KROHNE OPTIMASSSsors User Manual

Corrosion Guide Rev 1.05 Jan 2006

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DDIISSCCLLAAIIMMEERR::

KROHNE does not represent or warrant the accuracy of the information included in this guide for end user applications. The data presented is based on
published data and field experience. However, only the end-user is aware of the specific chemical makeup of their process and must therefore accept the
ultimate responsibility for the suitability of the wetted parts for the process. Responsibility as to suitability and intended use of our instruments rests solely
with the end user!

Corrosion & Abrasion Guidelines for Coriolis Meters

2

Corrosion Guide Rev 1.05 Jan 2006

Contents:

1 Corrosion of Wetted Parts

1.1 Introduction . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .3

1.2 Material Compatibility . . . . . . . . . . . . . . . . . . . . . . . . .3

1.3 Material Information . . . . . . . . . . . . . . . . . . . . . . . . . .3

1.3.1 What is Stainless Steel? . . . . . . . . . . . . . . . .4

1.4 NACE Information . . . . . . . . . . . . . . . . . . . . . . . . . . . .4

1.5 Galvanic Corrosion with Titanium . . . . . . . . . . . . . . . .4

1.6 Problem Applications . . . . . . . . . . . . . . . . . . . . . . . . . .5

1.7 Using Material Compatibility Tables . . . . . . . . . . . . . .5

2 Abrasion Guidelines

2.1 Introduction . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .14

2.2 Protecting Flanges with Transition Pieces . . . . . . . . .14

2.3 Managing Fluid Velocity . . . . . . . . . . . . . . . . . . . . . . .14

2.4 Titanium as the standard material . . . . . . . . . . . . . . . .14

2.5 Conditioning the fluid flow . . . . . . . . . . . . . . . . . . . . . .15

2.6 Installation of the Flow Meter . . . . . . . . . . . . . . . . . . .15

2.7 Inclusion of air or gas in the fluid . . . . . . . . . . . . . . . .15

2.8 Consider installing the meter in a by-pass . . . . . . . . .15

2.9 Conclusions . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .15

3 Environmental Protection

3.1 Housing Specifications . . . . . . . . . . . . . . . . . . . . . . . .16

Corrosion Guide Rev 1.05 Jan 2006

3

Element Typical Specification

C 0.013 0.035 Max

Mn 1.6 2.0 Max

P 0.028 0.045 Max

S 0.009 0.030 Max

Si 0.38 1.0 Max

Cr 16.84 16.0...18.0

Ni 11. 2 6 10.0...15.0

Mo 2.12 2.0...3.0

Fe Balance Balance

Specifications for SS316L

Element Typical Specification

Al 3.0 2.5...3.5

V 2.5 2.0...3.0

Fe 0.13 0.25 Max

C 0.05 0.08 Max

Ti Balance Balance

Specifications for Titanium Gr9

Stainless Steel

318L

7000 series

All wetted parts: UNS S31803 to
ASTM A789, A790, A479 and A240
(also known as DUPLEX Stainless
Steel SAF2205).

This 318L stainless steel is NACE
approved.

ALL hygienic and aseptic process
connections: 316L UNS 31603 or
equivalent (also NACE approved).

Hastelloy C22

7000 series

All wetted parts: UNS NO6022 to
ASTM B619, B622, B626, B574
and B575

This HC-22 is NACE approved.

Titanium

7000 series

Measuring tube: UNS R56320 to
ASTM B338 titanium grade 9

Flange raised faces: UNS R50400
to ASTM B348 and B265 titanium
grade 2.

Titanium grade 9 is not NACE
approved.

Stainless Steel

316L

3000, 8000 / 9000

series

All wetted parts: 316L UNS 31603
or equivalent.

316L is NACE Approved.

Hastelloy C22

3000, 8000 / 9000

series

All wetted parts: UNS NO6022 to
ASTM B622, B626, B564, B574
and B575.

Hastelloy C22 is NACE approved.

1. Corrosion Of Wetted Parts

1.1 Introduction:

General corrosion guidelines for process vessels,
pipework and parts (such as thermo-wells or MID
flowmeter earthing rings) cannot be applied to Coriolis
mass flowmeters, since they refer to the bulk removal
of material from comparatively thick walled compo­nents, and they also tend not to address specific
localised corrosion mechanisms.

Greater care must be taken in the case of mass
flowmeters, since the tube wall thicknesses are in the
region of 0.2 … 2mm (depending on meter size), so
the removal of even a small amount of material can
cause a measurement problem or a meter tube
mechanical failure.

Additionally, localised corrosion effects such as pitting
or stress corrosion cracking can occur even without
corrosion of the overall tube. If severe enough, these
effects may cause a meter tube mechanical failure.

For these reasons you will find that many fluids will be
shown as unsuitable in this guide for use with mass
flowmeters when compared to more general corrosion
guidelines.

1.2 Material Compatibility

1.3 Material information

The Optimass meter range can be supplied with wet­ted parts (measuring tubes and connections) in the fol­lowing materials:

Oxidising

environment

Tantalum

Chlorides

Titanium

C-276

C-4

Ni-Cr-Mo Alloy

No 20 Alloy (Stainless)

Inconel

316 Stainless

Reducing

environment

Zirconium

Ni-Mo Alloy

C-22

Monel

Monel

304 Stainless

Non Chlorides

Oxidizing

Acids

Increasing

aggressivness

Reducing

Agents

4

Corrosion Guide Rev 1.05 Jan 2006

Element Typical Specification

C 0.02 0.030 Max

Mn 0.70 2.0 Max

P 0.025 0.030 Max

S 0.001 0.020 Max

Si 0.40 1.0 Max

Cr 22.4 21.0...23.0

Ni 5.8 4.5...6.5

Mo 3.3 2.5...3.5

N 0.16 0.08...0.2

Fe Balance Balance

Specifications for SS318L

Element Typical Specification

Cr 21.6 20.00...22.5

Mo 13.7 12.5...14.5

W 2.9 2.5...3.5

Fe 4.7 2.0...6.0

Co 1.1 2.5 Max

Mn 0.3 0.5 Max

V 0.13 0.35 Max

Ni Balance Balance

Specifications for Hasteloy C22

Please be aware that 318L is a “shorthand” expression
KRONHE have adopted for the material to aid our cus­tomers’ understanding that the material is a low carbon
stainless steel of a speciifc composition, in the same
way that 316L is used as “shorthand” for UNS S31603.

318L is more expensive to use than 316L, but we need
to consider the technical benefits that it brings. 318L
has a much higher tensile strength compared to 316L.
We use this property in our meter to manage the stress
caused by lengthening of the tube under thermal
expansion. If we used 316L, the tube would deform
well below the +100

0

C maximum we specify for 318L.

The corrosion resistance of 318L is equal to 316L. The
standard surface roughness is similar and it can be pol­ished to the same fine surface finish of <0.5 um Ra for
hygienic and aseptic applications. 318L is extensively
used worldwide, where customers utilise the higher ten­sile strength to reduce wall thickness (and so the cost
and weight) of process plant and piping. This means that
there should be no reluctance from our customers in
accepting this material.

