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MiniPurge Type X / ET Size 2 Manual

ML 443

Contents 1. Specification Sheet – MiniPurge Type X Systems 2. Application Suitability 3. Description and Principle of Operation 4. Installation of the System 5. Commissioning 6. Maintenance of the System 7. Fault Finding 8. Approval Documents 9. Glossary

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1 Expo Technologies UK T: +44 (0) 20 8398 8011 E: [email protected]

Expo Technologies US T: +1 (440) 247 5314 E:[email protected]

Expo Technologies China T: +86 532 8906 9858 E: [email protected]

Approval / Certification

Europe EN60079-0, EN60079-2 Sira 01ATEX1295X 2813 II 2 (2) G D Ex [pxb] ia IIC T5 Gb Ex [pxb] ia IIIC T100ºC Db Tamb -20ºC +55ºC

IEC IEC60079-0, IEC60079-2 IECEx SIR 07.0027X Ex [pxb] ia IIC T5 Gb Ex [pxb] ia IIIC T100ºC Db Tamb -20ºC +55ºC

Brazil INMETRO - TUV TÜV 12.1462X Ex [pxb] ia IIC T5 Gb Ex [pxb] ia IIIC T100ºC Db -20°C ≤ Ta ≤ +55°C

USA / Canada NFPA 496 FM 1X8A4AE Class I Div 1 Groups A, B, C & D For limitations and conditions of use refer to the applicable certificate at the back of this manual.

MiniPurge Housing

ss = 316L Stainless Steel (NROB finish) Neoprene “Top” Mount Gasket pm = Panel Mount (Side/Front Mount) 316L

Stainless Steel (NROB finish)

Presurization Method

CF = Continuous Flow LC = Leakage Compensation

1. Specification Sheet – MiniPurge Type X Systems

Supply Pressure: Must be regulated at inlet Minimum 60 psi / 0.4 MPa / 4 bar Maximum 115 psi / 0.8 MPa / 8 bar Air Quality: Compressed air / Nitrogen to instrument quality Ambient Temperature: -20ºC to + 55ºC Leakage Compensation: Variable up to 9 scfm / 250 Nl/min to compensate for leakage of enclosure Purge Timer: Adjustable between 99 minutes(-0+3 seconds) Flow & Pressure Sensors: CF: One sensor for both “Low Pressure and Flow”: 1” WC / 250 Pa (2.5 mbar) LC: “Low Pressure Sensor” 0.2” WC / 50 Pa (0.5 mbar) “Flow Sensor” 1.13” WC/ 280 Pa / (2.8 mbar) Relief Valve: System: CF LC Model No: RLV36/ss RLV36/FS/ss Opening Pressure: 4” WC / 1 kPa (10 mbar) 4” WC / 1 kPa (10 mbar) Purge Flow Rate: N/A (see Spark Arrestor) 16 scfm / 450 Nl/min Material: 316L Stainless Steel, Spark Arrestor: Stainless Steel mesh, Gasket: Neoprene Spark Arrestor Unit Model No: SAU40 (CF systems only) Purge / Dilution Flow Rate: 8 - 16 scfm / 225 - 450 Nl/min 4 user selectable orifice plates Material: Stainless Steel Bulkhead Pipe Fittings: Air Supply: 1/2” NPT Output: 1/2” NPT Signal: 1/8” NPT Visual Indicators: CF: Alarm / Pressurized (Red / Green) Purge Complete (Black / Yellow) LC: Alarm / Pressurized (Red / Green) Purge Complete (Black / Yellow) Action on “Loss of Pressure”: CF: Action on “Loss of Pressure” = “Alarm & Trip”. Option /AO specifies an “Alarm Only” kit. LC: Action on “Loss of Pressure” = “Alarm & Trip” or “Alarm Only”. LC Model is user selectable.

Size 2 = MiniPurge Purge flow rate 450 Nl /min, 16 scfm

Purge System Type

07 = MiniPurge

Power & Alarm (Signals)

PO = Pneumatic Output “Power” : On Purge Complete = 30 psi / 0.2 MPa / 2 bar Signal “Alarm” : Loss of Pressure = No signal ”Pressurized” = 30 psi / 0.2 MPa / 2 bar Signal PA = Power and Alarm Terminal Box Ex e IIC T5 Gb Power and Alarm Terminal Box Ex e IIC T4 Gb “Power” ; 250 Vac 4 Amp AC15 2PNO – Ex d IIC T6 “Alarm” : 250 Vac 4 Amp AC15 SPCO – Ex d IIC T6 (European and IEC Systems Only)

IS = Intrinsically Safe, Ex i & Ex i circuit “Power” : used with others’ Ex i equipment “Alarm” : Relay / Barrier

ET = Electronic Timer

Model No. (Example): 07 2XLC / ss / ET / PO / WM (Note: Not all codes are applicable)

Options as Required

AO = Alarm Only MO = Manual Override MK = MIU Mounting Kit (PO systems only) WM = Wall Mounting Bars

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Expo Technologies UK T: +44 (0) 20 8398 8011

E: [email protected]

Expo Technologies US T: +1 (440) 247 5314

E:[email protected]

Expo Technologies China T: +86 532 8906 9858


2. Application Suitability

MiniPurge Systems are certified for use in Hazardous Areas, where the Hazardous Area is non-mining (i.e. above ground) and the hazard is caused by flammable gasses, vapours or dust. Depending on the model, the systems may be used in IECEx, ATEX Zone 1(21) - Category 2 and NEC 500 Class I, Div 1.

MiniPurge systems may be used for hazards of any gas group. However, apparatus

associated with the MiniPurge system, such as Intrinsically Safe signalling circuits and flameproof enclosures containing switching devices may be limited in their gas group. The certification documentation supplied with any such devices must be checked to ensure their suitability. This system is designed for use primarily with compressed air. Where other inert compressed gasses are used (Nitrogen, for example) the user must take suitable precautions so that the build up of the inert gas does not present a hazard to health. Consult the Control of Substances Hazardous to Health (COSHH) data sheet for the gas used. Where a risk of asphyxiation exists, a warning label must be fitted to the Pressurized Enclosure.

The following materials are used in the construction of MiniPurge systems. If substances that will adversely affect any of these materials are present in the surrounding environment, please consult Expo for further guidance. Materials of construction:

• Stainless Steel • Aluminium • Acrylic • Polycarbonate

• Mild (carbon) Steel • Nylon • Silicone Rubber • ABS

• Brass • Polyurethane • Neoprene • Glass Filled Polyester

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3. Description and Principle of Operation

All Expo Technologies MiniPurge pressurization systems provide: a) a method of pressurizing a Pressurized Enclosure (PE) while at the same time compensating for any leakage, together with b) a method of purging the enclosure, before power is applied, to remove any flammable gas that may have entered the enclosure while it was not pressurized,

c) visual indication of the MiniPurge system status, and d) an output to provide remote indication or control.

