US2629895A - Method of and apparatus for making flake sulfur - Google Patents
Method of and apparatus for making flake sulfur Download PDFInfo
- Publication number
- US2629895A US2629895A US215180A US21518051A US2629895A US 2629895 A US2629895 A US 2629895A US 215180 A US215180 A US 215180A US 21518051 A US21518051 A US 21518051A US 2629895 A US2629895 A US 2629895A
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- United States
- Prior art keywords
- sulphur
- water
- solidified
- layer
- plates
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 title claims description 71
- 238000000034 method Methods 0.000 title description 9
- 229910052717 sulfur Inorganic materials 0.000 title description 6
- 239000011593 sulfur Substances 0.000 title description 6
- 239000005864 Sulphur Substances 0.000 claims description 65
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 44
- 238000000151 deposition Methods 0.000 claims description 10
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 239000000498 cooling water Substances 0.000 claims description 2
- 238000000605 extraction Methods 0.000 claims description 2
- 239000007788 liquid Substances 0.000 description 29
- 239000010408 film Substances 0.000 description 13
- 238000001816 cooling Methods 0.000 description 8
- 230000008878 coupling Effects 0.000 description 7
- 238000010168 coupling process Methods 0.000 description 7
- 238000005859 coupling reaction Methods 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- 238000010276 construction Methods 0.000 description 3
- 210000002445 nipple Anatomy 0.000 description 3
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 238000000429 assembly Methods 0.000 description 2
- 230000000712 assembly Effects 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 239000010409 thin film Substances 0.000 description 2
- 229910000746 Structural steel Inorganic materials 0.000 description 1
- 239000007799 cork Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B17/00—Sulfur; Compounds thereof
- C01B17/02—Preparation of sulfur; Purification
- C01B17/04—Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides
- C01B17/0404—Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides by processes comprising a dry catalytic conversion of hydrogen sulfide-containing gases, e.g. the Claus process
- C01B17/0426—Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides by processes comprising a dry catalytic conversion of hydrogen sulfide-containing gases, e.g. the Claus process characterised by the catalytic conversion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/0207—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B17/00—Sulfur; Compounds thereof
- C01B17/02—Preparation of sulfur; Purification
- C01B17/0237—Converting into particles, e.g. by granulation, milling
Definitions
- Another object of the present invention is to provide apparatus, as characterized above, in-
- Fig. 1 is an elevational view, with parts omitted, of a sulphur flaking machine constructed in accordance with the present invention
- Fig. 2 is a plan view of the machine shown in Fig. 1;
- Fig. 3 is an elevational view, partly in section, and with parts omitted for clarity, of the machine shown in Fig. '1;
- Fig. 4 is a horizontal sectional view, with parts omitted, taken on the .line 4-4 of Fig. '1;
- Fig. 5 is a perspective view of a water jacket- .ing pan
- Fig. -6 is a detail view showing how the water ,jacketing pansare secured to the annular plates;
- Fig. '7 is a vertical sectional detail view showing the manner in which an inlet water connection is made to the pan;
- Fig. 8 is a vertical sectional detail view showing the manner in which an outlet water connection is made to the pan
- Fig.9 is an elevational detail view showing the manner .in which a breaker is mounted
- the aforesaid .co-pending application involves a system for recovering elemental sulphur in liquid form from gases containing hydrogen sulphide, and the conversion of the liquid sulphur into solidified flakes.
- the system includes a sulphur flaking apparatus for converting the recoveredliquid sulphur into solidified sulphur flakes.
- the present invention is drawn to the novel method of and the particular apparatus for converting liquid sulphur into solidified flakes .as
- the structural frame is formed of structural steel members and is shown :as including four vertical frame members 23 having their upper end portions bent over the top of the cylindrical member and secured to a plate carrying an upper vertical guide bearing 24 for a vertical shaft 25 extending .centrally of the cylinder .20 and having a lower step bearing 26 mounted on a concrete foundation block "21.
- Upper and lower radial arms 28, "29 connect'the shaft to the cylinder.
- the structural frame 22 also includes four vertical frame members 30 and three vertical spaced horizontal bracing frames .3 I, .each formed by four .structural chan- .nel members 32 having their-endssecured .tothe .as .by a plurality of circumferentially spaced L- shaped members 3!; having their .legs suitably secured to the cylinder and the respective plates .(see Figs. 4 and 7).
- the outer peripheral edge portions of the .annular plates . are supported "by a plurality of .roller assemblies .35 carried'by four vertical frame members .36 each of .which is secured to the three vertically spaced angle'braces 33 in each corner of the structural frame assembly (see Fig. 2), and by the vertical frame members 23 (see Fig. 3).
- Each of the roller assemblies is identical in construction and, as best seen in *Fig. 3, comprises an upper inverted .U-shaped member 31 having a roller 38 journalled therein and a lower U-shaped member 39 having a roller 40 journalled therein. Th members 31 and 39 are secured to the respective frame member on which they are mounted in spaced apart relation, as by means of brackets which may be welded or bolted to the frame member.
- Rotation of the cylinder and the annular plates is effected as by means of a sprocket chain 4
- the sprocket chain meshes with a sprocket 43 mounted on the upper end of a shaft 44 driven by a motor 45 through suitable reduction gearing 46 (see Figs. 1 and 9.)
