Search over 40,000 articles from the original, classic Encyclopedia Britannica, 11th Edition.
|
See also:COPPER (See also:symbol Cu, atomic See also:weight 63.1, H=1, or 63.6, O = 16) , a See also:metal which has been known to and used by the human See also:race from the most remote periods . Its alloy with See also:tin (See also:bronze) was the first metallic See also:compound in See also:common use by mankind, and so extensive and characteristic was its employment in pre-historic times that the See also:epoch is known as the Bronze See also:Age . By the Greeks and See also:Romans both the metal and its See also:alloys were indifferently known as xaAicbr and aes . As, according to See also:Pliny, the See also:Roman See also:supply was chiefly See also:drawn from See also:Cyprus, it came to be termed aes cyprium, which was gradually shortened to cyprium, . and corrupted into cuprum, whence comes the See also:English word See also:copper, the See also:French cuivre, and the See also:German Kupfer . Copper is a brilliant metal of a See also:peculiar red See also:colour which assumes a pinkish or yellowish tinge on a freshly fractured See also:surface of the pure metal, and is purplish when the metal contains cuprous See also:oxide . Its specific gravity varies between 8.91 and 8.95, according to the treatment to which it may have been subjected; J . F . W . Hampe gives 8.945 (1o) for perfectly pure and compact copper . See also:Ordinary commercial copper is somewhat porous and has a specific gravity ranging from 8.2 to 8.5 . It takes a brilliant See also:polish, is in a high degree malleable and ductile, and in tenacity it only falls See also:short of See also:iron, exceeding in that quality both See also:silver and See also:gold . By different authorities its melting-point is stated at from l000° to 1200° C.; C . T . Heycock and F . H . See also:Neville give 1o8o •5; P . Dejean gives 1085° as the freezing-point . The molten metal is See also:sea-See also:green in colour, and at higher temperatures (in the electric arc) it vaporizes and See also:burns with a green See also:flame . G . W . A . Kahlbaum succeeded in subliming the metal in a vacuum, and H . See also:Moissan (Compt. rend., 1905, 141, p . 853) distilled it in the electric See also:furnace . Molten copper absorbs See also:carbon monoxide, See also:hydrogen and See also:sulphur dioxide; it also appears to decompose See also:hydrocarbons (methane, ethane), absorbing the hydrogen and the carbon separating out . These occluded gases are all liberated when the copper cools, and so give rise to porous castings, unless See also:special precautions are taken . The gases are also expelled from the molten metal by See also:lead, carbon dioxide, or See also:water vapour . Its specific See also:heat is o•o899 at o° C. and 0•0942 at See also:Ioo°; the coefficient of linear expansion per I° C. is o•oo1869 . In electric conductivity it stands next to silver; the conducting See also:power of silver being equal to Too, that of perfectly pure copper is given by A . Matthiessen as 96.4 at 13° C . Copper is not affected by exposure in dry See also:air, but in a moist See also:atmosphere, containing carbonic See also:acid, it becomes coated with a green basic carbonate . When heated or rubbed it emits a peculiar disagreeable odour . Sulphuric and hydrochloric acids have little or no See also:action upon it at ordinary temperatures, even when in a See also:fine See also:state of See also:division; but on See also:heating, copper sulphate and sulphur dioxide are formed in the first See also:case, and cuprous chloride and hydrogen in the second . Concentrated nitric acid has also very little action, but with the dilute acid a vigorous action ensues . The first products of this reaction are copper nitrate and nitric oxide, but, as the concentration of the copper nitrate increases, nitrous oxide and, eventually, See also:free See also:nitrogen are liberated . Many colloidal solutions of copper have been obtained .
A reddish-See also: It is not infrequently found in See also:serpentine, and in basic eruptive rocks, where it occurs as See also:veins and in amygdales . The largest known deposits are those in the See also:Lake See also:Superior region, near Keweenaw Point, See also:Michigan, where masses upwards of 400 tons in See also:weight have been discovered . The metal was formerly worked by the See also:Indians for implements and ornaments . It occurs in a See also:series of amygdaloidal dolerites or diabases, and in the associated sandstones and conglomerates . Native silver occurs with the copper, in some cases embedded in it, like crystals in a See also:porphyry . The copper is also accompanied by See also:epidote, See also:calcite, See also:prehnite, See also:analcite and other zeolitic minerals . Pseudomorphs after calcite are known; and it is notable that native copper occurs pseudomorphous after See also:aragonite at Corocoro, in See also:Bolivia, where the copper is disseminated through See also:sandstone . Ores.—The See also:principal ores of copper are the oxides See also:cuprite and See also:melaconite, the See also:carbonates See also:malachite and chessylite, the basic chloride See also:atacamite, the silicate See also:chrysocolla, the sulphides chalcocite, chalcopyrite, See also:erubescite and See also:tetrahedrite . Cuprite (q.v.) occurs in most cupriferous mines, but never by itself in large quantities . Melaconite (q.v.) was formerly largely worked in the Lake Superior region, and is abundant in some of the mines of See also:Tennessee and the See also:Mississippi valley . Malachite is a valuable ore containing about 56% of the metal; it is obtained in very large quantities from See also:South See also:Australia, See also:Siberia and other localities . Frequently intermixed with the green malachite is the See also:blue carbonate chessylite or See also:azurite (q.v.), an ore containing when pure 55'16% of the metal . Atacamite (q.v.) occurs chiefly in See also:Chile and See also:Peru . Chrysocolla (q.v.) contains in the pure state 30% of the metal; it is an abundant ore in Chile, See also:Wisconsin and See also:Missouri . The sulphur compounds of copper are, however, the most valuable from the economic point of view . Chalcocite, redruthite, copper-glance (q.v.) or vitreous copper (Cu2S) contains about 8o % of copper . Copper See also:pyrites, or chalcopyrite, contains 34.6% of copper when pure; but many of the ores, such as those worked specially by wet processes on See also:account of the presence of a large proportion of iron sulphide, contain less than 5% of copper . Cornish ores are almost entirely pyritic; and indeed it is from such ores that by far the largest proportion of copper is extracted throughout the See also:world . In See also:Cornwall copper lodes usually run See also:east and See also:west . They occur both in the " killas " or See also:clay-See also:slate, and in the " growan " or See also:granite . Erubescite (q.v.), bornite, or horseflesh ore is much richer in copper than the ordinary pyrites, and contains 56 or 57% of copper . Tetrahedrite (q.v.), fahlerz, or See also:grey copper, contains from 30 to 48% of copper, with See also:arsenic, See also:antimony, iron and sometimes See also:zinc, silver or See also:mercury . Other copper minerals are percylite (PbCuC12(OH)2), boleite (3PbCuC12(OH)2, AgC1), stromeyerite ((Cu, Ag)2S}, cubanite (CuS, Fe2S3), See also:stannite (Cu2S, FeSnS3), tennantite'(3Cu2S, As2S3), emplectite (Cu2S, Bi2S3), wolfsbergite (Cu2S, Sb2S3), famatinite (3Cu2S, Sb2S5) and enargite (3Cu2S, As2S5) . For other minerals, see Compounds of Copper below .
Metallurgy.—Copper is obtained from its ores by three principal methods, which may be denominated—(r) the pyro-metallurgical or dry method, (2) the hydro-metallurgical or wet method, and (3) the electro-metallurgical method
.
The methods of working vary according to the nature of the ores treated and See also:local circumstances
.
The dry method, or ordinary smelting, cannot be profitably practised with ores containing less than 4% of copper, for which and for still poorer ores the wet See also:process is preferred
.
Copper Smelting.—We shall first give the See also:general principles which underlie the methods for the dry extraction of copper, and then proceed to a more detailed discussion of the plant used
.
Since all sulphuretted copper ores (and these are of the most economic importance) are invariably contaminated with arsenic and antimony, it is necessary to eliminate these impurities, as far as possible, at a very See also:early See also:stage
.