The MiniPurge system comprises a number of component units. The units required depend on the type of system selected. These are summarised in Table 1. The general description and function of each is as follows: 3.1 Control Unit (CU) The Control Unit (CU) is the heart of the system. It contains a pneumatic logic circuit specially designed and built to control the functions required for purge and pressurization. For all systems this includes air filtration, pressure and purge flow measurement, electronic purge timing, and local visual indication of Pressurized/Alarm and flow sensed. It also provides the outputs for power and remote alarm control corresponding to the output type selected. 3.2 Relief Valve (RLV)

The Relief Valve unit is fitted to the PE to provide a means of limiting the maximum pressure experienced by the PE during operation. The RLV model number has a suffix giving the diameter of the valve aperture in millimetres e.g. RLV36 (= 36mm bore). The RLV also incorporates a Spark Arrestor to prevent sparks being ejected from the PE into the classified area. In Leakage Compensation systems, the RLV is combined with the flow measurement mechanism.

Figure 1 LC Relief Valve

3.3 Calibrated Outlet Orifice/Spark Arrestor (SAU) Continuous Flow systems incorporate the SAU40. This unit has a range of interchangeable calibrated orifice plates, which are used to measure the flow through the PE. 3.4 The Methods of Pressurizing a) CF - Continuous Flow A Continuous Flow (CF) of protective gas is passed through the PE. Initially this flow is verified and performs the purging phase of the operation. When the purging phase is completed – i.e. the purge time has elapsed- the same flow of protective gas maintains the pressurization of the enclosure. This flow may be required to dilute an internal source of hazardous gas release.

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D.P. HI /

"OR"

GATE

'PURGE

COMPLETE'

VALVE

B

A

PURGE OUTLET TO

ENCLOSURE PRESSURE

TEST POINT (PLUGGED)

IN-LINE RESTRICTOR

LOGIC

GAUGE

PRESSURE

REGULATOR

2 barg

30 psi

D.P. LO /

MINIMUM PRESSURE /

FLOW SENSOR

ALARM INDICATOR 1

RED = ALARM

GREEN = PRESSURIZED

FILTER

t

PURGE FLOW

SENSORTIMER

VALVE

PURGE SUPPLY

AIR OR INERT

GAS

PURGE

INDICATOR 2

YELLOW =

PURGING

Figure 2 Continuous Flow Circuit Diagram

b) LC - Leakage Compensation Initially a high flow of protective gas is passed through the enclosure. This flow is verified and performs the purging phase of the operation. When the purging phase is completed – i.e. the purge time has elapsed - the flow of protective gas is provided via an adjustable valve so that it just compensates for any leakage from the PE in addition to maintaining its pressurization. If leakage is less than 5 l/min then the LCV will be awkward to set. You will find that the RLV spring will cycle open and closed. If this happens contact our service department for advice.

'PURGE

COMPLETE'

VALVE

ENCLOSURE

PRESSURE

TEST POINT

(PLUGGED)

D.P. HI / ENCLOSURE PRESSURE

PURGE OUTLET TO PRESSURIZED ENCLOSURE

PURGE VALVE

PILOT RESTRICTOR

LOGIC GAUGE

PRESSURE

REGULATOR

2 barg

30 psi

"OR"

IN-LINE RESTRICTOR

GATE

PURGE

VALVE

LEAKAGE

COMPENSATION

VALVE

TIMER

VALVE

D.P. LO / RLV CONNECTION

ALARM

INDICATOR 1

RED = ALARM

GREEN =

PRESSURIZED

PURGE

INDICATOR 2

YELLOW =

PURGING

ALARM

& TRIP

SENSOR

MINIMUMPRESSURE

ALARM ONLY (OPTION)

AIR OR INERT

GAS

FILTER

t

PURGE FLOW

SENSOR

ELECTRONIC

TIMER

B

A

Figure 3 Leakage Compensation Circuit Diagram

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3.5 Type of Output The functions of the outputs are power control and alarm/pressurized indication. Power control provides a signal to switch the power to the PE. Alarm output provides a passive signal to indicate remotely when the enclosure is not pressurized and an active signal when pressurized. a) PO- Pneumatic Output The power control and pressurized outputs are pneumatic signals, which may be used to operate other devices to provide power switching or alarm indication. The lack of any output signal indicates incomplete purge and alarm. In many instances these outputs may be

connected to the Expo range of MiniPurge Interface Unit s (MIU).

Figure 4 Typical MiniPurge Interface Unit type (MIU/dA)

Figure 5 Pneumatic Output Option

b) IS - Intrinsically Safe Output The power control and alarm outputs are volt free contacts which form part of an Intrinsically Safe (IS) circuit which then provides power control or alarm outputs in a safe (unclassified) area. These contacts must only be connected to IS circuits as the switch contacts are in the hazardous area. In many instances these outputs may be connected to the Expo range of

MiniPurge Interface Units (MIU).

Figure 6 Intrinsically Safe (IS) Option

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c) PA - Power and Alarm

Figure 7 Ex de Power and Alarm (PA) Option

The Terminal Box is increased safety (Ex e) certified and incorporates the terminal connection points for the alarm and interlock switches. All contacts provided are volt free (dry). Cable entry methods (for example conduit or cable glands) must be certified to IECEx, ATEX or INMETRO standards. The main requirement is that IP66 (or better) ingress protection must be provided by use of seals or washers.

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4. Installation of the System

This MiniPurge is designed for use under normal industrial conditions of ambient temperature, humidity and vibration. Please consult Expo before installing this equipment in conditions that may cause stresses beyond normal industrial conditions.

The MiniPurge system shall be installed in accordance with relevant standards, such as IEC / EN 60079-14, NEC 500, NFPA 496 and any local codes of practice that are in force.

There are up to three components for the MiniPurge system, dependent upon the system type:

System type Control Unit (CU) Relief Valve (RLV)

Spark Arrestor Unit

Leakage Compensation YES YES Integral to RLV

Continuous Flow YES YES YES (SAU40)

Table 1 System Components

4.1 Control Unit (CU)

The MiniPurge system should be installed either directly on or close to the PE. See mounting details. Generally, the most convenient arrangement is to install the CU on the top of the PE.

