US213471A - Improvement in processes of and apparatus for reducing grain in vacuo - Google Patents
Improvement in processes of and apparatus for reducing grain in vacuo Download PDFInfo
- Publication number
- US213471A US213471A US213471DA US213471A US 213471 A US213471 A US 213471A US 213471D A US213471D A US 213471DA US 213471 A US213471 A US 213471A
- Authority
- US
- United States
- Prior art keywords
- air
- vacuo
- improvement
- processes
- grain
- 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.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title description 6
- 235000013339 cereals Nutrition 0.000 description 20
- 235000013312 flour Nutrition 0.000 description 18
- 239000000126 substance Substances 0.000 description 18
- 230000000694 effects Effects 0.000 description 10
- 241000209149 Zea Species 0.000 description 4
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 4
- 238000010276 construction Methods 0.000 description 4
- 235000005822 corn Nutrition 0.000 description 4
- 235000005824 corn Nutrition 0.000 description 4
- 239000008187 granular material Substances 0.000 description 4
- 235000012054 meals Nutrition 0.000 description 4
- 238000010298 pulverizing process Methods 0.000 description 4
- 210000000188 Diaphragm Anatomy 0.000 description 2
- 240000008529 Triticum aestivum Species 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- 230000000266 injurious Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000006011 modification reaction Methods 0.000 description 2
- 238000009527 percussion Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000004321 preservation Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000004642 transportation engineering Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 235000021307 wheat Nutrition 0.000 description 2
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C13/00—Disintegrating by mills having rotary beater elements ; Hammer mills
- B02C13/22—Disintegrating by mills having rotary beater elements ; Hammer mills with intermeshing pins ; Pin Disk Mills
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S241/00—Solid material comminution or disintegration
- Y10S241/14—Grinding in inert, controlled atmosphere
Definitions
- This invention relates to apparatus in which the pulveri'zatipn or reduction to flour or powder of grain, seeds, or granular substances of any description is effected by percussion, in lieu of by grinding or crushing-that is to say, by means of heaters acting upon the grain or granular substances while in the act of fallin g, or while they are being projected through the apparatus.
- Figure 1 represents a part longitudinal section and part elevation of the apparatus, and Fig. 2 is a transverse section of the same.
- Two shafts, B B are employed, placed end to end, supported on frames A A, and rotating in opposite directions in bearings G O, of peculiar construction, enabling the shafts to be regularly and constantly lubricated even when. rotating at high rates of speed.
- the ends of the shafts which are in juxtaposition, carry disks D D, upon which the cages or heaters d at are fixed in concentric rows, rotating in a case, E, strengthened externally by angle-irons made to fit as closely as possible over the said disks.
- the shafts are passed through stuffing-boxes e e in the side of the case.
- the shafts are driven by pulleys F F, which are keyed upon them and caused to rotate in opposite directions by a belt carried over the main driving-shaft.
- the case E is connected to a hopper, L, for containing the substance to be treated by means of a tube, G, bifurcated at the end within the case, so as to deliver the substance at the center of the cage, and provided with an apparatus for excluding air atthe other end, where it is connected to the hopper.
- This apparatus consists of a cylinder, H, divided into several approximately air-tight compartments by radial partitions m, attached to a shaft, 00, passed through the center of the cylinder, and caused to rotate by a pulley, O, driven by a belt connected to the main driving-shaft.
- each compartment is presented in turn to the aperture at the bottom of the hopper L it is filled with the grain or other substance to be pulverized or reduced, andas it continues to rotate it carries the same round to the aper ture on the top of the feed-pipe G, into which its contents are discharged, while all air, except that which is contained in the interstices of the grains or granules, is effectually excluded.
- a similar arrangement is provided for the discharge of the flour or pulverized substance through a pipe, 2', at the lower part of the case for excluding air at this point, this apparatus being likewise actuated by a belt and pulley, O, driven by the main driving-shaft.
