different discharge types The choice is related to the discharge time and the end of discharge voltage There are of course many applications where there are multiple discharges and so the optimum ra...

Страница 12: ...cations 5 3 Type H The SBH is designed for applications where there is a demand for a relatively high current over short periods usually less than 30 minutes in duration The applications can have freq...

Страница 13: ...sistance of a block battery cell depends on the performance type and at normal temperature has the values given in Table 3 in milliohms per Ah of capacity To obtain the internal resistance of a cell i...

Страница 14: ...e for operating temperatures from 30 C to 50 C Figure 1 a Temperature derating factors for H type plate 1 2 1 0 8 0 6 0 4 0 2 40 20 0 20 40 Derating factor special electrolyte required for continuous...

Страница 15: ...ncountered in stationary applications This can vary from low depth of discharges to discharges of up to 100 and the number of cycles that the product will be able to provide will depend on the depth o...

Страница 16: ...s reduced to less than 1 year if used at 50 C 15 Figure 2 Capacity loss on open circuit stand 100 90 80 70 60 50 0 50 100 150 200 250 300 350 400 Percentage of initial capacity 40 C Open circuit perio...

Страница 17: ...f discharge of the electrodes The overcharge current is a function of both voltage and temperature so both have an influence on the consumption of water Figure 5 gives typical water consumption values...

Страница 18: ...previous discharge The factors used for this will depend on the depth of discharge the rate of discharge and the charge voltage and current A requirement for a high state of charge does not justify a...

Страница 19: ...and so the minimum voltage for the single level and the two level charge voltage is the normally recommended value This also helps within a voltage window to obtain the lowest and most effective end o...

Страница 20: ...w than the two rate charger The two rate charger has an initial high voltage stage to charge the battery followed by a lower voltage maintenance charge This allows the battery to be charged quickly an...

Страница 21: ...tage 1 50 volts per cell Charge Time hours Charging Voltage 1 40 volts per cell Charging Voltage 1 45 volts per cell Charging Voltage 1 55 volts per cell Current Limit 0 2 C5A Temperature 20 25 C H ty...

Страница 22: ...harge times from a fully discharged state for the L block 130 120 110 100 90 80 70 60 50 40 30 20 10 0 0 5 10 15 20 25 30 35 Available Capacity of rated capacity Charging Voltage 1 50 volts per cell C...

Страница 23: ...A constant current first charge is preferable and this should be such as to supply 300 of the rated capacity of the cell Thus a 250 Ah cell will require 750 ampere hours input e g 50 amperes for 15 h...

Страница 24: ...cid batteries this will lead to failure of the battery and is unacceptable The block battery is designed to make recovery from this situation possible Overcharge In the case of the block battery with...

Страница 25: ...0 45 liters of hydrogen 10 Installation and storage 10 1 Batteries on arrival On receiving the battery open the cases and check for any indication of damage in transit Remove the cells and any access...

Страница 26: ...0 45 liters of hydrogen 10 Installation and storage 10 1 Batteries on arrival On receiving the battery open the cases and check for any indication of damage in transit Remove the cells and any access...

Страница 27: ...of 2 for example the air in the room will need changing 3 2 1 5 times per hour In practice a typical figure for natural room ventilation is about 2 5 air changes per hour and so in this case it would...

Страница 28: ...of 2 for example the air in the room will need changing 3 2 1 5 times per hour In practice a typical figure for natural room ventilation is about 2 5 air changes per hour and so in this case it would...

Страница 29: ...tery operations the electrolyte will retain its effectiveness for the life of the battery Thus normally it is not necessary to change the electrolyte However under certain battery operating conditions...

Страница 30: ...Saft Argentina SA Buenos Aires Tel 54 11 4 686 1994 Fax 54 11 4 686 1925 AUSTRALIA Saft Pty Ltd Seven Hills Tel 61 2 9674 0700 Fax 61 2 9620 9990 BELGIUM NV Safta SA Brussels Tel 32 2 556 44 00 Fax 3...

Отзывы: