Presentation is loading. Please wait.

Presentation is loading. Please wait.

Materials & Corrosion.

Similar presentations

Presentation on theme: "Materials & Corrosion."— Presentation transcript:

1 Materials & Corrosion

2 Why worry about corrosion?
“One large chemical company spent more than $400,000 per year for corrosion maintenance in its sulfuric acid plants, even though the corrosion conditions were not considered to be particularly severe.”

3 Why worry about corrosion?
“A refinery employing a new process developed a serious problem after just 16 weeks of operation; some parts showed a corrosion loss of as much as 1/8 inch.”

4 Why worry about corrosion?
“The trend in the chemical process industries toward higher temperatures and pressures has made possible new processes or improvements in old processes. Higher temperatures and pressures usualy involve more severe corrosion conditions. Many of the present day operations would not have been possible or economical w/o the use of corrosion-resistant materials.”

5 Why Worry about Corrosion?
Safety/Health Environment Operability Profitability Product Quality Appearance of Facilities/Equipment Badly corroded and rusted equipment in a plant would leave a poor impression on the observer “A chemical plant effected an anuual savings of more than $10,000 merely by changing the bolt material on some equipment from one alloy to another more resistant to the conditions involved. The cost of this change was negligible. Slight changes in the process sometimes reduce the corrosiveness of plant liquors without affecting the process itself, thus permitting the use of less expensive materials! These changes can often be made after the plant is in operation, but original preventive measures are more desirable. Corrosion difficulties can often be ‘designed out’ of equipment, and the time to do this is in the original design of the plant! It is easier and cheaper to erase lines on a drawing than to repair or replace failed equipment in a plant.

6 Examples of Corrosion Erosion-corrosion of copper water pipe (tubing)
Chloride Stress corrosion cracking of stainless steels Chloride pitting of stainless steel Nitric acid attack of titanium tubing

7 Corrosive Environments
Atmospheric Industrial Urban Rural Marine Water Seawater Freshwater Tapwater Treated water

8 Corrosive Environments
Soil Industrial – commercial/institutional

9 Definition of corrosion
Is the chemical or electro-chemical reaction between a material – usually a metal – ant it’s environment that produces a deterioration of the material and it’s properties.

10 Factors Influencing Corrosion
Design, fabrication & materials Design/configuration Forming, welding, heat treating Metallurgy, composition Environmental factors Process chemistry including: pH Dissolved materials Salt Metal ions Gases (O2, N2, CO2, ammonia, chlorine etc.) Suspended matter Temperature Flow velocity Micro-organisms

11 Types of Corrosion 2 Main Types:
General corrosion is the loss material over the entire surface, at a relatively constant rate. The metal is thinned fairly uniformly, without appreciable localized attack. Localized Attack is specific to certain areas of the material, and can take many forms.

12 Forms of Localized Attack
Pitting is corrosion that produces sites of localized attack that are small relative to the overall exposed surface area. It is the most common form of corrosion in aqueous environments, and the major cause of corrosion service failures in the chemical processing industry.

13 Forms of Localized Attack cont’d
CREVICE CORROSION is attack at narrow spaces or gaps between two metal surfaces, or between a metal and non-metal. It can occur at cracks or seams in a metal, or under a washer, gasket, or deposit. Crevice corrosion results from a difference between the chemistry of the bulk environment and that in or at the crevice.

14 Forms of Localized Attack cont’d
BIOLOGICAL ATTACK is that which caused or accelerated by organisms on the affected surface. Fouling organic deposits may cause crevice corrosion, or organisms may produce chemicals that cause corrosion.

15 EROSION CORROSION is acceleration of material loss due to the combined effects of corrosion plus removal of material by the moving fluid.

16 Forms of Localized Attack cont’d
CAVITATION & IMPINGEMENT is material loss due to collapse of voids or cavities in the fluid, due to pressure changes (cavitation), or due to impingement of liquid droplets. This may be strictly mechanical damage, or may be worsened by the effects of corrosion.

17 S.E.M. What is it?

18 Forms of Localized Attack cont’d
Fretting is a process combining wear and corrosion in removal of material from contacting solid surfaces. It typically involves very small relative movements of the components, oxidation of the surfaces, and abrasion by the oxidation products. It often occurs between a shaft and a component fitted on the shaft.

19 Forms of Localized Attack cont’d
INTERGRANULAR ATTACK is corrosion at the boundaries of a metal grain, with little or no attack of the grain. It results in weakening of the metal, or separation at the grain boundary. (The composition and corrosion resistance of a metal grain varies from the surface to the interior.)

20 Forms of localized Attack cont’d
DEALLOYING ATTACK is preferential removal of one constituent of an alloy in a corrosive environment. An example is the “dezincification” of brass, in which zinc is leached from the brass in some aqueous streams, leaving a weak structure of copper and copper oxide.