Must be mounted vertically as shown in MiniPurge Configuration XBR-7TD0-003. The CU can be mounted on the side of the PE using the rear mounting fixings. The piped connections to the PE should be made using metallic tube through suitable bulkhead connections. The CU can be remote mounted using the wall mounting bars (/WM option) and should be installed as close as possible to the PE. It should be installed so that the system indicators and certification labels may be readily observed. 4.2 Relief Valve (RLV) and Spark Arrestor Unit (SAU) To achieve efficient purging the points where air enters and exits the PE should normally be at opposite ends of the PE. These items must be mounted vertically. The RLV or SAU are recommended to be situated at the bottom, or on the side of the enclosure at the bottom, when the CU is top mounted on the enclosure, thus achieving top to bottom purging. The purge air may be piped within the PE to ensure purging of potential dead air spots. It is important that the interior and exterior of the Spark Arrestor is kept clean and debris is not allowed to accumulate which might affect the calibration of the device. In particular the exterior of the Spark Arrestor should not be painted or blocked off in any way. 4.3 Connections to Protective Gas Supply The MiniPurge® system should be connected to a protective gas supply, which is suitable for purging and pressurization. The supply pipe connection to the MiniPurge® must be appropriate for the maximum input flow rate for the application. The air supply must be regulated at a pressure less than the maximum stated inlet pressure. The air supply must be clean, non-flammable and from a non-hazardous location. The air should be of Instrument Air Quality. Although the purge control system will operate with lower air quality, its operational life will be adversely affected. The equipment that is being protected by the MiniPurge® may also suffer because of poor air quality.

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With reference to BS ISO 8573-1: 2010, Instrument Air is typically specified as: Particle Class 1 In each cubic metre of compressed air, the particulate count should not exceed 20,000 particles in the 0.1 to 0.5 micron size range, 400 particles in the 0.5 to 1 micron size range and 10 particles in the 1 to 5 micron size range. Humidity or pressure dew point The dew point, at line pressure, shall be at least 10 °C below the minimum local recorded ambient temperature at the plant site. In no case, should the dew point at line pressure exceed +3 °C. Oil Class 2

In each cubic metre of compressed air, not more than 0.1mg of oil is allowed. This is a total level for liquid oil, oil aerosol and oil vapour. When an inert gas is being used to supply the purge system, risk of asphyxiation exists. Refer to Application Suitability section.

Before connection of the air supply to the purge system, the supply pipe work should be flushed through with instrument quality air to remove any debris that may remain in the pipes. This must be carried out for at least 10 seconds for every meter of supply pipe.

Unless a supply shut-off valve has been fitted to the MiniPurge® system, an external shut-off valve with the same, or larger, thread size as the Control Unit inlet fitting should be fitted by the installer to prevent any restriction of purge flow.

The purge air from the MiniPurge® Control Unit should be piped within the pressurized enclosure to ensure purging of potential dead air spots. The purge system is fitted with an internal regulator factory set to 3 bar feeding the logic. 4.4 Purge Air from CU to PE When the CU is mounted directly on the top of the PE, no connection will normally be necessary, as the purge air will discharge into the PE directly. When the CU is not mounted on the top of the PE, or where internal air distribution is necessary a connection should be made from the purge air outlet on the CU (normally ½” NPT Female), via pipe pressure rated at least to the supply pressure, to the PE. This should be kept as short as possible and should be adequately sized to ensure that the full purge flow can be delivered. 4.5 CU to Enclosure Pressure Monitor When the CU is mounted directly on the top of the PE, no connection will normally be necessary, as the enclosure pressure monitor point will sense directly inside the PE. If the CU is not mounted directly on the top of the PE or if there are fans, which may create localised low-pressure areas within the PE, it is necessary to pipe this connection. The connection is made to the enclosure pressure sensor fitting (normally 1/8” NPT Female) on the CU. There is virtually no flow in this circuit, so small bore tube may be used. Expo recommends 6mm O/D stainless steel tube. Make sure that all connections are free of leaks. 4.6 CU to Flow Sensor In Continuous Flow (CF) systems, a Differential Pressure Sensor is combined with the Minimum Pressure Sensor and measures the "DP HI (High) / Enclosure Pressure" within the PE and the

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pressure in the monitoring device at the back of the SAU "DP LO (Low) SAU Connection". This connection requires a pipe connection between the CU and the SAU40. In Leakage Compensation (LC) systems a dedicated Purge Flow Sensor measures the differential pressure between the "DP HI (High) / Enclosure Pressure" and the pressure in the monitoring device at the back of the RLV "DP LO (Low) RLV Connection". This connection requires a pipe to connect the CU to the RLV36. 4.7 Power Supplies and their Isolation All power entering the PE shall be provided with a means of isolation. This requirement also applies to any external power sources, which are connected to equipment such as "volt-free" or "dry" contacts within the PE. Printer signal, network cards, etc need isolation. Exception: Power to other apparatus that is already suitable for the hazardous area need not to

be isolated by the MiniPurge system.

In all cases the application and the isolation of the power must be controlled by the MiniPurge system. Refer to Specification Sheet for output options available. 4.8 Adjustments and Settings Purge Time If no specific purge test has been performed on the PE, the volume of the PE must be determined by the manufacturer or user and the necessary purging time calculated based on the purge flow rate specified by the “standard” being used. It is the user's responsibility to verify

or enter this data on the PE and/or MiniPurge system nameplate. Ask Expo if in doubt. The IEC / EN 60079-2 permit 5 volume changes and an example of the calculations is as follows:

If the PE external dimensions indicate an internal volume of 1000 Litres then, 1000 litres enclosure volume x 5 volume changes = 12 minutes purge time

450 litres/minute purge flow rate If the PE is a motor, experience of purge testing shows that it is prudent to multiply the motor internal "free” volume by ten to get the purging volume.

1000 litres enclosure volume x 10 volume changes = 23 minutes purge time 450 litres/minute purge flow rate

The following applies for NFPA 496 standards where 4 complete volume changes are permitted for enclosures except when the PE contains a motor when 10 volume changes are required.

If the PE external dimensions indicate a total volume of 40 cubic foot, then, 40 cubic foot enclosure volume x 4 volume changes = 10 minutes purge time

16 cubic foot/minute purge flow rate, (see above) If the same PE contains a motor, then,

40 cubic foot enclosure volume x 10 volume changes = 25 minutes purge time 16 cubic foot/minute purge flow rate, (see above)

The standard MiniPurge units have an electronic timer system as shown in Figure 8 MiniPurge Timer Selector Switches. The purge time is set by adjusting the Timer Selector Switches so that the time equals or exceeds the required purge time. If the time is set to ‘00’, the purge time will be indefinite.

Figure 8 MiniPurge Timer Selector Switches

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Purge Flow Rate (Orifice Size Selection) – Only for CF Systems The purge flow rate is selected by placing the appropriate orifice plate in the SAU. The purge flow rates given in Table 2 are based on standard setting of the flow sensor of 2.5mbar, 1” WC, 250Pa. For LC systems the purge flow rate is set by the selection of the RLV and is not user adjustable.

Orifice Plate Number

Continuous Flow Rate with 2.5 mbarg, 1” WC, 250 Pa flow sensor set point

N litre/minute SCFM

1 225 8 2 275 10 3 365 13 4 450 16

Table 2 Purge Flow Rates

Action on Loss of Pressurization The action on loss of pressurization is the responsibility of the user. The action on loss of pressurization can be set to ALARMS ONLY (AO), or ALARM AND AUTOMATIC DISCONNECT OF POWER (A&T). For both Leakage Compensation and Continuous Flow systems, the action on loss of pressurization is set by moving the jumper tube (see Figure 9 Action on Loss of Pressurization Jumper Tube). The standard setting is Alarm and Trip where the link is from C to A&T, with a plug in AO. Changing to Alarm Only (AO) is user adjustable by moving the link from C to AO, and plugging A&T.