KROHNE is the only company to offer a stainless steel
straight tube mass flowmeter.

1.4 NACE Information

National Association of Chemical Engineers (NACE stan­dard MR0175-2000) is a material requirements standard
relating to the general problems of Sulphide Stress
Cracking (SSC) of metals directed towards sour environ­ments.

1.5 Galvanic Corrosion with Titanium

This can occur when a titanium tube meter is placed in
contact with other metals, for instance in a steel
pipeline. As titanium is a “noble” metal, the other mate­rial will normally corrode in preference to the titanium.

In the case of stainless steel pipelines, titanium is very
close in the galvanic table therefore galvanic corrosion
is unlikely to be a problem and no precautions are nec­essary.

If carbon steel pipelines are used, galvanic corrosion of
the carbon steel may occur with certain acids. This cor­rosion process causes small amounts of hydrogen gas
to be liberated at the wetted metal-to-metal contact
area. This hydrogen gas may then cause embrittlement
in the titanium. This can be avoided by electrically insu­lating the Optimass from the pipeline using insulating
gaskets, bolt sleeves and washers.

Of course the use of an alternative tube material e.g.
Hastelloy C-22 will prevent the problem entirely.

1.3.1 What is 318L Stainless steel?

Many customers have asked “what is the 318L stainless
steel that you use in the Optimass 7000 single straight
tube meter, and why do you use this material instead of
316L”? Measuring instruments are more normally manu­factured with wetted parts from 316L stainless steel,
which is a 100% austenic structure steel, with composi­tion 18% .Chrome, 8% Nickel, 2.5% Molybdenum, with
the balance Iron.

318L is a 50% austenitic / 50% ferritic structure steel
(typically known as "duplex"), with (typical) composition
22% Chrome, 5% Nickel, 3% Molybdenum, with the bal­ance Iron.

This material is defined under the following internation­al codes:

•

UNS S31803

•

ASTM A789, A790, A479, A420

•

DIN 1.4462

Corrosion Guide Rev 1.05 Jan 2006

5

Remember in all cases KROHNE cannot accept
responsibility for the final choice of material. The ulti­mate responsibility lies with the end user. We can only
advise based on our experience!

Explanation of data tables

1. Key to symbols used

Symbol Meaning



Suitable, with a corrosion rate less than

0.05 mm (0.002”) per year

X Unsuitable, due to higher corrosion rate

nd No data is currently available

1.6 Problem Applications

Hydrochloric acid (HCl):

This acid normally contains fluoride and chloride impu­rities that will promote stress corrosion cracking in all
tube materials. This effect will always cause a meter
failure even if there is no bulk removal of tube material.
For this reason we do not recommend Optimass
meters for any HCl application.

Instead look to alternative instrument technologies such
as capacitive MID (Capaflux) or variable area flowme­ters (H250 PTFE).

Methanol:

“Pure” methanol (> 98% purity) tends to cause the
removal of the protective oxide layer on a titanium
measuring tube thus promoting corrosion. Titanium
therefore cannot be used. Stainless steel or Hastelloy
C-22 are suitable alternatives for these applications.

Methanol with a minimum 2%, or greater, water content
does not exhibit this tendency and can be freely used
with all tube materials.

Oxygen gas:

There is a risk of ignition where an oxygen rich (> 35%
O

2

) gas mixture is used with a titanium measuring

tube.Always offer stainless steel as an
alternative.Remember also that the “degreasing” option
for wetted parts should also be offered for use with oxy­gen gas applications.

Passivation of meters

A “passivation fluid” is normally composed of a mixture
of nitric acid (HNO

3

) and hydrofluoric acid (HF) and is
used to ‘passivate’ (clean) stainless steel pipework in
high purity systems, typically found in the pharmaceuti­cal industry. The process removes weld discoloration,
dirt, grease, metal particles, etc.

The nitric acid has negligible corrosive effect, but
hydrofluoric acid is very aggressive even at levels less
than 0.5% for all wetted tube materials. It is recom­mended that any meter is removed and replaced with
spool pieces during the passivation process. This is
due to the relatively thin wall of mass flow meter tubes;
the customer’s pipework being relatively thick is toler­ant to a small loss of material.

1.7 Using Material Compatibility Tables.

Identify the chemical to be used either by name or by
the Formula.

Check that you know the concentration of the chemical
and that it is within the concentrations listed in column

3.

Identify the best material for the application and then
check that this is acceptable for the customer.

2. Where a temperature is given, this signifies suit­ability only up to this point (e.g. 212/100 denotes
up to 212

o

F or 100oC). Where no temperature is
given, this signifies suitability up to the lower of
either the boiling point of the product, or the
maximum operating temperature of the Optimass
flowmeter concerned.

The first temperature given is always in Fahrenheit
and the second in Centigrade/Celsius.

3. Always check the relevant technical data sheet
for the maximum operating temperature of the
meter series and wetted material.

4. For the purposes of corrosion resistance, stain­less steel grades 316L and 318L can be consid­ered as both being the same.

6

Corrosion Guide Rev 1.05 Jan 2006

Fluid Chem. Formula Concentration

Stainless Steel

Max

oF/o

C

Hastelloy C-22

Max

oF/o

C

Titanium

Max

oF/o

C

Acetaldehyde CH3CHO 100% 200/93 200/93 300/149

Acetate CH3CO2CH3 100% 400/204 400/204 400/204

Acetic Acid CH3COOH 20% 400/204 300/149 260/127

Acetic Acid CH3COOH 50% 160/71 210/99 260/127

Acetic Acid CH3COOH 80% 160/71 210/99 260/127

Acetic Acid CH3COOH 95% X 200/93 210/99

Acetic Acid CH3COOH 100% X 200/93 200/93

Acetone CH3COCH3 100% 400/204 140/60 200/93

Acetyl Chloride CH3COCI 100% 70/21 99/37 220/105

Acetylene CH2 100% 400/204 220/105 79/26

Adipic Acid (CH2)5(COOH)2 100% 50/10 200/93 428/220

Air

  

