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US1627488A - Ball mill - Google Patents

Ball mill
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US1627488A
US1627488AUS59542AUS5954225AUS1627488AUS 1627488 AUS1627488 AUS 1627488AUS 59542 AUS59542 AUS 59542AUS 5954225 AUS5954225 AUS 5954225AUS 1627488 AUS1627488 AUS 1627488A
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mill
hollow shaft
impeller
screen
chamber
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Paul L Crowe
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P. L. CROWE May 3. 1927.
BALL MILL s Sheets-Sheet 1 Filed Sept. 50 1925 JWWGJZ f or- PQ zzZZL 5/"0 ATTORNEY P. L. CROWE BALL MILL May 3; 1927. 1,627,488
Filed Sept. so 1925 s Sheets-Sheet 2 PQuZZ. C/vzd INVENTOR 1,627,488 May 1927' P. L. CROWE BALL MILL Filed Sept. 50 1925 s Sheets-Sheet 3 N SK yaw/ya i x aea m PATENT OFFICE.
PAUL L. CROWE, 01F BALTIMORE, MARYLAND.
BALL
MILL.
' Application filed September 30, 1925. Serial No. 59,542.
My present invention has reference to improvements in centrifugal pulverizing and blowing apparatus for combustible material, such as coal by the use of which the ground material can be fed to a furnace for its combustion and supplying the heat of combustion to a heating apparatus for various uses of heat in trade and resides in the operative relation of means of confining necessary adjuncts for the complete combination of parts necessary to create a unification thereof as a whole, in operating the parts and obtaining the desired results.
A further object is the reduction of fuel to the required fineness for its combustion in furnaces of any size, style or construction.
Another object is to supply the demand for any conditions of capacity.
Another object is the provision of a device of this character which may be arranged in any position that maa be available and yet properly supply the emand for its heating capacity.
Another object is to supply the demand for quickness of service.
Another object is to sup ly a mill for the degree of fineness of corn ustion' to fulfill the necessities of variable furnace constructions. i
With these and other objects in view which may come to light in these specifications, theinvention resides .in the novel association of parts and in the unique construction hereinafter described and definitely claimed.
In the drawings: Figure 1 is a central longitudinal sectional view through a mill in accordance with this invention.
Figure 2 is an end view thereof. Figure 3 is a sectional view on theline 33 of Figure 1. 4
Figure 4 is a sectional view on the line 4-4 of Figure 1.
Figure 5 is a longitudinal sectional view through another form of the improvement.
Figure 6 is a sectional-view through a further modified form of the improvement. Figure 7 is a similar view of a further modification.
Figure 8 is a similar ther modification.
Figure 9 is a similar view of a still further modification.
Fig. 10' is a similar view of a 'ther modification.
It will be noted as "view of a still forstill fur the description progresses that my invention consists in a ball mill furnace feeding device with such apparatus as is required to blow, induce, regulate, supply, collect, force, create, use, induct, impel, and repel, expel, propel, separate, contract, retract, extract, abrade, attrlte, receive, produce, forward, deliver-as well as generate power for feeding coal to and from the feeding and reduction appuratus to boilers and other furnaces in a refined combustible for refined combustion uni-.
versally.
The principle involved'in this invention is that coal is conveyed to and into-the apparatus for the pulverizin'g thereof, the action of the process and method is centrifugal by the use of'the impeller and the power ha hind it and also with the use of small balls and flint pebbles manufactured-for the reduction of the material to be ground. As this process continues the coal is fed evenly, the fine particles being sufficiently ground to pass through a 95 to 98 of 100 screen'mesh, the flow of air carries the ground fuel through the screen mesh into the impeller, and is in turn forced by the impeller into the feeding tube and into the furnace. V 7
As the fuel particles are reduced in size in the mill compartment by the abrasion of the balls and pebbles, the weight and speed of, and the turningmovement of the apparatus and mill compartment or chamber will cause the reduction of the fuel to a fineness best suited for the combustion thereof and for the furnace chamber requirements for which certain degrees of fineness of fuel may be adapted.
The mill chambers or compartments can be constructed to comply with the requirements of the consumer, orthe manufacturing plant, for quantities and capacities and for the dryness of the fuel to the degree of combustion requirements.