Figure 9 Action on loss of pressurization jumper tube

The selection for action on loss of pressurization depends on the area of operation and the following guidelines should be followed. The user must make use of this alarm facility in accordance with the local code of practice for "action on pressure or flow failure". Most codes include the following recommendations: Zone 1 Installations: Alarm and automatic disconnect of power. Exception: If the equipment inside the PE is suitable for use in Zone 2, the power trip may be performed manually, (no automatic power trip), if the pressure or flow failure persists for an unacceptable time. Zone 2 Installations: Where automatic timing is preferred, Alarm Only on pressure or flow failure with power being

removed manually by turning off the air supply to the MiniPurge system if the failure persists for an unacceptable time. Class I Division 1 Installations: Alarm and Automatic Trip of Power. Note: NFPA 496 states power to the circuits shall be permitted to be continued for a short period if immediate loss of power would result in a more hazardous condition and if both audible and visual alarms are provided at a constantly attended location.

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Class I Division 2 Installations: Where automatic timing is preferred, Alarm Only on pressure or flow failure with power being

removed manually by turning off the air supply to the MiniPurge system if the failure persists for an unacceptable time. 4.9 Internal Gas Release If the PE contains an internal source of release of flammable gas or vapour, the procedures for assessment of the release as given in NFPA 496 or IEC / EN 60079-2 should be used. Expo is pleased to provide assistance or consultancy and advice on such matters. The user must verify that the specifications of the Expo system e.g. pressure, continuous flow (dilution) rate and type of protective gas are correct for the specific application. 4.10 Multiple Enclosures More than one PE can be protected by a single system. Where PE’s are connected and purged in "series" e.g. "Daisy Chained", the RLV and when using a CF system, the SAU40 should be fitted on the last enclosure with the Purge Inlet connected to the first enclosure. The bore and length of the pipe or conduit used to interconnect the enclosures is critical and will determine the maximum pressure experienced by the first enclosure in the series. Advice on sizing can be obtained from the Expo sales office but in general terms when using RLV36 or SAU40, the pipe

bore size should not be less than 36mm (1½”).

A common fault of installing small bore pipe leads to over pressurizing of all but the last enclosure. PE’s should not be connected in parallel.

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5. Commissioning

Start by checking that the system has been installed in accordance with this manual.

Disconnect the supply pipe from the inlet to the MiniPurge system and blow it through for at least 10 seconds per meter (3ft) of length to remove any debris or condensation. Connect a temporary pressure gauge or water manometer to

the PE or MiniPurge system pressure test point (Remove the red plug on the low pressure sensor and connect 4mm OD nylon tube).

Figure 20 PE or MiniPurge system pressure test point

Unless a supply shut-off valve has been specially fitted inside the MiniPurge system, it may be advisable to install an external shutoff valve with the same, or larger, thread size as the

MiniPurge CU inlet fitting upstream of the connection. 5.1 Continuous Flow (CF) Systems Open the Flow Control Valve (FCV) until the alarm/pressurized indicator just turns from red to green. Clockwise will reduce the flow and anti-clockwise will increase the airflow. If the FCV is opened fully and the indicator has still not turned green, check the air supply pressure at the inlet to the Control Unit while flow is taking place. It must be above the minimum 4 bar/ 60 psig/ 400kPa specified.

Check that the internal logic gauge reads 2bar /30 psig/200kPa. The electronic timer will start as soon as the ‘alarm/pressurized’ indicator turns from red (alarm) to green (pressurized). Check that the time delay between the indicator flashing yellow and the application of power to the PE is not less than the minimum time required to purge the PE. When the purge time has been completed, the ‘purge complete’ indicator will stop flashing. After the power has been turned on by the CU, the air flow will continue at the same rate to provide dilution as required.

Figure 11 Flow Control Valve (FCV)

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5.2 Leakage Compensation Systems (LC)

• Open the Leakage Compensation Valve (LCV) fully, turn anti-clockwise.

• Clockwise will reduce the flow and anti-clockwise will increase the airflow.

• Open the supply regulator SLOWLY and allow the PE pressure to rise until the RLV opens. Check that the RLV opens at or below the figure specified in the documentation.

• RLV tolerance +0, -20% of default setting.

• Repeat the test several times.

• Open the supply regulator to between 4 and 8 barg / 60 and 115 psi / 400 and 800 kPa and the purging flow will start.

• Check that the internal logic gauge reads 2 bar /30 psi / 200 kPa

Figure 12 Leakage Compensation Valve (LCV)

At this time the "alarm/pressurized” indicator should be green and the "purging” indicator should be flashing yellow. If the “purging” indicator remains black the flow through the RLV is below the minimum for which the flow sensor has been calibrated. Check the air supply pressure at the inlet to the Control Unit while purging is taking place. It must be above the minimum specified. The electronic purge timer will start as soon as the "purging" indicator starts flashing yellow. Check that the time delay between the “purging” indicator flashing yellow and the application of power to the PE is not less than the minimum time required purging the PE. Times in excess of the minimum are permitted. If the time is too short, it must be increased accordingly. After the power has been applied via the CU, the purging valve will close and the air flow into the enclosure will be controlled by the LCV. The initial setting of fully open will normally be too high. It should now be adjusted to set the PE pressure and leakage. There are three possible situations:

Air continues to come out through the RLV Spark Arrestor after power has been applied in considerable quantity. The LCV is much too far open, and the air flow is holding the RLV open continuously. Close the LCV slowly. The PE pressure will start to fall as the flow decreases but eventually the RLV will close and the enclosure pressure rise again. At this point the RLV may start to open intermittently as the PE pressure rises to the point where it exceeds the RLV opening pressure. When the RLV opens the pressure will fall quickly to the point where the RLV re-closes and the enclosure pressure starts to rise again. This is entirely normal for this type of RLV.

If the RLV is opening intermittently the LCV is slightly too far open. When the RLV opens, the enclosure pressure falls quickly to the point where the RLV re-closes and the enclosure pressure starts to rise again. This is entirely normal for this type of RLV and shows that it is working correctly. Continue then to close the LCV until the cycling stops and the enclosure pressure starts to fall. Carefully adjust the LCV until the PE pressure is approximately 50% of the RLV opening pressure and stable. This pressure may be around 5 mbarg / 2” WC / 500 Pa and will be the "normal working pressure".

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We recommend that the setting of the minimum pressure sensor be checked at this time. Note the position of the LCV knob. (A pencil mark placed on the knob at "12 O'clock” can be used). Slowly lower the PE pressure by closing the LCV further, counting the number of turns from the "normal working pressure" position. Note the pressure at which the "alarm/pressurized" indicator turns from green to red and check that it is not lower than the figure given in the documentation. Check also the "alarm" electrical contacts. As soon as the "alarm/pressurized" indicator turns red, the system will start to re-purge. If Alarm and Trip function is selected the enclosure power will be switched off. While it is re-purging return the LCV to its "normal working pressure" position so that, at the end of purging, the enclosure pressure should immediately settle down at the correct "normal" pressure.

