Alpha OGi bloc User Manual

Nominal data:
Nominal voltage UN: 2.0 V x number of cells Nominal capacity CN = C10: 10 hour dis­charge (see type plate and technical data in these instructions) Nominal discharge current: IN = I10: Final discharge voltage Us: see technical data in these instructions Nominal temperature TN: 20°C "LA": antimony content < 2% in the grids (earthcarriers) of the positive electrodes
Non-compliance with operating instruc­tions, repairsmade with other than original parts, tamperingor use of additives for the electrolyte (alleged"enhancing agents") render the warrantynull and void.
1. Commissioning of filled and charged batteries
Before commissioning all blocks must be inspected for mechanical damage, cells must be connected with the correct polarity and con­nectors firmly seated. The following torques apply for screw connectors: M 10 with 17 Nm +/ _ 1 Nm If necessary the terminal covers must be put on. Check the electrolyte level in all cells. If nec­essary top up to maximum level with purified water as under DIN 43530 Part 4. With charger off and loads isolated connect battery to the direct current power supply maintaining correct polarity (positive terminal to positive post). Switch on the charger and charge as under Section 2.2.
2. Operation
For the operation of stationary battery installationsDIN VDE 0510 Part 1 (draft) and DIN VDE 0510 Part 2 apply.
2.1 Discharging
Never allow the final discharge voltage of the battery to drop below that assigned for the discharge current. Unless the manufacturer has specified otherwise, no more than the nominal capacity is to be consumed. Charge immediately after discharge as well as partial discharge.
2.2 Charging
All charging procedures with their limit values may be employed as under DIN 41773 (IU characteristic) DIN 41774 (W characteristic DIN 41776 (I characteristic). Depending on charger type and charging characteristic alternating currents flow through the battery superimposing onto the direct cur­rent. These alternating currents and the reaction of the loads lead to an additional warming of the battery and strain on the electrodes with pos­sible resulting damage (see 2.5). Depending on the system at hand charging may be carried out under the following opera­tions: a) S
tand-by parallel operation and floating operation Here the load, direct current and battery are continuously connected in parallel. Thereby the charging voltage is the operating voltage of the battery and at the same time the battery installation voltage. With st
and-by parallel operation the direct cur­rent is at any time capable of supplying the maximum load current and the battery charg­ing current. The battery only supplies current when the direct current source fails. The charge voltage should be set at 2.23 V +/_1% x number of cells measured at the battery's terminals. To reduce the recharging time a charging stage canbe applied in which the charging voltage is 2.33 to 2.4 V x number of cells (stand-by parallelparallel operation with recharging stage). Automatic changeover to the charging voltage of 2.23 V
+/_ 1% x number of cells follows. With the floating operation
the direct current source is not able to supply the maximum load current at all times. The load current intermittent Iy supercedes the nominal current of the direct current source. During this period the battery supplies power. It is not fully charged at all times. Therefore, depending on the load the charge voltage must be set at 2.23 to 2.30 V x number of cells. b) Switch mode operation When charging the battery is separated from the load. Towards the end of the charging process the charge voltage of the battery is
2.6 - 2.75 V/cell. The charging process must be monitored (see Sections 2.4, 2.5 and 2.6) On reaching a fully charged state the charging process must be stopped or switched to float chargeas under Section 2.3. c) Battery operation (charge/discharge opera
­tion) The load is supplied only by the battery. Hereby the charge voltage of the battery towards the end of the charging process is 2.6
- 2.75 V/ cell. The charging process must be monitored (see Sections 2.4, 2.5 and 2.6). On reaching a fully charged state the charging process must be switched off. The battery can be switched to the load as necessary.
2.3 Maintaining the full charge
(float charge) Devices complying with the stipulations under DIN 41773 must be used. They are to be set so that the average cell voltage is
2.23 V +/_ 1% and the electrolyte density does not decrease over a protracted period.
2.4 Equalizing charge
Because it is possible to exceed the permitted load voltages, appropriate measures must be taken, e.g. switch off the load. Equalizing charges are required after exhaus­tive discharges and after inadequate charges; they can be carried out as follows:
- up to 72 hours at constant voltage of max.
2.4 V/cell - as under Table 1 with I and W characteristic. On exceeding the maximum temperature of 55°C charging must either be stopped or pro­ceed with reduced current or be switched to float charge to allow the temperature to drop. The equalizing charge is completed when the electrolyte densities and cell voltages no longer increase within 2 hours.
