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Free FloatThermostatic Air VentInline RepairableCast Steel

TLV JH7.2R-X Free Float Steam Trap

TLV JH7.2R-X and JH7.2R-B free float steam traps with thermostatic air venting. Cast steel construction for medium-size and high-pressure process equipment, handling pressures up to 46 barg and temperatures up to 425°C.

TLV JH7.2R-X Free Float Steam Trap

TLV JH7.2R-X and JH7.2R-B are reliable and durable cast steel free float steam traps designed for use on medium-size process equipment. The JH7.2R-B model is also suitable for high-pressure process applications. These inline repairable steam traps discharge condensate continuously and automatically at a temperature slightly lower than the saturation temperature.

TLV JH7.2R-X Free Float Steam Trap Features

Features

  • Self-modulating free float provides continuous, smooth, low-velocity condensate discharge as process loads vary.
  • Constant water seal design ensures a steam-tight seal, even under low-load conditions.
  • JH7.2R-X: Thermostatic capsule (X-element) with “fail open” feature vents air automatically at close-to-steam temperature.
  • JH7.2R-B: Thermostatic bimetal air vent valve vents air automatically for rapid startup.
  • Built-in screen with large surface area ensures extended trouble-free operation.
  • Easy, inline access to internal parts simplifies cleaning and reduces maintenance costs.

Specifications

WARNING

Maximum allowable pressure (PMA) is 46 barg and maximum allowable temperature (TMA) is 400 °C / 425 °C. These are PRESSURE SHELL DESIGN CONDITIONS, NOT OPERATING CONDITIONS. To avoid abnormal operation, accidents or serious injury, DO NOT use this product outside of the specification range.

ModelJH7.2R-XJH7.2R-B
ConnectionSocket Welded, FlangedSocket Welded, Flanged
SizeDN 40, 50DN 40, 50
Orifice No.2, 5, 10, 14, 22, 322, 5, 10, 14, 22, 32, 40, 46
Maximum Operating Pressure (PMO)2, 5, 10, 14, 22, 32 barg2, 5, 10, 14, 22, 32, 40, 46 barg
Maximum Differential Pressure (ΔPMX)2, 5, 10, 14, 22, 32 bar2, 5, 10, 14, 22, 32, 40, 46 bar
Maximum Operating Temperature (TMO)240 °C400 °C / 425 °C*
Type of Air VentX-element (6 °C subcooling)Bimetal (vents air up to approx. 100 °C)

* With PN flange

Materials

TLV JH7.2R-X Materials

No.DescriptionMaterialDINASTM/AISI
1BodyCast Steel A216 Gr.WCB1.0619
2CoverCarbon Steel A1051.0460
3FloatStainless Steel SUS316L1.4404AISI316L
5Orifice GasketSoft Iron SUYP1.1121AISI1010
6Orifice PlugCast Stainless Steel A351 Gr.CF81.4312
8Screen inside/outsideStainless Steel SUS430/3041.4016/1.4301AISI430/304

Dimensions

Socket Welded

TLV JH7.2R-X Socket Welded Dimensions

DNL (mm)H (mm)H1 (mm)W (mm)h (mm)Weight (kg)
404013202442501335
504013202442501638

Flanged

TLV JH7.2R-X Flanged Dimensions

DNL (DIN PN25/40)L (ASME 150RF)L (ASME 300RF)L (ASME 600RF)HH1WWeight (kg)
4040740641342932024425035
5041141041643532024425040

Discharge Capacity

JH7.2R-XTLV JH7.2R-X Discharge Capacity

JH7.2R-BTLV JH7.2R-X TLV JH7.2R-B Discharge Capacity

INFO

  1. Line numbers within the graph are orifice numbers.
  2. Differential pressure is the difference between the inlet and outlet pressure of the trap.
  3. Capacities are based on continuous discharge of condensate 6 °C below saturated steam temperature.
  4. Recommended safety factor: at least 1.5.

Safety Considerations

DANGER

NEVER apply direct heat to the float. The float may explode due to increased internal pressure, causing accidents leading to serious injury or damage to property and equipment.

Proper Installation

  1. Before installation, be sure to remove all protective seals.
  2. Before installing the trap, blow out the inlet piping to remove all dirt and oil.
  3. When hoisting the product, hang the rope around the inlet/outlet as close to the body as possible.
  4. Install the steam trap within the allowable inclination and make sure that the arrow mark on the body corresponds with the direction of flow.
  5. 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.
  6. Support the pipes properly within 800 mm on either side of the trap.
  7. Install a bypass valve to discharge condensate, and inlet and outlet valves to isolate the trap in the event of trap failure or when performing maintenance.
  8. Install a check valve at the trap outlet whenever more than one trap is connected to the condensate collection pipeline.
  9. The use of unions is recommended 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:

  • Is the pipe diameter suitable? (Install a catchpot with the proper diameter. Make sure the flow of condensate is not obstructed.)
  • Has the trap been installed within the allowable inclination and with the arrow on the body pointing in the direction of flow?
  • Has sufficient space been secured for maintenance?
  • Have maintenance valves been installed at the inlet and outlet? If the outlet is subject to back pressure, has a check valve been installed?
  • To prevent rust and scale from flowing into the trap, connect the inlet pipe 25 - 50 mm above the base of the T - pipe.
  • When installing on the blind end, make sure nothing obstructs the flow of condensate.

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
Body, Cover(s)Check inside for damage, dirt, grease, oil film, rust or scale
GasketsCheck for warping or damage
X-elementCheck for damage
Screen(s)Check for clogging, corrosion or damage
FloatCheck for deformation, damage, oil film or water inside
Air Vent Valve Seat, OrificeCheck for rust, scale, oil film, wear or damage

Troubleshooting

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

ProblemCauseRemedy
No condensate is discharged (blocked) or discharge is poorFloat is damaged or filled with condensateReplace the float
Orifice, screen or piping are clogged with rust or scaleClean
X-element is damagedReplace the X-element
The trap operating pressure exceeds the maximum specified pressure, or there is insufficient pressure differentialCompare specifications and actual operating conditions
Steam locking has occurredBlowdown through the bypass or close the trap inlet valve and allow the trap to cool
Steam is discharged or leaks from the trap outlet (blowing / steam leakage)Rust and scale have accumulated around the orifice or under the floatClean
Orifice is damagedReplace with new orifice
Float is deformed or coated with scaleClean or replace the float
Trap is installed above the maximum allowable inclination angleCorrect the installation
Vibration of trap occursLengthen inlet piping, then fasten it securely
The X-element is damaged, or clogged with rust or scale.Clean or replace the X-element
Steam leaks from a place other than the trap outletDeterioration of or damage to gasketsReplace the gaskets
Leakage from eroded cavities of body or coverReplace the trap
Improper tightening torque for cover was usedTighten to the proper torque
Float is frequently damagedWater hammer occursExamine the piping for problems that can cause water hammer