Aluminium Chloride AlCl3 10% X 220/105 200/93

Aluminium Chloride AlCl3 40% X 220/105 X

Aluminium Chloride AlCl3 100% X 158/70 X

Aluminium Fluoride AlCl3 20% X X X

Aluminium Nitrate AlNO3 100% 302/150 X 208/98

Aluminium Sulphate Al2SO4 6.50% X 285/140 220/105

Aluminium Sulphate Al2SO4 40% X 285/140 220/105

Aluminium Sulphate Al2SO4 100% X nd 200/93

Ammonia (anhydrous) dry NH3 always 100% 248/120 248/120 77/25

Ammonia (aqueous) NH3 + water 30% 158/70 158/70 X

Ammonia (aqueous) NH3 + water 50% 86/30 302/150 X

Ammonium Acetate NH4CH3COO 15% 220/105 220/105 77/25

Ammonium Acetate NH4CH3COO 55% 170/77 nd nd

Ammonium Bicarbonate NH4HCO3 50% X nd 212/100

Ammonium Carbonate (NH4)2CO3 50% X X



Ammonium Chlorate (NH4)ClO3 30% nd nd 122/50

Ammonium Chloride NH4Cl 40% X 221/105 221/105

Ammonium Fluoride NH4F 25% X 170/77 nd

Ammonium Hydroxide NH4OH 45% X X 170/77

Ammonium Nitrate NH4NO3 28% 280/137 80/27



Ammonium Oxalate (NH4)C2O4 10% X 75/24 75/24

Ammonium Perchlorate NH4ClO4 20% 170/77 X 285/140

Ammonium Phosphate (NH4)3PO4 10% X 140/60 248/120

Ammonium Phosphate (NH4)3PO4 100% X 140/60 140/60

Ammonium Sulphate (NH4)2SO4 10% X 220/104 248/120

Ammonium Sulphate (NH4)2SO4 100% X X 248/120

Aniline C6H6NH2 100% 509/265 248/120 230/110

Aniline hydro chloride C6H5NH2xHCl 25% X nd 212/100

Aqua Regia HCl / H2SO4 100% X X X

Argon Ar 100%

  

Barium Carbonate BaCO3 100% X X 77/25

Barium Chloride BaCl2 25% X 158/70 122/50

Barium Hydroxide Ba(OH)2 10% 225/107 225/107 77/25

Barium Nitrate Ba(NO3)2 20% 150/65 X 77/25

Benzene C6H6 100% X X 240/116

Benzoic Acid C6H5COOH 10% X 180/82 248/120

Benzoic Acid C6H5COOH 100% X 180/82 248/120

Benzyl Chloride C7H7Cl 100% X X 140/60

Boric Acid BH3 10% X 320/160 320/160

Boric Acid BH3 100% nd nd 77/25

Bromine Liquid Br 100% X X X

Butyric Acid CH3(CH2)2COOH 100% X 260/127 225/107

Calcium Carbonate CaCO3 100%



Calcium Chloride CaCl2 75% X 221/105 O 221/105

Calcium Chloride CaCl2 100% X 392/200 X

 = Compatible

X = Not Compatible nd = No Data Available

7

Corrosion Guide Rev 1.05 Jan 2006

Fluid Chem. Formula Concentration

Stainless Steel

Max oF/oC

Hastelloy C-22

Max oF/oC

Titanium

Max oF/oC

Calcium Hydroxide Ca(OH)2 50% X 212/100 171/77

Calcium Hypochlorite Ca(Ocl)2 15% X 122/50 221/105

Calcium Hypochlorite Ca(Ocl)2 95% X X 221/105

Calcium Sulphate CaSO4 10% nd X nd

Calcium Sulphate CaSO4 100% X nd 140/60

Calcium Hypochlorite CaCl2+6H2O 15% X 122/50 221/105

Calcium Hypochlorite CaCl2+6H2O 95% X X 221/105
Carbon Tetrachloride
(anhydrous)

dry CCl4 100% 140/60 140/60 248/120

Carbonic Acid Saturated X

 

Chlorine (anhydrous) dry Cl2 any X X X

Chlorine (aqueous) Cl2 + water any X X X

Chloroacetic Acid CH2CICOOH 85% X X 221/105

Chloroform CHCl3 100% 80/27 80/21 221/105

Chlorosulphonic Acid HCISO3 100% X 185/85 X

Chromic Acid H8CrO5 25% X 167/75 221/105

Chromic Acid H8CrO5 50% X 75/24 221/105

Chromic Acid H8CrO5 100% X X 221/105

Citric Acid C6H8O7 25% X 221/105 212/100

Citric Acid C6H8O7 60% X 221/105 X

Copper Nitrate Cu(NO3)2 100% 280/138 X 77/25

Copper Sulphate CuSO4 100% X X 221/105

Cupric Chloride CuCl2 any X X X

Cupric Cyanide CuCN 100% X X 77/25

Cuprous Chloride CuCl 55% nd nd 194/90

Dichloroacetic Acid CHCl2COOH any nd nd X

Diethyl Phthalate C12H14O4 100% 221/105 nd 221/105

Ethyl Alcohol (Ethanol) C2H5OH 100% 221/105 221/105 221/105

Ethylene gas C2H4 100%

  

Ethylene dichloride
(anhydrous)

dry C2H2Cl2 100% X 221/105 221/105

Ethyl Acetate CH3 COOC2H5 100% 320/160 320/160 221/105

Ferric Chloride FeCl3 100% X X 248/120

Ferric Hydroxide Fe(OH)3 6% 70/21 80/27 68/20

Ferric Hydroxide Fe(OH)3 100% 70/21 80/27 nd

Ferric Sulphate Fe2(SO4)3 15% 221/105 104/40 221/105

Ferric Sulphate Fe2(SO4)3 35% X 104/40 221/105

Ferric Sulphate Fe2(SO4)3 100% X X 221/105

Ferrous Sulphate FeSO4 100% X X 248/120

Fluoboric Acid HBF4 30% 80/27 200/93 X

Fluorine (anhydrous) dry F any X X X

Fluosilicic Acid H2SiF6 any X X X

Formaldehyde CH2O 100% 221/105 X 221/105

Formic Acid (aerated) HCOO4 50% X 221/105 221/105

Formic Acid (non-aerated) HCOO4 85% X 221/105 X

Heptane C6H12 100% 221/105 221/105 221/105

Hydrazine (NH2)2 100%

  

Hydrobromic Acid HBO3 100% X 140/60 X

Hydrochloric Acid HCL + water any X X X

Hydrofluoric Acid HF + water any X X X

Hydrogen gas H

  

Hydrogen Chloride gas HCL any X X X

Hydrogen Cyanide NCN 100% 88/31 88/31 88/31

Hydrogen Fluoride gas HF any X X X

Hydrogen Peroxide H2O2 50% 194/90 194/90 X

Hydrogen Peroxide H2O2 90% 118/48 118/48 X

Iodine Liquid I2 100% X



77/25

 = Compatible

X = Not Compatible nd = No Data Available

8

Corrosion Guide Rev 1.05 Jan 2006

Fluid Chem. Formula Concentration

Stainless Steel

Max oF/oC

Hastelloy C-22

Max oF/oC

Titanium

Max oF/oC

Lactic Acid CH3CHOHCOOH 25% 122/50 122/50 122/50

Lithium Chloride LiCl 50% X 212/100 212/100

Magnesium Chloride MgCl2 50% X 280/138 248/120

Magnesium Hydroxide Mg(OH)2 100% 212/100 212/100 167/75

Magnesium Sulphate MgSO4 50% nd 200/93 200/93

Maleic Acid CH2(COOH)2 100% X 176/80 248/120

Manganese Chloride MnCl2 45% X 212/100 212/100

Mercuric Chloride HgCl2 10% X X 266/130

Mercuric Cyanide Hg(CN)2 10% 95/35 X 95/35

Methanol + > 2% H2O C2H4OH 98%

  