This is effected by calcination or roasting
.
The roasted ore is then smelted to a mixture of copper and iron sulphides, known as copper " matte " or " coarse-metal," which contains little or no arsenic, antimony or See also:silica
.
The coarse-metal is now smelted, with See also:coke and siliceous fluxes (in See also:order to slag off the irqn), and the product, consisting of an impure copper sulphide, is variously known as
blue-metal," when more or less iron is still See also:present, " pimple-metal," when free copper and more or less copper oxide is present, or " fine " or " See also: The plant in which the operations are conducted varies in different countries . But though this or that process takes its name from the See also:country in which it has been mainly See also:developed, this does not mean that only that process is there followed . The " English process " is made up of the following operations: (r) calcination; (2) smelting in reverberatory furnaces to form the matte; (3) roasting the matte; and (4) subsequent smelting in reverberatory furnaces to fine- or white-metal; (5) treating the fine-metal in reverberatory furnaces to coarse- or See also:blister-copper, either with or without previous calcination; (6) refining of the coarse-copper . A shorter process (the so-called " direct process ") converts the fine-metal into refined copper directly . The " Welsh process " closely resembles the English method; the See also:main difference consists in the enrichment of the matte by smelting with the See also:rich copper-bearing slags obtained in subsequent operations . The " German or Swedish process " is characterized by the introduction of blast-furnaces . It is made up of the following operations: (I) calcination, (2) smelting in blast-furnaces to form the matte, (3) roasting the matte, (4) smelting in blast-furnaces with coke and fluxes to " See also:black- " or " coarse-metal," (5) refining the coarse-metal . The " Anglo-German Process " is a See also:combination of the two preceding, and consists in smelting the calcined ores in See also:shaft furnaces, concentrating the matte in reverberatory furnaces, and smelting to coarse-metal in either . The impurities contained in coarse-copper are mainly iron, lead, zinc, See also:cobalt, See also:nickel, See also:bismuth, arsenic, antimony, sulphur, See also:selenium and See also:tellurium . These can be eliminated by an oxidizing See also:fusion, and slagging or volatilizing the products resulting from this operation, or by See also:electrolysis (see below) . In the process of oxidation, a certain amount of cuprous oxide is always formed, which melts in with the copper and diminishes its softness and tenacity . It is, therefore, necessary to reconvert the oxide into the metal . This is effected by stirring the molten metal with a See also:pole of green See also:wood (" poling "); the products which arise from the See also:combustion and See also:distillation of the wood reduce the oxide to metal, and if the operation be properly conducted " tough-See also:pitch " copper, soft, malleable and exhibiting a lustrous silky fracture, is obtained . The surface of the molten metal is protected from oxidation by a layer of See also:anthracite or See also:charcoal . ".See also:Bean-shot " eopper is obtained by throwing the molten metal into hot water; if See also:cold water be used, " feathered-shot " copper is formed . " Rosette " copper is obtained as thin plates of a characteristic dark-red colour, by pouring water upon the surface of the molten metal, and removing the crust formed . " See also:Japan " copper is See also:purple-red in colour, and is formed by casting into ingots, weighing from six ounces to a See also:pound, and rapidly cooling by See also:immersion in water . The colour of these two varieties is due to a layer of oxide . " See also:Tile " copper is an impure copper, and is obtained by refining the first tappings . " Best-selected " copper is a purer variety . Calcination or Roasting and Calcining Furnaces.—The roasting should be conducted so as to eliminate as much of the arsenic and antimony as possible, and to leave just enough sulphur as is necessary to combine with all the copper present when the calcined ore is smelted . The process is effected either in heaps, stalls, shaft furnaces, reverberatory furnaces or muffle furnaces . See also:Stall and heap roasting require considerable See also:time, and can only be economically employed when the loss of the sulphur is of no consequence; they also occupy much space, but they have the See also:advantage of requiring little See also:fuel and handling . Shaft furnaces are in use for ores rich in sulphur, and where it is desirable to convert the See also:waste gases into sulphuric acid . Reverberatory roasting does not admit of the utilization of the waste gases, and requires fine ores and much labour and fuel; it has, however, the advantage of being rapid . Muffle furnaces are suitable for fine ores which are liable to decrepitate or See also:sinter . They involve high cost in fuel and labour, but permit the utilization of the waste gases . Reverberatory furnaces of three types are employed in calcining copper ores: (i) fixed furnaces, with either See also:hand or See also:mechanical rabbling; (2) furnaces with movable beds; (3) furnaces with rotating working See also:chambers . Hand rabbling in fixed furnaces has been largely superseded by mechanical rabbling . Of mechanically rabbling furnaces we may mention the O'Harra modified by See also:Allen-Brown, the Hixon, the See also:Keller-Gaylord-See also:Cole, the Ropp, the See also:Spence, the Wethey, the See also:Parkes, See also:Pearce's " See also:Turret " and Brown's " Horseshoe " furnaces . See also:Blake's and See also:Brunton's furnaces are reverberatory furnaces with a movable See also:bed . Furnaces with rotating working chambers admit of continuous working; the fuel and labour See also:costs are both See also:low . In the White-See also:Howell revolving furnace with lifters—a modification of the Oxland—the ore is fed and discharged in a continuous stream . The See also:Bruckner See also:cylinder resembles the Elliot and See also:Russell black ash furnace; its cylinder tapers slightly towards each end, and is generally i8 ft. See also:long by 8 ft . 6 in. in its greatest See also:diameter . Its See also:charge of from 8 to 12 tons of ore or concentrates is slowly agitated at a See also:rate of three revolutions a See also:minute, and in from 24 to 36 See also:hours it is reduced from say 40 or 35 % to 7 % of sulphur . The ore is under better See also:control than is possible with the continuous feed and See also:discharge, and when sufficiently roasted can be passed red-hot to the reverberatory furnace . These advantages compensate for the See also:wear and See also:tear and the cost of moving the heavy dead-weight . Shaft calcining furnaces are available for fine ores and permit the recovery of the sulphur . They are square, oblong or circular in See also:section, and the interior is fitted with See also:horizontal or inclined plates or prisms, which regulate the fall of the ore . In the Gerstenhoffer and Hasenclever-Helbig furnaces the fall is retarded by prisms and inclined plates . In other furnaces the ore rests on a series of horizontal plates, and either remains on the same See also:plate throughout the operation (011ivier and Perret furnace), or is passed from plate to plate by hand (Maletra), or by mechanical means (Spence and M'Dougall) . The M'Dougall furnace is turret-shaped, and consists of a series of circular hearths, on which the ore is agitated by rakes attached to revolving arms and made to fall from See also:hearth to hearth . It has been modified by Herreshoff, who uses a large hollow revolving central shaft cooled by a current of air . The shaft is provided with sockets, into which movable arms with their rakes are readily dropped . The See also:Peter Spence type of calcining furnace has been followed in a large number of inventions . In some the rakes are attached to rigid frames, with a reciprocating See also:motion; in others to See also:cross-bars moved by revolving chains . Some ofthese furnaces are straight, others circular . Some have only one hearth, others three . This and the previous type of furnace, owing to their large capacity, are at present in greatest favour . The M'Dougall-Herreshoff, working on ores of over 30% of sulphur, requires no fuel; but in furnaces of the reverberatory type fuel must be used, as an excess of air enters through the slotted sides and the hinged doors which open and shut frequently to permit of the passage of the rakes . The See also:consumption of fuel, however, does not exceed r of See also:coal to ro of ore . The quantity of ore which these large furnaces, with a hearth See also:area as See also:great as 2000 ft. and over, will roast varies from 40 to 6o tons a See also:day . Shaft calcining furnaces like the Gerstenhoffer, Hasenclever, and others designed for burning pyrites fines have not found favour in See also:modern copper See also:works . The Fusion of Ores in Reverberatory and See also:Cupola Furnaces.