CORROSION RESISTANCE OF HASTEllOY®AllOYS - Haynes ...
CORROSION RESISTANCE OF HASTEllOY®AllOYS - Haynes ...
CORROSION RESISTANCE OF HASTEllOY®AllOYS - Haynes ...
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Type<br />
316<br />
Concen- Temperature HASTEllOY~ alloy Staintration,<br />
less<br />
Corrosive Media percent deg. F deg. C 8/8-2 C/C-276 G/G-3 Steel Conditions<br />
Paper Bleaching 1 132 56 - E - E atmosphere over a 1%slurry of paper pulp; 0.05 chlorine, trace chlorine<br />
dioxide, pH 7.0, moderate aeration<br />
Paper Bleaching 1 145 63 - E - E paper pulp 1% slurry; 0.01% chlorine, trace chlorine dioxide, pH 5.2,<br />
moderate aeration<br />
Paper Bleaching 1 150 66 - E - E atmosphere over a 1% slurry of paper pulp; 0.01% chlorine, trace<br />
chlorine dioxide, pH 5.2<br />
Paper Pulp, Bleached 1.5 135-165 57-74 - E - E calcium chloride 0.3%, residual chlorine dioxide .002%, pH 5.5 to 6.0, extensive<br />
aeration<br />
Paper Pulp, Bleached - 135-165 57-74 S E - E 1.5% CaCI, pH 5.5 to 6.0, 95 days, aeration and agitation extensive<br />
Paper Pulp Slurry 1 114 46 - E - E Chlorine - .01%, pH 5.5 to 6.0<br />
Duration of test - 58 days<br />
Aeration - moderate<br />
Agitation - moderate<br />
Type of test - field<br />
Process involved - paper pulp bleaching<br />
Paper Stock - 75 24 - E - - 0.15 gil HCI, 0.02 gil free chlorine<br />
Paper Stock - 155 68 - E - - Kraft pulp stock, pH 9.5-10, moderate aeration, floYl rate of 4500 g.p.m.,<br />
337-hr. test<br />
Peanut Oil - to 125 to 52 E - - - sulfonation of peanut and corn oil<br />
Pentane - 70 21 G E - - plus traces of HCI, moisture and air. Alloy C=0.8 mpy<br />
Pepsin - to 150 to 66 S - - - extraction of pepsin with one percent HCI and organic acids, pH 4.8-7.0<br />
Perchloric Acid 72 75-212 24-100 - G - U<br />
Perchloroethylene - - 250 121 - E - - HCI and C1 2 , duration of test - 47 days<br />
Carbon Tetrachloride<br />
Perchloryl Fluoride - 86 30 - E - E 519 hrs., lab test, tank placed in air cabinet<br />
Phenol 95 302-320 150-160 E - - - plus 5 percent acetophenone, mildly boiling solution<br />
Phenol - 125 52 S E - - chlorination process, exposed 19 days in liquid phase<br />
- 125 52 E E - - exposed 19 days in vapor phase.<br />
Phenol OJ-Carbonate 90 380 193 E - - - plus 11 percent phenol and 1 percent AICI 3<br />
Phenol Formaldehyde - 212 100 E E E U sulfuric acid, phosphoric acid, lime, caustic, moderate aeration<br />
Phenol Formaldehyde - 265 129 G E E E Duration of test - 107 days<br />
Aeration - present<br />
Agitation - present<br />
Type of test - field<br />
Process involved - phenolic resin<br />
Remarks - vapors present intermittently during operating cycle_<br />
Phenol, Paratertiary - 500 260 - E - - plus formaldehyde, turpentine, boron trifluoride, and oxalic acid in kettle.<br />
Butyl<br />
Alloy C=0.2 mpy<br />
Phenol Sulfonic Acid 30 75 24 E - - - during production from phenol and concentrated sulfuric acid.<br />
30 250 121 E - - -<br />
Phenolpthalein 100 175 79 E - - - fusion of phenolpthalein<br />
Phenyl Piperazine - 176-436 80-225 G S - - 245 hrs., production of phenyl piperazine from aniline, hydrogen<br />
chloride, and diethylanolamine.<br />
Phosgene 5 307 153 E E - E chlorobenzene 70%; polyisocyanate 25%; phenyl isocyanate (trace).<br />
Phosgene 50 45 7 - E - E monochlorobenzene 40%, HCII0%, traces of isocyanate, liquid phase, air<br />
free<br />
Phosgene - 250 121 E E - E HCI and chlorinated solvents<br />
Phosgene Gas - 752 400 S S - -<br />
Phosgene Vapor - 122 50 E E - G 984 hrs., lab test<br />
Phosphoric Acid 0.5 60 16 S - - - H 3 P0 4 catalyst plus organics<br />
Phosphoric Acid 3-14 150 66 - E - - small amounts of fluorine compounds<br />
E - Less than 2 mpy (0.05 mm/y)<br />
G- 2 mpy (0.05 mm/y) to 10 mpy (0.25 mm/y)<br />
S - Over 10 mpy (0.25 mm/y) to 20 mpy (0.51 mm/y)<br />
B - Over 20 mpy (0.51 mm/y) to 50 mpy (1.27 mm/y)<br />
U - More than 50 mpy (1.27 mm/y)<br />
33