Methanol + > 50ppm H20 C2H40H 99.99%

 

X

Methanol pure C2H40H 100%

 

X

Methyl Ethyl Ketone CH3CH2COCH3 100% 200/93 200/93 200/93

Methyl Methacrylate C5H8O2 100%

  

Methylene Chloride CH2Cl2 100% X X 239/115
Mono Sodium

Orthophosphate in water

NaPO3 200 millimoles nd nd 86/30

Monochloacetic Acid CH2ClCOOH 100% nd nd



N-Butyric Acid CH3(CH2)2COOH 100% X 212/100 212/100

Nickel Chloride NiCl2 100% X 194/90 194/90

Nickel Nitrate Ni(NO3)2 50% X



77/25

Nickel Sulphamate 50%



Nitric Acid HNO3 100% “red fuming” 75/24 75/24 140/60

Nitric Acid HNO3 70% 75/24 75/24 140/ 60

Nitric Acid HNO3 50% 100/38 75/24 140/ 60

Nitric Acid HNO3 40% 125/52 75/24 140/ 60

Nitric Acid HNO3 30% 130/66 75/24 140/ 60

Nitric Acid HNO3 20% 176/80 130/66 140/ 60

Oxalic Acid (COOH)2 100% X 212/100 X

Oxygen rich gas mixture O2 > 35%

 

X

“Passivation” fluid Mixture HNO3 + HF X X X

Pentane C5H10 100% X

 

Perchloric Acid HClO4 any X 212/100 nd

Phenol C6H5OH 95% 131/55



X

Phosphoric Acid H3PO4 100% X X X

Phosphoric Acid H3PO4 98% X 77/25 X

Phosphoric Acid H3PO4 20% X 77/25 77/25

Phosphoric Acid H3PO4 5% 77/25 77/25 77/25

Potassium Bromide KBr 100% X X



Potassium Bromide KBr 30% X 95/35



Potassium Chloride KCI 99% X

 

Potassium Hydroxide KOH 40% 170/77 170/77 170/77

Potassium Iodide KI 75% 212/100 212/100 212/100

Potassium Nitrate KNO3 100% X 212/100 240/115

Potassium Permanganate KMnO4 100% X

 

Potassium Sulphate K2SO4 25% 212/100 X 240/115

Propanol (Propyl Alcohol) C3H6OH 100%

  

Seawater (Brine) C3H6OH 100% X

 

Silver Nitrate AgNO3 70% 85/30 85/30 212/70

Sodium Bisulphate NaHSO4 20% X X 85/30

Sodium Carbonate Na2CO3 100% 212/100 212/100 212/100

Sodium Chlorate NaCIO3 100% X 302/150 302/150

Sodium Chloride NaCI 100% X 212/100 212/100

Sodium Cyanide NaCN 50% 77/25 nd 266/130

Sodium Dichromate Na2Cr 100% X 80/27 77/25

Sodium Formate HCOONa 50% 131/55 131/55 nd

 = Compatible

X = Not Compatible nd = No Data Available

9

Corrosion Guide Rev 1.05 Jan 2006

Fluid Chem. Formula Concentration

Stainless Steel

Max

oF/o

C

Hastelloy C-22

Max

oF/o

C

Titanium

Max

oF/o

C

Sodium Hydroxide NaOH 45% X 104/40 131/55

Sodium Hydroxide NaOH 75% X 104/40 X

Sodium Hypochlorite NaOCl any X X X

Sodium Iodide NaI 65% X nd 212/100

Sodium Nitrate NaNO3 60% 233/112 233/112 248/120

Sodium Nitrate NaNO3 100% X X 248/120

Sodium Nitrite NaNO2 50% 212/100 212/100 266/130

Sodium Peroxide (Na)2O2 15% 212/100 X X

Sodium Phosphate NaPO4 15% X 212/100 212/100

Sodium Silicate Na2SiO3 100% 212/100 212/100 212/100

Sodium Sulphate Na2SO4 20% 212/100 212/100 X

Sodium Sulphide Na2S 50% X 212/100 X

Sodium Sulphite NaSO3 25% 212/100 212/100 212/100

Sodium Sulphite NaSO3 50% nd nd 212/100

Stannic Chloride SnCl2 any X X X

Stearic Acid CH2(CH2)16COOH 100%



212/100 X

Succinic Acid (CH2 COOH)2 50% X X



Sulphamic Acid NH2 SO2 OH any X nd X

Sulphur (molten) S 100%

  

Sulphuric Acid H2SO4

10%velocity

< 3 m/s

100/38 100/38 X

Sulphuric Acid H2SO4

25%velocity

< 3 m/s

75/24 100/38 X

Sulphuric Acid H2SO4

40%velocity

< 3 m/s

X 100/38 X

Sulphuric Acid H2SO4

55%velocity

< 3 m/s

X 86/30 X

Sulphurous Acid H2SO3 10% X X 175/80

Tannic Acid C76H52O46 95% 212/100 X 212/100

Tartaric Acid (CHOHCOOH) 2 50% 212/100 X 122/50

Terephthalic Acid C8H6O4 77%

  

Tetrachlorethane C2H2Cl4 100% X 160/71 160/71
Tetrachlorethylene
(Perchloroethylene)

Cl2C:CCl2 100% X 285/140 X

Thionyl Chloride SO2Cl2 100% X nd 104/40

Toluene C6H5CH3 100%

 

Trichlorethane C2H3Cl3 100% X X 77/25

Tricloroacetic Acid CCl3COOH 50% X 212/100 nd

Trisodium Phosphate (Na)3PO4 90% X



nd

Urea (NH2)2CO 100% 194/90 194/90 194/90

Zinc Chloride ZnCL2 75% X



212/100

Zinc Chloride ZnCL2 100% X



X

Zinc Sulphate ZnSO4 35% X 212/100 212/100

 = Compatible

X = Not Compatible nd = No Data Available

10

Corrosion Guide Rev 1.05 Jan 2006

Chem. Formula Fluid Concentration

Stainless Steel

Max oF/oC

Hastelloy C-22

Max oF/oC

Titanium

Max oF/oC

Air

  

Carbonic Acid Saturated X

 

Nickel Sulphamate 50%



(CH2 COOH)2 Succinic Acid 50% X X



(CH2)5(COOH)2 Adipic Acid 100% 50/10 200/93 428/220

(CHOHCOOH) 2 Tartaric Acid 50% 212/100 X 122/50

(COOH)2 Oxalic Acid 100% X 212/100 X

(Na)2O2 Sodium Peroxide 15% 212/100 X X

(Na)3PO4 Trisodium Phosphate 90% X



nd

(NH2)2 Hydrazine 100%

  