—After the ore has been partially calcined, it is smelted to See also:extract its earthy matter and to concentrate the copper with See also:part of its iron and sulphur into a matte . In reverberatory furnaces it is smelted by fuel in a fireplace, See also:separate from the ore, and in cupolas the fuel, generally coke, is in direct contact with the ore . When See also:Swansea was the centre of the copper-smelting See also:industry in See also:Europe, many varieties of ores from different mines were smelted in the same furnaces, and the Welsh reverberatory furnaces were used . To-day more than eight-tenths of the copper ores of the world are reduced to impure copper bars or to fine copper at the mines; and where the See also:character of the ore permits, the cupola furnace is found more economical in both fuel and labour than the reverberatory . The Welsh method finds adherents only in See also:Wales and Chile . In See also:America the usual method is to roast ores or concentrates so that the matte yielded by either the reverberatory or cupola furnace will run from 45 to 50% in copper, and then to See also:transfer to the Bessemer converter, which blows it up to 99 % . In See also:Butte, See also:Montana, reverberatories have in the past been preferred to cupola furnaces, as the charge has consisted mainly of fine roasted concentrates; but the cupola is gaining ground there . At the See also:Boston and Great Falls (Montana) works tilting reverberatories, modelled after open hearth See also:steel furnaces, were first erected; but they were found to possess objectionable features . Now both these and the See also:egg-shaped reverberatories are being abandoned for furnaces as long as 43 ft . 6 in. from See also:bridge to bridge and of a width of 15 ft . 9 in. heated by See also:gas, with re-generative checker See also:work at each end, and fed with ore or See also:con, centrates, red-hot from the calciners, through a See also:line of hoppers suspended above the roof . Furnaces of this See also:size See also:smelt 200 tons of charge a day . But even when the old type of reverberatory is preferred, as at the Argo works, at See also:Denver, where rich gold. and silver-bearing copper matte is made, the growth of the furnace in size has been steady . See also:Richard Pearce's reverberatories in 1878 had an area of hearth of 15 ft. by 9 ft . 8 in., and smelted 12 tons of cold charge daily, with a consumption of i ton of coal to 2.4 tons of ore . In r900 the furnaces were 35 ft. by 16 ft., and smelt 5o tons daily of hot ore, with the consumption of i ton of coal to 3.7 tons of ore . The See also:home of cupola smelting was See also:Germany, where it has never ceased to make steady progress . In See also:Mansfeld See also:brick cupola furnaces are without a See also:rival in size, equipment and performance . They are See also:round stacks, designed on the See also:model of iron blast furnaces, 29 ft. high, fed mechanically, and provided with stoves to heat the blast by the furnace gases . The low percentage of sulphur in the roasted ore is little more than enough to produce a matte of 40 to 45%, and therefore the escaping gases are better fitted than those of most copper cupola furnaces for burning in a See also:stove . But as the slag carries on an See also:average 46 % of silica, it is only through the utmost skill that it can be made to run as low on an average as o•3 % in copper oxide . As the matte contains on an average o•2% of silver, it is still treated by the Ziervogel wet method of extraction, the management dreading the loss which might occur in the Bessemer process of concentration, applied as preliminary to electrolytic separation . Blast furnaces of large size, built of brick, have been constructed for treating the richest aDd more silicious ores of Rio Tinto, and the Rio Tinto See also:Company has introduced converters at the mine . This method of extraction contrasts favourably in time with the leaching process, which is so slow that over ro,000,000 tons of ore are always under treatment on the immense leaching floors of the company's works in See also:Spain . In the See also:United States the cupola has undergone a See also:radical modification in being built of water-jacketed sections . The first water-jacketed cupola which came into general use was a circular inverted See also:cone, with a slight See also:taper, of 36 inches diameter at the tuyeres, and composed of an See also:outer and an inner metal See also:shell, between which water circulated . As greater size has been demanded, See also:oval and rectangular furnaces—as large as 18o in. by 56 in. at the tuyereshave been built in sections of See also:cast or See also:sheet iron or steel . A single section can be removed and replaced without entirely emptying the stack, as a shell of congealed slag always coats the inner surface of the jacket . The largest furnaces are those of the Boston & Montana Company at Great Falls, Montana, which have put through 500 tons of charge daily, pouring their melted slag and matte into large See also:wells of ro ft. in diameter . A combined brick- and water-cooled furnace has been adopted by the Iron See also:Mountain Company at See also:Keswick, Cal., for matte concentration .
In it the cooling is effected by water pipes, interposed horizontally between the layers of bricks
.
The Mt
.
See also:Lyell smelting works in See also:Tasmania, which are of special See also:interest, will be referred to later
.
(See Pyritic Smelting below.)
Concentrating Matte to Copper in the Bessemer Converter.—As soon as the pneumatic method of decarburizing See also:pig iron was accepted as practicable, experiments were made with a view to Bessemerizing copper ores and mattes
.
One of the earliest and most exhaustive series of experiments was made on Rio Tinto ores at the See also: Vessels of several designs are used—some modelled exactly after steel converters, other See also:barrel-shaped, but all with side tuyeres elevated about so in. above the level of the bottom lining . Practice, however, in treating copper matte differs essentially from the treatment of pig iron, inasmuch as from 20 to 30% of iron must be eliminated as slag and an See also:equivalent quantity of silica must be supplied . The only See also:practical mode of doing this, as yet devised, is by lining the converter with a silicious mixture . This is so rapidly consumed that the converters must be cooled and partially relined after 3 to 6 charges, dependent on the iron contents of the matte . When available, a silicious rock containing copper or the See also:precious metals is of course preferred to barren lining . The material for lining, and the frequent replacement thereof, constitute the principal expense of the method . The other items of cost are labour, the quantity of which depends on the mechanical appliances provided for handling the converter shells and inserting the lining; and the blast, which in barrel-shaped converters is low and in See also:vertical converters is high, and which varies therefore from 3 to 15 lb to the square See also:inch . The quantity of air consumed in a converter which will See also:blow up about 35 tons of matte per day is about 3000 cub. ft. per minute . The operation of raising a charge of 50% matte to copper usually consists of two blows . The first blow occupies about 25 minutes, and oxidizes all but a small quantity of the iron and some of the sulphur, raisingthe product to white metal . The slag is then poured and skimmed, the blast turned on and converter retilted . During the second blow the sulphur is rapidly oxidized, and the charge reduced to metal of 99% in from 30 to 40 minutes . Little or no slag results from the second blow . That from the first blow contains between 1% and 2% of copper, and is usually poured from ladles operated by an electric See also:crane into a reverberatory, or into the settling well of the cupola . The matte also, in all economically planned works, is conveyed, still molten, by electric See also:cranes from the furnace to the converters . When lead or zinc is not present in notable quantity, the loss of the precious metals by volatilization is slight, but more than 5% of these metals in the matte is prohibitive . Under favourable conditions in the larger works of the United States the cost of converting a 50% matte to metallic copper is generally understood to be only about 15w to 3- of a cent per lb. of refined copper . Pyritic Smelting.—The heat generated by the oxidation of iron and sulphur has always been used to maintain combustion in the kilns or stalls for roasting pyrites . Pyritic smelting is a development of the See also:Russian engineer Semenikov's treatment (proposed in 1866) of copper matte in a Bessemer converter . Since John Hollway's and other early experiments of See also:Lawrence See also:Austin and See also:Robert Sticht, no serious attempts have been made to utilize the heat escaping from a converting See also:vessel in smelting ore and matte either in the same apparatus or in a separate furnace . But considerable progress has been made in smelting highly sulphuretted ores by the heat of their own oxidizable constituents . At Tilt See also:Cove, See also:Newfoundland, the Cape Copper . Company smelted copper ore, with just the proper proportion of sulphur, iron and silica, successfully without any fuel, when once the initial charge had been fused with coke . The furnaces used were of ordinary See also:design and built of brick . Lump ore alone was fed, and the resulting matte showed a concentration of only 3 into i . When, however, a hot blast is used on highly sulphuretted copper ores, a concentration of 8 of ore into 1 of matte is obtained, with a consumption of less than one-third the fuel which would be consumed in smelting the charge had the ore been previously calcined . A great impetus to pyritic smelting was given by the investigations of W . L . Austin, of Denver, See also:Colorado, and both at See also:Leadville and Silverton raw ores are successfully smelted with as low a fuel consumption as 3 of coke to too of charge . Two types of pyritic smelting may be distinguished: one, in which the operation is solely sustained by the combustion of the sulphur in the ores, without the assistance of fuel or a hot blast; the other in which the operation is accelerated by fuel, or a hot blast, or both . The largest See also:establishment in which advantage is taken of the self-contained fuel is at the smelting works of the Mt . Lyell Company, Tasmania . There the blast is raised from 600° to 700 F. in stoves heated by extraneous fuel, and the raw ore smelted with only 3 % of coke . The ore is a compact iron pyrites containing copper 2.5%, silver 3'83 oz., gold 0.139 oz . It is smelted raw with hot blast in cupola furnaces, the largest being 210 in. by 40 in . The resulting matte runs 25% .
