this residual distillate contain much naphthaline, in which case it will solidify partially or entirely, and the solid part is rejected and the fluid part only of this residual distillate is added to the dead oil. The camphole, after this distillation, is now agitated either with common hydrochloric acid, or with dilute, sulphuric, or nitric acid, formed by mixing the strong acids of commerce with about six times their bulk in water. This agitation is continued for a convenient length of time, and may be done in an open vessel with a stirrer. Having allowed the fluids to separate, I draw off the acid, and then I sometimes repeat the agitation with a further quantity of dilute acid with the addition of some chloride of lime in the proportion of a quarter of a pound of chloride of lime to a gallon of the acid, but this may be omitted. The oil is drawn off and well washed with water, from which it is separated, and then rectified. It may be rectified by passing steam through it, or by distilling from a retort to which fire is directly applied, but in either case it is convenient to place between the retort and the condenser a vessel similar to the dry lime purifiers used for purifying coal gas, in which lime is placed on plates or gratings in a chamber having only two openings, so that the vapors pass over the lime, and I prefer to have this lime purifier of such size that it may contain lime conveniently spread in the quantity of about half a pound of lime, more or less, to a gallon of the oil placed in the retort, but a smaller vessel may be used. This vessel is so arranged that the vapor of the oil, or water and oil, as it leaves the retort, passes over the lime which deprives it of dry acid remaining in it, and then passing into the condenser is reduced to the fluid form. But I prefer to rectify it in a retort over fire directly applied without the presence of water or steam, and to use a thermometer inserted in the retort, and to cease receiving as camphole when the temperature in the retort reaches 190 degs. By this means I obtain the oil colorless, and it should be of specific gravity, .890 or .900, or if the distillation be not continued so far, the specific gravity may be so low as.870. Concentrated sulphuric and nitric acid, separately or mixed, may be used in the purification of camphole; but I prefer not to use such acids, as a considerable loss of hydrocarbon is thereby sustained, and the use of concentrated nitric acid sometimes confers a yellow color on the oil which it does not lose on rectification. I sometimes repeat this treatment with alkali and acid once or oftener. Canphole so purified is applicable, either alone or mixed with the common naphtha of commerce, or mixed with some of the oils having lower boiling points separated in my processes, or with the pyroxylic spirit for burning in lamps. It is also useful as a substitute for oil of turpentine in making varnishes.

For the purification of the dead oil I adopt the same method of digesting with an alkali as that which I have described for

camphole, but I prefer to use a stronger lye and in larger proportions, and to continue the digestion for a longer time before I change the outlet and commence distillation, since the dead oil contains a larger quantity of acid substances. The same description of apparatus and the same sorts of alkali are applicable to the dead oil as to the camphole, but caustic alkalies are much to be preferred to carbonates. And in rectifying the dead oil from which the camphole has been previously separated by distillation, which is that which I prefer to treat in this manner, though the method is equally applicable to dead oil from which the camphole has not been removed after digestion with the alkali. If the lye be not drawn off, very little oil will be carried over with the water which distils off first, and whether the lye be or be not drawn off, I prefer to receive separately all the oil which comes over, before the temperature in the retort reaches 200 degs., and if there be little naphthaline present, I add this oil to the camphole of the corresponding degree of purity. If there be much naphthaline present, I reject so much of that part of the distillate from the dead oil as solidities in the cold, which will be the case in some instances while the temperature is rising from 210 degs. to 220 degs., or even higher And the quantity which it will be convenient to reject may be ascertained by observing whether a thin film of the distillate received on a cold surface solidifies, when the temperature in the retort is above 210 degs., when it ceases to solidify; on being so examined I commence to receive the mortuole for purification. If none solidify on cooling, I receive all the distillate above 200 degs. together, till the temperature in the retort reaches 280 degs. or 290 degs., I reject what comes over above as containing too much paranaphthaline. And, instead of treating the oil with dilute acid, I treat the dead oil, after distilling from the caustic lye, with oil of vitriol, in the proportion of one pound of oil of vitriol to one gallon of oil, and with or without the addition of a small quantity of nitric acid; I agitate the acid with the oil in a suitable vessel for one or two hours, and I prefer to allow the oil to stand with the acid for two or three days, and to repeat the agitation occasionally. I then draw off the oil from the acid, after having allowed it to settle. Finally I distil it through a dry lime purifier, as described for the purification of camphole. The oil should be collected in this rectification between the temperature of 220 degs. and 280 degs. This oil will be of a pale yellow, or almost colorless. I sometimes repeat this treatment of the mortuole with acids and alkali, once or oftener.

It is convenient sometimes further to purify the mortuole, camphole, and other oils, and spirituous substances, by filtering them through finely divided carbon, for which purpose I prefer animal charcoal or lampblack, which has been digested for a short time in oil of vitriol, or boiled in a solution of carbonate of potash, and then dried and heated to redness in a closed vessel

recently before use. And the filtration may be conveniently conducted by placing the oil in the filtering apparatus, over a vessel or receiver, into which the oil will be forced through the filterer by the pressure of the air, when the air is exhausted from the receiver. By further treatment with caustic alkali or lime, and with sulphuric acid, and by subsequent rectification, the mortuole may be obtained quite colorless. The oil so obtained is applicable to many of the purposes to which oil of turpentine is applied, and also to many of the purposes to which fixed oils are applicable, and it is applicable either alone or mixed with the more volatile hydrocarbons to burning in naphtha vapor pressure lamps, and when mixed with pyroxylic spirit in suitable proportions, to burning in lamps in which oil of turpentine or the fixed oils are burned.

