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80 barg Max Pressure475 °C Max TempInline Replaceable ModuleAir-Jacketed

TLV HR80A Thermodynamic Steam Trap, 80 barg

TLV HR80A alloy steel thermodynamic disc trap with thermostatic air venting. Features an air jacket, inline replaceable module, and handles up to 80 barg and 475 °C.

TLV HR80A Thermodynamic Steam Trap, 80 barg

TLV HR80A is an alloy steel thermodynamic disc trap with thermostatic air venting, designed for the drainage of high-pressure and high-temperature steam mains and turbines. It features an air-jacketed design that reduces radiant heat loss, minimizing no-load cycling and extending the service life of the trap. The HR80A operates within a pressure range of 0.8 to 80 barg (0.08 to 8.0 MPaG) and can handle maximum operating temperatures up to 475 °C.

The trap incorporates an inline replaceable valve module for ease of maintenance and lower repair costs. A bimetal ring provides quick thermostatic air venting for fast start-up and the elimination of air binding.

Related Models

The TLV HR-A series also includes the HR150A (up to 150 barg) and HR260A (up to 260 barg, suitable for supercritical steam). This page focuses on the HR80A specifications.

Features

  1. Inline replaceable valve module for ease of maintenance and low cost of repair.
  2. Lapped disc provides a steam-tight seal.
  3. Air jacket reduces radiant heat loss to reduce no-load cycling and extend life.
  4. Quick thermostatic air venting with bimetal ring for fast start-up and elimination of air binding.
  5. Built-in screen with large surface area for extended trouble-free operation.
  6. Hardened working surfaces guarantee long service life.

Specifications

ConnectionSocket WeldedButt WeldedFlanged
SizeDN 15, 20, 25DN 15, 25DN 15, 20, 25
Maximum Operating Pressure (PMO)80 barg80 barg80 barg
Minimum Operating Pressure8 barg8 barg8 barg
Maximum Operating Temperature (TMO)475 °C475 °C475 °C
Maximum Allowable Pressure (PMA)102 barg @ 40 °C102 barg @ 40 °C102 barg @ 40 °C
Maximum Allowable Temperature (TMA)550 °C @ 31 barg550 °C @ 31 barg550 °C @ 31 barg
Maximum Back Pressure50% of Inlet Pressure50% of Inlet Pressure50% of Inlet Pressure

WARNING

Maximum allowable pressure (PMA) and maximum allowable temperature (TMA) 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.

TLV HR80A pressure and temperature rating graph

Configuration and Parts

TLV HR80A cross-section configuration and parts diagram

No.DescriptionMaterialDINASTM/AISI
1BodyAlloy Steel A182 F22 Cl.31.7380A182 F22 Cl.3
2CoverStainless Steel SUS4031.4000AISI403
3Module Valve SeatStainless Steel SUS440C1.4125AISI440C
4DiscStainless Steel SUS440C1.4125AISI440C
5Air Vent RingBimetal--
6Disc Holder RingStainless Steel SUS6301.4542AISI630
7Module Gasket (large)Graphite/Stainless Steel-/1.4833-/AISI309S+Cb
8Module Gasket (small)Graphite/Stainless Steel-/1.4833-/AISI309S+Cb
9Screen inside/outsideStainless Steel SUS430/3041.4016/1.4301AISI430/304
10Cover BoltAlloy Steel SNB161.7711A193 Gr.B16
11NameplateStainless Steel SUS3041.4301AISI304
12CapStainless Steel SUS3041.4301AISI304
13Set ScrewStainless Steel SUS3041.4301AISI304
14Guide PinStainless Steel SUS3041.4301AISI304

Dimensions

Socket Welded

TLV HR80A socket welded dimensions diagram

DNL (mm)H (mm)H1 (mm)φD (mm)φC (mm)h (mm)Weight (kg)
15110115904821.8143.9
20110115904827.2143.8
25110115904833.9143.7
(ASME B16.11-2005, other standards available)

Butt Welded

TLV HR80A butt welded dimensions diagram

DNL (mm)H (mm)H1 (mm)φD (mm)φd (mm)h (mm)Weight (kg)
15110115902217203.8
25110115903428203.8
(DIN 3239 Form C (PN 100), other standards available)

Flanged

TLV HR80A flanged dimensions diagram

DNL (150RF)L (300RF)L (600RF)L (900RF)H (mm)H1 (mm)Weight* (kg)
15180180180210150909.6
201901901902201509011
252202202202301509014
Weight is for Class 900RF.

Discharge Capacity

TLV HR80A discharge capacity chart

  1. Differential pressure is the difference between the inlet and outlet pressure of the trap.
  2. Recommended safety factor: at least 2.

Installation and Piping Arrangement

  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. 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.
  3. Support the pipes properly within 800 mm (2.5 ft) on either side of the trap.
  4. Install a bypass valve to discharge condensate, and inlet and outlet valves to isolate the trap in the event of trap failure or maintenance.
  5. Install a check valve at the trap outlet whenever more than one trap is connected to the condensate collection pipeline.
  6. 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).

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.

Inspection and Maintenance

Operational inspections should be performed at least twice per year, or as called for by trap operating conditions.

PartInspection Procedure
Sealing surfacesCheck for damage or dirt on the sealing surfaces
ScreenCheck for clogging or corrosion damage
Bimetal ringCheck for rust, scale, oil film, warping or damage
Disc holderCheck for rust, scale, oil film, warping or damage
DiscCheck for wear and damage, scratches, on the surface where it contacts the valve seat, and dirt or oil film
Module valve seatCheck discharge channel and grooves for rust and scale inside
Body, CoverCheck inside for erosion, dirt, grease, rust or scale

Troubleshooting

ProblemCauseRemedy
No condensate is discharged (blocked) or discharge is poorScreen is clogged with rust or scaleClean
Air vent ring (bimetal) is broken or worn, causing air-bindingReplace air vent ring
Disc holder ring is broken or worn, causing air-bindingReplace disc holder ring
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
Air vent ring (bimetal) or disc holder ring is broken, obstructing valve closureReplace air vent ring or disc holder ring
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 damaged or openReplace or close bypass valve
Cover is loose or module gaskets are damagedTighten cover or replace module gaskets