This is reconcentrated raw in hot-blast cupolas to 55%, and blown directly into copper in converters
.
Thus these ores, as heavily charged with sulphur as those of the Rio Tinto, are speedily reduced by three operations and without roasting, with a saving of 97.6% of the copper, 93'2% of the silver and 93.6% of the gold
.
Pyritic smelting has met with a varying economic success
.
According to See also:Herbert See also:Lang, its most prominent See also:chance of success is in localities where fuel is dear, and the ores contain precious metals and sufficient sulphides and arsenides to render profitable dressing unnecessary
.
The Nicholls and See also:
Ores in which the copper is present as oxide or carbonate are soluble in sulphuric or hydrochloric acids, ferrous chloride, ferric sulphate,ammoniacal compounds and See also:sodium thiosulphate
.
Of these solvents, only the first three are of economic importance
.
The choice of sulphuric or hydrochloric acid depends mainly upon the cost, both acting with about the same rapidity; thus if a Leblanc soda factory is near at hand, then hydrochloric acid would most certainly be employed
.
Ferrous chloride is not much used; the See also:Douglas-See also:Hunt process uses a mixture of See also:salt and ferrous sulphate which involves the formation of ferrous chloride, and the new Douglas-Hunt process employs sulphuric acid in which ferrous chloride is added after leaching
.
Sulphuric acid may be applied as such on the ores placed in lead, brick, or See also: The advantage of this method rests chiefly on the small amount of iron required; but its disadvantages are that any silver present in the ores goes into solution, the formation of basic salts, and the difficulty of filtering from the iron oxides . A modification of the method was designed to remedy these defects . The ore is first treated with dilute sulphuric acid, and then ferrous or See also:calcium chloride added, thus forming copper chlorides . If calcium chloride be used the precipitated calcium sulphate must be removed by filtration . Sulphur dioxide is then blown in, and the precipitate is treated with iron, which produces metallic copper, or See also:milk of See also:lime, which produces cuprous oxide . Hot air is blown into the filtrate, which contains ferrous or calcium chlorides, to expel the excess of sulphur dioxide, and the liquid can then be used again . In this process (" new Douglas-Hunt") there are no iron oxides formed, the silver is not dissolved, and the quantity of iron necessary is relatively small, since all the copper is in the cuprous See also:condition . It is not used in the treatment of ores, but finds application in the case of calcined argentiferous lead and copper mattes . The precipitation of the copper from the solution, in which it is present as sulphate, or as cuprous and cupric chlorides, is generally effected by metallic iron . Either wrought, pig, iron sponge or iron bars are employed, and it is important to See also:notice that the form in which the copper is precipitated, and also the time taken for the separation, largely depend upon the condition in which the iron is applied . Spongy iron acts most rapidly, and after this follow iron turnings and then sheet clippings . Other precipitants such as sulphuretted hydrogen and solutions of sulphides, which precipitate the copper as sulphides, and milk of lime, which gives copper oxides, have not met with commercial success . When using iron as the precipitant, it is desirable that the solution should be as neutral as possible, and the quantity of ferric salts present should be reduced to a minimum; otherwise, a certain amount of iron would be used up by the free acid and in reducing the ferric salts . Ores in which the copper is present as sulphate are directly lixiviated and treated with iron . Mine waters generally contain the copper in this form, and it is extracted by conducting the waters along troughs fitted with iron gratings . The wet extraction of metallic copper from ores in which it occurs as the sulphide, may be considered to involve the following operations: (1) See also:conversion of the copper into a soluble form, (2) dissolving out the soluble copper salt, (3) the precipitation of the copper . Copper sulphide may be converted either into the sulphate, which is soluble in water; the oxide, soluble in sulphuric or hydrochloric acid; cupric chloride, soluble in water; or cuprous chloride, which is soluble in solutions of metallic chlorides . The conversion into sulphate is generally effected by the oxidizing processes of weathering, calcination, heating with iron nitrate or ferric sulphate . It may also be accomplished by calcination with ferrous sulphate, or other easily decomposable sulphates, such as See also:aluminium sulphate . Weathering is a very slow, and, therefore, an expensive process; moreover, the entire conversion is only accomplished after a number of years . Calcination is only advisable for ores which contain relatively much iron pyrites and little copper pyrites . Also, however slowly the calcination may be conducted, there is always more or less copper sulphide See also:left unchanged, and some copper oxide formed . Calcination with ferrous sulphate converts all the copper sulphide into sulphate . Heap roasting has been successfully employed at Agordo, in the Venetian See also:Alps, and at Majdanpek in See also:Servia .
Josef Perino's process, which consists in heating the ore with iron nitrate to 500-1500 C., is said to possess several advantages, but it has not been applied commercially
.
Ferric sulphate is only used as an See also:auxiliary to the weathering process and in an electrolytic process
.
The conversion of the sulphide into oxide is adopted where the Douglas-Hunt process is employed, or where hydrochloric or sulphuric acids are cheap
.
The calcination is effected in reverberatory furnaces, or in muffle furnaces, if the sulphur is to be recovered
.
Heap, stall or shaft furnace roasting is not very satisfactory, as it is very difficult to transform all the sulphide into oxide
.
The conversion of copper sulphide into the chlorides may be accomplished by calcining with common salt, or by treating the ores with ferrous chloride and hydrochloric acid or with ferric chloride
.
The dry way is best; the wet way is only employed when fuel is very dear, or when it is absolutely necessary that no noxious vapours should See also:escape into the atmosphere
.
The dry method consists in an oxidizing roasting of the ores, and a subsequent chloridizing roasting with either common salt or Abraumsalz in reverberatory or muffle furnaces
.
The bulk of the copper is thus transformed into cupric chloride, little cuprous chloride being obtained
.