- a more or less perfect vacuum is maintained within the case by means of a pump, J, Fig. 2, on what is known as Greindls system, connected to the case by a pipe, j, and actuated by the main driving-shaft; or an ejector, K, Fig. 2, provided with a check-valve, may be employed for efiecting the same object by means of a-jet of steam obtained either direct from the boiler or from the exhaust-pipe of the engine.
- air may be exhausted from the chamber in which the cages rotate by means of apparatus other than those hereinbefore specifiedsuch, for example,as ordinary air-pumps.
- the air may also be exhausted through hollow shafts; or the outlet or outlets for the air may be situated at any part of the case which may be found most convenient, according to circumstances, and the said outlets maybe provided with wire-gauze diaphragms, as shown at k 7:, Fig. 2, in a conical chamber which will not impede the passage of the air, while the wire-gauze prevents the escape of the flour; and for the same purpose the pipe through which the air is exhausted may be made siphon form, as shown in dotted lines at l l, Fig. 2; or the apparatus described for the discharge of the tlour may be replaced by a powerful fan, exhausting the air within the case, and delivering the flour to a bolting apparatus, which will thus be enabled to work easily and economically under pressure.
- This improved pulverizing or disintegrating apparatus working in a rarefied atmosphere possesses other important advantages besides the great saving in motive power.
- the rarefaction or exhaustion of the air in the chamber in which the cages work has the effect of considerably reducing the temperature in the said chamber and maintaining it at a very low degree, which, in the production of flour or meal in general, and corn or wheat and flour in particular, is a most important object.
- This rarefaction or exhaustion of the air also has the effect of facilitating the free fall or projection of the grains or granules, also of prolnotin g the evaporation of the water contained in the grain, so as to greatly facilitate its decortication.
- the last-named effect of the rarefaetion or exhaustion of the air enables dry meal or flour to be obtained direct from the mill, and, consequently, in the best possible condition forits transportation or preservation.
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- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Cereal-Derived Products (AREA)
Description
J. B. TOUPFLIN. I Process of and Apparatus for Reducing Grain in ,Vacum N0.-213,47l Patented Mar. 18,1879.
N.FETERS, PHOTO-UTHOGRAPNER. WASHINGTON. n c.
UNITED STATES PATENT OFFICE.
JEAN B. TOUFFLIN, OF PARIS, FRANCE.
IMPROVEMENT IN PROCESSES UP AND APPARATUS FOR REDUCING GRAIN IN VACUO.
Specification forming part of Letters Patent No. 2 13,471, dated March 18, 1879 application filed October 15, 1878; patented in England, July 30, 1878.
To all whom it may concern:
Be it known that I, JEAN BENJAMIN Tour- FLIN, of Paris, in the Republic of France, have invented certain new and useful Improvements in Reducing Grain and other Substances, and in the apparatus employed therein, of which improvements the following is a full, clear, and exact description.
This invention relates to apparatus in which the pulveri'zatipn or reduction to flour or powder of grain, seeds, or granular substances of any description is effected by percussion, in lieu of by grinding or crushing-that is to say, by means of heaters acting upon the grain or granular substances while in the act of fallin g, or while they are being projected through the apparatus.
In disintegrators or pulverizing apparatus of every description (Whether with a vertical or horizontal axis) the following phenomena are produced when the said apparatus are caused to rotate in, their cases, which are usually of considerable size, videlicet: The motion of the plates or disks which carry the bars or heaters in circular rows, thus forming a'series of cages, causes air to be drawn in through the feeding-hopper, through the openin g for the discharge of the flour, and in some cases through the hollow shafts on which are mounted the disks carrying the heaters. This air is then forced out into a passage provided for the purpose, and usually placed on the top of the case of the apparatus.
Experience has shown that under these conditions the greater part of the motive power is absorbed by the mere setting of he heaters in motion, even when the apparat is running empty.
In order to reduce the amount of the power thus expended in driving the apparatus, it is necessary to remove, as far as practicable, one of the principal causes of this expenditure of power-that is to say, the resistance of the air to be displacedwhich object the said invention is designed to effect; and in order that the said invention may be fully understood, I shallnowproceed more particularly to describe the same, and for that purpose shall refer to the several figures on the accompanying sheet of drawings, which illustrate an apparatus construoted and arranged in accordance with the said invention, and more particularly applicable to the reduction of corn to the condition of flour.