If, at the end of purging, the PE pressure falls below the minimum pressure sensor setting and the LCV is fully open, the system will start to purge again. This is indicative of excessive leakage from the enclosure. In this case, check the enclosure for leakage, and reduce or eliminate the leaks. This time, at the end of purging, the enclosure should stay pressurized and the RLV action is as in a) or b) above. Proceed as described above.

5.3 Normal operation Turn the air supply on or off to start or stop the system. After this the pressurizing and purging sequence is entirely automatic

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6. Maintenance of the System

The maintenance recommended for the system consists of the following items, supplemented by any additional local requirements imposed by the local Code of Practice. Expo recommends that the commissioning tests be repeated at least every six to 24 months dependant on site conditions. In addition, the following checks are also recommended at that time:

• Check the RLV and all Spark Arrestors. Remove all debris & corrosion or replace with a spare.

• Check the condition of the air supply filter element. Clean or replace it as necessary.

At least every two years check the following additional items:

• Apparatus is suitable for the Hazardous Location

• There are no unauthorised modifications

• The air supply must be to the correct quality, refer to section Air Quality

• The interlocks and alarms function correctly

• Approval labels are legible and undamaged

• Adequate spares are carried

• The action on pressure failure is correct

The Intrinsically Safe Battery Pack should be changed at least every three years, and the commissioning tests repeated. After the timing phase has elapsed, the battery may be ‘hot-swapped’ in a hazardous environment without effecting the operation of the MiniPurge Ex px system. Recommended spares ETM-IS31-001 Intrinsically Safe Battery Pack Pressure Sensor calibration If it is decided that the minimum pressure /purge flow sensor needs recalibrating it must be returned to Expo for this service. Filter cleaning If the filter element needs cleaning the filter bowl can be unscrewed and removed. The filter element also unscrews and can then be cleaned in soapy water or replaced. Do not use solvents on any part of the filter assembly.

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7. Fault Finding

If the system does not behave in the manner described above, there is a fault. Some of the more likely faults are dealt with below. If a cure cannot be affected by following the procedure shown below, please call Expo (24 hour answering) or your supplier for further assistance. The system has been designed for ease of fault finding and the many of the components fitted are plug-in or manifold mounted. Check components by substitution only after establishing that such action is necessary. If the system is less than 12 months old, parts under warranty should be returned to Expo for investigation, with a full report of the fault and the system serial number. As with any pneumatic system the greatest enemies are water, oil and dirt in the air supply. For this reason, the air system must always incorporate a dust and water filter. This can be part of the Expo system or can be provided by others. However, dirt can enter from other sources and it is vital therefore that the procedures described in Section 2 is carried out before using the system for the first time or following any disconnection of the pipe-work. Failure to perform this work may cause damage that will not be covered under warranty. Before making the following checks verify that both the main air supply pressure to the purge system & the regulated pressure to the logic are as specified on the system specification sheet. Different flow charts for faulting have been provided for both the CF and LC options.

ML443 | v14 Page




Fault Finding (CF)

Is the PE strong enough?

Is the Pressure / Flow Sensor out of calibration or

faulty?

Pressurized indicator will not turn green or Purging

indicator will not flash yellow

Call Expo

Is the supply pipe to the air inlet as least 12mm I.D?

Is there excessive

leakage from the PE?

Is the air supply pressure incorrect?

No

Check the air supply pressure at the inlet to the MiniPurge is stable between 4 - 8 Barg / 60 - 115 psi

Yes

Replace pipe work

No

Yes

Any significant leakage must be corrected. Check for leaks down the cables or conduit. Ensure leakage does not exceed 250 Nl/min (9 scfm)

Yes

No

Yes

No

The standard requires that the PE is tested to 1.5 times the Relief Valve opening pressure e.g. 15 mbarg for many systems. Has this been done?

No

The basic operation of the Pressure Sensor can be checked by unscrewing the 60mm diameter diaphragm housing and, by using a rubber pad, e.g. an eraser, block the 12mm threaded hole in the top of the valve module. The valve should operate and the indicator turn green. If this is correct, the sensor diaphragm needs recalibrating or replacing.

Yes

ML443 | v14




E:[email protected]



For PO option only Is there pressure at the

power switch output bulkhead and at the power switch? Is the power switch OK?

Is the Purge time correct?

System fails to switch power on after the purge time has

elapsed.

Call Expo

Has the purge time completed

its course?

Is Power available?

No

Yes

Check the small indicator button

on the timer valve. When the valve has timed

out, it should return out when

depressed.

No

Yes

Yes

Check if the external Power Switch contacts close at 1.4 Barg

No

Note the timer setting. Reset the timer to the minimum available purging period and check

the operation on that purge time. Ensure that the purge time is returned to its original setting and checked before putting the system back into service.

No

For PO option only Is the tube to the power switch air

tight?

Ensure fitting nuts are tightened and that the tube is not damaged. Check and repair as necessary.

No

Yes

Yes

Is Power isolator closed?

No

Yes

Yes

Are the fuses or circuit breaker?

OK?

No

ML443 | v14 Page




Is the Pressurized Enclosure

pressure too high?

Is there debris on the RLV disk allowing air to leak from the

valve?

Relief Valve opens

continuously or intermittently.

Call Expo

Remove the RLV cover and clean the valve

disk. If it is necessary to remove the disk and spring from the RLV, draw a line around it with a pencil to allow accurate replacement

before removal, otherwise the opening

pressure may be affected.

The Flow Control Valve (FCV) is too far open.

Adjust the FCV clockwise to reduce the

PE pressure

No

Yes

No

Yes

ML443 | v14




E:[email protected]



Fault Finding (LC)

Is the actual PE pressure below

the setting of the Minimum

Pressure Sensor?

Is the Leakage Compensation

Valve setting too low causing the

MiniPurge to auto-repurge?

System purges correctly but the alarm comes on at the end of purge time and the purging cycle is

repeated.

Call Expo

Increase the PE pressure by turning the Leakage Compensation

Valve anti-clockwise.

Check the PE pressure with a manometer or

gauge.

Yes

No

Yes

No

Yes

ML443 | v14 Page




Is the tube between the RLV tapping and flow sensor air tight?

Is the PE strong enough?

Is the Purge Flow Sensor out of calibration or

faulty?

Purging indicator will not flash "Yellow" during

Purging.

Call Expo

Is the supply pipe to the air inlet as least 12mm I.D?

Is there excessive

leakage from the PE?

Is the air supply pressure incorrect?

