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CONDENSATE LEVEL SWITCHES
FOR STEAM SERVICE

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Situation: A steam condensate level switch operates only occasionally; usually when a control system component (valve, D/P cell, computer, etc.) has failed. It is the last line of defense against a catastrophic failure such as a steam explosion, burnout, turbine damage, etc. It must always work reliably.

Solution: A device of the simplest design, which has the longest history of no-failure reliability, will be the best choice. Delta Controls’ Series 700 mechanical float and displacer actuated level switches fit the description and are the best choice for these applications. They have been in worldwide steam condensate service for over 25 years without a failure.

You must select the proper sensing element and body to insure that the inherent reliability is achieved. The basis and rules for hardware selection follow.

Saturated condition is defined as when the steam liquid and vapor phases are in equilibrium and neither condensation nor evaporation is occurring. There is a corresponding temperature at which saturation conditions occur for every specific pressure reading.

The density of the steam vapor varies with the pressure and becomes a significant factor at 650 PSIG and higher. The weight of the vapor pushes down while the weight of the condensate pushes up on the sensing element. The actual net SPG lifting the element is the SPG of the condensate minus the SPG of the vapor. This value must be equal to or higher than the "MIN SPG" spec for the sensing element selected.

It is possible to "superheat" the vapor to a higher than saturation temperature at the system pressure. In this case, the density of the vapor is lower than it is at saturation conditions. The minimum SPG difference will always occur at saturated conditions; therefore the sensing device will see a higher net SPG under superheated conditions and will continue to work reliably at higher temperatures.

The rule is: Size the sensing element (float or Displacer) for saturated conditions at the highest working pressure; Be sure that it will also physically contain the highest temperature and maximum pressure to be encountered in the applications. Contact Shreveport Engineering for any Application Assistance that you may need, or with any questions that you may have.

The table below shows the density in terms of SPG, which is based on the density of water at 77° F (25° C) and 1 atmosphere (standard temperature and pressure reference conditions) Linear interpolation for pressures other than the steam / condensate saturation conditions shown will be adequate in most cases.

Saturated Steam Conditions

SPG @ Saturation

Saturated

SPG @ Saturation

PSIG

°F

Bar

°C

Liq

Vap

Net

PSIG

° F

Bar

°C

Liq

Vap

Net

15

250

1.0

122

0.944

0.001

0.941

750

512

51.7

267

0.773

0.027

0.746

50

298

3.4

149

0.918

0.002

0.916

850

527

58.6

275

0.758

0.030

0.728

100

358

6.9

171

0.896

0.004

0.892

900

534

62.1

279

0.751

0.033

0.718

125

353

8.6

179

0.888

0.005

0.883

1000

545

69.0

285

0.741

0.036

0.705

150

366

10.3

187

0.880

0.005

0.874

1250

572

86.2

300

0.711

0.046

0.665

250

406

17.2

209

0.854

0.009

0.845

1500

596

103.4

313

0.681

0.058

0.623

400

447

27.6

232

0.825

0.014

0.811

1750

617

120.7

381

0.656

0.072

0.583

450

459

37.0

238

0.816

0.016

0.800

1800

621

124.1

327

0.647

0.073

0.573

500

471

34.5

244

0.808

0.018

0.790

2000

636

137.9

336

0.622

0.085

0.537

550

479

40.0

248

0.800

0.019

0.781

2250

652

155.2

344

0.597

0.098

0.499

600

490

41.4

254

0.792

0.022

0.771

2500

668

172.4

353

0.557

0.122

0.435

650

497

44.8

258

0.784

0.023

0.761

2750

682

190.0

361

0.516

0.147

0.369

700

506

48.3

263

0.777

0.025

0.746

3000

695

207.0

368

0.462

0.186

0.276

3135

703

216.0

373

0.393

0.212

0.181

@ 3191.5 PSIG (220 Bar) and 705.4° F (374.1° C); both liquid and vapor = 0.3181 SPG density units and have the same density, which is 19.84 lbs/ft3 (318.1Kg/M3)


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