Figure 1 represents a part longitudinal section and part elevation of the apparatus, and Fig. 2 is a transverse section of the same.
Two shafts, B B, are employed, placed end to end, supported on frames A A, and rotating in opposite directions in bearings G O, of peculiar construction, enabling the shafts to be regularly and constantly lubricated even when. rotating at high rates of speed. The ends of the shafts, which are in juxtaposition, carry disks D D, upon which the cages or heaters d at are fixed in concentric rows, rotating in a case, E, strengthened externally by angle-irons made to fit as closely as possible over the said disks. The shafts are passed through stuffing-boxes e e in the side of the case.
The shafts are driven by pulleys F F, which are keyed upon them and caused to rotate in opposite directions by a belt carried over the main driving-shaft. The case E is connected to a hopper, L, for containing the substance to be treated by means of a tube, G, bifurcated at the end within the case, so as to deliver the substance at the center of the cage, and provided with an apparatus for excluding air atthe other end, where it is connected to the hopper. This apparatus consists of a cylinder, H, divided into several approximately air-tight compartments by radial partitions m, attached to a shaft, 00, passed through the center of the cylinder, and caused to rotate by a pulley, O, driven by a belt connected to the main driving-shaft.
As each compartment is presented in turn to the aperture at the bottom of the hopper L it is filled with the grain or other substance to be pulverized or reduced, andas it continues to rotate it carries the same round to the aper ture on the top of the feed-pipe G, into which its contents are discharged, while all air, except that which is contained in the interstices of the grains or granules, is effectually excluded.
A similar arrangement is provided for the discharge of the flour or pulverized substance through a pipe, 2', at the lower part of the case for excluding air at this point, this apparatus being likewise actuated by a belt and pulley, O, driven by the main driving-shaft.
A more or less perfect vacuum is maintained within the case by means of a pump, J, Fig. 2, on what is known as Greindls system, connected to the case by a pipe, j, and actuated by the main driving-shaft; or an ejector, K, Fig. 2, provided with a check-valve, may be employed for efiecting the same object by means of a-jet of steam obtained either direct from the boiler or from the exhaust-pipe of the engine.
The air within the case being continually exhausted and rarefied by the action of the Greindl pump or ejector, the injurious resistance hereiubefore referred to is considerably reduced, if not completely obviated.
Itis evident that air may be exhausted from the chamber in which the cages rotate by means of apparatus other than those hereinbefore specifiedsuch, for example,as ordinary air-pumps. The air may also be exhausted through hollow shafts; or the outlet or outlets for the air may be situated at any part of the case which may be found most convenient, according to circumstances, and the said outlets maybe provided with wire-gauze diaphragms, as shown at k 7:, Fig. 2, in a conical chamber which will not impede the passage of the air, while the wire-gauze prevents the escape of the flour; and for the same purpose the pipe through which the air is exhausted may be made siphon form, as shown in dotted lines at l l, Fig. 2; or the apparatus described for the discharge of the tlour may be replaced by a powerful fan, exhausting the air within the case, and delivering the flour to a bolting apparatus, which will thus be enabled to work easily and economically under pressure.
This improved pulverizing or disintegrating apparatus working in a rarefied atmosphere possesses other important advantages besides the great saving in motive power. The rarefaction or exhaustion of the air in the chamber in which the cages work has the effect of considerably reducing the temperature in the said chamber and maintaining it at a very low degree, which, in the production of flour or meal in general, and corn or wheat and flour in particular, is a most important object. This rarefaction or exhaustion of the air also has the effect of facilitating the free fall or projection of the grains or granules, also of prolnotin g the evaporation of the water contained in the grain, so as to greatly facilitate its decortication.
Moreover, the last-named effect of the rarefaetion or exhaustion of the air enables dry meal or flour to be obtained direct from the mill, and, consequently, in the best possible condition forits transportation or preservation.