No

Check the air supply pressure at the inlet to the MiniPurge is stable between 4 - 8 Barg / 60 - 115 psi

Yes

Replace pipe work

No

Yes

Any significant leakage must be corrected. Check for leaks down the cables or conduit. Ensure leakage does not exceed 250 Nl/min (9 cfm)

Yes

No

No

The standard requires that the PE is tested to 1.5 times the Relief Valve opening pressure e.g. 15 mbarg for many systems. Has this been done?

No

The operation of the Purge Flow Sensor can be checked by carefully removing the insulated female spade crimp terminals* on the underside of the hexagonal sensor. A wire link across them should operate the Electronic Timer and the ‘purging’ indicator flash yellow. If this is correct, the sensor diaphragm needs recalibrating or replacing, if not, replace the I.S. Battery Pack.

Yes


No

Yes

Yes

ML443 | v14




E:[email protected]



For PO option only Is there pressure at the

power switch output bulkhead and at the power switch? Is the power switch OK?

Is the Purge time correct?

System fails to switch power on after the purge time has

elapsed.

Call Expo

Has the purge time completed

its course?

Is Power available?

No

Yes Check the small indicator button on the timer valve. When the valve has timed out, it should return out when depressed.

No

Yes

Yes

Check if the external Power Switch contacts close at 1.4 Barg

No

Note the timer setting. Reset the timer to the minimum available purging period and check the operation on that purge time. Ensure that the purge time is returned to its original setting and checked before putting the system back into service.

No

For PO option only Is the tube to the power switch air

tight?


No

Yes

Yes

Is Power isolator closed?

No

Yes

Yes

Are the fuses or circuit breaker?

OK?

No

ML443 | v14 Page




Is the Pressurized Enclosure

pressure too high?

Is there debris on the RLV disk allowing air to leak from the

valve?

Relief Valve opens

continuously or intermittently.

Call Expo

Remove the RLV cover and clean the valve

disk. If it is necessary to remove the disk and spring from the RLV, draw a line around it with a pencil to allow accurate replacement

before removal, otherwise the opening

pressure may be affected.

The Leakage

Compensation Valve (LCV) is too far open.

Adjust the LCV clockwise to reduce the

PE pressure

No

Yes

No

Yes

ML443 | v14




E:[email protected]



8. Approval Documents

Certificates can be found in the accompanying booklet (ML499) or download the certificates at www.expoworldwide.com/downloads.

System Certificate Certificate Number

MiniPurge IECEx Certificate IECEx SIR 07.0027X

ATEX Certificate 01ATEX 1295X

INMETRO/TÜV TÜV 12.1462X

FM Certificate 1X8A4.AE

Electronic Timer IECEx Certificate FME 10.0001X

ATEX Certificate 10 ATEX0003X

For PA Option Only Certificate Certificate Number

Ex e junction box IECEx Certificate IECEx EXV 19.0057X

ATEX Certificate ExVeritas 19 ATEX0542X

Ex d switches IECEx Certificate IECEx EPS 14.0092X

ATEX Certificate EPS 14 ATEX 1 766 X

9. Glossary

Acronym Description

A&T Alarm and Trip

AO Alarm Only

CF Continuous Flow

CU Control Unit

FCV Flow Control Valve

FM Factory Mutual

IS Intrinsically Safe

LC Leakage Compensation

LCV Leakage Compensation Valve

MIU MiniPurge Interface Unit

PA Ex d Power and Alarm Switch Wired to Ex e terminal box

PE Pressurized Enclosure

PO Pneumatic Output

RLV Relief Valve

SAU Spark Arrestor Unit

UL Underwriter Laboratories

Min

iPur

ge

FLA

TNE

SS

TO

BE

LE

SS

TH

AN

0.4

mm

OV

ER

AN

Y 1

00m

m L

EN

GTH

UN

SP

EC

IFIE

DTO

LER

AN

CE

S

MA

TER

IAL

DR'W

N

APP'

D

CHK'

D

DR

AW

ING

STA

TUS

:A

PP

RO

VE

D:

MO

D. N

o:D

ATE

:

ISS

UE

:

3rd

AN

GLE

PR

OJE

CTI

ON

DIM

EN

SIO

NS

IN m

m

DO

NO

T S

CA

LE

Expo

Tec

hnol

ogie

s Li

mite

d

JOB

No:

FIN

ISH

TITL

E

CU

STO

ME

R:

SH

EE

T N

o.O

F

SU

RR

EY

TW

16 5

DB

UN

ITE

D K

ING

DO

M

DR

AW

ING

No.

SC

ALE

The

cont

ents

of t

his

draw

ing

/ doc

umen

t are

Cop

yrig

ht ã

Exp

o Te

chno

logi

es L

imite

d. T

hey

are

to b

e tre

ated

as

conf

iden

tial a

nd a

re re

turn

able

upon

requ

est.

The

y ar

e no

t to

be c

opie

d or

com

mun

icat

ed in

par

t or i

n w

hole

with

out w

ritte

n co

nsen

t fro

m E

xpo

Tech

nolo

gies

Lim

ited,

nei

ther

are

they

to b

e us

ed in

any

way

aga

inst

our

inte

rest

s.

NO

DE

C P

LAC

E ±

0.5

1 D

EC

PLA

CE

±0.

22

DE

C P

LAC

E ±

0.1

150

[5.9

1"]

102

[4.0

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240 [9.45"]

129

[5.0

8"]

270 [10.63"]MOUNTING BAR HOLES

12

NO

TES

MIN

IPU

RG

E M

UST

BE

MO

UN

TED

WIT

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URG

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UTL

ET

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VER

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E PO

INTI

NG

DO

WN

.

APP

RO

XIM

ATE

WEI

GH

T: 6

.1 k

g [1

3.3

lb].

EQU

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NT

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HO

WN

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REF

ER T

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-7TD

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R M

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AIL

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78 [

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90[3

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] LEAKAG

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(LC)

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(CF)

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AFT

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PU

RG

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ALA

RM

IND

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R 1

ALARM

RED

RED

RED

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GREEN

GREEN

GREEN

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EIN

DIC

ATO

R 2

PURGING

YELL

OW

YELL

OW

YELL

OW

PURGECOMPLETE

BLAC

K

BLAC

K

BLAC

K

IND

ICATO

RS

27.0

5 [1

.06"

] APP

RO

X.

1. 2. 3. 4.

20 [

0.79

"]

28 [1.10"]

95[3

.74"

]

IS O

PTIO

N:

HO

LE S

UIT

ABLE

FO

RG

LAN

D M

20 O

R 1

/2"

NPT

65 [2.56"]

95 [3.74"]

125 [4.92"]

162 [6.38"]

20 [

0.79

"]

42 [

1.65

"]

42 [

1.65

"]

SYS

TEM

BREA

THER

-D

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4-8

MAX b

arg

[60-

115

psi]

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F

74 [2.91"]

REM

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[7.0

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180 [7.09"]

240

[9.4

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290 [11.42"]

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PTF

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FOR M

6 O

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FIXIN

G(S

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M6

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STU

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ITH

PA O

PTIO

N)

PAO

PTIO

N

31 [1.22"]

8 [0.31"]

PA.