This method had been long proposed by See also: The wet method is employed at Rio Tinto, the particular variant being known as the " Dotsch " process . This consists in stacking the broken ore in heaps and adding a mixture of sodium sulphate and ferric chloride in the proportions necessary for the entire conversion of the iron into ferric sulphate . The heaps are moistened with ferric chloride solution, and the reaction is nfaintained by the liquid percolating through the heap . The liquid is run off at the See also:base of the heaps into the precipitating tanks, where the copper is thrown down by means of metallic iron . The ferrous chloride formed at the same time is converted into ferric chloride which can be used to moisten the heaps . This conversion is effected by allowing the ferrous chloride liquors slowly to descend a See also:tower, filled with pieces of wood, coke or See also:quartz, where it meets an ascending current of See also:chlorine . The sulphate, oxide or chlorides, which are obtained from the sulphuretted ores, are lixiviated and the metal precipitated in the same manner as we have previously described . The metal so obtained is known as " See also:cement " copper . If it contains more than 55% of copper it is directly refined, while if it contains a See also:lower percentage it is smelted with matte or calcined copper pyrites . The chief impurities are basic salts of iron, free iron, See also:graphite, and sometimes silica, antimony and iron arsenates . Washing removes some of these impurities, but some copper always passes into the slimes . If much carbonaceous matter be present (and this is generally so when iron sponge is used as the precipitant) the crude product is heated to redness in the air; this burns out the carbon, and, at the same time, oxidizes a little of the copper, which must be subsequently reduced . A similar operation is conducted when arsenic is present; basic-lined reverberatory furnaces have been used for the same purpose . Electrolytic Refining.—The principles have long been known on which is based the electrolytic separation of copper from the certain elements which generally accompany it, whether these, like silver and gold, are valuable, or, like arsenic, antimony, bismuth, selenium and tellurium, are merely impurities . But it was not until the See also:dynamo was improved as a See also:machine for generating large quantities of See also:electricity at a very low cost that the electrolysis of copper could be practised on a commercial See also:scale . To-day, by See also:reason of other uses to which electricity is applied, electrically deposited copper of high conductivity is in ever-increasing demand, and commands a higher See also:price than copper refined by fusion . This increase in value permits of copper with 4 not over L2 or $ro See also:worth of the precious metals being profitably subjected to electrolytic treatment . Thus many million ounces of silver and a great See also:deal of gold are recovered which formerly were lost . The earliest serious See also:attempt to refine copper industrially was made by G . R . See also:Elkington, whose first patent is dated 1865 . He cast crude copper, as obtained from the ore, into plates which were used as anodes, sheets of electro-deposited copper forming the cathodes . Six anodes were suspended, alternately with four cathodes, in a saturated solution of copper sulphate in a cylindrical See also:fire-clay trough, all the anodes being connected in one parallel See also:group, and all the cathodes in another . A See also:hundred or more jars were coupled in series, the cathodes of one to the anodes of the next, and were so arranged that with the aid of side-pipes with leaden connexions and See also:india-See also:rubber See also:joints the electrolyte could, once daily, be made to circulate through them all from the See also:top of one See also:jar to the bottom of the next .
The current from a See also:Wilde's dynamo was passed, apparently with a current See also:density of 5 or 6 amperes per sq. ft., until the anodes were too crippled for further use
.
The cathodes, when thick enough, were either cast and rolled or sent into the See also:market direct
.
Silver and other insoluble impurities collected at the bottom of the trough up to the level of the lower side-See also:tube, and were then run off through a plug in the bottom into settling tanks, from which they were removed for metallurgical treatment
.
The electrolyte was used until the See also:accumulation of iron in it was too great, but was mixed from time to time with a little water acidulated by sulphuric acid
.
This process is of historic interest, and in principle it is identical with that now used
.
The modifications introduced have been chiefly in details, in order to economize materials and labour, to ensure purity of product, and to increase the rate of deposition
.
The See also:chemistry of the process has been studied by See also: It should be observed that the free acid is gradually neutralized, partly by chemical action on certain constituents of the slime, partly by local action between different metals of the anode, both of which effect solution independently of the current, and partly by the peroxidation (or aeration) of ferrous sulphate formed from the iron in the anode . At the same time there is a See also:gradual substitution of other metals for copper in the solution, because although copper plus other (more electro-See also:positive) metals are constantly dissolving at the anode, only copper is deposited at the cathode . Hence the See also:composition and acidity of the solution, on which so much depends, must be constantly watched . The dependence of the mechanical qualities of the copper upon the current-density employed is well known . A very weak current gives a See also:pale and brittle deposit, but as the current-density is in-creased up to a certain point, the properties of the metal improve; beyond this point they deteriorate, the colour becoming darker and the deposit less coherent, until at last it is dark brown and spongy or pulverulent . The presence of even a small proportion of hydrochloric acid imparts a brown tint to the deposit . See also:Baron H. v . Hiibl (Miltheil. See also:des k. k. mililar-geograph . Inst., 1886, vol. vi. p . 51) has found that with neutral solutions a 5 % solution of copper sulphate gave no See also:good result, while with a go ''A solution the best deposit was obtained with a current-density of 28 amperes per sq. ft.; with solutions containing 2 % of sulphuric acid, the 5 % solution gave good deposits with current-densities of 4 to 7.5 amperes, and the 20% solution with 11.5 to 37 amperes, per sq. ft . The maximum current-densities for a pure acid solution at See also:rest were : for 15 % pure copper sulphate solutions 14 to 21 amperes, and for 20 % solutions 18.5 to 28 amperes, per sq. ft.; but when the solutions were kept in See also:gentle motion these See also:maxima could be increased to 21-28 and 28-37 amperes per sq. ft. respectively . The See also:necessity for adjusting the current-density to the composition and treatment of the electrolyte is thus apparent .
The advantage of keeping the solution in motion is due partly to the renewal of solution thus effected in the neighbourhood of the electrodes, and partly to the neutralization of the tendency of liquids undergoing electrolysis to separate into layers, due to the different specific gravities of the solutions flowing from the opposing electrodes
.
Such an irregular See also:distribution of the See also:bath, with strong copper sulphate solution from the anode at the bottom and acid solution from the cathode at the top, not only alters the conductivity in differeit strata and so causes irregular current-distribution, but may lead to the current-density in the upper layers being too great for the proportion of copper there present
.
Irregular and defective deposits are therefore obtained
.
See also:Provision for circulation of solution is made in the systems of copper-refining now in use
.
