Paratene Home Product Search Technical Reports Distributors Commercial Terms Contacts
Paratene™ M390
Back to Acid Cleaning Products


Download Brochure
Download Product Data Sheet
Download Material Safety Data Sheet
Paratene™ M390
“Organic Acid for Industrial Cleaning - A Technical Comparison”
Acids are the most commonly used chemicals for the removal of scales and deposits from industrial systems. Paratene™ M390 is a strong organic acid that combines the best properties of inorganic acids with the benefits of the weaker organic acids.

Any acid used in cleaning must meet several criteria:
• Utility – the acid must dissolve the scale or deposit in question
• Efficiency – the acid must dissolve the scale by using the minimum of chemical at a rapid rate.
• Compatibility – the acid must not damage the equipment or process.
• Safety – the acid must be easy to handle, and simple to dispose.

Physical Properties Comparison
The following table shows the molecular weights and Ka values for several common acids. The
hydrogen ion activity of an acid solution is related to the Ka value and the acid concentration.

Acid Ka Value Molecular Weight
(g/mole)
Paratene™ M390 8.30E+01 96.11
Hydrochloric 1.00E+03 36.5
Sulphuric 1.00E+03 98
Phosphoric 7.30E-03 97
Sulphamic 1.02E-01 97
Formic 1.77E-04 46
Acetic 1.75E-05 60
Citric 7.50E-04 210.14


As can been seen above, the strong acids - hydrochloric, sulphuric, and M390 have substantially higher Ka values than the other acids. The hydrogen ion strength of a solution relates to each acid and its Ka value using the following formula.

(1) Ka = [H + ][A - ]/[HA]

The above formula gives the relationship between the hydrogen ions available in solution and the acid concentration. The hydrogen ion activity is then proportional to the reaction rate of the acid. There fore more hydrogen ions in solution the quicker the acid will dissolve many scales.

Process Patent Pending

A second consideration is that cleaning acids are typically applied on a percentage weight basis, but the actual activity of each acid is dependant on the molar concentration. The table below represents the molar concentrations for each of the acids considered.

Cleaning Agent Molarity
Weight
%
HCl H2SO4 H2PO4 M390 Sulphamic Formic Acetic Citric
0.5 0.14 0.05 0.05 0.05 0.051 0.11 0.083 0.024
1 0.27 0.10 0.10 0.10 0.10 0.22 0.17 0.048
2 0.55 0.20 0.21 0.21 0.21 0.43 0.33 0.095
3 0.82 0.31 0.31 0.31 0.31 0.65 0.5 0.14
5 1.37 0.51 0.51 0.52 0.51 1.09 0.83 0.24
10 2.7 1.02 1.03 1.04 1.03 2.17 1.67 0.48


By considering the information represented in both tables, we can produce the following graph to compare the relative performance of different acids.

The graph clearly shows that Paratene™ M390 provides more available acid strength for all of the acids considered with the exception being hydrochloric.
Process Patent Pending


Cation Solubility g/100g of water
M390 Sulphuric Hydrochloric
Calcium 94.2 0.209 59.3
Barium 68 0 31
Magnesium 35 26 54.2
Copper 60 14 6.9

A third consideration in determining the ability of an acid to dissolve a particular scale or deposit also depends on the solubility of the resulting ions in the spent acid solution. The table below shows some common cation solubility’s.

Materials Compatibility, Corrosion and Temperature Limits
Acids are corrosive to most metals. Corrosion Inhibitors may be added to reduce the corrosion rates,but in some cases the inhibitors cannot prevent secondary problems such as stress cracking.

