US467041A - Method of and apparatus for the manufacture of lead fiber - Google Patents
Method of and apparatus for the manufacture of lead fiber Download PDFInfo
- Publication number
- US467041A US467041A US467041DA US467041A US 467041 A US467041 A US 467041A US 467041D A US467041D A US 467041DA US 467041 A US467041 A US 467041A
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- Prior art keywords
- lead
- fiber
- chamber
- molten
- manufacture
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- 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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- 239000000835 fiber Substances 0.000 title description 38
- 238000004519 manufacturing process Methods 0.000 title description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 229910000004 White lead Inorganic materials 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 238000001816 cooling Methods 0.000 description 4
- 230000000875 corresponding Effects 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate dianion Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 2
- 229910000003 Lead carbonate Inorganic materials 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 239000000110 cooling liquid Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- RYZCLUQMCYZBJQ-UHFFFAOYSA-H lead(2+);dicarbonate;dihydroxide Chemical compound [OH-].[OH-].[Pb+2].[Pb+2].[Pb+2].[O-]C([O-])=O.[O-]C([O-])=O RYZCLUQMCYZBJQ-UHFFFAOYSA-H 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000006011 modification reaction Methods 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 230000001105 regulatory Effects 0.000 description 2
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
- B22D11/005—Continuous casting of metals, i.e. casting in indefinite lengths of wire
Definitions
- This invention relates to a novel method and apparatus for the. manufacture of lead fiber, especially adapted,a mong other things, to be used in the preparation of lead carbonate or white lead.
- the lead must be in a condition to fiow, which is effected by heating the metallic lead -to its melting po1nt;
- the molten lead in a finely-divided state should not be sufficiently hot to cause the said finely-divided lead or fiber to break upinto shot or very small pieces, and I have found by practice that the lead should not be heated substantially above 800 Fahrenheit, and, third, 2. very considerable pressure is required to force the molten lead through one or more orifices sufiiciently small to form lead fiber of the required thickness or diameter.
- the conditions required to be met for the successful production of lead fiber of a consid erable or desired length are. fulfilled in the following manner, namely: The lead is melted and maintained in a heated chamber at a temperature substantially near the melting point, whereby the first and second conditions before referred to are met, and a sufficient depth or body of molten lead is maintained in the chamber or receptacle to obtain the pressure required to force the bottom layer of molten lead out through the discharge orifice or orifices.
- Figure l isasid'e elevation, partially broken out, of an apparatus by which my improved method may be carried into eifect;
- Fig. 2 an apparatus by which my improved method may be carried into eifect;
- FIG. 1 end elevation of the apparatus shown in Fig. 1, looking toward the left; Fig. 3, a sectional detail to be referred to, and Fig. at a modification in section to be referred to.
- A represents a chamber or receptacle in which the lead to be made into fiber is maintained in a molten condition by means of heat, which may and preferably will be generated in a combustion-chamber or furnace A, upon which the chamber or receptacle A may be supported.
- the chamber or receptacle A and the furnace or combustion-chamber A may be made ofiron or other suitable material, and the receptacle A may be of square, round, or of any other desired shape, but of sulficient height to contain a body or column of molten lead sufifiicient to obtain the pressure required to force the molten lead out of the chamber or receptacle.
- I may employ any other desired formsuch, for instance, as shown in Fig. 4, wherein the pipe I) has screwed upon it a cap I), provided with a substantially large opening or orifice b, and between which cap and the pipe 11 a perpendicular plate or screen If is secured. Th e pipes b may be screwed or otherwise secured to the chamber A.
- the molten lead as it issues from the orilices b is preferably discharged upon an endless belt or web 0, traveling through water or other cooling-liquid c, contained in a vat c' which in practice is made of a width corresponding to the height of the column of molten lead maintained in the chamber A; or the said vat may be substantiallynarrow and set at a distance from ,the discharge-orifice I)" corresponding to the height of the column of lead in the chamber A, for as the column of molten lead increases in height the stream of molten lead discharged through the orifice b will increase in length and will attain a considerablelength before striking the water.
- the molten lead passes through a sufficient' distance in air to enable it to set, so that when it strikes the water the thin stream of lead will break up into fibers or pieces of considerable length, and not into small pieces, or what is practically called shot, as would be the case if the thin stream of molten lead struck the water before becoming set.
