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High PressureAlloy Steel

TLV HR150A Thermodynamic Steam Trap

TLV HR150A thermodynamic steam trap for high pressures. Suitable for small or medium capacity drainage of high pressure and temperature steam mains and turbines.

TLV HR150A Thermodynamic Steam Trap

TLV HR150A thermodynamic steam trap for high pressures can be used without adjustment for small or medium capacity applications such as the drainage of high pressure and temperature steam mains and turbines.

Configuration

TLV HR150A configuration cross section

No.DescriptionNo.Description
1Body11Nameplate (not shown)
2Cover12Cap
3Module Valve Seat13Set Screw (not shown)
4Disc14Guide Pin
5Air Vent Ring15Flange
6Disc Holder Ring16Cover Nut
7Module Gasket (large)17Hexagon Nut
8Module Gasket (small)18Eye Nut
9Screen19Spacer
10Cover Bolt

Specifications

  • Minimum Operating Pressure: 1.6 MPaG (230 psig)
  • Maximum Allowable Back Pressure: 50% of inlet pressure

WARNING

Maximum allowable pressure (PMA) and maximum allowable temperature (TMA) are PRESSURE SHELL DESIGN CONDITIONS, NOT OPERATING CONDITIONS. To avoid malfunctions, product damage, accidents or serious injury install properly and DO NOT use this product outside the specification range.

Proper Installation

  1. The trap can be installed either horizontally or vertically, but make sure the arrow on the trap points in the direction of flow.
  2. Before installation, be sure to remove all protective seals.
  3. Before installing the trap, blow out the inlet piping to remove all dirt and oil.
  4. Install the trap in the lowest part of the pipeline or equipment so the condensate flows naturally into the trap by gravity. The inlet pipe should be as short and have as few bends as possible.
  5. Support the pipes properly within 800 mm (2.5 ft) on either side of the trap.
  6. Install a bypass valve to discharge condensate, and inlet and outlet valves to isolate the trap in the event of trap failure or maintenance.
  7. Install a check valve at the trap outlet whenever more than one trap is connected to the condensate collection pipeline.
  8. In order to avoid excessive back pressure, make sure the discharge pipes are large enough; (the outlet back pressure allowance should be no more than 50% of the inlet steam pressure).
  9. We recommend unions to facilitate connection and disconnection of screwed models.

Piping Arrangement

Check to make sure that the pipes connected to the trap have been installed properly.

  1. Is the pipe diameter suitable?
  2. Has sufficient space been secured for maintenance?
  3. Have maintenance valves been installed at inlet and outlet? If the outlet is subject to back pressure, has a check valve been installed?
  4. Is the inlet pipe as short as possible, with as few bends as possible, and installed so that the condensate will flow naturally down into the trap?

Start-up Procedure

IMPORTANT START-UP PROCEDURE

To ensure proper operation, slowly open the inlet valve slightly. Initially OPEN THE VALVE ONLY 1/32 TURN in order to supply steam to the trap very slowly, then WAIT FOR AT LEAST 30 SECONDS for air to vent before fully opening the inlet valve.

Operational Check

A visual inspection can be carried out to aid in determining the necessity for immediate maintenance or repair, if the trap is open to atmosphere.

StateDescription
NormalCondensate is discharged in a short blast followed by a longer period of no drainage. During the discharge, flash steam may be seen. A small amount of flash steam may be visible after the discharge.
BlockedNo condensate is discharged. The trap is quiet and makes no noise. The surface temperature of the trap is low.
BlowingLive steam continually flows from the outlet, and there is a continuous metallic sound.
Steam LeakageLive steam is discharged through the trap outlet together with condensate, accompanied by a high-pitched sound.
ChatteringThe trap does not close properly. Steam is discharged from the trap in short rapid bursts.

Inspection and Maintenance

Operational inspections should be performed at least twice per year, or as called for by trap operating conditions. Steam trap failure may result in temperature drop in the equipment, poor product quality or losses due to steam leakage.

Parts Inspection Procedure:

  • Sealing surfaces: Check for damage or dirt on the sealing surfaces
  • Screen: Check for clogging or corrosion damage
  • Disc: Check for wear and damage, scratches, on the surface where it contacts the valve seat, and dirt or oil film
  • Module valve seat: Check discharge channel and grooves for rust and scale inside
  • Body, Cover: Check inside for erosion, dirt, grease, rust or scale

Troubleshooting

If the expected performance is unachievable after installation of the trap, check the following points for appropriate corrective measures.

ProblemCauseRemedy
No condensate is discharged (blocked) or discharge is poorScreen is clogged with rust or scaleClean
Disc is sticking to valve seat (due to oil, etc.)Clean
Steam-locking has occurredPerform a bypass blow-down, or close the trap inlet valve and allow the trap to cool. Piping correction may also be required.
Trap capacity is insufficientChange to trap of suitable capacity
Differential pressure is lowStudy inlet/outlet pressure, including rise in outlet pipe
Steam leakage or blowing (from valve seat)Valve closure is obstructed by scale, etc.Clean or replace screen
Disc or valve seat is wornReplace worn parts
Back pressure exceeds allowable valueUse within pressure range
Trap is being used below minimum operating pressureUse within pressure range
Disc is sticking to top of cover (due to oil, etc.)Clean
Valve chattering (Leakage)Foreign matter or oil film on disc or valve seatClean
Scratches on disc or valve seatReplace disc or module valve seat
Disc or valve seat is wornReplace disc or module valve seat
Leakage from a location other than valve seatBypass valve is broken or openReplace or close bypass valve
Cover is loose or module gasket is damagedTighten cover or replace module gasket