- is provided with an upstanding annular flange 41 adjacent its outer periphery and an upstanding annular flange 48 adjacent its inner periphery (see Figs. 3 and 10).
- the surfaces of the plates between the inner and outer upstanding flanges are designed to have liquid sulphur deposited thereon as the plates are rotated by means of a plural ty of perforated horizontally extending branch conduits 49 connected to a vertically extending header or conduit 50 which is connected to a pipe line 5
- a plural ty of horizontally extending perforated branch water conduits 52 are provided.
- Each of the branch conduits ex tends across one of the plates 2
- the branch water conduits are connected to a vertical water header 53 which is connected to a source of water supply, not shown (see Figs. 1 and 2).
- each of the conduits 52 is shown as having secured thereto a downwardly and forwardly extending generally rectangular metal lip 54 having a felt pad 55 suitably secured to the upper portion of its surface just below the row of perforations in the pipe (see Fig. 11).
- additional means for cooling the sulphur may be provided.
- additional cooling means are provided by water jacketing the bottoms of the portions of the plates 2
- is water jacketed in the same manner and, as shown, a plurality of pans 56 (see Figs. 1, 3, 4 and 5) are secured to the under surfaces of the plates.
- Each pan is substantially trapezoidal in shape and its upstanding walls are provided with a laterally extending flange around their upper edges.
- the pans are removably secured to the under sides of the plates 2
- Cork gaskets 58 may be inserted between the flanges and the steel plates, if desired (see Fig. 6).
- the flanges along the inner and outer walls of the pans are secured to the under side of the plates 2
- Each of the inlet pipes 60 is made up of a series of short pipe sections 62, union couplings 63, and valve T fittings 64 connected together so that each valve T fitting is positioned to be connected to one of the pans of the series of pans under each of the annular plates 2
- Each of the inlet pipes 60 is fixedly connected at its upper end to a compartment in an annular compartmentized open top trough 55 which is secured to the shaft 25 and rotates with the cylinder 20.
- Water is supplied to the compartmentized trough 55 by means of a plurality of arcuate perforated pipes 66 (four such being shown), each of which is positioned to supply water to a series of compartments in the trough.
- Each arcuate pipe 66 is connected to a valved down-comer pipe 61.
- the down-comer pipes 51 are connected to a single down-comer pipe 68 carried by a pipe 69 which is connected to the source of water supply (not shown).
- the construction and arrangement are such that each separate series or group of compartments in the trough 65 will have a separate controlled water supply, thus permitting control of the rate of flow of the water through the pipes 60 and thereby permitting control of the temperature of the cooling pans (see Fig. l).
- each water inlet pipe 50 is connected to each of its respective pans is identical and the details thereof are shown in Fig. 7.
- the valved T fitting 64 has its stem or lateral branch 10 projecting through an opening formed in the cylinder 20 and connected to a spur tube H in the pan, as by means of nipple i2 and a coupling 13, respectively.
- a gasket may be positioned between the coupling and the wall of the pan and a lock nut may be threaded on the spur tube, if desired, all as shown in Fig. 7.
- the inner peripheral edge of the T fitting stem forms a seat for a valve disc M mounted on the end of a threaded valve stem i5 screwed in a cap or plug member 16, which, in turn, is screwed in the side wall of the T fitting opposite the stem branch.
- the flow of water into the pan may be controlled by adjusting the valve disc relative to its seat.
- is made up of a series of short pipe sections ll, union couplings l8, and T fittings 19, connected together so that each T fitting is positioned to be connected to one of the pans of the series of pans under each of the annular plates 2
- has its bottom pipe section projecting downwardly into an open top annular trough fixedly mounted on the concrete support 28.
- the annular trough 89 may be provided with a drain pipe and a plurality of the bottom pipe sections of the outlet pipes 6
- is connected to each of its respective pans.
- the sfitting 19 has its .stem orlateral branch 31 projecting through an opening formed in thecylinder 2t and connected to an elbow fitting'ilz by means of a nipple 83.
- the elbow fitting 82 is connected to a nipple 3a which extends through a disc flange bolted onto the upper surface of the plate 2! adjacent its inner edge, and is threaded into an opening ends .to upright angle frame members 99, 91 -(see Figsl and 2)..
- Each .of the troughs '85 is'positioned to extend inwardly over one of the am nular plates 2 I and each has a ramp '92 extending downwardly into engagement with the upper surface of the plate and positioned to scoop the sulphur up into the trough, and a screw conveyor 93 having its inner end journalled in a suitable bearing formed on the closed inner end of the trough and its outer end portion journalled in a suitable bearing formed in the outer side *wall of .the vertical chute 88 and carrying a bevelled gear at which meshes with a bevelled gear t5 fixedly mounted on a vertical shaft 96.
- vertical shaft 96 drives all of'the screw conveyors and, in turn, is driven, as bymeans of a niotcrdl, through reduction gearing 98.
- the vertical shaft 86 may be mounted in vertically spaced bracket bearings 99 suitably secured to the outside wall of the chute 88 (see Figs. 1. 2 and 4).
- the ramp or scoop 82 is provided with upright flanges It? along its longitudinal side edges and fits between i the outer and inner flanges on the plate 25 (see Fig. 9).
- Suitable means are provided for breaking up the solidified layer of sulphur on each of the plates 2i before it is scooped up into the trough associated with the plate.
