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Air Solubility in Water

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20/03/13 Air Solubility in Water

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Air Solubility in Water

Amount of air that can be dissolved in water - decrease with temperature - increase withpressure

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The amount of air that can be dissolved in water increase with the system pressure and decrease with thetemperature.

Deaeration

When fresh water is heated up, air bubbles start to form. The water can obviously not hold the dissolved air with

increasing temperature. At 100 oC (212 oF) water starts to boil - the bubbles are formed by evaporated water orsteam. If the water is cooled down and then again reheated, bubbles will not appear until the water starts to boil.The water is deaerated.

Solubility Ratio

The solubility of air in water can be expressed as a solubility ratio:

Sa = ma / mw (1)

where

Sa = solubility ratio

ma = mass of air (lbm, kg)

mw = mass of water (lbm, kg)

Henry's Law

Solution of air in water follows Henry's Law - "the amount of air dissolved in a fluid is proportional with thepressure of the system" - and can be expressed as:

c = pg / kH (2)

where

c = solubility of dissolved gas

kH = proportionality constant depending on the nature of the gas and the solvent

pg = partial pressure of the gas

The solubility of oxygen in water is higher than the solubility of nitrogen. Air dissolved in water containsapproximately 35.6% oxygen compared to 21% in air.

Solubility of Air in Water

Solubility of air in water - expressed as ratio of absorbed air volume to water volume:

Temperature

(oF)

Gauge Pressure (psig)

0 20 40 60 80 100

40 0.0258 0.0613 0.0967 0.1321 0.1676 0.2030

50 0.0223 0.0529 0.0836 0.1143 0.1449 0.1756

60 0.0197 0.0469 0.0742 0.1014 0.1296 0.1559

70 0.0177 0.0423 0.0669 0.0916 0.1162 0.1408

80 0.0161 0.0387 0.0614 0.0840 0.1067 0.1293

90 0.0147 0.0358 0.0589 0.0750 0.0990 0.1201

100 0.0136 0.0334 0.0536 0.0730 0.0928 0.1126

110 0.0126 0.0314 0.0501 0.0699 0.0877 0.1065

120 0.0117 0.0296 0.0475 0.0654 0.0833 0.1012

130 0.0107 0.0280 0.0452 0.0624 0.0796 0.0968

140 0.0098 0.0265 0.0432 0.0598 0.0765 0.0931

150 0.0089 0.0251 0.0413 0.0574 0.0736 0.0898

160 0.0079 0.0237 0.0395 0.0553 0.0711 0.0869

170 0.0068 0.0223 0.0378 0.0534 0.0689 0.0844

180 0.0055 0.0208 0.0361 0.0514 0.0667 0.0820

190 0.0041 0.0192 0.0344 0.0496 0.0647 0.0799

200 0.0024 0.0175 0.0326 0.0477 0.0628 0.0779

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Page 2: Air Solubility in Water

20/03/13 Air Solubility in Water

www.engineeringtoolbox.com/air-solubility-water-d_639.html 2/3

210 0.0004 0.0155 0.0306 0.0457 0.0607 0.0758

Example - Calculating Air Dissolved in Water

Air dissolved in water can be calculated with Henry's law.

Henry Law's Constants at a system temperature of 25oC (77oF)

Oxygen - O2 : 756.7 atm/(mol/litre)

Nitrogen - N2 : 1600 atm/(mol/litre)

Molar Weights

Oxygen - O2 : 31.9988 g/mol

Nitrogen - N2 : 28.0134 g/mol

Partial fraction in Air

Oxygen - O2 : ~ 0.21

Nitrogen - N2 : ~ 0.79

Oxygen dissolved in the Water at atmospheric pressure can be calculated as:

co = (1 atm) 0.21 / (756.7 atm/(mol/litre)) (31.9988 g/mol)

= 0.0089 g/litre

~ 0.0089 g/kg

Nitrogen dissolved in the Water at atmospheric pressure can be calculated as:

cn = (1 atm) 0.79 / (1600 atm/(mol/litre)) (28.0134 g/mol)

= 0.0138 g/litre

~ 0.0138 g/kg

Since air is the sum of Nitrogen and Oxygen:

ca = (0.0089 g/litre) + (0.0138 g/litre)

= 0.0227 g/litre

~ 0.023 g/kg

Calculating air dissolved in water for some other pressures at temperature 25oC (77oF) can be summarized to:

Pressure, abs (atm) 1 2 3 4 5 6

Dissolved Air in Water

(25oC) (g/kg)0.023 0.045 0.068 0.091 0.114 0.136

Dissolved Oxygen in Fresh Water

Deariation

For maximum deaeration the water should be heated up to 212 oF (100 oC) at atmospheric pressure. This iscommon in steam systems where fresh water is supplied to the system through an heated deaeration tower on thetop of the condensate receiver tank.

It is also common to install deaeration devices on the hot sides of heat exchangers in heating distribution systemsto force the dissolved air out of the system.

Note! Since the maximum deaeration is limited by the minimum static pressure and maximum temperature in thesystem - the best deaeration result is achieved in positions at the hottest and highest levels of the systems -and/or at the suction side of pumps.

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