Referring now to the drawings in detail and Figures 1 to 4 in particular, the numeral 1 designates a suitable base having a central upright or standard 2 and end up rights orstandards 3. All of the standards terminate in bearings which are preferably cut at an angle and have fixed thereon removable bearing sections or caps. The bearings are preferably provided with raceways for anti-frictional elements. the end bearings being closed, as at 4, and receive therein the uprights 5 on the outer ends ofmill casings 6. The bearing for thecentral standard 2 receives therethrough a short hollow shaft whose flanged ends are bolted, as at 7, to longer hollow shafts centrally between the two mills. The removably connected hollow shaft sections present a unitary structure, which is indicated by the numeral 8 when connected together. 1
The bearing for thecentral standard 2 also supports thereon an upwardly disposedhopper 9. This hopper is divided by acentral partition 10 into opposite compartments. The inner heads of themill bodies 6 are in the nature of removable discs which are inwardly concaved. These heads are indicated for distinction by the numeral 11 and each of the said heads has a plurality of preferably equiedistantly spacedopenings 12 therethrough. The outer hollow head of each of the mill bodies provide impeller chambers 13.
The portions of the hollow shaft 8 disposed centrally in the impeller chambers 13 are formed withdisk flanges 14, and in the impeller chambers at or on the opposite faces of the flanges there are oppositely directedcurved fan blades 15 and 16, respectively. Theinner fan blades 16 have their inner ends reduced by being cut angularly toward thediscs 14, as indicated by thenumerals 17, for the passage of air. 1
The heads 11 of therespective mill casings 6 have arranged between and connected to or formed with one of the confronting faces thereof atubular screen 19 of fine mesh. The screens are preferably formedof segmental plates having reduced lapping edges which are bolted together. Thetubular screens 19, that form the outer hollow shafts, surround the hollow shaft and star Wheels or spiders are preferably secured on the hollow shaft 8 and to the arms of which the screen plates are bolted. The central portion 7 of the hollow shaft 8 is provided with right angularly disposed openings 20 designed to register with oppositely disposed openings in the central bearing. These last; mentioned openingsare provided with oppositely extending flow tubes for distri-- bution of the fuel. The space between the ends of the hollow shaft 8 and the closed ends 4 of the outer bearings has the wallprovided thereby also formed with oppo-K sitely directed aligning openings, and screwed or otherwise secured in these open- .ings there areflow tubes 21.
Thecompartments 22 and 23 provided in thehopper 9 have arranged in the mouths thereof, the nozzle ends ofpipe members 24 which are connected to the furnace lining and through which the impeller draws sufficiently warm air to raise the temperature in the mill to the degree for the proper dryness and combustion of the pulverized fuel. The passages through thepipes 24 are controlled byvalves 25,,
The mill chambers are partly filled with impact, attrition balls and pebbles of all sizes and the coal is fed through one or both ofthe hoppers into the mill compartments,
and while the mill is in operation and introtubes in the second direction from the ap-' paratus and the said fuel is from thence directed through suitable pipes connected to flow tubes to burners in the furnace. The burners may be directly connected to the flow tubes, should the furnaces be in close proximity to the mill, and any burner, conventional or special may be employed. Heated air is sucked by the impellers into the mill chamber to dry the coal before and after pulverization and to render the same in a better combustible state.
The grinding compartments in the mills are closed at their inner periphery and outer wall by headed cast iron plates which have reduced overlapping edges that are fastened together and to the impeller body. The pulverizing is, of course, effected by the turning movement of the impeller and the effect of the attrition balls and the compartment walls in the mill, the larger diameter having the effect of more economy in the motor power and such difference in construction as shown is necessary in the manufacture of the pulverizer in different sizes.
El In Figure 5 I have illustrated another form of the improvement in which both fine and coarse combustible material is simul taneously pulverized. Themill body 27 has one end formed with ahollow shaft 28 that is journaled in suitable bearings on the supporting frame. Removably secured at this end of the mill there is ahopper 29 that communicates with the bore of thehollow shaft 28, the said hopper being formed with aflow pipe 30. The opposite end of the mill body is provided with animpeller chamber 31. The inner wall of the impeller chamber is closed by ascreen 32. The impeller comprises a central portion ordisc 33 on whose opposite faces there are arranged oppositely directedfan blades 34 and 35. This end of the mill is also formed with ahollow shaft 36 which is reticulated outward of its bearing to provide a screen. Thehollow screen shaft 36 is closed by the central non-reticulated portion of adisc 37. The portion of the disc outward of the hollow screen shaft is formed with annular series of restricted apertures 88 and provides a second screen.