What I here claim in respect to this second part of my inven tion, is the purification of the spirituous substances and oils which I manufacture from coal-tar, by treatment with chemical agents, according to principles laid down, depending on the nature of the spirituous substance and oils aforesaid, and of the impurities desired to be removed.

I also claim the use of nitric or nitrous acid, of nitro-muriatic acid, and of chromic acid, and the salts of those acids in the purification of empyreumatic and bituminous volatile oils, and the purification of certain of the oils manufactured from coal-tar by digestion with alkalies in the manner above described, and by distilling them so that their vapor is passed over lime, in the manner above described, and the purification of a spirituous substance obtained from coal-tar by congelation and pressure, which substance so purified I call absolute benzole.

ART. II.-GOLD ORES AND THEIR WORKING.

As the attention of those who are engaged in the working of gold ores, appears at the present time, to be more particularly directed to the mechanical appliances, by which the separation of the gold from the gangue-stone can be produced, than to the various descriptions of ore which are presented to their operations; I have thought it the most advisable plan to follow, in these papers now submitted to the public, to give a brief description of the most common methods of crushing and amalgamating now in vogue, and also to show the principles which actuate such manipulations, and to endeavor to point out such adaptations of those principles, as appear to me to be the most likely to aid in obtaining such results, as the labors of those interested are endeavoring to produce.

Perhaps the most correct method of procedure would be, to first describe the varieties of gold ores, their usual position, their characteristics, and attendant phenomena, together with their chemical constituents, and some observations upon their formation, such as may be drawn from actual observation and close examination.

But practical utility being my aim, and as the various ores are to a great extent well understood by those who are working them, I shall defer this part of the subject until after the appliances have been fully treated upon, and then take it up, in the hope of presenting the whole subject to the miner and general reader, in a plain and simple manner, which, if it does not present any new truths, will at least bring together, in a collated form, many of those already known.

Leaving, therefore, the description of mining and of the ores, I would, before entering upon that of the varied machinery, state a few important facts and principles, that during the working of the ore must never be lost sight of.

1st. Regularity and uniformity of "feeding," or supplying the machinery with ore, must be rigidly observed.

If the ore at any portion of the work is crowded into the machinery, without a due regard to the quantity that is to be regularly supplied to it, it follows that either the crushing or the amalgamation must be proportionably imperfect. If, in the crushing department, the ore will be passed through the crusher, not reduced to that extreme state of disintegration, which is requisite to liberate the minute particles of gold contained in it. This point has been fully borne out in my own experience, and corroborated by that of all practical operators with whom I have corresponded or conversed upon the subject. Numerous authorities to substantiate this rule could be quoted; but that of Hocheder in his valuable experiments, is directly to the point. He found that regularity was essentially requisite. That care was necessary that the ore was not passed over the works too coarsely ground; as when such was the case, much of the gold was washed away in the grains of the ore. He says, "The quantity of coarse stamped jacotinga [ore] which is rolling over the skins, into the river, attracted my attention, and I separated a portion of it from the fine stamped jacotinga, by means of a sieve, and caused the coarse grains to be pounded to a fine state, which showed, by washing, very good samples of gold. But the coarse grains with their contents are lost." In the amalgamating department the quantity of ore, if too great, will prevent that direct contact of the gold and mercury, so necessary to produce the desired amalgam, and consequently much of the gold will be lost by being washed away. If, on the other hand, the quantity of ore be deficient, valuable time will be sacrificed and an undue wear of machinery will be produced. The gold, in this case,

will, much of it, be washed away by the quantity of water being disproportioned to the amount of ore. The flouring of the mercury will also be greatly increased, entailing an additional loss, if the supply of ore is insufficient. As I have already brought Hocheder forward as a witness, with his experiments, I will avail myself of his able scrutiny once more. He found that from forty to fifty per cent. of the gold was lost by being stamped to too fine a powder; as by this means "the smallest particles of gold, stamped nearly to the state of slime, and which lose the action of specific gravity, will alone amount to from twenty to twenty-five per cent.; which is never to be gained by any means of separation founded on mechanical principles.'

2d. The "feeding" must be slowly performed.

Gamboa, on "amalgamation," states to this purport, in regard to slow manipulations.-In Guanaxuato, where the matrix is hard, and the ore finely disseminated through it, and more pains are taken in this operation, it is not usual to allow the charge to exceed six or seven quintals; to grind which, four and twenty hours are employed, and sometimes, if the ore be rich, as much as eight and forty hours.

A great advantage is derived from reducing the ore to the fine powder thus obtained, as appears from the analysis of the residue of the amalgamating process; and that it would be highly advantageous to the other districts to follow the example of Guanaxuato. Hocheder also insists upon slowly operating the ores. My own experience was to this effect; I was using a new crusher, "Bullock's Quartz Crusher," and supposed that all that was necessary was to crush as fast as possible, and rush the slime through the amalgamating apparatus. I crushed the quartz rock at the rate of from two to two and a half tons per hour, but I obtained no gold. I supposed that the large amount of mercury used was not "charged," as the point of saturation it must reach before it will yield amalgam, is termed, and worked on until I was sure that it was so; I then continued to pass the slime through as rapidly as ever; but obtained no gold. This was to me a mystery; assays proved the ore to be rich; panning showed it to be so; particles of gold were visible in much of the ore, but when it was operated upon the precious metal disappeared. I then began to work more slowly, and found reason to be encouraged; and continued the slow movement until I had brought down the crushing action to the capacity of the amalgamating force employed, and the result of the last experiment tried upon one ton of ore, which gave fifty-six dwts. of amalgam, proved that the work must be slowly performed.

3d. A state of rest must be allowed to the ore, as frequently as can be done, during the manipulation.

4th. While in that state of rest, a continued showering of water-drops should be maintained from a moderate elevation,