21 Forms of Localized Attack cont’d
GALVANIC ATTACK is attack of a metal that is in electrical contact with a more noble metal, or a non-metallic conductor, in a corrosive environment. Examples are: corrosion of copper or brass couple to steel in an aqueous environment: or corrosion of a zinc coating on steel. The latter is done intentionally to protect the steel, as in roofing nails, fencing, corrugated galvanized sheets, etc.

22 Types of Corrosion Environmentally-induced cracking:
Stress-corrosion cracking (SCC) is due to the combined effects of a corrodent and sustained tensile stress. SCC of AUSTENTITIC (300-series) stainless steels by chorides is a major problem in the chemical industry. SCC can be caused in copper alloys in nitrates, and in steel by caustic. To increase production, the temperature of the cooling medium in a heat-exchanger system was lowered and the time required per batch decreased. Lowering the temperature of the cooling medium resulted, however, I more severe thermal gradients across the metal wall, They in turn, induced higher stresses in the metal. Stress corrosion cracking of the vessels occurred quickly, an the plant was shut down with production delayed for some time.

23 Environmentally-induced Cracking
CORROSION FATIGUE occurs in a cyclically loaded part in a corrosive environment. It occurs at lower stress levels or after fewer cycles that would be the case in the absence of the corrosive environment.

24 Environmentally-induced Cracking
Hydrogen-induced cracking or Embrittlement is reduction of the ductility or toughness of a metal due to the presence of atomic hydrogen. The hydrogen can be present due to introduction into the molten metal, or through absorption by the solid metal.

25 Environmentally-induced Cracking cont’d
LIQUID METAL EMBRITTLEMENT is brittle failure of a normally ductile metal when coated with a thin film of liquid metal followed by stressing in tension. Examples of LME may occur when steel is brazed, soldered, welded, or plated, or dip-coated with zinc, cadmium, or tin.

26 Corrosion Control Materials selection Design Method of Operation
Barriers/coatings Paint systems Linings – e.g. rubber or plastic Cladding – metal on metal Galvanizing Plating Glass/ceramic – e.g. porcelain on steel Inhibitors Cathodic/Anodic Protection

27 Factors affecting choice of an engineering material
Strength Appearance Corrosion resistance Materials Selection Availability Fabricability Cost

28 Corrosion-resistant Materials
All materials are resistant to corrosion in some specific environments. For example, carbon steel is resistant to many process and aqueous liquids. It may corrode slowly or not at all. Steel is the main material used in chemical plant equipment. The term corrosion-resistant is used to refer to materials that resist attack in specific or unusually corrosive environments.

29 Corrosion-Resistant Materials
The following is a list of a few materials used in various corrosive services: Stainless steels Nickel & nickel alloys Reactive & refractory metals such as tantalum, titanium, zirconium, & their alloys Copper/copper alloys (brasses, bronzes)

30 Corrosive-Resistant Materials
Aluminum Lead Chromium Plastics, such as teflon, PVC, nylon, polypropylene, polyethylene, etc. Rubbers/elastomers such as nitrile (NBR or BUNA-N) EPDM (e.g. NORDEL), Viton, NEOPRENE, butyl, etc. COMPOSITES, e.g. fiber-reinforced plastic (FRP, fiberglass) GLASS & CERAMICS, tile, porcelain, brick

31 STAINLESS STEELS Iron-based alloys, with at least 10.5% Chromium
Chromium-rich oxide surface film “passive” Forms and heals in oxygen Additives of nickel, molybdenum, copper, titanium, aluminum, silicon, niobium, nitrogen, sulphur, selenium Processing applications, cutlery, decorative, health and sanitary, dairy, transportation, medical

32 STAINLESS STEELS FERRITIC Iron plus 10-25% chromium (BCC) Magnetic
High strength, limited toughness Good ductility & fabricability Examples : 405,409, 429, 430, 434, 442, monit

33 STAINLESS STEELS AUSTENTITIC Iron plus chromium plus nickel (FCC)
Also molybdenum, manganese, copper, nitrogen, others Non-magnetic (Usually) Relatively low strength High ductility/toughness Susceptible to chloride attack (SCC, pitting) Good fabricability Examples: 201, 202, 205, 301, 302, 303, 304, 304L, 305, 308, 309, 310,316, 316L, 317, 321, 330, 347, 348, 384, 904L, nitronic types, Alloy 20, 20Cb-3, sanicro 28

34 STAINLESS STEELS DUPLEX Mixed structure of BCC ferrite & FCC austenite
High corrosion resistance, SCC-resistant High strength, good toughness Examples: 329, 2205, 2507, 3RE60, 7-Mo PLUS, Ferralium 255

35 STAINLESS STEELS MARTENSITIC Martensitic structure (distorted BCC)
Lower chromium: % Higher carbon: 0.15% min Magnetic, hardenable High strength – limited toughness Lower corrosion resistance Examples: 403, 410, 414, 416, 420, 431, 440