- Each of these means is identical in construction and the details thereof are shown in Figs. 9 and 10.
- a heavy breaker bar Hill is pivotally suspended from a U-shaped crank shaft 92, as by means of a spaced pair of arms W3.
- Ihe crank shaft IE2 is journalled in the depending legs 195 of an inverted LJ-shaped bracket member :95.
- the member ⁇ at is secured to a bracket arm iilt connected at one end to an upright structural angle member is? which, in turn, is secured to the tiered cross brace members 33 in one corner of the structural frame (see Fig. 2).
- the arm I98 extends across the plate 2! in position to place the breaker bar iii! adjacent the bottom of the ramp or scoop 92 (see Figs. 2 and 9).
- the inner end of the crank shaft Hi2 as viewed in Figs. 9 and 10, has a crank i138 formed thereon and positioned to extend across and be engaged by the teeth of a rotating ratchet or cam ring m9.
- the ratchet or cam ring is shown as encircling the cylinder at and as being mounted on a plurality of circumferentially spaced vertical rods HQ secured to the inner end portion of the plates 2i (see Figs. 9 and 10).
- the sulphur flaking machine may be made of any suitable material, such a's st'r'ucsteel. However, all the parts thereof which preferably made of stainlesss'teel.
- Apparatus for the conversion of liquid sulphur into solidified flakes which comprises at least one rotatable metal plate having a fiat upper surface; means for rotating said plate about a vertical axis; means including a conduit for depositing a film of water on said plate at one point in its path of travel; means including a conduit for depositing a layer of liquid sulphur on the water film formed on said member at another and adjacent point in its path of travel; heat exchanging means mounted on the bottom of said movable plate for cooling and solidifying the liquid sulphur thereon; and means for breaking up and removing the solidified sulphur from said plate at a third point in its path of travel.
- Apparatus for the conversion of liquid sulphur into solidified flakes which comprises at least one rotatable annular flat metal plate; a perforated pipe extending radially of said plate at one point for depositing a film of water thereon as the plate rotates; a perforated pipe extending radially of said plate at a point spaced from said first point for depositing a layer of liquid sulphur on the water film formed on the rotating plate; cooling means including conduits and water jacketing pans mounted on the bottom of said plate for cooling and solidifying the liquid sulphur; and mean including a breaker bar and scoop for cracking the solidified layer of sulphur into flakes and removing the flakes from the plate as it rotates.
- Apparatus for the conversion of liquid sulphur into solidified flakes which comprises a vertical rotatable cylinder having a plurality of axially spaced annular radially extending metal plates secured thereto; means including a water header having a plurality of branch perforated pipes each extending radially of one of said plates for sprinkling a film of water thereon as the cylinder rotates; means including a liquid sulphur header having a, plurality of branch perforated pipes each extending radially of one of said plates and spaced from the corresponding water branch pipe for depositing a layer of liquid sulphur on the water film formed on the plate as it rotates; means including pipes and water Jacketing pans mounted on the bottoms of said plates for cooling and solidifying the layers of liquid sulphur deposited thereon; and means mounted above each plate for breaking up and removing the solidified layer of sulphur therefrom as the plate rotates.
- Apparatus as set forth in claim 4, wherein the means for breaking up and removing the solidified layer of sulphur from each plate comprises a breaker bar pivotally mounted for a rising and falling engagement with the plate, a scoop having a screw conveyor mounted therein, and a vertical conduit connected to each scoop to receive the broken up flakes of sulphur.
- each of the perforated pipes for sprinkling water is provided with a generally rectangular downwardly and forwardly depending metal lip having a felt pad secured thereto to insure that a continuous film of water is deposited on the plate and prevent back flow of the sulphur thereon.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
March 3, 1953 E. B. MILLER 2,629,895
METHOD OF AND APPARATUS FOR MAKING FLAKE SULFUR Filed March 12, 1951' 4 Sheets-Sheet l INVENTOR FE. .1. .ERNfl'I'BM/LLER BY d nuvw ATTORNEYS March 3, 1953 E. B. MILLER 2,629,895
METHOD OF AND APPARATUS FOR MAKING FLAKE SULFUR Filed March 12, 1951 4 Sheets-Sheet 2 M 9 1 IE 25-12- Iii M4 E 152E. .10 I; in sz':
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ATTORNEYS March 3, 1953 E. B. MILLER 2,629,895
METHOD OF AND APPARATUS FOR MAKING FLAKE SULFUR Filed March 12, 1951 4 Sheets-Sheet 5 Baa-.2.
w a? Z J! J 6/ 17 5 78 7 77 A 5 JE\ 79 77 Vfl- =57? 78 JZZZ A i I /M 80 f 4 H Jag- F u F 1 INVENTOR Eeuesrfi M14151? I BY davm, v M
ATTORNEYS March 3, 1953 E. B. MILLER 2,529,395
METHOD OF AND APPARATUS FOR MAKING FLAKE SULFUR Filed March 12, 1951 4 Sheets-Sheet 4 4 i INVENTOR 7i \w a Emmy-5 M4 use M 1 2 BY 4.74M. Y M
ATTORNEYS Patented Mar. 3, 1953 UNITED STATES PATENT OFFICE l'ilIETHOD OF AND APPARATUS FOR MAKING FLAKE SULFUR Ernest B. Miller, Houston, Tex., assignor to Jefferson Lake Sulphur Company, New Orleans, La., a corporation of New Jersey Original application March '12, 1951, Serial No.