(NH2)2CO Urea 100% 194/90 194/90 194/90

(NH4)2CO3 Ammonium Carbonate 50% X X



(NH4)2SO4 Ammonium Sulphate 10% X 220/104 248/120

(NH4)2SO4 Ammonium Sulphate 100% X X 248/120

(NH4)3PO4 Ammonium Phosphate 10% X 140/60 248/120

(NH4)3PO4 Ammonium Phosphate 100% X 140/60 140/60

(NH4)C2O4 Ammonium Oxalate 10% X 75/24 75/24

(NH4)ClO3 Ammonium Chlorate 30% nd nd 122/50

AgNO3 Silver Nitrate 70% 85/30 85/30 212/70

Al2SO4 Aluminium Sulphate 6.50% X 285/140 220/105

Al2SO4 Aluminium Sulphate 40% X 285/140 220/105

Al2SO4 Aluminium Sulphate 100% X nd 200/93

AlCl3 Aluminium Chloride 10% X 220 /105 200/93

AlCl3 Aluminium Chloride 40% X 220 / 105 X

AlCl3 Aluminium Chloride 100% X 158/70 X

AlCl3 Aluminium Fluoride 20% X X X

AlNO3 Aluminium Nitrate 100% 302/150 X 208/98

Ar Argon 100%

  

Ba(NO3)2 Barium Nitrate 20% 150/65 X 77/25

Ba(OH)2 Barium Hydroxide 10% 225/107 225/107 77/25

BaCl2 Barium Chloride 25% X 158/70 122/50

BaCO3 Barium Carbonate 100% X X 77/25

BH3 Boric Acid 10% X 320/160 320/160

BH3 Boric Acid 100% nd nd 77/25

Br Bromine Liquid 100% X X X

C12H14O4 Diethyl Phthalate 100% 221/105 nd 221/105

C2H2Cl2 dry

Ethylene dichloride
(anhydrous)

100% X 221/105 221/105

C2H2Cl4 Tetrachlorethane 100% X 160/71 160/71

C2H3Cl3 Trichlorethane 100% X X 77/25

C2H4 Ethylene gas 100%

  

C2H40H Methanol + > 50ppm H20 99.99%

 

X

C2H40H Methanol pure 100%

 

X

2H4OH Methanol + > 2% H2O 98%

  

C2H5OH Ethyl Alcohol (Ethanol) 100% 221/105 221/105 221/105

C3H6OH Propanol (Propyl Alcohol) 100%

  

C3H6OH Seawater (Brine) 100% X

 

C5H10 Pentane 100% X

 

C5H8O2 Methyl Methacrylate 100%

  

C6H12 Heptane 100% 221/105 221/105 221/105

C6H5CH3 Toluene 100%

  

C6H5COOH Benzoic Acid 10% X 180/82 248/120

C6H5COOH Benzoic Acid 100% X 180/82 248/120

C6H5NH2xHCl Aniline hydro chloride 25% X nd 212/100

C6H5OH Phenol 95% 131/55



X

C6H6 Benzene 100% X X 240/116

C6H6NH2 Aniline 100% 509/265 248/120 230/110

 = Compatible

X = Not Compatible nd = No Data Available

11

Corrosion Guide Rev 1.05 Jan 2006

Chem. Formula Fluid Concentration

Stainless Steel

Max oF/oC

Hastelloy C-22

Max oF/oC

Titanium

Max oF/oC

C6H8O7 Citric Acid 25% X 221/105 212/100

C6H8O7 Citric Acid 60% X 221/105 X

C76H52O46 Tannic Acid 95% 212/100 X 212/100

C7H7Cl Benzyl Chloride 100% X X 140/60

C8H6O4 Terephthalic Acid 77%

  

Ca(Ocl)2 Calcium Hypochlorite 15% X 122/50 221/105

Ca(Ocl)2 Calcium Hypochlorite 95% X X 221/105

Ca(OH)2 Calcium Hydroxide 50% X 212/100 171/77

CaCl2 Calcium Chloride 75% X 221/105 221/105

CaCl2 Calcium Chloride 100% X 392/200 X

CaCl2+6H2O Calcium Hypochlorite 15% X 122/50 221/105

CaCl2+6H2O Calcium Hypochlorite 95% X X 221/105

CaCO3 Calcium Carbonate 100%

  

CaSO4 Calcium Sulphate 10% nd X nd

CaSO4 Calcium Sulphate 100% X nd 140/60

CCl3COOH Tricloroacetic Acid 50% X 212/100 nd

CCl4 dry

Carbon Tetrachloride
(anhydrous)

100% 140/60 140/60 248/120

CH2 Acetylene 100% 400/204 220/105 79/26

CH2(CH2)16COOH Stearic Acid 100%



212/100 X

CH2(COOH)2 Maleic Acid 100% X 176/80 248/120

CH2CICOOH Chloroacetic Acid 85% X X 221/105

CH2Cl2 Methylene Chloride 100% X X 239/115

CH2ClCOOH Monochloacetic Acid 100% nd nd



CH2O Formaldehyde 100% 221/105 X 221/105

CH3 COOC2H5 Ethyl Acetate 100% 320/160 320/160 221/105

CH3(CH2)2COOH Butyric Acid 100% X 260/127 225/107

CH3(CH2)2COOH N-Butyric Acid 100% X 212/100 212/100

CH3CH2COCH3 Methyl Ethyl Ketone 100% 200/93 200/93 200/93

CH3CHO Acetaldehyde 100% 200/93 200/93 300/149

CH3CHOHCOOH Lactic Acid 25% 122/50 122/50 122/50

CH3CO2CH3 Acetate 100% 400/204 400/204 400/204

CH3COCH3 Acetone 100% 400/204 140/60 200/93

CH3COCI Acetyl Chloride 100% 70/21 99/37 220/105

CH3COOH Acetic Acid 20% 400/204 300/149 260/127

CH3COOH Acetic Acid 50% 160/71 210/99 260/127

CH3COOH Acetic Acid 80% 160/71 210/99 260/127

CH3COOH Acetic Acid 95% X 200/93 210/99

CH3COOH Acetic Acid 100% X 200/93 200/93

CHCl2COOH Dichloroacetic Acid any nd nd X

CHCl3 Chloroform 100% 80/27 80/21 221/105

Cl2 + water Chlorine (aqueous) any X X X

Cl2 dry Chlorine (anhydrous) any X X X

Cl2C:CCl2

Tetrachlorethylene
(Perchloroethylene)