OPT

ION

:CU

STO

MER

TO

SIT

EAN

D D

RIL

L IN

PUT

GLA

ND

HO

LE

Min

iPur

ge

FLA

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SS

TO

BE

LE

SS

TH

AN

0.4

mm

OV

ER

AN

Y 1

00m

m L

EN

GTH

UN

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ISS

UE

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3rd

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PR

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s Li

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JOB

No:

FIN

ISH

TITL

E

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STO

ME

R:

SH

EE

T N

o.O

F

SU

RR

EY

TW

16 5

DB

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ITE

D K

ING

DO

M

DR

AW

ING

No.

SC

ALE

The

cont

ents

of t

his

draw

ing

/ doc

umen

t are

Cop

yrig

ht ã

Exp

o Te

chno

logi

es L

imite

d. T

hey

are

to b

e tre

ated

as

conf

iden

tial a

nd a

re re

turn

able

upon

requ

est.

The

y ar

e no

t to

be c

opie

d or

com

mun

icat

ed in

par

t or i

n w

hole

with

out w

ritte

n co

nsen

t fro

m E

xpo

Tech

nolo

gies

Lim

ited,

nei

ther

are

they

to b

e us

ed in

any

way

aga

inst

our

inte

rest

s.

NO

DE

C P

LAC

E ±

0.5

1 D

EC

PLA

CE

±0.

22

DE

C P

LAC

E ±

0.1

NO

TES

MIN

IPU

RG

E M

UST

BE

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UN

TED

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H P

URG

E O

UTL

ET

PIPE

IN

VER

TICAL

PLAN

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INTI

NG

DO

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.

APP

RO

XIM

ATE

WEI

GH

T: 6

.1 k

g [1

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RG

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OU

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DET

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1. 2. 3.8

INTE

RN

AL

STU

DS

M6

x 15

LO

NG

CU

TOU

T D

ETAIL

65 [2.56"]

95 [3.74"]

162 [6.38"]

240 [9.45"]

90[3

.54"

]

145

[5.7

1"]

42.5 [1.67"]

79.5 [3.13"]

96[3

.78"

]

= 30

0 [1

1.81

"] =

300 [11.81"]

8 H

OLE

S ø

7.5

TO S

UIT

INTE

RN

AL

STU

DS I

NCU

TOU

T D

ETAIL

= =

84[3

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]

45 [

1.77

"]

IND

ICATO

RS -

SEE

TABLE

ON

SH

EET

1

12

FILT

ER D

RAIN

1/8

" N

PTF

AIR

SU

PPLY

4 -

MAX 8

bar

g (6

0 -

115

psi)

1/2"

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F

SYS

TEM

BREA

THER

DO

NO

T O

BSTR

UCT

FLO

W S

WIT

CH

- L

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OPT

ION

ON

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8" N

PTF

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SU

RE

PRES

SU

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1/8"

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F

PURG

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ET1/

2" N

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2 CABLE

GLA

ND

HO

LES S

UIT

ABLE

FO

R M

20 O

R 1

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FO

R C

ON

NEC

TIO

N T

O R

EMO

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A B

OX.

FOR I

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OPT

ION

USE

LOW

ER H

OLE

ON

LY.

MIN

IPU

RG

E SU

PPLI

ED W

ITH

BO

TH H

OLE

S P

LUG

GED

.

= 276 [10.87"] =

= 254 [10.00"] =

= 172 [6.77"] =

= 2

54 [

10.0

0"]

=

= 1

72 [

6.77

"] =

= 2

76 [

10.8

7"]

=

PAN

EL M

OU

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NG

OPT

ION

PASSIV

E ALA

RM

/PRES

SU

RIZ

ED S

IGN

AL

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F

20 [

0.79

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FLA

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SS

TO

BE

LE

SS

TH

AN

0.4

mm

OV

ER

AN

Y 1

00m

m L

EN

GTH

UN

SP

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DTO

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S

MA

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DR'W

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:

ISS

UE

:

3rd

AN

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PR

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CTI

ON

DIM

EN

SIO

NS

IN m

m

DO

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CA

LE

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Tec

hnol

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s Li

mite

d

JOB

No:

FIN

ISH

TITL

E

CU

STO

ME

R:

SH

EE

T N

o.O

F

SU

RR

EY

TW

16 5

DB

UN

ITE

D K

ING

DO

M

DR

AW

ING

No.

SC

ALE

The

cont

ents

of t

his

draw

ing

/ doc

umen

t are

Cop

yrig

ht ã

Exp

o Te

chno

logi

es L

imite

d. T

hey

are

to b

e tre

ated

as

conf

iden

tial a

nd a

re re

turn

able

upon

requ

est.

The

y ar

e no

t to

be c

opie

d or

com

mun

icat

ed in

par

t or i

n w

hole

with

out w

ritte

n co

nsen

t fro

m E

xpo

Tech

nolo

gies

Lim

ited,

nei

ther

are

they

to b

e us

ed in

any

way

aga

inst

our

inte

rest

s.

NO

DE

C P

LAC

E ±

0.5

1 D

EC

PLA

CE

±0.

22

DE

C P

LAC

E ±

0.1

15

2614

19

22161

213

187

MIN

IMU

M P

RES

SU

RE

SEN

SO

R

"OR"

GATE

LEAKAG

E CO

MPE

NSATI

ON

VALV

E

PURG

E BO

OST

VALV

E

PLU

G 4

mm

(EN

CLO

SU

RE

PRES

SU

RE

TEST

POIN

T)

PURG

E CO

MPL

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E

LOG

IC A

IR S

UPP

LY R

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LATO

R

ELEC

TRO

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ER

BLA

CK C

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AR (

PLU

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ED)

IND

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SU

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IND

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ING

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PURG

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OW

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R

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1

MAIN

AIR

SU

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TER,

AU

TOM

ATI

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RAIN

15

TIM

ER V

ALV

E

19 22 2616 17 1814

ALA

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LY P

USH

-IN

FIT

TIN

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AN

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PU

SH

-IN

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TIN

G

PURG

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WIT

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ES

"ACTI

ON

ON

ALA

RM

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PTIO

N P

IPE

34 763533

123

3335

34

ENCLO

SU

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PRES

SU

RE

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POIN

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ON

PO

OPT

ION

SH

OW

N (

ITEM

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OTT

EDREM

OVED

FO

R C

F AN

D I

TEM

13

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LACED

BY

TIM

ER S

WIT

CH

)

26

17

INTE

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AL

CO

MPO

NEN

TS

I.S.

BATT

ERY

PACK

13

76

8

FLA

TNE

SS

TO

BE

LE

SS

TH

AN

0.4

mm

OV

ER

AN

Y 1

00m

m L

EN

GTH

UN

SP

EC

IFIE

DTO

LER

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CE

S

MA

TER

IAL

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The c

onte

nts

of

this

dra

win

g /

docum

ent

are

Copyright

E

xpo T

echnolo

gie

s L

imited.