Divided and this application .March 12, 1951, Serial No. 215,180
6 Claims.
provide improved apparatus for continuously converting liquid sulphur into sulphur flakes.
Another object of the present invention is to provide apparatus, as characterized above, in-
cluding a plurality of rotatable water-jacketed annular plates; means for depositing a layer of liquid sulphur-superimposed upon a film of water on the upper surfaces of the plates; and means for cracking and removing the layers of deposited sulphur after they have solidified.
Other objects and advantages of the invention will appear in the following specification when considered in connection with the accompanying drawings, wherein:
Fig. 1 is an elevational view, with parts omitted, of a sulphur flaking machine constructed in accordance with the present invention;
Fig. 2 is a plan view of the machine shown in Fig. 1;
Fig. 3 is an elevational view, partly in section, and with parts omitted for clarity, of the machine shown in Fig. '1;
Fig. 4 is a horizontal sectional view, with parts omitted, taken on the .line 4-4 of Fig. '1;
Fig. 5 is a perspective view of a water jacket- .ing pan;
Fig. -6 .is a detail view showing how the water ,jacketing pansare secured to the annular plates;
.Fig. '7 is a vertical sectional detail view showing the manner in which an inlet water connection is made to the pan;
Fig. 8 is a vertical sectional detail view showing the manner in which an outlet water connection is made to the pan;
Fig.9 is an elevational detail view showing the manner .in which a breaker is mounted;
pipe.
This application is a division of my .co-pend- .ing application, Ser. No. 215,178, filed March "12,
l951,for'Method for the'Recovery o'fElemental Sulphur in Liquid FormFrom Gases Containing Hydrogen sulphide, and the Conversion of the Liquid. Sulphur into solidified Flakes.
The aforesaid .co-pending application involves a system for recovering elemental sulphur in liquid form from gases containing hydrogen sulphide, and the conversion of the liquid sulphur into solidified flakes.
The system includes a sulphur flaking apparatus for converting the recoveredliquid sulphur into solidified sulphur flakes.
The present invention is drawn to the novel method of and the particular apparatus for converting liquid sulphur into solidified flakes .as
disclosed in said co-pending application.
Referring now to the drawings, there'is shown in Figs. 1, 2 and '3, one embodiment of apparatus and the arrangement thereof ;'for carrying out the method of this invention. As there shown,
a vertical rotatable open-ended cylindrical member 20 having a plurality of axially spaced annular plates 2| secured thereto, is mounted within a suitable structural frame, indicated generally at 22. The structural frame is formed of structural steel members and is shown :as including four vertical frame members 23 having their upper end portions bent over the top of the cylindrical member and secured to a plate carrying an upper vertical guide bearing 24 for a vertical shaft 25 extending .centrally of the cylinder .20 and having a lower step bearing 26 mounted on a concrete foundation block "21. Upper and lower radial arms 28, "29 connect'the shaft to the cylinder. The structural frame 22 also includes four vertical frame members 30 and three vertical spaced horizontal bracing frames .3 I, .each formed by four .structural chan- .nel members 32 having their-endssecured .tothe .as .by a plurality of circumferentially spaced L- shaped members 3!; having their .legs suitably secured to the cylinder and the respective plates .(see Figs. 4 and 7). The outer peripheral edge portions of the .annular plates .are supported "by a plurality of .roller assemblies .35 carried'by four vertical frame members .36 each of .which is secured to the three vertically spaced angle'braces 33 in each corner of the structural frame assembly (see Fig. 2), and by the vertical frame members 23 (see Fig. 3).
Each of the roller assemblies is identical in construction and, as best seen in *Fig. 3, comprises an upper inverted .U-shaped member 31 having a roller 38 journalled therein and a lower U-shaped member 39 having a roller 40 journalled therein. Th members 31 and 39 are secured to the respective frame member on which they are mounted in spaced apart relation, as by means of brackets which may be welded or bolted to the frame member.
Rotation of the cylinder and the annular plates is effected as by means of a sprocket chain 4| carried by a depending ring member 42 secured to the bottom outer edge of the bottom plate 2| (see Figs. 9 and 10). The sprocket chain meshes with a sprocket 43 mounted on the upper end of a shaft 44 driven by a motor 45 through suitable reduction gearing 46 (see Figs. 1 and 9.)
Each of the annular plates 2| is provided with an upstanding annular flange 41 adjacent its outer periphery and an upstanding annular flange 48 adjacent its inner periphery (see Figs. 3 and 10). The surfaces of the plates between the inner and outer upstanding flanges are designed to have liquid sulphur deposited thereon as the plates are rotated by means of a plural ty of perforated horizontally extending branch conduits 49 connected to a vertically extending header or conduit 50 which is connected to a pipe line 5| which delivers liquid sulphur from a source of supply, not shown (see Figs. 1 and 2). All of the liquid sulphur pipe lines and conduits may be steam jacketed, if desired.
In order to prevent the liquid sulphur from sticking to the plates, a plural ty of horizontally extending perforated branch water conduits 52 are provided. Each of the branch conduits ex tends across one of the plates 2| and is positioned ahead of the branch conduit 49 which deposits liquid sulphur on the plate, so that a water film may be deposited on the plate as it rotates, before the sulphur is deposited. The branch water conduits are connected to a vertical water header 53 which is connected to a source of water supply, not shown (see Figs. 1 and 2).