See also: H . Thofehrn in America and J . C . See also:Graham iii England have patented processes by which jets of the electrolyte are caused to impinge with considerable force upon the surface of the cathode, so that the renewal of the liquid at this point takes See also:place very rapidly, and current-densities per sq. ft. of 5o to too amperes are recommended by the former, and of 300 amperes by the latter . Graham has described experiments in this direction, using a See also:jet of electrolyte forced (beneath the surface of the bath) through a hole in the anode upon the surface of the cathode . Whilst the jet was playing, a good deposit was formed with so high a current-density as 28o amperes per sq. ft., but if the jet was checked, the deposit (now in a still liquid) was instantaneously ruined . When two or more jets were used side by side the deposit was good opposite the centre of each, but See also:bad at the point where two currents met, because the rate of flow was reduced . By introducing perforated See also:shields of ebonite between the electrodes, so that the full current-density was only attained at the centres of the jets, these See also:ill effects could be prevented . One of the chief troubles met with was the formation of arborescent growths around the edges of the cathode, due to the greater current-density in this region; this, however, was also obviated by the use of screens . By means of a very brisk rotation of cathode, combined with a rapid current of electrolyte, J . W . See also:Swan has succeeded in depositing excellent copper at current-densities exceeding woo amperes per sq. ft . The methods by which such results are to be obtained cannot, however, as yet be practised economically on a working scale; one great difficulty in applying them to the refining of metals is that the jets of liquid would be liable to carry with them articles of anode mud, and Swan has shown that the presence of solid particles in the electrolyte is one of the most fruitful causes of the well-known nodular growths on electrodeposited copper . Experiments on a working scale with one of the jet processes in America have, it is reported, been given up after a full trial . In copper-refining practice, the current-density commonly ranges from 7.5 to 12 or 15, and occasionally to 18, amperes per sq. ft . The See also:electrical pressure required to force a current of this intensity through the solution, and to overcome a certain opposing electromotive force arising from the more electro-negative impurities of the anode, depends upon the composition of the bath and of the anodes, the distance between the electrodes, and the temperature, but under the usual working conditions averages 0.3 volt for every pair of electrodes in series . In nearly all the processes now used, the solution contains about I q to 2 lb of copper sulphate and from 5 to 10 oz. of sulphuric acid per gallon of water, and the space between the electrodes is from 11 to 2 in., whilst the See also:total area of cathode surface in each tank may be 200 sq. ft., more or less . The anodes are usually cast copper plates about (say) 3 ft. by 2 ft. by or t in . The cathodes are frequently of electro-deposited copper, deposited to a thickness of aboutz in. on black-leaded copper plates, from which they are stripped before use . The tanks are commonly constructed of wood lined with lead, or tarred inside, and are placed in See also:terrace See also:fashion each a little higher than the next in series, to facilitate the flow of solution through them all from a cistern at one end to a well at the other . Gangways are left between adjoining rows of tanks, and an overhead travelling-crane facilitates the removal of the electrodes . The arrangement of the tanks depends largely upon the voltage available from the electric generator selected; commonly they are divided into See also:groups, all the See also:baths in each group being in series . In the huge See also:Anaconda plant, for example, in which 15o tons of refined copper can be produced daily by the Thofehrn multiple system (not the jet system alluded to above), there are 600 tanks about 84 ft. by 4; ft. by 3; ft. deep, arranged in three groups of 200 tanks in series . The connexions are made by copper rods, each of which, in length, is twice the width of the tank, with a See also:bayonet-See also:bend in the See also:middle, and serves to support the cathodes in the one and the anodes in the next tank . Self-registering voltmeters indicate at any moment the potential difference in every tank, and therefore give notice of short circuits occur-See also:ring at any part of the See also:installation . The chief See also:differences between the commercial systems of refining See also:lie in the arrangement of the baths, in the disposition and manner of supporting the electrodes in each, in the method of circulating the solution, and in the current-density employed . The various systems are often classed in two groups, known respectively as the Multiple and Series systems, depending upon the arrangement of the electrodes in each tank . Under the multiple system anodes and cathodes are placed alternately, all the anodes in one tank being connected to one See also:rod, and all the cathodes to another, and the potential difference between the terminals of each tank is that between a single pair of plates . Under the series system only the first anode and the last cathode are connected to the conductors; between these are suspended, isolated from one another, a number of intermediate bi-polar electrode plates of raw copper, each of these plates acting on one side as a cathode, receiving a deposit of copper, and on the other as an anode, passing into solution; the voltage between the terminals of the tank will be as many times as great as that between a single pair of plates as there are spaces between electrodes in the tank . In time the original impure copper of the plates becomes replaced by refined copper, but if the plates are initially very impure and dissolve irregularly, it may happen that much residual scrap may have to be remelted, or that some of the metal may be twice refined, thus involving awaste of See also:energy . Moreover, the high potential difference between the terminals of the series tank introduces a greater danger of short-circuiting through scraps of metal at the bottom of the bath ; for this reason, also, lead-lined vats are inadmissible, and tarred slate tanks are often used instead . A valuable comparison of the multiple and series systems has been published by E . Keller (see The Mineral Industry, New See also:York, 1899, vol . Vii. p . 229) . G . Kroupa has calculated that the cost of refining is 8s. per ton of copper higher under the series than it is under the multiple system ; but against this, it must be remembered that the new works of the See also:Baltimore Copper Smelting and See also:Rolling Company, which are as large as those of the Anaconda Copper See also:Mining Company, are using the See also:Hayden process, which is the chief representative of the several series systems . In this system rolled copper anodes are used; these, being purer than many cast anodes, having See also:flat surfaces, and being held in place by guides, dissolve with great regularity and require a space of only t in. between the electrodes, so that the potential difference between each pair of plates may be reduced to 0.15–0.2 volt . J . A . W . Borchers, in Germany, and A . E . See also:Schneider and O . Szontagh, in America, have introduced a method of circulating the solution in each vat by forcing air into a vertical See also:pipe communicating between the bottom and top of a tank, with the result that the bubbling of the air upward aspirates solution through the vertical pipe from below, at the same time aerating it, and causing it to overflow into the top of the tank . Obviously this slow circulation has but little effect on the rate at which the copper may be de-posited . The electrolyte, when too impure for further use, is commonly recrystallized, or electrolysed with insoluble anodes to recover the copper . The yield of copper per ampere (in round See also:numbers, z oz. of copper per ampere per diem) by See also:Faraday's See also:law is never attained in practice ; and although 98 % may with care be obtained, from 94 to 96% represents the more usual current-efficiency . With 100 % current-efficiency and a potential difference of 0.3 volt between the electrodes, lb of copper should require about 0.154 electrical See also:horse-power hours as the amount of energy to be expended in the tank for its See also:production . In practice the See also:expenditure is somewhat greater than this; in large works the See also:gross horse-power required for the refining itself and for power and See also:lighting in the factory may not exceed 0.19 to 0.2 (or in smaller works 0.25) horse-power hours per pound of copper refined . Many attempts have been made to use crude sulphide of copper or matte as an anode, and recover the copper at the cathode, the sulphur and other insoluble constitutents being left at the anode . The best known of these is the Marchese process, which was tested on a working scale at See also:Genoa and See also:Stolberg in Rhenish See also:Prussia . As the operation proceeded, it was found that the voltage had to be raised until it became prohibitive, while the anodes rapidly became honeycombed through and, crumbling away, filled up the space at "the bottom of the vat . The process was abandoned, but in a modified form appears to be now in use in Nijni-See also:Novgorod