2.5 Alternating currents with periodic deviations
On recharging up to 2.4 V/cell as under oper­ation modes a) to c) the actual value of the alternating current is ocassionally permitted to reach max. 20 Aper 100 Ah nominal capacity. Above 2.4 V/cells 10 Aper 100 Ah nominal capacity may not be exceeded. In a fully charged state with a charge voltage of 2.23 to 2.30 V/cell the actual value of the alternating current may not exceed 5 Aper 100 Ah nominal capacity.
Observe operating instructions and affix close within sight of the battery! Work on batteries only under instrustions of skilled personnel!
Smoking prohibitet! Do not expose battery to open flame glowing fire or sparks as explo­sion and fire hazard exists!
When working on batteries wear protective glasses and clothing!Observe the accident prevention rules as well as DIN VDE 0510, VDE 0105 part 1 !
Explosion and fire hazard, avoid short circuits! Caution! Metal parts of the battery cells are always live, therefore do not place items or tools on the battery!
Electrolyte is strongly corrosive!
Monobloc batteries/cells are very heavy! Ensure secure installation! Only use suitable transport equip­ment!
Dangerous voltage!
Acid splashes in the eyes or on the skin must be washed out or off with plenty of water.Then see a doctor immediately. Acid on clothing should be washed out with water!
Assembled by:____________________________ on:______________________________________ Start-up by:_______________________________ on:______________________________________ Safety marking affixed by:________________________________ on:______________________________________
OPERATING INSTRUCTIONS
Stationary vented lead-acid batteries OGi bloc
Ue (V/cell) 1.80 1.75 1.75 1.70 1.65 1.65 1.60 Dimensions Masse/Weight
C10 C5 C3 C1 C1/2 C1/6 C1/12 L W Hmax Bat.+el. el. Ri Ik
TYPE C (Ah) (mm) (mm) (mm) (kg) (kg) (m/bl.) (kA)
12V 1 OGi 25 29.0 25.5 22.5 16.8 14.3 9.2 6.7 272 205 375 33 11 16.97 0.72 12V 2 OGi 50 55.0 49.5 44.7 32.8 28.0 18.0 13.1 272 205 375 41 10.9 8.91 1.41 12V 3 OGi 75 80.0 74.5 67.5 49.6 42.2 27.3 19.8 272 205 375 49 10.8 5.94 2.11 12V 4 OGi 100 105.0 98.5 89.4 65.7 56.1 36.1 26.1 272 205 375 58 10.7 4.46 2.81 12V 5 OGi 125 135.0 123.0 111.3 81.6 69.0 44.3 31.7 380 205 375 78 15.7 3.57 3.52 12V 6 OGi 150 165.0 148.5 133.8 98.2 82.5 52.7 37.1 380 205 375 86 15.5 2.97 4.22 6V 7 OGi 175 193.0 172.5 156.0 114.1 94.0 58.7 40.8 272 205 375 49 11.3 1.27 4.93 6V 8 OGi 200 228.0 197.5 178.8 130.0 108.0 67.3 46.8 272 205 375 53 11.1 1.11 5.63 6V 9 OGi 225 254.0 221.5 200.7 145.8 121.5 75.5 52.6 380 205 375 68 16.4 0.99 6.36 6V 10 OGi 250 270.0 247.0 223.5 161.7 133.0 80.5 55.3 380 205 375 72 16.3 0.89 7.04 6V 11 OGi 275 304.0 271.5 245.1 177.6 146.0 88.5 60.7 380 205 375 75 16.2 0.81 7.78 6V 12 OGi 300 320.0 296.0 268.2 194.4 159.5 96.5 66.3 380 205 375 79 16 0.74 8.44 2V 24 OGi 600 684.0 592.5 536.4 390.0 324.0 201.9 140.4 205 272 375 53 11.1 0.13 16.42 2V 30 OGi 750 810.0 741.0 670.5 485.1 399.0 241.5 165.9 205 380 375 72 16.3 0.10 21.89 2V 36 OGi 900 960.0 888.0 804.6 583.2 478.5 289.5 198.9 205 380 375 79 16 0.08 24.63
2.6 Charging currents
The charging currents are not limited to
2.4 V/ cell. When exceeding the charging voltage of 2.4 V/cell greater water decompo­sition occurs. The charging currents per 100 Ah nominal capacity shown in Table 1 may not be exceeded.
