US894764A - Process of preparing arsenic trioxid. - Google Patents

Description

No. 894,5 4. PATENTED JULY 28, 1908.

U. WEDGE.

Rooms 0? PREPARING ARSENIG TRIOXID.

APPLICATION FILED JUNE 15, 1906.

4 SHEETS-SHEET 1.

No. 894,764. PATENTED JULY 28, 1908.

U. WEDGE.

Y PROCESS OF PREPARING ARSENIG TRIOXID.

APPLICATION IILBD'JUNE 15, 1906.

4 SHEETS-SHEET 2.

No. 894,764. PATENTED JULY 28, 1908.

U. WEDGE.

PROCESS OF PREPARING ARSENIO- TRIOXID.

APPLIGATION FILED JUNE 15, 1906. P

- 4 SHEETS-SHEET s.

4 SHEETS-SHEBT 4.

PATENTED JULY 28, 1908.

. U. WEDGE.

PROGBSS OF PREPARINGARSE'NIO TRIOXID.

APPLICATION FILED JUNE 15, 1906.

UNITED, STATES PAT NT oFFro UTLEY wnpen, or ARDMORE,PENNSYLVANIA.

rnocnss or rnnrnnrnefnnsnme 'rrtroxn")- Lia-894,7 4.

Specification of Letters Patent. Patented July 28,1908. Application filed June 15,1905. cuisine. 821,887.

To all whom ttma'y concern}- Be a known that 1, Hum WEDGE, a citi.

zen of the United "States,'residing in Ardmore, Pennsylvania, have invented certain Improvements in Processes of Preparing Arsenic Trioxid, -of which'thefollowing is a.

specification. I V k v I The 0b ]60t of my lnventlon 1s torecover, 1n

commercial form, the arsenic triox'id contained in the sulfid of arsenic which is at present a waste product :of sulfuric acid manufacture. "-Thisobject I attain by sub:

jecting the sulfid to ajsufiicient degreepf' heat to fuse the same while at the same time be provided for,

it is gently agitated as by causing it to flow in a sluggish stream down the inclined bed or hearth of a furnace, the vapors'evolv'ed by this treatment being then subjected to a subhmating process whereby the arsenic trioxid permittedto escape. v

In the accompanying drawings Figure I1 isa longitudinal section of a stationary furis recovered while the sulfurous acid gas is nace which I have devisediforlthe purpose of carrying out my invention; Fig. 2 is a sectional plan viewof the same on the line a a,

Fig. 1; Fig. 3 is a transverse section on the line bb, Fig. 1 Fig.4 is a longitudinal section of a rotary furnace for thecarrying out of my invention; Fig. 5-is a transverse section of the same on the line cc, Fig. 4, and

Fig. 6 is a view, partly in side'elevation and partly in section, andon a reducedscale,

illustrating another embodiment of my in-' vention.

I will first describe the stationary furnace shown in Figs. 1, 2 and 3, and the method of carrying out myinvention with the aid of such furnace. a

- The hearth oft he furnace has upper and lower horizontal sections land 2 on different levels and an intermediate inclined connect ing section 3, these sections of-the hearth being composed of slabs, tiles or bricks of refractory, material, and being supported upon side walls 4, end walls 5 and transverse piers or arches 6 so as'to form, beneath the hearth, a-series of connected flues 7, which receive the products of combustion from a furnace and after they have circulated through-the fines and beneath the hearth discharge them into a stack 10 at onecorner of the furnace. Any desired flow of "the products of combustion beneath the hearth of the furnace may by proper disposition .of the piers or arches 6. V p

the same. faces are being constantly exposed to the- The archedto 11 of the furnace is hollow and contains ami 12 which isalso in com munication atone end through a passage 12 with the stack 10 and at the other end with the uppermost of a pair of communicating transverse flues 12 and 14, the lowermost of which flues receives the tion from a furnace 15.

Interposed between the upper and lower products of combusflues13 and 14 are two tiers of slabs or tiles 16 and--17 com osed of refractory material, these tiers ofs abs ortiles being separated slightly so as to form between them a contracted passage 19 communicating at one end with the furnace chamber 20, and at the other end with a neck 21 which leads to the s'ublimating chamber 22. I

In either or both of the side walls of the furnace adjacent .to the upper section 1 of the hearth, is a feed opening 23, and in the end wall adjacent to the lower section 2 of the hearth is a delivery opening 24, these openings permitting the inflow of sufficient air to support the combustion of the mass deposited upon the hearth of the furnace.