100% X 285/140 X

Cu(NO3)2 Copper Nitrate 100% 280/138 X 77/25

CuCl Cuprous Chloride 55% nd nd 194/90

CuCl2 Cupric Chloride any X X X

CuCN Cupric Cyanide 100% X X 77/25

CuSO4 Copper Sulphate 100% X X 221/105

F dry Fluorine (anhydrous) any X X X

Fe(OH)3 Ferric Hydroxide 6% 70/21 80/27 68/20

Fe(OH)3 Ferric Hydroxide 100% 70/21 80/27 nd

Fe2(SO4)3 Ferric Sulphate 15% 221/105 104/40 221/105

Fe2(SO4)3 Ferric Sulphate 35% X 104/40 221/105

Fe2(SO4)3 Ferric Sulphate 100% X X 221/105

 = Compatible

X = Not Compatible nd = No Data Available

12

Corrosion Guide Rev 1.05 Jan 2006

Chem. Formula Fluid Concentration

Stainless Steel

Max oF/oC

Hastelloy C-22

Max oF/oC

Titanium

Max oF/oC

FeCl3 Ferric Chloride 100% X X 248/120

FeSO4 Ferrous Sulphate 100% X X 248/120

H Hydrogen gas



H2O2 Hydrogen Peroxide 50% 194/90 194/90 X

H2O2 Hydrogen Peroxide 90% 118/48 118/48 X

H2SiF6 Fluosilicic Acid any X X X

H2SO3 Sulphurous Acid 10% X X 175/80

H2SO4 Sulphuric Acid

10%

velocity < 3 m/s

100/38 100/38 X

H2SO4 Sulphuric Acid

25%

velocity < 3 m/s

75/24 100/38 X

H2SO4 Sulphuric Acid

40%

velocity < 3 m/s

X 100/38 X

H2SO4 Sulphuric Acid

55%

velocity < 3 m/s

X 86/30 X

H3PO4 Phosphoric Acid 100% X X X

H3PO4 Phosphoric Acid 98% X 77/25 X

H3PO4 Phosphoric Acid 20% X 77/25 77/25

H3PO4 Phosphoric Acid 5% 77/25 77/25 77/25

H8CrO5 Chromic Acid 25% X 167/75 221/105

H8CrO5 Chromic Acid 50% X 75/24 221/105

H8CrO5 Chromic Acid 100% X X 221/105

HBF4 Fluoboric Acid 30% 80/27 200/93 X

HBO3 Hydrobromic Acid 100% X 140/60 X

HCISO3 Chlorosulphonic Acid 100% X 185/85 X

HCL Hydrogen Chloride gas any X X X

HCl / H2SO4 Aqua Regia 100% X X X

HCL + water Hydrochloric Acid any X X X

HClO4 Perchloric Acid any X 212/100 nd

HCOO4 Formic Acid (aerated) 50% X 221/105 221/105

HCOO4 Formic Acid (non-aerated) 85% X 221/105 X

HCOONa Sodium Formate 50% 131/55 131/55 nd

HF Hydrogen Fluoride gas any X X X

HF + water Hydrofluoric Acid any X X X

Hg(CN)2 Mercuric Cyanide 10% 95/35 X 95/35

HgCl2 Mercuric Chloride 10% X X 266/130

HNO3 Nitric Acid 100% “red fuming” 75/24 75/24 X

HNO3 Nitric Acid 75% 75/24 75/24 140/ 60

HNO3 Nitric Acid 70% 75/24 75/24 140/ 60

HNO3 Nitric Acid 50% 100/38 75/24 140/ 60

HNO3 Nitric Acid 40% 125/52 75/24 140/ 60

HNO3 Nitric Acid 30% 130/66 75/24 140/ 60

HNO3 Nitric Acid 20% 176/80 130/66 140/ 60

HNO3 + HF Mixture “Passivation” fluid X X X

I2 Iodine Liquid 100% X



77/25

K2SO4 Potassium Sulphate 25% 212/100 X 240/115

KBr Potassium Bromide 100% X X



KBr Potassium Bromide 30% X 95/35



KCI Potassium Chloride 99% X

 

KI Potassium Iodide 75% 212/100 212/100 212/100

KMnO4 Potassium Permanganate 100% X



KNO3 Potassium Nitrate 100% X 212/100 240/115

KOH Potassium Hydroxide 40% 170/77 170/77 170/77

LiCl Lithium Chloride 50% X 212/100 212/100

Mg(OH)2 Magnesium Hydroxide 100% 212/100 212/100 67/75

MgCl2 Magnesium Chloride 50% X 280/138 248/120

MgSO4 Magnesium Sulphate 50% nd 200/93 200/93

MnCl2 Manganese Chloride 45% X 212/100 212/100

Na2CO3 Sodium Carbonate 100% 212/100 212/100 212/100

 = Compatible

X = Not Compatible nd = No Data Available

13

Corrosion Guide Rev 1.05 Jan 2006

Chem. Formula Fluid Concentration

Stainless Steel

Max oF/oC

Hastelloy C-22

Max oF/oC

Titanium

Max oF/oC

Sodium Dichromate 100% X 80/27 77/25

Na2S Sodium Sulphide 50% X 212/100 X

Na2SiO3 Sodium Silicate 100% 212/100 212/100 212/100

Na2SO4 Sodium Sulphate 20% 212/100 212/100 X

NaCI Sodium Chloride 100% X 212/100 212/100

NaCIO3 Sodium Chlorate 100% X 302/150 302/150

NaCN Sodium Cyanide 50% 77/25 nd 266/130

NaHSO4 Sodium Bisulphate 20% X X 85/30

NaI Sodium Iodide 65% X nd 212/100

NaNO2 Sodium Nitrite 50% 212/100 212/100 266/130

NaNO3 Sodium Nitrate 60% 233/112 233/112 248/120

NaNO3 Sodium Nitrate 100% X X 248/120

NaOCl Sodium Hypochlorite any X X X

NaOH Sodium Hydroxide 45% X 0/40 0/55

NaOH Sodium Hydroxide 75% X 0/40 X

NaPO3

Mono Sodium
Orthophosphate in water

200 millimoles nd nd O86/30

NaPO4 Sodium Phosphate 15% X 212/100 212/100

NaSO3 Sodium Sulphite 25% 212/100 212/100 212/100

NaSO3 Sodium Sulphite 50% nd nd 212/100

NCN Hydrogen Cyanide 100% 88/31 88/31 88/31

NH2 SO2 OH Sulphamic Acid any X nd X

NH3 + water Ammonia (aqueous) 30% 158/70 158/70 X

NH3 + water Ammonia (aqueous) 50% 86/30 302/150 X

NH3 dry Ammonia (anhydrous) always 100% 248/120 248/120 77/25

NH4CH3COO Ammonium Acetate 15% 220/105 220/105 77/25

NH4CH3COO Ammonium Acetate 55% 170/77 nd nd

NH4Cl Ammonium Chloride 40% X 221/105 221/105

NH4ClO4 Ammonium Perchlorate 20% 170/77 X 285/140

NH4F Ammonium Fluoride 25% X 170/77 nd

NH4HCO3 Ammonium Bicarbonate 50% X nd 212/100

NH4NO3 Ammonium Nitrate 28% 280/137 80/27



NH4OH Ammonium Hydroxide 45% X X 170/77

Ni(NO3)2 Nickel Nitrate 50% X



77/25

NiCl2 Nickel Chloride 100% X 194/90 194/90

O2 Oxygen rich gas mixture > 35%



X

S Sulphur (molten) 100%

  

SnCl2 Stannic Chloride any X X X

SO2Cl2 Thionyl Chloride 100% X nd 104/40

ZnCL2 Zinc Chloride 75% X



212/100

ZnCL2 Zinc Chloride 100% X



X

ZnSO4 Zinc Sulphate 35% X 212/100 212/100

 = Compatible

X = Not Compatible nd = No Data Available

If you do not find the required fluid in the table, please contact your nearest sales office.