They a

re t

o b

e t

reate

d a

s c

onfidential and a

re r

etu

rnable

upon r

equest.

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re n

ot

to b

e c

opie

d o

r com

munic

ate

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art

or

in w

hole

without

written c

onsent

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Expo T

echnolo

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o b

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= 1

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= 1

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= 2

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68

[2.68"]

AC

D

A

68

[2.68"]

= 150 [5.91"] =

= =

62

[2.44"]

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= =

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3 [9

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EN

CL

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UR

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RO

NT

10 [0.39"]

= 1

60

[6

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= 1

93

[7

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36

0 [

14

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10.5 [0.41"]

68

[2.68"]

D

BAA

= 150 [5.91"] =

CA

62

[2.44"]

68

[2.68"]

CU

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UT

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IZE

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NC

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= 150 [5.91"] =

68

[2.68"]

BA

= =

= =

62

[2.44"]

A

38

[1

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"]

5 [0.20"]

10 [0.41"]

= =

= =

= =

= =

= =

DE

SC

RIP

TIO

N

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Ø

7.5

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ALE

The c

onte

nts

of

this

dra

win

g /

docum

ent

are

Copyright

E

xpo T

echnolo

gie

s L

imited.

They a

re t

o b

e t

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s c

onfidential and a

re r

etu

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They a

re n

ot

to b

e c

opie

d o

r com

munic

ate

d in p

art

or

in w

hole

without

written c

onsent

from

Expo T

echnolo

gie

s L

imited,

neither

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o b

e u

sed in a

ny w

ay a

gain

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our

inte

rests

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NO

DE

C P

LA

CE

±0.5

1 D

EC

PL

AC

E ±

0.2

2 D

EC

PL

AC

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275 [10.83"]

= 210 [8.27"] =

NO

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EN

CL

OS

UR

E M

OU

NT

ING

EIT

HE

R T

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4 x

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4 x

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G W

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L B

AR

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18

0 [7

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12

5 [4

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DE

TA

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LL

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365 [14.37"]

= 390 [15.35"] WALL BARS =

305 [12.01"]

= 270 [10.63"] WALL BARS =

15

0 [5

.91

"]

22

5 [8

.86

"]

18

8 [7

.40

"]

15

5 [6

.10

"]

30

0 [

11

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13

2 [5

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18

0 [7

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90

[3

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DE

TA

IL 'F

'

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LL

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= 180 [7.09"] =

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DE

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LO

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.

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4 H

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INT

35

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[7/8

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48

[1

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NO

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E M

OU

NT

ING

EIT

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R T

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4 x

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"] H

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4 x

M6

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UD

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G W

AL

L B

AR

S

NO

TE

EN

CL

OS

UR

E M

OU

NT

ING

EIT

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R T

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4 x

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4 x

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G W

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4 W

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x 1

6 L

ON

G F

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HO

LE

S IN

WA

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Ø7.5

[9/3

2"]

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EL

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M6

x 1

6 L

ON

G F

OR

WA

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HO

LE

S IN

WA

LL

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RS

Ø7.5

[9/3

2"]

2 H

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ES

Ø14 [

9/1

6"]

HO

LE

Ø2

2.5

[7

/8"]

2 H

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ES

Ø1

4 [9

/16

"]

2 H

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ES

Ø1

4 [9

/16

"]

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LE

Ø22.5

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"]

150 [5.91"]

FLA

TN

ES

S T

O B

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S T

HA

N 0

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m O

VE

R A

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100m

m L

EN

GT

H

UN

SP

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TO

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L

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US

:

AP

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:

MO

D.

No:

DA

TE

:

ISS

UE

:

3rd

AN

GLE

PR

OJE

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ION

DIM

EN

SIO

NS

IN

mm

DO

NO

T S

CA

LE

Exp

o T

ech

no

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ies

Lim

ited

JO

B N

o:

FIN

ISH

TIT

LE

CU

ST

OM

ER

:S

HE

ET

No

.O

F

SU

RR

EY

K

T7 0

RH

UN

ITE

D K

ING

DO

M

DR

AW

ING

No

.

SC

ALE

The c

onte

nts

of

this

dra

win

g /

docum

ent

are

Copyright

E

xpo T

echnolo

gie

s L

imited.

They a

re t

o b

e t

reate

d a

s c

onfidential and a

re r

etu

rnable

upon r

equest.

They a

re n

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e c

opie

d o

r com

munic

ate

d in p

art

or

in w

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without

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onsent

from

Expo T

echnolo

gie

s L

imited,

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o b

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sed in a

ny w

ay a

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our

inte

rests

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NO

DE

C P

LA

CE

±0.5

1 D

EC

PL

AC

E ±

0.2

2 D

EC

PL

AC

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= 2

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1 1

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CU

TO

UT

=

= 3

20

[1

2 1

9/3

2"]

PA

NE

L O

UT

LIN

E =

= 120 [4 23/32"] =

= 225 [8 27/32"] =

= 1

70

[6

11

/16

"] =

= 3

05

[1

2"]

=

= 210 [8 9/32"] CUTOUT =

= 240 [9 7/16"] PANEL OUTLINE =

DE

TA

IL 'A

'

PA

NE

L M

OU

NT

SIZ

E 1

8 O

FF

HO

LE

S Ø

7.5

[9/3

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= 290 [11 13/32"] PANEL OUTLINE =

= 254 [10"] CUTOUT =

= 276 [10 7/8"] =

= 172 [6 25/32"] =

= 2

76

[1

0 7

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=

= 1

72

[6

25

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= 2

90

[1

1 1

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PA

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UT

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= 2

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[1

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TO

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8 O

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5 L

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:

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3rd

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88 [

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T Y

133

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170

[6.6

9"]

185

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DEP

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28 [

1.10

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33 [

1.30

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37 [

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RLV

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52

MIN

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= =

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=

= 64 [2.52"] =

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= 76

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3"]

=

46 [1.81"]

133 [5.24"]

= =

62 [

2.44

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RLV OU

TLIN

E

= 88

[3.

46"]

=

=

10

9 [4

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] =

56 [2.2"]

170 [6.69"]

65 [2.56"]

185 [7.28"]

RLV OU

TLIN

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[This Page Intentionally Left Blank]

Expo Technologies USAExpo Technologies Inc.

9140 Ravenna Road Unit #3Twinsburg,

OH 440878, USAT: +1 440 247 5314F: +1 330 487 0611


Expo Technologies UKExpo Technologies Ltd.

Unit 2 The Summit, Hanworth RoadSunbury-On-Thames,

TW16 5DB, UKT: +44 20 8398 8011F: +44 20 8398 8014


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329 Huashan Er LuJimo City, Qingdao,

266200 ChinaT: +86 532 8906 9858F: +86 532 8906 9858


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