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Britain SEC Battery


¡ñ Reduces float current by up to 50%.
¡ñ Reduces gassing by up to 80%.
¡ñ Will minimize water loss from the cell.
¡ñ Reduces cell failure due to dry out, a major failure mode of VRLA batterieso.
¡ñ Batteries will have full design life when used at temperatures up to 30 C.
¡ñ Reduces cell heating reducing the possibility of thermal runaway.
¡ñ Energy saving from reduced float current and cell cooling requirements.
¡ñ Maintains full cell capacity by preventing depolarization of the negative plate
In keeping with our philosophy to stay at the forefront of the ever expanding Telecom standby battery market we have extended our range of 19" front terminal batteries up to 175 ah capacity at 12 volts. These batteries include sever innovative features: triple barrier terminal post seal, high Tin / Calcium positive plate alloy for improved, by up to 65%, deep cycle capability of the 12TLA batteries and the 'Word First' Monobloc Catalyst.

Sealed Valve Regulated Construction Battery Life in Cycle Life

* These batteries are of the Absorbed Glass Mat (AG M) or

CELLYTE 12FTG batteries are suitable for deep gelled gelled electrolyte technology (Gel). The electrolyt e in the cell is

immobilized in a specially form ulated non woven glass mat

separator or in a thixatropic Gel. All the acid is abs orbed in this

manner providing a safe non-spillable battery.

Battery Life in Cycle Life

* CELLYTE 12FTG batteries are suitable for deep

cycle service battery life will depend on temperature,

depth and frequency of cycling, however the use of

the optional Catvent Catalyst will improve life in

temperatures up to 30 C.

Gas Recombination System

* The gasses generated in the normal charge / disc harge use ofa rechargeable lead acid battery are internally recombinedduring normal operating parameters and in normal operationaluse, more than 99% of the gas generated is recombined.

Battery One-Way Safety Valve

* When pressure builds up in the cell the B & S

German safety one-way valve opens at 2-3 psi and

releases the excessive pressure and then closes.

The one-way valve does not allow the ingress

of oxygen which is harmful and reduces battery life.

SEC Catvent - Catalyst Vent (Optional)

* SEC's VRLA cells incorporate the Phi ladelphia Scientific Monoblocprecious metal Catalyst Catvent which prevents the negativeplate from depolarizing reduces the cell float current by upto 50%, reduces the cell gassing by about 80% , reduces celldry out which is the major cause of VRLA battery failure

Temperature Range for Normal Operation

* CELLYTE 12FTG batteries have a wide operating temperaturerange -25 C. to +55 C. However for maximum life it isrecommended to operate the battery at 20 C. to 30 C.

Battery Maintenance

* The battery has been designed and built such that no addition

of electrolyte or water is needed during the life of the batt ery.

 

 

Plate Design and Paste Formulation

* SEC has optimised the plate and paste f ormulation to maximise

the operating life of the battery. The High Tin (1.6%) / Calcium

plate alloy is used to extend battery life and cycling c apability.

Past formulation will provide excellent recovery from deep

discharge. With low self dis charge to ensure maximum storage

time when not in use

 

 

Battery Life in Float Service

* CELLYTE 12FTA&G batteries are suitable f or float / standby

service with a design life of 12 years at 20C.


CELLYTE 12FTA&G Bloc Data & Dimensions

SEC Battery

type

Nominal

Capacity 1.80 vpc

Short circuit Amps

Intermal Resistance Ohms

Maximum Charge Current

Terminal type

Battery

Overall Battery Dimensions

Weight

Length

Width

Height

Kg

lbs

Inch

mm

Inch

mm

Inch

mm

12FTA55

55

1900

4.5

10

FT4-M6

18.0 39.6

10.83 275

4.134 105

8.858 225

12FTA80

80

2400

4.0

15

FT4-M8

28.0 61.6

15.55 395

4.331 110

11.34 288

12FTA90

90

2700

3.7

17

FT4-M8

31.0 68.2

19.29 490

4.331 110

9.055 230

12FTA100

100

3000

3.2

18

FT4-M8

34.0 74.8

15.55 395

4.331 110

11.34 288

12FTA105

105

3200

3.1

19

FT4-M8

35.0 77.0

21.65 550

4.331 110

9.37 238

12FTA105US

105

320

3.1

19

FT4-M8

35.0 77.0

19.29 490

4.331 110

9.055 230

12FTA120

120

3550

2.9

19

FT4-M8

38.0 83.6

21.65 550

4.331 110

9.37 238

12FTA125

125

4200

2.8

25

FT4-M8

42.0 92.4

21.65 550

4.331 110

11.34 288

12FTA155

155

4800

2.6

30

FT4-M8

50.0 110

21.65 550

4.331 110

11..34 288

12FTA175

175

5300

2.4

34

FT4-M8

57.0 125

21.65 550

4.331 110

12.6 320

6 mm Female Terminal - FT 4 = 16 mm with M6 Bolt

8 mm Female Terminal - FT 5 = 16 mm with M8 Bolt

 

Specifications

  • POSITIVE PLATE: Lead calcium flat plate grid
  • NEGATIVE PLATE: Flat pasted grid
  • ELECTROLYTE: Sulphuric acid or thixotropic Gel
  • CATALYST VENT: CatventTM (optional)
  • CONTAINER: Grade ABS V-0
  • SEPARATORS: Microporous separator
  • FLOAT VOLTAGE: 2.25 vpc at 20/25oC
  • MAX CHARGE VOLTAGE: 2.35 vpc at 20/25oC
  • SAFETY ONE WAY VALVE: 1-3 p.s.i self-resealing
  • TERMINALS: Integral heavy duty brass insert
  • INTERCONNECTS: Copper bar or cables

Features

  • Maintenance Free
  • Front terminal battery
  • Tank formed flat Calcium plates
  • Manifolded gasing system
  • Incorporates precious metal catalyst Catvent

Benefits of Catalyst in SEC VRLA Batteries

Catalyst Reduces Float Current

One of the most immediate, observable effects of installing

a catalyst in a VRLA cell is a sudden drop in the float current.

Typically float currents are one half or less when a catalyst is

installed. Adding a catalyst to the cell prevents some of the

oxygen reaching the negative plate and allows the negative

plate to stay polarised. This means that less current needs to

be supplied to the cell from the charging system, manifesting

itself as lower float current, leading to the following benefit :-

* Minimize water loss

Gasses are recombined into water inside the cell rather

than exiting the cell. Too much gas leaving the cell can

lead to premature dry-out and cell failure. Cell dry out has

been predominant cause of customer dissatisfaction with

VRLA technology.

* Increased life

There are many potential failure modes of VRLA cells.

A number of these failure modes can be mitigated by the

catalyst technology such as: Cell dry out, positive plate

corrosion, thermal runaway, capacity loss due to negative

plate depolarization.

* Minimize positive plate corrosion

A reduction in float current reduces the amount of over- charge

on the positive plate which directly impacts thecorrosion rate.

The design life of a lead acid cell is basedon the corrosion

of the plate barring any other unforeseenfailure modes.

* Maintain cell capacity

Many VRLA cells in service are failing capacity tests

because their negative plates are depolarized In fact

significant capacity increases have been seen on some

cells just by installing a catalyst.

 

 
 
®2005 Suntel Energy Technology Co., Ltd