M390 1-20 max 90 A B A A A A A A A X X A
HCl 3 - 15 max 80 A B X X A A A A A X X A
HCl/Thiourea X 5 -15/0.5 -2 55-75 A B X X X X X X X X X X
HCl/ABF 3 - 15/0.5 - 3 max 80 A B X X A A A B B X X X
HCl/Boric 5/2 65-80 A B X X A B A B B X X C
H2SO4 5 - 10 max 80 A B B B B B A B B X X X
H2SO4/ABF 2.5/0.5 max 80 A B B B B B A B B X X X
Sulphamic max 10 20-85 A B A A X X X X B X X X
Phosphoric 1 -21 Max 80 A B A A A A B X X X X X
CrO3 max 10 120 A B X X A X X B B A A B
NaBromate 40-70 A A X X X A X X B A X X
Citrosolve 5 65-150 A A A A X X X X B A X X
Citric 3-5 50-100 A A A A A X A X B X X X
Formic 3 -10 50 - 150 A A A A A X A X B X X X
Glycolic 3-5 51 - 150 A A A A A X A X B X X X
Formic/Glycolic 2/1 52 - 150 A A A A A A A A B X X X
Formic/Citric 2/1 53 - 150 A A A A A A A A B X X X
Nitric 1-10 80 X X A A X X A A X X B A
H2O2 <5 40 -60 A X A A X X B B X X B A
SHP 5 50 A X A A X X B B X X X A

A-Good B-Fair C-Poor X-Unsatisfactory

The chart above illustrates that Paratene™ M390 has a greater range of compatibility with more metals than any of the other acid solutions.

When applied with the correct corrosion inhibitor, the rate of corrosion for most acids can be controlled.

Acid Wt% Molarity
Moles/liter
Temperature
(°C)
Inhibitor
Rate (mpy)
without
inhibitor
Rate mpy
0.2%
Inhibitor
Hydrochloric 5 1.36 60 I201 859 25
M390 10 1.04 60 I205 859 16
Sulphuric 10 1.02 60 I205 6311 12
Sulphamic 10 1.03 70 I205 3972 35

The above table compares corrosion results under similar temperatures and molarity, and shows that Inhibited M390 has comparable corrosion rates to comparatively inhibited HCl solutions.

Environmental and Disposal Problems
The direct disposal of strong acids is not practical. Acid solutions are corrosive and can cause damage to the equipment as well as the environment, and must be neutralized prior to their disposal. In addition the system being cleaned will contribute other ions into the acid solution that may increase the toxicity of the spent solution and increase the considerations for proper disposal.

The neutralized solutions salts such as sodium, iron, and calcium salts of sulphate, phosphate or nitrate are typically not considered to be an environmental problem except where they act as eutrifecation agents, where they encourage the growth of algae. In the case of the salts of hydrochloric acid – calcium, sodium or iron chloride can cause serious negative problems on non-salt water plants and animals, which limits the options for disposing hydrochloric solutions. In Western Canada, and particularly Alberta, the disposal of salt water solutions is common place due the availability of injection wells.

The relative toxicity for various acid solutions is provided in the table below.
EC50 mg/L
Acid Dapnia Magna Algae Activated Sludge Biodegradable
M390 260 72 530 Yes
Citric acid >100 >100 >100 Yes
Sulfuric 43 No data No data No
Hydrochloric 560 800 1000 No
Acetic 100 75 No effect Yes


When dealing with the safe handling of acids several issues are frequently causes of concern. One concern is the relative vapour pressure of the acids – acids that generate a lot of vapour are both inhalation hazards and environmental risks. Additionally acids like sulfuric also have serious problems in the heat of reaction both in mixing the acid with water and with neutralizing the acid for disposal.

Acid Vapour Pressure mmHg at 25°C
M390 0.0267
Hydrochloric 25
Sulphuric 0.3
Acetic 11
Formic 44


Paratene™ M390 is an excellent choice in cleaning applications to dissolve scale and deposits from a variety of process systems constructed of common or uncommon metallurgy. Paratene™ M390 provides rapid and efficient removal of deposits while remaining both safer in handling and disposal than many other acids.


Woodrising Resources Ltd
#2 321 37 Ave NE
Calgary AB T2E 6P6
Canada
www.paratene.com
403-216-2130
Paratene™ is a wholly owned registered tradename of Woodrising Resources Ltd.

Process Patent Pending