When the furnace is in operation the products of combustion circulate through the flues 7', 13 and 14 and through the flue or passage 12, and the hearth and roof of the furnace and also the slabs or tiles 16 and 17 become highly heated;

Thesulfid of-arsenic which results as a a, waste product of sulfuric acid manufacture, is

usually a combination ofthe'trisulfid and the pentasulfid ,and owing to the loosely combined atoms of sulfur in the latter, the compound will, when thrown and spread upon the upper section 1 of the hearth, be readily fused or melted by the heat and will flow in a sluggish stream down the inclined section 3 of saidhearth and onto the base section 2 of By reason of such flow new surheat of the hearth and to the heat radiated from the roof of the furnace, the result of such treatment being the evolution of arseni ous oxidvapor and-sulfurous acid gas, which pass throughthe contracted passage 19 between the slabs 16and 17, and are there sub- .prefer to employ the rotary furnace shown in Figs. 4 and 5, in which 25 represents a cylindrical kiln lined with refractory material and mounted at a slight inclinationupon suitable supporting rollers, said kiln being provided with gearing whereby it may be slowly rotated, as usual in kilns of this type.

At the upper or elevated end of the kiln is a feeding device 26 for the sulfid, and a pipe 27 for supplying fuel in the form of gas or vapor, this fuel being preferably such that perfect combustion can take place in the kiln in order that the arsenic trioXid may not be discolored or rendered impure by admixture of carbonaceous matter or other impurities therewith.

The kiln 25 delivers into a vertical receiver 29 having therein aseries of brick checker work or other obstructions 30 and 31 with fuel pipes 32 and 33 for maintaining the same in a properly heated condition. In connection with this receiver, I have shown a form of condensing apparatus different from that illustrated in Fig. 1, and consisting of a tower 35, of somewhat the same character, as the Glover tower used in sulfuric acid manufacture, the lower end of this tower communicating through a flue 34 in the receiver 29, with the upper end of the latter, whereby the gases and vapors are discharged from the receiver into the tower, and pass upwardly through the latter, being spread or scattered by checkerwork obstructions 36. During such flow the gases and vapors are subjected to the action of downwardly flowing volumes of water, introduced at the top of the tower, and the arsenic trioxid is carried down by the water flow to the bottom of thetower, where it accumulates until re moved for drying. In many cases, this alternative method is the preferable one, as any sulfur which may be carried off by the gases or vapors from the furnace will float upon. the surface ofthe water at the base of the tower and can be skimmed off, while any sulfuric acid can be removed by decanting the water from the maid after the latter has settled.

In a furnace of the type shown in Fig. 4 the fused ormelted sulfid flows in a stream down the inclined bed of the furnace, and is also carried up on the rising side of the same and permitted to flew back into the main stream. As there may, in consequence of this agitation of the mass, be a greater tendency on the part of the evolved vapors or gases to carry off particles of unreduced sulfid, I provide a series of reheating or regenerating actions by the use of the successive bodies of heated checker Work in the receiver 29.

In the passage of arsenic vapors through a condensing chamber, arsenic trioxid will con dense at an earlier stage of such passage than will the sulfid, and in some cases I take advantage of this fact by subjecting the vapors to heat in their passage from a primary to a secondary condensing chamber, one means of accomplishing this result being shown in Fig. 6, in which 22 and 22 represent two condensing chambers, connected by a reheater similar to that shown in Fig. 1, and comprising a contracted passage 19 formed between upper and lower slabs 16 and 17 which are interposed between upper and lower heat conducting flues 13 and 14. This supple mentary treatment will, in many cases, ell'ect oxidation of sulfid which has escaped the preceding treatment, and will thus increase the percentage of oxid deposited in the secondary condensing chamber 22.

By my method of treating the suliid of arsenic, I am enabled to recover the arsenic trioxid in a commercially pure state, and therefore utilize what is at present hot only a waste product of sulfuric acid manufacture, but also a source of annoyance in establishments'which have no adequate means for its disposal.

I claim 1. The mode herein described of recovering arsenic trioXid from sulfid of arsenic by first subjecting the fused and flowing suliid to the action of heat and then cooling the evolved gases to condense the same.

2. The mode herein described of recovering arsenic trioXid from sulfid of arsenic by first subjecting the sulfid to the action of heat, then further heating the evolved gases and then cooling-the gases to condense the same.

3. The mode herein described of ritcovee ing arsenic trioxid from sulfid of arsenic by first subjecting the sulfid to heat, then repeatedly reheating the. evolved gases, and then cooling the gases to condense the same.

4. The mode herein described of recovering arsenic trioxid from sul'fid of arsenic, by

first subjecting the sulfid to heat, and then cooling the gases to condense the same by subjecting them to a water flow.

5. The mode herein described of reeovering arsenic trioXid from sulfid of arsenic by first heating the same, then subjecting the. evolved gases to successive coolings to eondense the same, and reheating said gases be tween successive coolings.

In testimony whereof, I have signed my name to this specification, in the presence of two subscribing witnesses.

UTLEY W1C] )G E.

Witnesses HAMILTON D. TURNER, KATE A. BEADLE.

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