- the lead fiber be discharged onto the endless belt 0, so that the said fiber may be easily and quickly deposited upon a tray or suitable.
- receptacle located outside the vat c ,-and which maybe readily removed and a new or empty one substituted therefor.
- the endless belt or web 0 is passed about a shaft or roller cl, located at one end of the tank or vat 0 below the water-line, and under rollers (1* d located below the water-line at the other end of the vat c and then over rollers (1 (i supported in suitable bearings outside the vat or tank, and then about a roller (1", also supported in bearings outside the tank below the rollers (Z' d.
- the endless belt 0 may be made to travel by means of a belt not shown, but which is passed about apulley d on .the shaft or roller (1'.
- the chamber or receptacle A has connected to it a pyrometer (1 of any usual or wellknown construction, by which the temperature of the lead within the said chamber may be ascertained.
- the furnace orcombustion-chambcrA may be provided with the usual door 6 and damper e, by which the draft may be regulated.
- the lead fiber will preferably be about one foot in length for the best results.
- the column of molten lead may and preferabl y will be maintained at a substantially constant level or height by a supply of molten lead from a ladle, crucible, or other meltingpotf, from which the molten lead may be discharged in a practically continuous stream through a discharge-pipej", provided with a cock or valve f.
- I claim 1 The herein described method for the manufacture of lead fiber, which consists in foming molten lead through a substantially small orifice by the pressure of a column of the molten lead of a height or depth suliicient to obtain the pressure necessary to force the molten lead through the said orifice, substantially as described.
- the herein-described method for the manufacture of lead fiber which consists in heating the lead to'a temperature substantially near its melting-point and below $00 Fahrenheit, forcing the lead thus heated through a substantially small orifice by the pressure of a column of the lead maintained at a height not substantially below two and one-half feet, and, lastly, cooling the lead dis- 9 charged through the orifice, substantially as described.
- the herein-described method for the manufacture of lead fiber which consists, first, in heating the lead to a temperature substantially near its melting-point; second, forcing the lead thus heated through a substantially small orifice by the pressure of a column of the lead of a head sufficient to cause the molten lead to flow; third, permitting the lead forced through the orifice to become set, and, lastly, cooling the lead fiber after being set, wherebythe lead fiber may be broken up into pieces of considerable length, substantially as described.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
- Inorganic Fibers (AREA)
Description
(No Model.)
N..K. MORRIS.
METHOD 0]? AND APPARATUS FOR THE MANUFACTURE OF LEAD FIBER..
Patented Jan/12, 18 92.
\Y/ifgesses.
m WAFH v A. ll E J \Q' 11112:; Q
NITED, STATES PATENT OFFIGE',
NORMAN K. Moan-1s, or 1)EN\ ER,COLOR ADO.
METHOD OF AND APPARATUS FOR THE MANUFACTURE OF LEAD FIBEZR.
SPECIFICATION forming part of Letters Patent No. 467,041, dated January 12, 1892.
Ap lication filed March 10, 1891. serial No. 384,439. (No model.)
-.T0'a.Zl whom. it may concern:
Be it known that I, NORMAN K. MORRIS, of Denver, county of Arapahoe, Stateof Colorado, have invented an Improvement in Methods of and Apparatus for the Manufactureof Lead Fiber, of which the following description, in connection with the accompanying drawings, is a specification, likeletters on the drawings representing like parts.
This invention relates to a novel method and apparatus for the. manufacture of lead fiber, especially adapted,a mong other things, to be used in the preparation of lead carbonate or white lead.
It has been demonstrated that a superior quality of whitelead can be made 1n ashorter time when the metallic lead is In afinely-divided condition than when the lead is in large pieces or in a bulky condition. It. has also been demonstrated that lead in a finely-d1- vided condition is in the best form not only for the production of a superior carbonate or white lead, but also for convenience in handling and for supporting it in the most advantageous manner to permit of ready access to it of the corroding gas and vapor. lhe lead in fibrous form-that is, in fine string-like strips'-is acknowledged to be the best form inv which the lead may be put to obtain the best results.