in See also:Russia . See also:Siemens and Halske introduced a combined process in which the ore, after being part-roasted, is leached by solutions from a previous electrolytic operation, and the resulting copper solution electrolysed . In this process the anode solution had to be kept separate from the cathode solution, and the membrane which had in consequence to be used, was liable to become torn, and so to cause trouble by permitting the two solutions to mix . Modifications of the process have therefore been tried . Modern methods in copper smelting and refining have effected enormous See also:economy in time, space, and labour, and have consequently increased the world's output . With pyritic smelting a sulphuretted copper ore, fed into a cupola in the See also:morning, can be passed directly to the converter, blown up to metal, and shipped as 99% bars by evening—an operation which formerly, with heap roasting of the ore and repeated roasting of the mattes in stalls, would have occupied not less than four months . A large furnace and a Bessemer converter, the pair capable of making a million pounds of copper a See also:month from a low-grade sulphuretted ore, will not occupy a space of more than 25 ft. by zoo ft.; and whereas, in making metallic copper out of a low-grade sulphuretted ore, one day's labour used to be expended on every ton of ore treated, to-day one day's labour will carry at least four tons of ore through the different mechanical and metallurgical processes necessary to reduce them to metal . About 7o% of the world's See also:annual copper output is refined electrolytically, and from the 461,583 tons refined in the United States in 1907, there were recovered 13,995,436 oz. of silver and 272,150 oz. of gold . The recovery of these valuable metals has contributed in no small degree to the expansion of electrolytic refining . Production.—The See also:sources of copper, its applications and its metallurgy, have undergone great changes . Chile was the largest producer in 1869 with 54,867 tons; but in 1899 her production had fallen off to 25,000 tons . Great See also:Britain, though she had made See also:half the world's copper in 183o, held second place in r86o, making from native ores 15,968 tons; in 1900 her production was 777 tons, and in 1907, 711 tons . The United States made only 572 tons in 185o, and 12,600 tons in 1870; but she to-day makes more than 6o% of the world's total . In 1879, Spain was the largest producer, but now ranks third . The estimated total production for each See also:decade of the 19th See also:century in metric tons is here shown: 18oI-1810 91,000 1811-1820 96,000 1821-1830 135,000 1831-1840 ^ 218,400 1841-1850 • 291,000 1851-1860 • 506,999 1861-1870 900,000 1871-1880 I,189,000 1881-1890 . 2,373,398 1891-1900 3,708,901 The following table gives the output of various countries and the world's production for the years 1895, 1900, 1905, 1907:- Country . 1895 . 1900 . 1905 . 1907 . United States . . 175,294 274,933 397,003 398,736 Spain and See also:Portugal 55,755 53,718 45,527 50,470 Japan . . . 18,725 28,285 36,485 49,718 Chile 22,428 26,016 29,632 27,112 Germany . . 16,799 20,635 22,492 20,818 See also:Australasia Io,16o 23,368 34,483 41,910 See also:Mexico 12,806 22,473 70,010 61,127 Russia 5,364 8,128 8,839 15,240 World's production . 339,994 496,819 699,514 723,807 As the stock on hand rarely exceeds three months' demand, and is often little more than a month's supply, it is evident that consumption has kept See also:close See also:pace with production . The large demand for copper to be used in sheathing See also:ships ceased on the introduction of iron in See also:shipbuilding because of the difficulty of coating iron with an impervious layer of copper; but the consumption in the manufacture of electric apparatus and for electric conductors has far more than compensated . Alloys of Copper,-Copper unites with almost all other metals, and a large number of its alloys are of importance in the arts . The principal alloys in which it forms a leading ingredient are See also:brass, bronze, and German or nickel silver; under these several heads their respective applications and qualities will be found . Compounds of Copper.-Copper probably forms six oxides, viz . Cu40, Cu30, Cu2O, CuO, Cu20, and CuOs . The most important are cuprous oxide, Cu2O, and cupric oxide, CuO, both of Oxides which give rise to well-defined series of salts . The other and by oxides do not possess this See also:property, as is also the case droxides. of the hydrated oxides Cu3022H2O and Cu4025H2O, de-scribed by M . Siewert . Cuprous oxide, Cu2O, occurs in nature as the mineral cuprite (q.v.) . It may be prepared artificially by heating copper See also:wire to a white heat, and afterwards at a red heat, by the atmospheric oxidation of copper reduced in hydrogen, or by the slow oxidation of the metal udder water, It is obtained as a fine red crystalline precipitate by reducing an alkaline copper solution with See also:sugar . When finely divided it is of a fine red colour . It fuses at red heat, and See also:colours See also:glass a See also:ruby-red . The property was known to the ancients and during the middle ages; it was then lost for several centuries, to be rediscovered in about 1827 . Cuprous oxide is reduced by hydrogen, carbon monoxide, charcoal, or iron, to the metal ; it dissolves in hydrochloric acid forming cuprous chloride, and in other mineral acids to form cupric salts, with the separation of copper . It dissolves in See also:ammonia, forming a colourless solution which rapidly oxidizes and turns blue . A hydrated cuprous oxide, (4Cu2O, H20), is obtained as a See also:bright yellow See also:powder, when cuprous chloride is treated with potash or soda . It rapidly absorbs oxygen, assuming a blue colour . Cuprous oxide corresponds to the series of cuprous salts, which are mostly white in colour, insoluble in water, and readily oxidized to cupric salts . Cupric oxide, CuO, occurs in nature as the mineral melaconite (q.v.), and can be obtained as a hygroscopic black powder by the gentle ignition of copper nitrate, carbonate or hydroxide; also by heating the hydroxide . It oxidizes carbon compounds to carbon dioxide and water, and therefore finds extensive application in See also:analytical organic chemistry . It is also employed to colour glass, to which it imparts a See also:light green colour . Cupric hydroxide, Cu(OH)2, is obtained as a greenish-blue flocculent precipitate bymixing cold solutions of potash and a cupric salt . This precipitate always contains more or less potash, which cannot be entirely removed by washing . A purer product is obtained by adding ammonium chloride, filtering, and washing with hot water . Several hydrated oxides, e.g . Cu(OH),.3CuO,Cu(OH)2.6H2O,6CuO•See also:H2O, have been described . Both the oxide and hydroxide dissolve in ammonia to form a beautiful See also:azure-blue solution (Schweizer's reagent), which dissolves See also:cellulose, or perhaps, holds it in suspension as water does See also:starch; accordingly, the solution rapidly perforates See also:paper or See also:calico . The salts derived from cupric oxide are generally white when anhydrous, but blue or green when hydrated . Copper quadrantoxide, Cu40, is an See also:olive-green powder formed by mixing well-cooled solutions of copper sulphate and alkaline stannous chloride . The trientoxide, Cu3O, is obtained when cupric oxide is heated to 1500°-2000° C . It forms yellowish-red crystals, which scratch glass, and are unaffected by all acids except hydrofluoric; it also dissolves in molten potash . Copper dioxide, CuO2H20, is obtained as a yellowish-brown powder, by treating cupric See also:hydrate with hydrogen peroxide . When moist, it decomposes at about 6° C., but the dry substance must be heated to about 18o°, before decomposition sets in (see L . See also:Moser, Abst . J.C.S., 1907, H. p . 549) . Cuprous hydride, (CuH)a, was first obtained by See also:Wurtz in 1844, who treated a solution of copper sulphate with hypophosphorous acid, at a temperature not exceeding 7o° C . According to E . J . See also:Bartlett and W . H . See also:Merrill, it decomposes when heated, and gives cupric hydride, CuH2, as a reddish-brown spongy See also:mass, which turns to a See also:chocolate colour on exposure . It is a strong reducing See also:agent . Cuprous fluoride, CuF, is a ruby-red crystalline mass, formed by heating cuprous chloride in an atmosphere of hydrofluoric acid at 1100°-12oo° C . It is soluble in boiling hydrochloric acid, but it is not reprecipitated by water, as is the case with cuprous chloride . Cupric fluoride, CuF2, is obtained by dissolving cupric oxide in hydrofluoric acid . The hydrated form, (CuF2, 2H2O, 5HF),is obtained as blue crystals, sparingly soluble in cold water; when heated to See also:loo° C. it gives the compound CuF(OH), which, when heated with ammonium fluoride in a current of carbon dioxide, gives anhydrous copper fluoride as a white powder . Cuprous chloride, CuCI or Cu2C12, was obtained by Robert See also:Boyle by heating copper with mercuric chloride . It is also obtained by burning the metal in chlorine, by heating copper and cupric oxide with hydrochloric acid, or copper and cupric chloride with hydrochloric acid . It dissolves in the excess of acid, and is precipitated as a white crystalline powder on the addition of water . It melts at below red heat to a brown mass, and its vapour density at both red and white heat corresponds to the See also:formula Cu2Cl2• It turns dirty See also:violet on exposure to air and light; in moist air