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Hydrochloric acid corrosion

M hydrochloric acid (corrosive) until the pH of the effluent is acidic and then wash with distilled water until it is neutral. [Pg.244]

Hazard Decomposes violently with water to sulfuric acid and hydrochloric acid. Corrosive to tissue. [Pg.1064]

Phosgene is the acid dichloride of carbonic acid, HO-C(0)-OH, and, like aU acid chlorides, reacts rapidly with water to produce the corresponding acid and hydrogen chloride. Since carbonic acid is unstable, the ultimate products of reaction with water are hydrogen chloride and carbon dioxide. The hydrogen chloride produced dissolves in excess water to form hydrochloric acid (corrosive). [Pg.33]

Limescale rust removers Hydrochloric acid Corrosive, eye and skin irritant. Also found in toilet cleaners, metal polishes. [Pg.49]

A. Popova, M. Christov, T. Deligeorigiev, Influence of the molecular structure on the inhibitor properties of benzimidazole derivatives on mild steel corrosion in 1 M hydrochloric acid, Corrosion 59 (2003) 756-764. [Pg.596]

Washwater for the crude unit desalter on a once-through basis to remove chloride salts that promote hydrochloric acid corrosion in the crude tower overhead condensers... [Pg.611]

D. Descdting. This is particularly important because a combination of sulfide and hydrochloric acid corrosion is exceedingly troublesome. Reduction of the salt content to 5 to 10 lb per 1,000 bbl crude oil greatly reduces the sulfide corrosion. Canister linings may be used in the settler vessels. Injection of caustic ahead of settlers to a pH of 8 to 9 helps corrosion and aids settling. [Pg.280]

Chem. Descrip. Ethoxylated amine Uses Hydrochloric acid corrosion Inhibitor Features Low foaming, high detergent will provide Inhibition to 200 F Properties Liq. sol. In water. Isopropanol, cone, and dll. HCI dens. 9.01 Ib/gal pour pt. 0 F (2000 cps) flash pt. (TCC) > 200 F pH 9-10 Ardril DMD [Aquaness ]... [Pg.1308]

Hydrogen chloride released dissolves in water during condensation in the crude oil distillation column overhead or in the condenser, which cause corrosion of materials at these locations. The action of hydrochloric acid is favored and accelerated by the presence of hydrogen sulfide which results in the decomposition of sulfur-containing hydrocarbons this forces the refiner to inject a basic material like ammonia at the point where water condenses in the atmospheric distillation column. [Pg.329]

The corrosion rate of steel in carbonic acid is faster than in hydrochloric acid Correlations are available to predict the rate of steel corrosion for different partial pressures of CO2 and different temperatures. At high temperatures the iron carbonate forms a film of protective scale on the steel s surface, but this is easily washed away at lower temperatures (again a corrosion nomogram is available to predict the impact of the scale on the corrosion rate at various CO2 partial pressures and temperatures). [Pg.94]

Benzylatnine. Warm an alcoholic suspension of 118-5 g. of finely-powdered benzyl phthalimide with 25 g. of 100 per cent, hydrazine hydrate (CAUTION corrosive liquid) a white, gelatinous precipitate is produced rapidly. Decompose the latter (when its formation appears complete) by heating with excess of hydrochloric acid on a steam bath. Collect the phthalyl hydrazide which separates by suction filtration, and wash it with a little water. Concentrate the filtrate by distillation to remove alcohol, cool, filter from the small amount of precipitated phthalyl hydrazide, render alkaline with excess of sodium hydroxide solution, and extract the liberated benzylamine with ether. Dry the ethereal solution with potassium hydroxide pellets, remove the solvent (compare Fig. //, 13, 4) on a water bath and finally distil the residue. Collect the benzylamine at 185-187° the 3ueld is 50 g. [Pg.569]

Pure vanadium is a bright white metal, and is soft and duchle. It has good corrosion resistance to alkalis, sulfuric and hydrochloric acid, and salt water, but the metal oxidizes readily above 660oC. [Pg.72]

Technetium is a silvery-gray metal that tarnishes slowly in moist air. The common oxidation states of technetium are +7, +5, and +4. Under oxidizing conditions technetium (Vll) will exist as the pertechnetate ion, TcOr-. The chemistry of technetium is said to be similar to that of rhenium. Technetium dissolves in nitric acid, aqua regia, and cone, sulfuric acid, but is not soluble in hydrochloric acid of any strength. The element is a remarkable corrosion inhibitor for steel. The metal is an excellent superconductor at IIK and below. [Pg.107]

Tantalum and 2kconium exhibit the highest corrosion resistance to HCl. However, the corrosion resistance of 2ironium is severely impaHed by the presence of ferric or cupric chlorides. Tantalum—molybdenum alloys containing more than 50% tantalum are reported to have exceUent corrosion resistance (see Molybdenumand molybdenum alloys) (69). Pure molybdenum and tungsten are corrosion resistant in hydrochloric acid at room temperature and also in 10% acid at 100°C but not in boiling 20% acid. [Pg.446]