- I am aware that attempts have been made to manufacture lead fiber by means of machinery; but such attempts have not been practically and commercially successful, owing to the fact that peculiareconditlons are present which cannot be fulfilled or met practically by means of machinery.
For the successful manufacture of lead fiber three main or principalcondltions must be met, namely: First, the lead must be in a condition to fiow, which is effected by heating the metallic lead -to its melting po1nt; second, the molten lead in a finely-divided state should not be sufficiently hot to cause the said finely-divided lead or fiber to break upinto shot or very small pieces, and I have found by practice that the lead should not be heated substantially above 800 Fahrenheit, and, third, 2. very considerable pressure is required to force the molten lead through one or more orifices sufiiciently small to form lead fiber of the required thickness or diameter.
In accordance with my present invention the conditions required to be met for the successful production of lead fiber of a consid erable or desired length are. fulfilled in the following manner, namely: The lead is melted and maintained in a heated chamber at a temperature substantially near the melting point, whereby the first and second conditions before referred to are met, and a sufficient depth or body of molten lead is maintained in the chamber or receptacle to obtain the pressure required to force the bottom layer of molten lead out through the discharge orifice or orifices.
The particular features of my invention will be pointed out in the claims at the end of this specification.
Figure l isasid'e elevation, partially broken out, of an apparatus by which my improved method may be carried into eifect; Fig. 2, an
end elevation of the apparatus shown in Fig. 1, looking toward the left; Fig. 3, a sectional detail to be referred to, and Fig. at a modification in section to be referred to.
A represents a chamber or receptacle in which the lead to be made into fiber is maintained in a molten condition by means of heat, which may and preferably will be generated in a combustion-chamber or furnace A, upon which the chamber or receptacle A may be supported.
The chamber or receptacle A and the furnace or combustion-chamber A may be made ofiron or other suitable material, and the receptacle A may be of square, round, or of any other desired shape, but of sulficient height to contain a body or column of molten lead sufifiicient to obtain the pressure required to force the molten lead out of the chamber or receptacle.
In actual practice I have ascertained that for the'best results a column or body of from about two and one-half to about three feet is required, and have represented the height of the said column by the dotted line a.
, Owing to the very high specific gravity of lead (namely, 11.3) a column of molten lead of from two and one-half to three feet will exert a very considerable pressure, sufficient to force the said molten lead out through one or more discharge-nozzles I), provided, as herein shown, with a stop-cock b, the said nozzle having, as shown in Fig. 3, a cap 11 provided with one or more small orifices I as desired,
through which the lower layerof molten lead is forced by the superimposed column vof molten lead.
Instead of the perforated cap 11 shown in Fig. 8, I may employ any other desired formsuch, for instance, as shown in Fig. 4, wherein the pipe I) has screwed upon it a cap I), provided with a substantially large opening or orifice b, and between which cap and the pipe 11 a perpendicular plate or screen If is secured. Th e pipes b may be screwed or otherwise secured to the chamber A.
The molten lead as it issues from the orilices b is preferably discharged upon an endless belt or web 0, traveling through water or other cooling-liquid c, contained in a vat c' which in practice is made of a width corresponding to the height of the column of molten lead maintained in the chamber A; or the said vat may be substantiallynarrow and set at a distance from ,the discharge-orifice I)" corresponding to the height of the column of lead in the chamber A, for as the column of molten lead increases in height the stream of molten lead discharged through the orifice b will increase in length and will attain a considerablelength before striking the water. In this manner the molten lead passes through a sufficient' distance in air to enable it to set, so that when it strikes the water the thin stream of lead will break up into fibers or pieces of considerable length, and not into small pieces, or what is practically called shot, as would be the case if the thin stream of molten lead struck the water before becoming set.
I prefer that the lead fiber be discharged onto the endless belt 0, so that the said fiber may be easily and quickly deposited upon a tray or suitable. receptacle (I, located outside the vat c ,-and which maybe readily removed and a new or empty one substituted therefor.
The endless belt or web 0 is passed about a shaft or roller cl, located at one end of the tank or vat 0 below the water-line, and under rollers (1* d located below the water-line at the other end of the vat c and then over rollers (1 (i supported in suitable bearings outside the vat or tank, and then about a roller (1", also supported in bearings outside the tank below the rollers (Z' d.