In order to insure that a continuous thin film of water is deposited on the plates 2| and to prevent any possible flow of liquid sulphur to pass back of the perforated branch conduits 52, each of the conduits 52 is shown as having secured thereto a downwardly and forwardly extending generally rectangular metal lip 54 having a felt pad 55 suitably secured to the upper portion of its surface just below the row of perforations in the pipe (see Fig. 11).
While the thin layers of deposited liquid sulphur may be solidified by air cooling, additional means for cooling the sulphur may be provided. In the particular embodiment of the invention illustrated, additional cooling means are provided by water jacketing the bottoms of the portions of the plates 2| on which the sulphur is deposited. Each of the plates 2| is water jacketed in the same manner and, as shown, a plurality of pans 56 (see Figs. 1, 3, 4 and 5) are secured to the under surfaces of the plates. Each pan is substantially trapezoidal in shape and its upstanding walls are provided with a laterally extending flange around their upper edges. The pans are removably secured to the under sides of the plates 2|, as by means of radially extending steel strips 51 bolted to the under surfaces of the plates and securing the flanges of adjacent pans between itself and the plates. Cork gaskets 58 may be inserted between the flanges and the steel plates, if desired (see Fig. 6). The flanges along the inner and outer walls of the pans are secured to the under side of the plates 2|, as by bolting,
with an intervening gasket strip 59 to make it water-tight (see Figs. '7 and 8).
Mounted within the cylinder 20 are a plurality of water inlet pipes 60 and water outlet pipes 5|. Each of the inlet pipes 60 is made up of a series of short pipe sections 62, union couplings 63, and valve T fittings 64 connected together so that each valve T fitting is positioned to be connected to one of the pans of the series of pans under each of the annular plates 2|, and the union couplings are positioned on opposite sides of the valved T fittings to facilitate the connection or disconnection of the T fitting to its respective pan (see Fig. 3). Each of the inlet pipes 60 is fixedly connected at its upper end to a compartment in an annular compartmentized open top trough 55 which is secured to the shaft 25 and rotates with the cylinder 20. Water is supplied to the compartmentized trough 55 by means of a plurality of arcuate perforated pipes 66 (four such being shown), each of which is positioned to supply water to a series of compartments in the trough. Each arcuate pipe 66 is connected to a valved down-comer pipe 61. The down-comer pipes 51 are connected to a single down-comer pipe 68 carried by a pipe 69 which is connected to the source of water supply (not shown). The construction and arrangement are such that each separate series or group of compartments in the trough 65 will have a separate controlled water supply, thus permitting control of the rate of flow of the water through the pipes 60 and thereby permitting control of the temperature of the cooling pans (see Fig. l).
The manner in which each water inlet pipe 50 is connected to each of its respective pans is identical and the details thereof are shown in Fig. 7. As there shown, the valved T fitting 64 has its stem or lateral branch 10 projecting through an opening formed in the cylinder 20 and connected to a spur tube H in the pan, as by means of nipple i2 and a coupling 13, respectively. A gasket may be positioned between the coupling and the wall of the pan and a lock nut may be threaded on the spur tube, if desired, all as shown in Fig. 7. The inner peripheral edge of the T fitting stem forms a seat for a valve disc M mounted on the end of a threaded valve stem i5 screwed in a cap or plug member 16, which, in turn, is screwed in the side wall of the T fitting opposite the stem branch. The flow of water into the pan may be controlled by adjusting the valve disc relative to its seat.
Each of the water outlet pipes 6| is made up of a series of short pipe sections ll, union couplings l8, and T fittings 19, connected together so that each T fitting is positioned to be connected to one of the pans of the series of pans under each of the annular plates 2| and the union couplings are positioned on opposite sides of the T fittings to facilitate the connection or disconnection of the T fitting to its respective pan (see Fig. 3). Each of the outlet pipes 6| has its bottom pipe section projecting downwardly into an open top annular trough fixedly mounted on the concrete support 28. The annular trough 89 may be provided with a drain pipe and a plurality of the bottom pipe sections of the outlet pipes 6| may be provided with couplings to facilitate their removal to permit access to the interior of the drum 20, all as shown in Fig. 1.