The said invention is applicable to disintegrators generally constructed upon the principle of that hereinbefore described, and illustrated in the accompanying drawings, whether with vertical or horizontal axes, either solid or hollow, and with any required modifications in the details of construction.
Having now described and particularly ascertained the nature of the said invention, and the manner in which the same is or may be used or carried into effect, I would observe in conclusion that what I consider to be novel and original, and therefore claim as my invention, is-
1. The method of reducing grain and other substances by the action of heaters in a vacuum or partial vacuum, substantially in the manner aml by the means hereinbefore described.
2. The combination, with a disintegrator or apparatus for reducing grain and other substances by the action of heaters, of mechanism, as described, for making and maintaining in said disintegrator avacuum or partial vacuum, substantially as set forth.
In testimony whereof I have signed my name to this specification before two subscribing witnesses.
J. B. TOUFFLIN.
Witnesses:
EMILE BARRAUL'I, Arc. YINtK.
Publications (1)
Publication Number | Publication Date |
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US213471A true US213471A (en) | 1879-03-18 |
Family
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Family Applications (1)
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US213471D Expired - Lifetime US213471A (en) | Improvement in processes of and apparatus for reducing grain in vacuo |
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US (1) | US213471A (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2552603A (en) * | 1948-08-27 | 1951-05-15 | Herbert G Tanner | Apparatus and method to comminute solid particles in gas |
US2601953A (en) * | 1948-08-12 | 1952-07-01 | Gen Electric | Process of making chemically active graphitic carbon powder |
US2752097A (en) * | 1951-03-03 | 1956-06-26 | Microcyclomat Co | Method and apparatus for the production of fine and ultrafine particles |
US2768054A (en) * | 1952-12-30 | 1956-10-23 | Gen Aniline & Film Corp | Process of making acetate dyestuff powders |
US2807424A (en) * | 1955-08-01 | 1957-09-24 | Robert B Records | Tiltable axis attrition mill with hammer and knife rotor |
US3594874A (en) * | 1967-04-15 | 1971-07-27 | Yoshida Kogyo Kk | Slide fastener |
US3630774A (en) * | 1968-08-14 | 1971-12-28 | Corn Products Co | Disrupted granular starch products and methods of making them |
US4203555A (en) * | 1978-05-15 | 1980-05-20 | Dickson Thomas D Jr | Rotary foodstuff mill and milling process |
US4422578A (en) * | 1981-09-04 | 1983-12-27 | Stratford Squire International | Rotary grain mill having means for controlling air and grain flow therethrough, and method |
US4609157A (en) * | 1983-04-20 | 1986-09-02 | Compagnie Clayton | Machine for shredding waste |
-
0
- US US213471D patent/US213471A/en not_active Expired - Lifetime
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2601953A (en) * | 1948-08-12 | 1952-07-01 | Gen Electric | Process of making chemically active graphitic carbon powder |
US2552603A (en) * | 1948-08-27 | 1951-05-15 | Herbert G Tanner | Apparatus and method to comminute solid particles in gas |
US2752097A (en) * | 1951-03-03 | 1956-06-26 | Microcyclomat Co | Method and apparatus for the production of fine and ultrafine particles |
US2768054A (en) * | 1952-12-30 | 1956-10-23 | Gen Aniline & Film Corp | Process of making acetate dyestuff powders |
US2807424A (en) * | 1955-08-01 | 1957-09-24 | Robert B Records | Tiltable axis attrition mill with hammer and knife rotor |
US3594874A (en) * | 1967-04-15 | 1971-07-27 | Yoshida Kogyo Kk | Slide fastener |
US3630774A (en) * | 1968-08-14 | 1971-12-28 | Corn Products Co | Disrupted granular starch products and methods of making them |
US4203555A (en) * | 1978-05-15 | 1980-05-20 | Dickson Thomas D Jr | Rotary foodstuff mill and milling process |
US4422578A (en) * | 1981-09-04 | 1983-12-27 | Stratford Squire International | Rotary grain mill having means for controlling air and grain flow therethrough, and method |
US4609157A (en) * | 1983-04-20 | 1986-09-02 | Compagnie Clayton | Machine for shredding waste |
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