The endless belt 0 may be made to travel by means of a belt not shown, but which is passed about apulley d on .the shaft or roller (1'.
The chamber or receptacle A has connected to it a pyrometer (1 of any usual or wellknown construction, by which the temperature of the lead within the said chamber may be ascertained.
The furnace orcombustion-chambcrA may be provided with the usual door 6 and damper e, by which the draft may be regulated.
I have herein shown the chamber A asprovided with nine discharge-pipes b; but I do not desire to limit myself to any particular number, as the same may be varied as desired.
In practice the lead fiber will preferably be about one foot in length for the best results.
The column of molten lead may and preferabl y will be maintained at a substantially constant level or height by a supply of molten lead from a ladle, crucible, or other meltingpotf, from which the molten lead may be discharged in a practically continuous stream through a discharge-pipej", provided with a cock or valve f.
I claim 1. The herein described method for the manufacture of lead fiber, which consists in foming molten lead through a substantially small orifice by the pressure of a column of the molten lead of a height or depth suliicient to obtain the pressure necessary to force the molten lead through the said orifice, substantially as described.
9. The herein-described method for the manufacture of lead fiber, which consists in heating the lead to'a temperature substantially near its melting-point and below $00 Fahrenheit, forcing the lead thus heated through a substantially small orifice by the pressure of a column of the lead maintained at a height not substantially below two and one-half feet, and, lastly, cooling the lead dis- 9 charged through the orifice, substantially as described.
23. The herein-described method for the manufacture of lead fiber, which consists, first, in heating the lead to a temperature substantially near its melting-point; second, forcing the lead thus heated through a substantially small orifice by the pressure of a column of the lead of a head sufficient to cause the molten lead to flow; third, permitting the lead forced through the orifice to become set, and, lastly, cooling the lead fiber after being set, wherebythe lead fiber may be broken up into pieces of considerable length, substantially as described.
at. The combination, with a chamber or receptacle A to contain molten lead, a dischargepipe therefor provided with a substantially small orifice, and a furnace or combustionchamber A, substantially as described.
5. The combination, with a chamber or receptacle A to contain molten lead, a dischargepipe .therefor provided with a substantially small orifice, and a furnace or combustionchamber A, and a vat or tank to contain a cooling-fluid,and a traveling belt or web in said tank below the level of the cooling-fluid, substantially as described.
In testimony, whereof I have signed my name to this specification in the presence of two subscribing witnesses.
WILLL-m ROBINSON, WM. M. CHRISTIE.
Publications (1)
Publication Number | Publication Date |
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US467041A true US467041A (en) | 1892-01-12 |
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US467041D Expired - Lifetime US467041A (en) | Method of and apparatus for the manufacture of lead fiber |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2886866A (en) * | 1956-12-12 | 1959-05-19 | Marvalaud Inc | Apparatus and method for producing metal fibers and filaments |
US2907082A (en) * | 1956-02-06 | 1959-10-06 | Marvaland Inc | Production of continuous filaments of high vapor pressure metals |
US2939177A (en) * | 1955-02-08 | 1960-06-07 | Celanese Corp | Process of cutting partially coagulated esters of cellulose into short lengths |
US8273857B2 (en) | 2009-09-22 | 2012-09-25 | Jen-Chang Hsia | Compositions and methods of use of neurovascular protective multifunctional polynitroxylated pegylated carboxy hemoglobins for transfusion and critical care medicine |
-
0
- US US467041D patent/US467041A/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2939177A (en) * | 1955-02-08 | 1960-06-07 | Celanese Corp | Process of cutting partially coagulated esters of cellulose into short lengths |
US2907082A (en) * | 1956-02-06 | 1959-10-06 | Marvaland Inc | Production of continuous filaments of high vapor pressure metals |
US2886866A (en) * | 1956-12-12 | 1959-05-19 | Marvalaud Inc | Apparatus and method for producing metal fibers and filaments |
US8273857B2 (en) | 2009-09-22 | 2012-09-25 | Jen-Chang Hsia | Compositions and methods of use of neurovascular protective multifunctional polynitroxylated pegylated carboxy hemoglobins for transfusion and critical care medicine |
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