The manner in which each water outlet pipe 5| is connected to each of its respective pans is identical, and the'details thereof are shown in rig. e. As there shown, the sfitting 19 has its .stem orlateral branch 31 projecting through an opening formed in thecylinder 2t and connected to an elbow fitting'ilz by means of a nipple 83. The elbow fitting 82 is connected to a nipple 3a which extends through a disc flange bolted onto the upper surface of the plate 2! adjacent its inner edge, and is threaded into an opening ends .to upright angle frame members 99, 91 -(see Figsl and 2).. Each .of the troughs '85 is'positioned to extend inwardly over one of the am nular plates 2 I and each has a ramp '92 extending downwardly into engagement with the upper surface of the plate and positioned to scoop the sulphur up into the trough, and a screw conveyor 93 having its inner end journalled in a suitable bearing formed on the closed inner end of the trough and its outer end portion journalled in a suitable bearing formed in the outer side *wall of .the vertical chute 88 and carrying a bevelled gear at which meshes with a bevelled gear t5 fixedly mounted on a vertical shaft 96. The
Suitable means are provided for breaking up the solidified layer of sulphur on each of the plates 2i before it is scooped up into the trough associated with the plate. Each of these means is identical in construction and the details thereof are shown in Figs. 9 and 10. As there shown, a heavy breaker bar Hill is pivotally suspended from a U-shaped crank shaft 92, as by means of a spaced pair of arms W3. Ihe crank shaft IE2 is journalled in the depending legs 195 of an inverted LJ-shaped bracket member :95. The member {at is secured to a bracket arm iilt connected at one end to an upright structural angle member is? which, in turn, is secured to the tiered cross brace members 33 in one corner of the structural frame (see Fig. 2). The arm I98 extends across the plate 2! in position to place the breaker bar iii! adjacent the bottom of the ramp or scoop 92 (see Figs. 2 and 9). The inner end of the crank shaft Hi2, as viewed in Figs. 9 and 10, has a crank i138 formed thereon and positioned to extend across and be engaged by the teeth of a rotating ratchet or cam ring m9. The ratchet or cam ring is shown as encircling the cylinder at and as being mounted on a plurality of circumferentially spaced vertical rods HQ secured to the inner end portion of the plates 2i (see Figs. 9 and 10). The inclined upper surfaces of the teeth of the ratchet ring engage the crank its on the end of the crank shaft E92 as the ratchet ring rotates and causes an alternate rising and falling of the breaker bar ml, which results in breaking the solidified sulphur into 'tural come into contact with the liquid sulphur are 6 small pieces or flakes before it passes up the ramp or scoop 92 into the trough 36.
The operation of the device is believed obvious. As the cylinder 28 and the annular platesZl are rotated (in a counterclockwise direction as viewed in Fig. 2) a thin film of water is deposited 'on the upper surface of each of the plates 2! by the branch water pipes 52,-and a layer of liquid :sul-
phur is deposited on topof the film of water by the branch sulphur pipes 69. The 'thicknessof the layer of sulphur is determined by the speed of rotation of the plates and the rate of flow of the liquid sulphur. As the plates rotate, the layers of liquid sulphur thereon "are solidified by the air-and by the water jackets beneath theplates. As the solidified'layers of sulphur approach-the "ramps or scoops, they "are broken into small pieces or flakes by the constantrisin'g and falling cf'the The sulphur flakes fall through the chute 88 into the bottom of a vertical conveyor '(not shown) which lifts them into a storage hopper (not shown). The sulphur flaking machine may be made of any suitable material, such a's st'r'ucsteel. However, all the parts thereof which preferably made of stainlesss'teel.
From the foregoin description, it will heapparent that there has been provided 'a novel method of and improved apparatus for the conversion of liquid sulphur into sulphur flakes.
Obviously, the invention is not restrictedto the par icular embodiment thereof herein shown and described. Moreover, it is not indispensible that all of the features of the invention be used conjointly, since they may be employed advantageously in various combinations and sub-combinations.
What is claimed is:
1. In the formation of sulphur flakes from molten sulphur involving the depositing of a layer of molten sulphur on a previously wetted surface of a mOVlIlg carrier, the coolingof the sulphur layer to solidify it and the subsequent breaking up of the solidified layer into flakes, the improvement which comprises continuously rotating an annular metal carrier having a flat upper surface about a vertical axis; continuously applying a film of water on the upper surface of said carrier at one point in its path of travel; continuously depositing a thin layer of molten sulphur on the water film at another point in the path of travel of the carrier adjacent to the point where the water film is applied; continuously directing a stream of cooling water against the entire bottom surface of said carrier as it rotates, whereby the deposited layer of sulphur will be solidified due to the extraction of heat therefrom; and continuously breaking up and removing the solidified layer of sulphur at a third point in the path of travel of said carrier.
2. Apparatus for the conversion of liquid sulphur into solidified flakes which comprises at least one rotatable metal plate having a fiat upper surface; means for rotating said plate about a vertical axis; means including a conduit for depositing a film of water on said plate at one point in its path of travel; means including a conduit for depositing a layer of liquid sulphur on the water film formed on said member at another and adjacent point in its path of travel; heat exchanging means mounted on the bottom of said movable plate for cooling and solidifying the liquid sulphur thereon; and means for breaking up and removing the solidified sulphur from said plate at a third point in its path of travel.
3. Apparatus for the conversion of liquid sulphur into solidified flakes which comprises at least one rotatable annular flat metal plate; a perforated pipe extending radially of said plate at one point for depositing a film of water thereon as the plate rotates; a perforated pipe extending radially of said plate at a point spaced from said first point for depositing a layer of liquid sulphur on the water film formed on the rotating plate; cooling means including conduits and water jacketing pans mounted on the bottom of said plate for cooling and solidifying the liquid sulphur; and mean including a breaker bar and scoop for cracking the solidified layer of sulphur into flakes and removing the flakes from the plate as it rotates.
4. Apparatus for the conversion of liquid sulphur into solidified flakes which comprises a vertical rotatable cylinder having a plurality of axially spaced annular radially extending metal plates secured thereto; means including a water header having a plurality of branch perforated pipes each extending radially of one of said plates for sprinkling a film of water thereon as the cylinder rotates; means including a liquid sulphur header having a, plurality of branch perforated pipes each extending radially of one of said plates and spaced from the corresponding water branch pipe for depositing a layer of liquid sulphur on the water film formed on the plate as it rotates; means including pipes and water Jacketing pans mounted on the bottoms of said plates for cooling and solidifying the layers of liquid sulphur deposited thereon; and means mounted above each plate for breaking up and removing the solidified layer of sulphur therefrom as the plate rotates.