Chromium-nickel grades with copper, aluminum, titanium additions Hardened by ageing at moderately elevated temperatures Good formability (form then harden) Susceptible to heat damage Good corrosion resistance Examples: 15-5 PH, 17-4 PH, 17-7 PH, PH 14-4 Mo, Custom 450, custom 455

37 OTHER ALLOYS COPPER & IT’S ALLOYS Copper 99+% copper
Water service, marine, heat exchangers, architectural Not heat treatable Resists biofouling

38 COPPER & IT’S ALLOYS BRASSES 5-45% Zinc Dealloying above 15% zinc
Tin added to stop dealloying (admiralty and naval brasses)

39 COPPER & IT’S ALLOYS BRONZES Phosphour bronze – 10% tin
Silicon bronze – 1-3% Si Aluminum bronze – 5-10% Al

40 COPPER & IT’S ALLOYS CUPRO-NICKELS 90/10 Cu/Ni, 80/20, 70/30
Resistant to seawater, erosion, pitting

41 ALUMINUM & IT’S ALLOYS Protected by barrier oxide film
Corrodes at low and high pH Resistant to nitric acid (oxidizing) 1xxx – 99+% Al 2xxx alloyed with copper Strong, heat-treatable Lower corrosion resistance

42 ALUMINUM & IT’S ALLOYS 4xxx – alloyed with Si
5xxx – Al-Mg-Mn, Al-Mg-Cr, Al-Mg-Mn-Cr

43 NICKEL & IT’S ALLOYS NICKEL Alloy 200, commercially pure
Plating/cladding Resistant to caustic MONEL Alloy 400, approx. 30% copper Very good fabricability

44 NICKEL & IT’S ALLOYS NICKEL-MOLY Hastelloy B, B-2 Resistant to HCI
NICKEL-CHROMIUM Inconel or Alloy 600 (77% Ni-15%Cr-bal Fe)

45 NICKEL & IT’S ALLOYS Ni-Fe-Cr Incoloy or Alloy 800 (21Cr-32Ni-bal Fe)
Resistant to chlorides Ni-Fe-Cr-Mo Includes Alloys 20 & 20Cb3, Incoloy 825, Hastelloy F & G Increased resistance to sulphuric, phosphoric, and organic acids and to SCC and chloride pitting

46 NICKEL & IT’S ALLOYS Ni-Cr-Mo Hastelloy C, C276, C-22
Inconel or Alloy 625 Resistant to hot acid mixtures

Polyethylene, PP, ABS, PVC, CPVC, PVDC Fluorocarbons – PTFE or teflon, FEP, PFA, CTFE etc. Nylon Acetals, acrylics, polycarbonates, styrenes

48 Plastics Cont’d Thermosetting resins Usually reinforced with glass
Epoxy, phenolics, polyester, furanes Rubber & Elastomers Synthetic & natural rubbers Carbon & graphite Glass Ceramics & Refractories Concrete Wood

49 METALS MATERIAL Advantages Disadvantage Carbon Steel Stainless steel
Low cost, readily available, resists abrasion, standard fabrication, resists alkali Poor resistance to acids & strong alkali, often causes discolouration and contamination Stainless steel Resists most acids, reduces discolouration, available with a variety of alloys, abrasion less than mild steel Not resistant to chlorides, more expensive, fabrication more difficult, alloy materials may have catalytic effects Monel-Nickel Little discoloration, contamination, resistant to chlorides Not resistant to oxidizing environments, expensive Hasteloy Improved over Monel-Nickel More expensive than Monel-Nickel Other exotic metals Improves specific properties Can be very high cost

50 Non-metals Material Advantages Disadvantage Glass Plastics Ceramics
Useful in laboratory and batch system, low diffusion at walls Fragile, not resistant to high alkali, poor heat transfer, poor abrasion resistance Plastics Good at low temperature, large variety to select from with various characteristics, easy to fabricate, seldom discolours, minor catalytic effects possible Poor at high temperature, low strength, not resistant to high alkali conditions, low heat transfer, low cost Ceramics Withstands high temperatures, variety of formulations available, modest cost Poor abrasion properties, high diffusion at walls (in particular hydrogen), low heat transfer, may encourage catalytic reactions From "Analysis, Synthesis, and Design of Chemical Processes" Turton, Bailie, Whiting, Shaeiwitz

51 Tensile Strength of Steel

52 Data in Text In pages of the text you can find a table recommending specific materials for specific chemicals, and descriptions of some common alloys

53 The Methanol Project Process streams in the methanol section are not corrosive Sulphur can cause problems in earlier stages, but that is not our problem Long term storage (days) of methanol in carbon steel can cause side reactions that generate impurities which interfere with proper operation of fuel cells

54 Workshop What material should we use for the majority of the equipment in the methanol reaction and purification section? What equipment requires other material? What would be some good choices for that material?

Download ppt "Materials & Corrosion."

Similar presentations

Ads by Google