14

Corrosion Guide Rev 1.05 Jan 2006

Flow

Flange Bolt

Centralising

Sleeves

Gaskets

Transition

Piece

Pipe Work

Flow Meter

Flange Bolt

Typical Transition Piece Application

2. Abrasion Guidelines & information.

2.1 Introduction

For almost 10 years, the Krohne Corimass G Class
and Optimass 7000 series Coriolis mass flow meters
have been successfully used on abrasive fluids such as
slurries (mineral and metal mining) as wella as sand &
water mixtures.

In these applications, a single straight measuring tube
will always offer clear advantages over other designs
with tube geometries that suffer erosion and premature
failure of flow dividers and bends in the abrasive fluid
stream. Notwithstanding this, even a meter with a sin­gle straight tube will suffer some erosion unless simple
precautions are taken.

Other specific problems with abrasive fluids are typified
by their tendency to separate out with the heavier parti­cles falling to the bottom of the pipeline and the carrier
fluid flowing above in a stratified flow.

The purpose of this application guidance is to highlight
potential problems so that they can be mitigated
against during the planning and installation of the
meter.

2.2 Protecting Flanges with Transition Pieces

Since the meter measuring tube will typically have a
different internal diameter than the process pipework, a
“step change” will occur where the flanges are connect­ed. This edge presents a very obvious erosion point
and after a period, the weld between the flange raised
face and measuring tube could fail causing a leak path.

Transition pieces are stainless steel (although Hastelloy
can be used) discs that are sandwiched between the
two flanges, secured by through bolts and centred by
rubber sleeves around the bolts.

The taper on the internal diameter of the disc is manu­factured to correct the difference between the meter
and process pipe, thus providing a gradual transition
for the abrasive fluid into the meter.

They must be considered as “sacrificial wear parts”,
and should be removed periodically for inspection of
the internal taper dimension and replacement if neces­sary.

Prices for these parts are available from Krohne.

2.3 Managing fluid velocity

There are two considerations here based on the fluid
flow rate and density:

Maximum velocity

To prevent excessive erosion this should be never be
more that 4 m/sec (12 ft/sec).

Minimum velocity

So the particles and carrier are homogeneous mixed
this should be at least 1 m/s (3 ft/sec).

The Optimass sizing software will assist you in calculat­ing these limits. For abrasive slurries always size
according to these velocity limits, and not lowest meas­uring error which tends towards a smaller meter size
and hence a higher velocity.

2.4 Titanium as the standard material

Titanium should always be used as the standard mate­rial for measuring tubes. This is because size-for-size,
a titanium measuring tube has a greater wall thickness
than either stainless steel or Hastelloy. Simply put, this
tube has more material to erode before failure, so
extending the working lifetime of the meter.

Optimass Sizing Software Screen Shot

15

Corrosion Guide Rev 1.05 Jan 2006

Meter

size

Material Outside dia.

Wall

Thickness

Internal

dia.

40

T 38.10 ± 0.13 0.91 ± 0.09 36.28

H 38.10 ± 0.1 0.71 ± 0.07 36.68

S 38.10 ± 0.13 0.71 ± 0.07 36.68

50

T 50.80 ± 0.15 1.24 ± 0.01 48.32

H 50.80 ± 0.15 1.00 ± 0.01 48.80

S 48.26 ± 0.13 1.00 ± 0.01 46.26

80

T 73.00 ± 0.254 2.10 ± 0.02 68.80

H 73.03 ± 0.254 1.04 ± 0.01 70.95

S 73.00 ± 0.13 1.40 ± 0.01 70.20

All dimensions in mm

It should be noted that the exception to this is when
stainless steel or Hastelloy are required for fluid com­patibility (corrosion resistance).

2.5 Conditioning of the fluid flow profile
(as it enters the meter)

Firstly remember that a Coriolis mass flow meter direct­ly measures mass flow and density of the fluid. It does
not measure velocity, so from a measuring principle
standpoint there is no need for flow profile conditioning.

However with an abrasive fluid, there is the require­ment to condition the flow so that the abrasive particles
enter the meter parallel to the tube wall. This minimises
the probability that any given abrasive particle will
strike the tube wall and remove (erode) the tube mate­rial.

If the flow is “tumbling” or “swirling” as it enters the
meter, there is a risk that erosion will occur at the spe­cific point where the particles preferentially impact onto
the tube wall, so causing premature failure. These
problems are always associated with using a pipework
bend or elbow very close to the meter inlet.

Therefore we recommend a straight length of inlet
process pipe equal to at least 10, or preferably 20 x
pipe internal diameters.

2.6 Installation of the flow meter

In order to keep the heavy abrasive particles evenly
dispersed in the carrier fluid as a homogenous mixture
that is required for correct meter operation, we would
recommend a vertical meter installation. Otherwise
there is the tendency, especially at lower flow veloci­ties, for the fluid to separate out and become stratified.

Further, a flow direction vertically upwards is normally
preferred to ensure that meter is always full of liquid,
and does not “siphon” empty.

2.7 Inclusion of air or gas in the fluid

High density fluids such as mineral slurries typically
require a high drive energy due to their tendency
towards being inhomogeneously mixed.

Entrained air or gas will cause a further increase in the
required energy to drive (vibrate) the tube system. If

the inclusion is too great then the meter will not operate
correctly. This problem is particularly pronounced on
larger sized meters (T 50 & T 80), which typically are
used for abrasive fluid applications in order to reduce
the fluid velocity to acceptable levels.

So we would recommend that all efforts be made to
prevent the inclusion of air or gas in the fluid as part of
the process design, since from our experience once
entrained in the fluid it is virtually impossible to remove
prior to the metering point

2.8 Consider installing the meter in a by-pass

If the application is for density measurement only, then
often a more cost-effective solution is to install a small­er sized meter (although size 25 is smallest recom­mended) in a by-pass line off the main pipeline.

2.9 Conclusions

We are confident that if the seven steps above are fol­lowed correctly, then the probability of application relat­ed problems are greatly reduced and the operating life­time of the meter greatly increased.

3. Environmental Protection

The materials exposed to the environment as standard
are:

MFM x050 Ex

MFM x051 Ex

MFM xo50 Ex

MFM x051 Ex

MFC 050 Ex

MFC 051 Ex

•

304L Stainless Steel for the sen­sor body with optional
316LStainless Steel for offshore
applications.