2.7 Temperature
The recommended operating temperature for lead-acid batteries is 10°C to 30°C. The tech­nical data apply for the nominal temperature 20°C. The ideal operating temperature is 20°C +/_ 5 K. Higher temperatures shorten the service life. Lower temperatures reduce the available capacity. The maximum temper­ature of 55°C may not be exceeded.
2.8 Temperature-related charge voltage
A temperature-related adjustment of the charge voltage within the operating tempera­ture of 10°C to 30°C is not necessary. Should the temperature range be lower than 10°C and/or higher than 30°C a temperature related adjustment of the charge voltage should be made. The temperature correction factor is (-0.004 V/C per K). Should the temperature constantly rise above 40°C, then the factor is (0.003 V/C per K).
2.9 Electrolyte
The electrolyte is diluted sulphuric acid. The nominal electrolyte density is based on 20°C and the nominal electrolyte level when fully charged maximum +/ _ 0.01 kg/l. Higher temperatures reduce the electrolyte density, lower temperatures increase the electrolyte density. The associated correction factor is 0.0007 kg/l per K.
Example: electrolyte density of 1.23 kg/l at 35°C corresponds to a density of 1.24 kg/l at 20°C or electrolyte density of 1.25 kg/l at 5°C corresponds to a density of 1.24 kg/l at 20°C.
3. Battery maintenance and control
The electrolyte level must be checked regu­larly. If it has dropped to the lowest elec­trolyte level mark, purified water must be added as under DIN 43530 Part 4, maximum conducting capacity 30 _S/cm.To avoid leak­age currents keep the battery clean and dry. Cleaning the battery should be carried out as specified in the ZVEI pam­phlet on battery cleaning. Plastic battery components, in particular the vent caps, must only be cleaned with water containing no additives. At least every 6 months the following must be measured and recorded:
- battery voltage
- voltage of a few selected cells/monobloc batteries
- electrolyte density of a few selected monobloc batteries
- electrolyte temperature of a few selected monobloc batteries The following must be measured and record­ed annually:
- voltage of all bloc batteries
-electrolyte density of all bloc batteries
- electrolyte temperature of a few selected bloc batteries Should the float charge voltage in one cell deviate more than + 0.1 V or - 0.05 V from the average value (see 2.3), customer serv­ices must be called in. Annual visual checks:
- on bolted connectors, check that unsecured bolt connectors are firmly seated
- on battery installation or arrangement
- on ventilation.
4. Tests
Tests must be conducted according to DIN 43539 Part 1 and 4. In addition, special test instructions such as under DIN VDE 0107 and DIN VDE 0108 must be observed.
5. Faults
Should faults be detected in the battery or the charging device, customer services should be called in immediately. Measurement data under Section 3 simplify fault detection and removal. A service contract with us facilitates the time­ly detection of faults.
6. Storage and taking out of operation
Should cells/batteries be stored or taken out of operation for a longer period of time they mustbe placed, fully charged, in a dry, frost­free room. To avoid damage the following-charging methods can be chosen:
1. Equalizing charges on a quarterly basis as under Section 2.4. In average ambient tem­peratures of more than 30°C monthly equal­izing charges may be necessary.
2. Float charging as under Section 2.3.
7. Transport
Batteries which show no damage of any kind are not treated as dangerous goods under the road and railway transport regulations (GGVS and GGVE) if they are secured against short circuits, sliding, overturning or damage and stacked and secured appropri­ately on palettes (GGV's margin No. 2801 a). The batteries ready for dispatch must not show any exter­nal dangerous traces of acid. For all sealed batteries and cells whose ele­ments are leaking or damaged the exception­al regulation No. 69 applies.
8. Technical data
The nominal voltage, the number of blocks, the nominal capacity (C10 = CN) and the battery type are obtained from the type plate. Other capacities (Cn) at different discharge voltages (In) with the corresponding dis­charge times (tn)can be obtained from the OGi tables.
Charging Monobloc battery Cell procedure OGi bloc, OGi voltage
I-charact. 5,0 A 2,6-2,75 V W-charac- 7,0 A at 2,4 V
teristic 3,5 A at 2,65 V
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Alpha Industrial Power
MTI and Alpha Industrial Power reserve the right to make changes to the products and information contained in this document without notice. Copyright © 2009 MTI and Alpha Industrial Power. All Rights Reserved. Alpha® is a registered trademark of Alpha Technologies. member of The Alpha Group™ is a trademark of Alpha Technologies. AlphaCell™ is a trademark of Alpha Technologies.
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