5. Apparatus, as set forth in claim 4, wherein the means for breaking up and removing the solidified layer of sulphur from each plate comprises a breaker bar pivotally mounted for a rising and falling engagement with the plate, a scoop having a screw conveyor mounted therein, and a vertical conduit connected to each scoop to receive the broken up flakes of sulphur.
6. Apparatus, a set forth in claim 4, wherein each of the perforated pipes for sprinkling water is provided with a generally rectangular downwardly and forwardly depending metal lip having a felt pad secured thereto to insure that a continuous film of water is deposited on the plate and prevent back flow of the sulphur thereon.
ERNEST B. MILLER.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 254,464 Cheever Mar. 7, 1882 1,130,670 Christensen Mar. 2, 1915 1,417,542 Mauch May 30, 1922 1,419,911 Bacon et al June 20, 1922 2,335,726 Averns Nov. 30, 1943
Claims (1)
1. IN THE FORMATION OF SULPHUR FLAKES FROM MOLTEN SULPHUR INVOLVING THE DEPOSITING OF A LAYER OF MOLTEN SULPHUR ON A PREVIOUSLY WETTED SURFACE OF A MOVING CARRIER, THE COOLING OF THE SULPHUR LAYER TO SOLIDIFY IT AND THE SUBSEQUENT BREAKING UP OF THE SOLIDIFIED LAYER INTO FLAKES, THE IMPROVEMENT WHICH COMPRISES CONTINUOUSLY ROTATING AN ANNULAR METAL CARRIER HAVING A FLAT UPPER SURFACE ABOUT A VERTICAL AXIS; CONTINUOUSLY APPLYING A FILM OF WATER ON THE UPPER SURFACE OF SAID CARRIER AT ONE POINT IN ITS PATH OF TRAVEL; CONTINUOUSLY DEPOSITING A THIN LAYER OF MOLTEN SULPHUR ON THE WATER FILM AT ANOTHER POINT IN THE PATH OF TRAVEL OF THE CARRIER ADJACENT TO THE POINT WHERE THE WATER FILM IS APPLIED; CONTINUOUSLY DIRECTING A STREAM OF COOLING WATER AGAINST THE ENTIRE BOTTOM SURFACE OF SAID CARRIER AS IT ROTATES, WHEREBY THE DEPOSITED LAYER OF SULPHUR WILL BE SOLIDIFIED DUE TO THE EXTRACTION OF HEAT THEREFROM; AND CONTINUOUSLY BREAKING UP AND REMOVING THE SOLIDIFIED
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US215178A US2630374A (en) | 1951-03-12 | 1951-03-12 | Method for the recovery of elemental sulfur in liquid form from gases containing hydrogen sulfide and the conversion of the liquid sulfur into solidified flakes |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2629895A true US2629895A (en) | 1953-03-03 |
Family
ID=22801983
Family Applications (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US215178A Expired - Lifetime US2630374A (en) | 1951-03-12 | 1951-03-12 | Method for the recovery of elemental sulfur in liquid form from gases containing hydrogen sulfide and the conversion of the liquid sulfur into solidified flakes |
| US215179A Expired - Lifetime US2617718A (en) | 1951-03-12 | 1951-03-12 | Catalytic reactor |
| US215180A Expired - Lifetime US2629895A (en) | 1951-03-12 | 1951-03-12 | Method of and apparatus for making flake sulfur |
Family Applications Before (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US215178A Expired - Lifetime US2630374A (en) | 1951-03-12 | 1951-03-12 | Method for the recovery of elemental sulfur in liquid form from gases containing hydrogen sulfide and the conversion of the liquid sulfur into solidified flakes |
| US215179A Expired - Lifetime US2617718A (en) | 1951-03-12 | 1951-03-12 | Catalytic reactor |
Country Status (1)
| Country | Link |
|---|---|
| US (3) | US2630374A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4500349A (en) * | 1981-12-24 | 1985-02-19 | The Dow Chemical Company | Production of round salt coated metal granules |
| US4519758A (en) * | 1981-12-24 | 1985-05-28 | The Dow Chemical Company | Rotary cooling table |
Families Citing this family (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2758913A (en) * | 1951-10-11 | 1956-08-14 | Stanolind Oil & Gas Co | Process for sulfur recovery |
| US2834653A (en) * | 1953-02-24 | 1958-05-13 | American Smelting Refining | Production of sulfur from hydrogen sulfide and sulfur dioxide |
| US2765217A (en) * | 1952-07-09 | 1956-10-02 | Texas Gulf Sulphur Co | Cyclic process for recovering sulfur from hydrogen sulfide |
| US2785056A (en) * | 1953-11-02 | 1957-03-12 | Metallgesellschaft Ag | Process for the production of sulfur from hydrogen sulfide and sulfur dioxide or oxygen containing gases |
| US3074924A (en) * | 1956-04-25 | 1963-01-22 | Continental Oil Co | Continuous polymerization process |
| US3393050A (en) * | 1966-04-22 | 1968-07-16 | Pan American Petroleum Corp | Recovery of free sulfur from hydrogen sulfide-containing gas |