it absorbs oxygen and forms an oxychloride . Its solution in hydrochloric acid readily absorbs carbcn monoxide and See also:acetylene; hence it finds application in gas See also:analysis . Its solution in ammonia is at first colourless, but rapidly turns blue, owing to oxidation . This solution absorbs acetylene with the precipitation of red cuprous acetylide, Cu2C2, a very explosive compound . Cupric chloride, CuC12, is obtained by burning copper in an excess of chlorine, or by heating the hydrated chloride, obtained by dissolving the metal or cupric oxide in an excess of hydrochloric acid . It is a brown deliquescent powder, which rapidly forms the green hydrated salt CuC12, 2I-P2O on exposure . The oxychloride Cu302C12.4H2O is obtained as a pale blue precipitate when potash is added to an excess of cupric chloride . The oxychloride Cu40,C12,4H2O occurs in nature as the mineral atacamite . It may be artificially prepared by heating salt with ammonium copper sulphate to loo° . Other naturally occurring oxychlorides are botallackite and tallingite . " See also:Brunswick green," a light green pigment, is obtained from copper sulphate and See also:bleaching powder . The bromides closely resemble the chlorides and fluorides . Cuprous iodide, Cu2I2, is obtained as a white powder, which suffers little alteration on exposure, by the direct See also:union of its components or by mixing solutions of cuprous chloride in hydrochloric acid and See also:potassium iodide; or, with liberation of See also:iodine, by adding potassium iodide to a cupric salt . It absorbs ammonia, forming the compound Cu2I2, 4NH3 . Cupric iodide is only known in combination, as in CuI2, 4NH3, H2O, which is obtained by exposing Cu212,4NH3 to moist air . Cuprous sulphide, Cu2S, occurs in nature as the mineral chalcocite or copper-glance (q.v.), and may be obtained as a black brittle mass by the direct combination of its constituents . (See above, Metallurgy.) Cupric sulphide, CuS, occurs in nature as the mineral covellite . It may be prepared by heating cuprous sulphide with sulphur, or triturating cuprous sulphide with cold strong nitric acid, or as a dark brown precipitate by treating a copper solution with sulphuretted hydrogen . Several polysulphides, e.g . Cu2S5, Cu2S5, Cu4S5, Cu2S3, have been described; they are all unstable, decomposing. into cupric sulphide and sulphur . Cuprous sulphite, CuS03•H2O, is obtained as a brownish-red crystalline powder by treating cuprous hydrate with sulphurous acid . A cuproso-cupric sulphite, Cu2SO3, CuS03,2H2O, is obtained by mixing solutions of cupric sulphate and acid sodium sulphite . Cupric sulphate or " Blue Vitriol," CuSO4, is one of the most important salts of copper . It occurs in cupriferous mine waters and as the minerals chalcanthite or cyanosite, CuSO4.5H2O, and boothite, CuSO4.7H2O . Cupric sulphate is obtained commercially by the oxidation of sulphuretted copper ores (see above, Metallurgy; wet methods), or by dissolving cupric oxide in sulphuric acid . It was obtained in 1644 by See also:Van See also:Helmont, who heated copper with sulphur and moistened the See also:residue, and in 1648 by See also:Glauber, who dissolved copper in strong sulphuric acid . (For the mechanism of this reaction see C . H . Sluiter, Chem . Weekblad, 1906, 3, p . 63, and C . M. van See also:Deventer, ibid., 1906, 3, p . 515.) It crystallizes with five molecules of water as large blue triclinic prisms . When heated to loo°, it loses four molecules of water and forms the bluish-white monohydrate, which, on further heating to 250°-260°, is converted into the white CuSO4 . The anhydrous salt is very hygroscopic, and hence finds application as a desiccating agent . It also absorbs gaseous hydrochloric acid . Copper sulphate is readily soluble in water, but in-soluble in See also:alcohol; it dissolves in hydrochloric acid with a consider-able fall in temperature, cupric chloride being formed . The copper is readily replaced by iron, a See also:knife-blade placed in an aqueous solution being covered immediately with a bright red deposit of copper . At one time this was regarded as a transmutation of iron into copper . Several basic salts are known, some of which occur as minerals; of these, we may mention See also:brochantite (.v.), CuSO4, 3Cu(OH2), langite, CuSO4, 3Cu(OH)2, H20, lyellite (or devilline), warringtonite; woodwardite and enysite are hydrated copper-aluminium sulphates, See also:connellite is a basic copper chlorosulphate, and spangolite is a basic copper aluminium chlorosulphate . Copper sulphate finds application in calico printing and in the preparation of the pigment See also:Scheele's green . A copper nitride, Cu3N, is obtained by heating precipitated cuprous oxide in ammonia gas (A . Guntz and H . Bassett, See also:Bull . See also:Soc . Chim., 1906, 35, p . 201) . A maroon-coloured powder, of composition CuNO2, is formed when pure dry nitrogen dioxide is passed over finely-divided copper at 25°-30° . It decomposes when heated to 90°; with water it gives nitric oxide and cupric nitrate and nitrite . Cupric nitrate, Cu (NOs)2, is obtained by dissolving the metal or oxide in nitric acid . It forms dark blue prismatic crystals containing 3, 4, or 6 molecules of water according to the temperature of crystallization . The trihydrate melts at 114.5° and boils at 17o°, giving off nitric acid, and leaving the basic salt Cu(NO3)2.3Cu(OH)2 . The mineral gerhardtite is the basic nitrate Cu2(OH)3NOs . Copper combines directly with See also:phosphorus to form several compounds . The phosphide obtained by heating cupric phosphate, Cu2H2P2Os, in hydrogen, when mixed with potassium and cuprous sulphides or levigated coke, constitutes " See also:Abel's fuse," which is used as a primer . A phosphide, Cu2P2, is formed by passing phosphoretted hydrogen over heated cuprous chloride . (For other phosphides see E . See also:Heyn and 0 . See also:Bauer, See also:Rep . Chem . Soc., 1906, 3, p . 39.) Cupric phosphate, Cus(PO4)2, may be obtained by precipitating a copper solution with sodium phosphate . Basic copper See also:phosphates are of frequent occurrence in the mineral See also:kingdom . Of these we may notice libethenite, Cu2(OH)PO4; chalcosiderite, a basic copper iron phosphate; See also:torbernite, a copper uranyl phosphate; andrewsite, a hydrated copper iron phosphate; and henwoodite, a hydrated copper aluminium phosphate . Copper combines directly with arsenic td' form several arsenides, some of which occur in the mineral kingdom . Of these we may mention whitneyite, Cu9 As, algodonite, Cu9AS, and domeykite, Cu 3As . Copper arsenate is similar to cupric phosphate, and the resemblance is to be observed in the naturally occurring copper arsenates, which are generally isomorphous with the corresponding phosphates . See also:Olivenite corresponds to libethenite; clinoclase, euchroite, cornwallite and tyrolite are basic arsenates; zeunerite corresponds to torbernite; chalcophyllite (tamarite or " copper-See also:mica ") is a basic copper aluminium sulphato-arsenate, and bayldonite is a similar compound containing lead instead of aluminium . Copper arsenite forms the basis of a number of once valuable, but very poisonous, See also:pigments . Scheele's green is a basic copper arsenite; See also:Schweinfurt green, an aceto-arsenite; and Casselmann's green a compound of cupric sulphate with potassium or sodium acetate . Normal cupric carbonate, CuCO3, has not been definitely obtained, basic hydrated forms being formed when an alkaline carbonate is added to a cupric salt . Copper carbonates are of wide occurrence in the mineral kingdom, and constitute the valuable ores malachite and azurite . Copper See also:rust has the same composition as malachite; it results from the action of carbon dioxide and water on the metal . Copper carbonate is also the basis of the valuable blue to green pigments verditer, See also:Bremen blue and Bremen green . Mountain or mineral green is a naturally occurring carbonate . By the direct union of copper and See also:silicon, cuprosilicon, consisting mainly of Cu4Si, is obtained (See also:Lebeau, C.R., 1906; Vigouroux, ibid.) . Copper silicates occur in the mineral kingdom, many minerals owing their colour to the presence of a cupriferous See also:element . See also:Dioptase (q.v.) and chrysocolla (q.v.) are the most important forms . Detection.—Compounds of copper impart a bright green coloration to the flame of a See also:Bunsen burner . Ammonia gives a characteristic blue coloration when added to a solution of a copper salt; potassium ferrocyanide gives a brown precipitate, and, if the solution be very dilute, a brown colour is produced . This latter reaction will detect one partof copper in 500,000 of water . For the See also:borax beads and the qualitative separation of copper from other metals, see CHEMISTRY: Analytical . For the quantitative estimation, see See also:ASSAYING: Copper . See also:Medicine.—In medicine copper sulphate was employed as an emetic, but its employment for this purpose is now very rare, as it is exceedingly depressant, and if it fails to See also:act, may seriously damage the gastric mucous membrane . It is, however, a useful superficial See also:caustic and antiseptic . All copper compounds are poisonous, but not so harmful as the copper arsenical pigments . |
|
|
[back] HENRY COPPEE (1821-1895) |
[next] COPPERAS (Fr. couperose; Lat. cupri rosa. the flowe... |
There are no comments yet for this article.
Do not copy, download, transfer, or otherwise replicate the site content in whole or in part.
Links to articles and home page are encouraged.