•

Electronics housing is die cast
aluminium, powder coated.

•

The aluminium has a low copper
content (see specification table).

All above housings will be powder coated in silver and
All covers (screw-on type) will be painted in blue RAL
5005

MFC 300C

MFC 300F

MFC 300W

•

304L Stainless Steel for the sen­sor body with optional
316LStainless Steel for offshore
applications.

•

Electronics housing in Stainless
Steel 316L.

16

Corrosion Guide Rev 1.05 Jan 2006

Alloy type Si Fe Cu Mn Mg Cr Ni Zn Ti Pb

ADC 1
AlSi12Fe

11.0...13.0 1.3 1.0 0.3 0.3 - 0.5 0.5 - -

ADC 3
AlSi9Mg0,5Fe

9.0...10.0 3 1.0 0.3 0.4...0.6 - 0.5 0.5 - -

AlSi10Mg [Fe] 9.0...11.0 1.0 0.1 0.55 0.20...0.50 - 0.15 0.15 0.20 0.15

ALZn10Si8Mg 8.5...9.3 0.4 0.02 0.4 0.3...0.5 - - 9.0...10.0 0.1 -

For aggressive coastal or off shore based environments, KROHNE can provide an optional salt water resistant
coating. (see specifications below)

This is not in the standard price list. Please contact Product Management in Wellingborough, UK.

3.1 Housing Specifications

The MFC 050 and MFC 051 Range of Converters are available with KD(W) housings

KD Housing

This housing is prepared for long term applications in coastal and offshore environments.

KDW

The “W” suffix denotes the same specification as the standard KD housing but with the following additions:

•

Ingress protection IP 67

•

Special surface finish to:

•

Aluminium housing

•

Chromatized with (Henkel) Alodine 1200 S

•

Coated with Brillux 5910 Polyester powder

•

All outside threads have stainless steel inlays

•

Blue (RAL 5005) housing colour

•

1000 h spray test with sodium chloride solutions to:

•

DIN 50021:1988

•

ISO 1456:1974

•

ASTM B 117:1973

The MFC 300 Range of Converters are available with a SS 316L Housing

ADC 1

AlSi12Fe

ADC 3

AlSi9Mg0,5Fe

AlSi10Mg [Fe] ALZn10Si8Mg SS 316L

MFC050

 

MFC 051

 

MFC050 Ex

 

MFC051 Ex

 

MFC 300

  

MFC 300 Ex

  

17

Corrosion Guide Rev 1.05 Jan 2006

Sources of information:

ATI Wah Chung, Albany Oregon, Technical Data Sheet: TitAly-052

Haynes International, Kokomo, Indiana, USA

Sandvick AB, SE-811 81 Sandviken, Sweden

18

Corrosion Guide Rev 1.05 Jan 2006

Australia

KROHNE Australia Pty Ltd
Quantum Business Park
10/287 Victoria Rd
Rydalmere NSW 2116
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

Austria

KROHNE Austria Ges.m.b.H.
Modecenterstraße 14
A-1030 Wien
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

Belgium

KROHNE Belgium N.V.
Brusselstraat 320
B-1702 Groot Bijgaarden
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

Brazil

KROHNE Conaut
Controles Automaticos Ltda.
Estrada Louis Pasteur, 230 C.P. 56
06835 - 080 EMBU - SP
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

China

KROHNE Measurement Instruments
(Shanghai) Co. Ltd.
9th Floor, Xujiahui International Building
1033 Zhaojiabang Road
Shanghai 200030
P. R. China
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

CIS

Kanex KROHNE Engineering AG
Business-Centre Planeta, Office 403
Marxistskaja-Street 3
109147 Moscow/Russia
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

Czech Republic

KROHNE CZ, spol. s r.o.
Sobìšická 156
63800 Brno
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

France

KROHNE S.A.S.
Les Ors
BP 98
F-26103 ROMANS Cedex
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

Germany

KROHNE Messtechnik
GmbH & Co. KG
Ludwig-Krohne-Str.
D-47058 Duisburg
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

India

KROHNE Marshall Ltd.
A-34/35, M.I.D.C.
Industrial Area, H-Block,
Pimpri Poona 411018
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

Iran

KROHNE Liaison Office
North Sohrevardi Ave.
26, Sarmad St., Apt. #9
Tehran 15539
TEL.: ++98-21-874-5973
FAX: ++98-21-850-1268
e-mail: [e-mail]

Italy

KROHNE Italia Srl.
Via V. Monti 75
I-20145 Milano
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

Korea

KROHNE Korea
Room 508 Miwon Bldg
43 Yoido-Dong
Youngdeungpo-Ku
Seoul, Korea
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

Netherlands

KROHNE Altometer
Kerkeplaat 12
NL-3313 LC Dordrecht
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

Netherlands

KROHNE Nederland B.V.
Kerkeplaat 14
NL-3313 LC Dordrecht
TEL.: [phone]
FAX: [phone]
Service Direkt: [phone]
e-mail: [e-mail]

Norway

KROHNE Norway A.S.
Ekholtveien 114
NO-1526 Moss
P.O. Box 2178, NO-1521 Moss
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]
Internet: www.krohne.no

Singapore

Tokyo Keiso - KROHNE Singapore Pte. Ltd.
14, International Business Park,
Jurong East
Chiyoda Building #01-01/02
Singapore 609922
Singapore
TEL.: ++65-65-67-4548
FAX: ++65-65-67-9874

South Africa

KROHNE Pty. Ltd.
163 New Road
Halfway House Ext. 13
Midrand
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

Spain

I.I. KROHNE Iberia, S.r.L.
Poligono Industrial Nilo
Calle Brasil, n°. 5
E-28806 Alcalá de Henares-Madrid
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

Switzerland

KROHNE AG
Uferstr. 90
CH-4019 Basel
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

United Kingdom

KROHNE Ltd.
Rutherford Drive
Park Farm Industrial Estate

Wellingborough,
Northants NN8 6AE, UK

TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

USA

KROHNE Inc.
7 Dearborn Road
Peabody, MA 01960
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

Other Representatives

Algeria
Argentina
Belarus
Cameroon
Canada
Chile
Colombia
Croatia
Denmark
Ecuador
Egypt
Finland
Gabon
Ghana
Greece
Hong Kong
Hungary
Indonesia
Ivory Coast
Iran
Ireland
Israel
Japan
Jordan

Other Countries

KROHNE Messtechnik
GmbH & Co. KG
Ludwig-Krohne-Str.
D-47058 Duisburg
TEL.: [phone]
FAX: [phone]
e-mail: [e-mail]

Kuwait
Libya
Lithuania
Malaysia
Morocco
Mauritius
Mexico
New Zealand
Peru
Poland
Portugal
Romania
Saudi Arabia
Senegal
Slovakia
Slovenia
Sweden
Taiwan
Thailand
Turkey
Tunisia
Venezuela
Yugoslavia

Subject to change without notice