| US3407040A (en) * | 1966-09-22 | 1968-10-22 | Pan American Petroleum Corp | Recovery of free sulfur from sour gases |
| DE2501557A1 (en) * | 1975-01-16 | 1976-07-22 | Metallgesellschaft Ag | METHOD AND APPARATUS FOR THE OBTAINING ELEMENTAL SULFUR |
| US4411870A (en) * | 1981-12-28 | 1983-10-25 | Uop Inc. | Reactor system |
| US4411869A (en) * | 1981-12-28 | 1983-10-25 | Uop Inc. | Multiple stage reactor system |
| EP0137081B1 (en) * | 1981-12-28 | 1987-07-08 | Uop Inc. | Catalytic reactor system and hydrocarbon conversion process utilizing it |
| US6048507A (en) * | 1997-12-09 | 2000-04-11 | Limtech | Process for the purification of lithium carbonate |
| CA2434233C (en) * | 2003-07-03 | 2010-02-16 | Clean-Flo Gas Filtration Systems (1987) Ltd. | Method of scrubbing lower mass sulfides with a sulfide scrubbing medium capable of regeneration |
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| US254464A (en) * | 1882-03-07 | Apparatus for | ||
| US1130670A (en) * | 1913-02-08 | 1915-03-02 | Christen Christensen | Apparatus for cooling molten or emulsion-like substances on a cooling-surface. |
| US1417542A (en) * | 1921-05-10 | 1922-05-30 | John L Mauch | Process and apparatus for casting hot liquid material |
| US1419911A (en) * | 1921-05-31 | 1922-06-20 | Texas Gulf Sulphur Co | Solidifying sulphur |
| US2335726A (en) * | 1941-11-05 | 1943-11-30 | Courtaulds Ltd | Treatment of textile threads |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB120554A (en) * | 1917-11-08 | 1920-07-15 | William G Leamon | Improvements in Methods of Treating Gases Containing Hydrogen Sulphide. |
| GB267138A (en) * | 1926-03-04 | 1927-12-15 | Int Des Procedes Prudhomme Hou | Process and apparatus for the hot desulphurisation of gases derived from the distillation or the pyrogenation of solid, liquid or other combustibles |
| US1922872A (en) * | 1927-12-22 | 1933-08-15 | Gen Chemical Corp | Method of removing hydrogen sulphide from natural gas |
| US1947779A (en) * | 1930-04-25 | 1934-02-20 | Wilbert J Huff | Apparatus for purifying gas |
| US2270427A (en) * | 1939-08-15 | 1942-01-20 | American Smelting Refining | System for reducing sulphur dioxide to sulphur by natural gas |
| US2298641A (en) * | 1940-02-17 | 1942-10-13 | Phillips Petroleum Co | Treatment of hydrocarbon gases |
| US2386202A (en) * | 1941-12-01 | 1945-10-09 | Southern Acid & Sulphur Compan | Method for extraction of sulphur from gases |
| US2386390A (en) * | 1941-12-01 | 1945-10-09 | Willis C Fernelius | Apparatus for extracting sulphur from gases |
| US2388259A (en) * | 1942-07-17 | 1945-11-06 | American Smelting Refining | Recovery of sulphur from gaseous mixtures |
| US2384926A (en) * | 1942-12-17 | 1945-09-18 | Standard Oil Dev Co | Process for producing sulphur |
| US2431236A (en) * | 1943-08-04 | 1947-11-18 | American Smelting Refining | Production of sulphur from gaseous mixtures |
| US2534792A (en) * | 1945-01-25 | 1950-12-19 | Olin Mathieson | Reaction furnace and recovery units |
| US2497095A (en) * | 1945-01-25 | 1950-02-14 | Olin Mathieson | Recovery of elemental sulfur from acidic gases |
| US2561990A (en) * | 1947-10-14 | 1951-07-24 | Jefferson Lake Sulphur Co | Method of desulphurization of gases |
-
1951
- 1951-03-12 US US215178A patent/US2630374A/en not_active Expired - Lifetime
- 1951-03-12 US US215179A patent/US2617718A/en not_active Expired - Lifetime
- 1951-03-12 US US215180A patent/US2629895A/en not_active Expired - Lifetime
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US254464A (en) * | 1882-03-07 | Apparatus for | ||
| US1130670A (en) * | 1913-02-08 | 1915-03-02 | Christen Christensen | Apparatus for cooling molten or emulsion-like substances on a cooling-surface. |
| US1417542A (en) * | 1921-05-10 | 1922-05-30 | John L Mauch | Process and apparatus for casting hot liquid material |
| US1419911A (en) * | 1921-05-31 | 1922-06-20 | Texas Gulf Sulphur Co | Solidifying sulphur |
| US2335726A (en) * | 1941-11-05 | 1943-11-30 | Courtaulds Ltd | Treatment of textile threads |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4500349A (en) * | 1981-12-24 | 1985-02-19 | The Dow Chemical Company | Production of round salt coated metal granules |
| US4519758A (en) * | 1981-12-24 | 1985-05-28 | The Dow Chemical Company | Rotary cooling table |
Also Published As
| Publication number | Publication date |
|---|---|
| US2630374A (en) | 1953-03-03 |
| US2617718A (en) | 1952-11-11 |
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