Nickel-based aUoys have superior corrosion resistance to Hon-based aUoys. The only aUoys recommended for hot hydrochloric acid use are Ni—Mo aUoys containing 60—70% Ni and 25—33% Mo. Chlorimet (63 Ni, 32 Mo, 3 Fe) and HasteUoy (60 Ni, 28 Mo, 6 Fe) are found to be stable at aU acid concentrations in the absence of aH and Hon chlorides. Electroless nickel, a Ni—P aUoy containing 2—10% P, shows exceUent resistance to hot hydrogen chloride (71). The corrosion resistance increases with phosphoms content. This coating can be deposited on cast Hon, wrought Hon, mild steel, stainless steels, brass, bron2e, and aluminum (qv). [Pg.446]

Although lead chloride is moderately soluble in the acid, lead is also used occasionaUy in hydrochloric acid service. Addition of 6—25% Sb increases the corrosion resistance. AH and ferric chloride accelerate the corrosion. Durichlor (14.5% Si, 3% Mo, 82% Fe), a sUica-based aUoy, shows exceUent resistance to hot hydrochloric acid in the absence of ferric chloride. [Pg.446]

Cation exchangers are regenerated with mineral acids when used in the form. Sulfuric acid [8014-95-7] is preferred over hydrochloric acid [7647-01-0], HCl, in many countries because it is less expensive and less corrosive. However, the use of hydrochloric acid is the best method of overcoming precipitation problems in installations which deionize water with high concentrations of barium or calcium compared to other cations. A 4% acid concentration is common, although sulfuric acid regenerations may start as low as 0.8—1% to minimize calcium sulfate [7718-18-9] precipitation. [Pg.384]

Shipment nd Stora.ge, Sulfur monochloride is minimally corrosive to carbon steel and iron when dry. If it is necessary to avoid discoloration caused by iron sulfide formation or chloride stress cracking, 310 stainless steel should be used. Sulfur monochloride is shipped in tank cars, tank tmcks, and steel dmms. When wet, it behaves like hydrochloric acid and attacks steel, cast iron, aluminum, stainless steels, copper and copper alloys, and many nickel-based materials. Alloys of 62 Ni—28 Mo and 54 Ni—15 Cr—16 Mo are useful under these conditions. Under DOT HM-181 sulfur monochloride is classified as a Poison Inhalation Hazard (PIH) Zone B, as well as a Corrosive Material (DOT Hazard Class B). Shipment information is available (140). [Pg.138]

There are two serious problems associated with continuous tar distillation. Coal tar contains two types of components highly corrosive to ferrous metals. The ammonium salts, mainly ammonium chloride, associated with the entrained Hquor remain in the tar after dehydration, tend to dissociate with the production of hydrochloric acid and cause rapid deterioration of any part of the plant in which these vapors and steam are present above 240°C. Condensers on the dehydration column and fractionation columns are also attacked. This form of corrosion is controlled by the addition of alkaU (10% sodium carbonate solution or 40% caustic soda) to the cmde tar in an amount equivalent to the fixed ammonia content. [Pg.338]

Polytitanosiloxane (PTS) polymers containing Si—O—Ti linkages have also been synthesized through hydrolysis—polycondensation or hydrolysis—polycondensation—pyrolysis reactions involving clear precursor sol solutions consisting of monomeric silanes, TYZOR TET, methanol, water, and hydrochloric acid (Fig. 2). These PTS polymers could be used to form excellent corrosion protection coatings on aluminum substrates (171). [Pg.152]

Zirconium is totally resistant to attack of hydrochloric acid in all concentrations to temperatures well above boiling (Fig. 2). Aeration has no effect, but oxidizing agents such as cupric or ferric ions may cause pitting. Zirconium also has excellent corrosion resistance to hydrobromic and hydriodic acid. [Pg.429]

Compound (1) decomposes to form dichloroacetyl chloride, which in the presence of water decomposes to dichloroacetic acid and hydrochloric acid (HCl) with consequent increases in the corrosive action of the solvent on metal surfaces. Compound (2) decomposes to yield phosgene, carbon monoxide, and hydrogen chloride with an increase in the corrosive action on metal surfaces. [Pg.23]


See other pages where Hydrochloric acid corrosion is mentioned: [Pg.131]    [Pg.120]    [Pg.193]    [Pg.658]    [Pg.95]    [Pg.131]    [Pg.120]    [Pg.193]    [Pg.658]    [Pg.95]    [Pg.81]    [Pg.266]    [Pg.347]    [Pg.446]    [Pg.447]    [Pg.447]    [Pg.324]    [Pg.474]    [Pg.6]    [Pg.313]    [Pg.186]    [Pg.249]    [Pg.328]    [Pg.399]    [Pg.392]    [Pg.317]    [Pg.429]    [Pg.433]    [Pg.368]    [Pg.43]   
See also in sourсe #XX -- [ Pg.172 ]

See also in sourсe #XX -- [ Pg.282 , Pg.283 , Pg.289 , Pg.545 ]




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