The mesh of both of the screens is fine for pulverizin A hollow sherical body memer 39 encl bses the reticulated portion of the tubular screen and the screen disc and thebody 39 is formed at its outer end with aflow tube 40 and this tube is provided with a burner or has a pipe leading therefrom directed to a burner 1n the furnace. The bearing through which thehollow screen shaft 36 passes has arranged thereover ahopper 41 that communicates with the interior of thebody member 39. Aguard ring 42 is received in the inner or month end of thebody member 39 to protect the outflow of material fed into said body member into the hopper and likewise to hold theattrition balls 45 in the said body member. Themill body 27 has also arranged therein attrition balls 44 and preferably communicating with theho pers 29 and 41 there are the nozzle ends ofipe members 43 that are connected to the urna'ce linin s. The operation is similar to that prevlously described. The turning of the impeller and thebody 39 causes the attrition alls to act upon the material fed into the mills, and likewise caussecond support for the mill body.
ing the impeller to act upon the said material for sucking both atmospheric and heated air.
In Figure 6 themill body 46 hasanim polling chamber 47 at one end thereof and divided from the mill chamber by ascreen 48. Thescreen 48 has a tubular extension inthe nature of a hollow shaft 49 which is reticulated at its periphery. The impeller includes a.disc 54, on whose opposite faces there arefan blades 55 and 56, respectively.
The inner edges of thefan blades 55 are cut at an inward angle and the disc'54 is formed on a central hol ow shaft 53 that finds bears lugs on a support. The second end of the central hollow shaft finds a bearing in the he mill body 1s formed at its end, opposite the impeller, with ahopper 57 that has ahot air pipe 58 communicating therewith. In the mill body there are arrangedattrition balls 59. The operation of this mill is also similar to that previously described.
In Figure 7 themill construction, on the right hand side of the said figure is similar to that disclosed in Figure 6. Thismill bod v 60, however, has one end of its hollow shaft 61 closed. and on the end of the said mill bodv there is a central shaft that finds a airing in the central upright of the supporting frame, the hollow shaft 61 finding a bearing in one of the end uprights of the frame. Thesecond mill body 62 has a hollow shaft 63 that finds a bearing in the second end upright of the frame. The b hollow shaft 63 has its inner portion reticulated to provide a screen and the end of the hollow shaft is formed with a disc flange 64 which is apertured toprovidc a second screen. Attrition balls are arranged in both of the mill bodies and both of the said mill bodies are provided with hoppers for the inlet of material- The hoppers have arranged therein pipes whic communicate with a source of hot air, which air is induced into the mill bodies by the impellers.
In Figure 8 the mill body 7 2 is stepped throughout the length thereof and isintcriorly formed in ali n with the said steps, withring partitions 73 and 74, thering partition 74 being disposed opposite the screen 7 5 that forms the inner wall of the chamber for theimpeller 76. The compartments provided by t e partitions have arranged therein attrition balls of varying weights and sizes. The central member of the impeller has arranged on its sides 0 positely directed fan blades, as revionsly escribed, and the ends of thebody 72 are provided withhollow shafts 78 and 79 that find hearings in the supportin frame. Communicating I with the body t ere is ahopper 80 sup ortcd from one of the frame members an communicatin with the compartment 81 in the mill chamber. that previously descrlbed, except that the material is more quickly acted on by being snbjectedto the successive force of impact by the different sized balls in the several,
com artments. Air is forced into the mill by t e impeller and material is delivered through the hollow shaft 7 8 toa suitable burner. A multiplicity of grinding mills is illustrated in Figure 9 which may be either simultaneously or independently operated.
The mills have their hollow shafts journaled in suitable hearings on the supporting frames. One of the end mill bodies 86 is- The 0 eration is similar to a 1n. its inner and open face an inis also apertured to provide a second screen and this hollow screen shaft passes through a flange that surrounds an outer opening in the mill body 86 and is fixed to this flange. The lower portion of the hop er is formed with a ring guide 94 that 1s received in one of the open sides of the intermediate spherical mill body 95. This mill ody has centrally secured therein apartition 96,-the said partition being also secured to a hollow shaft 97 that is fixed on the inner wall of the impeller chamber 91 and provides an extension of the hollow shaft 90.
til)
The hollow shaft 97 is apertured to providev a screen. The second open end of the mill body 95 receives thereina downwardlyinclined ring guide 98, the upper portion of which merging into a hopper 99. At the opposite sides of the hopper 99 there is a chamber 100 for impellers, and the hollow shaft 97 merges into this casing. The second end of the casing is formed with an outwardly directed hollow shaft 101 that is received in a hollow substantially pear-shaped mill body 102. This mill is divided by flanged partitions into a plurality of compartments 103. The outer and open end of the mill 102 has secured therein a nonaperturedhollow shaft 104. The portions of the hollow shaft 101, communicating with the compartments 103 in the mill 102 are apertured, as at 105. Thehollow shaft 104 extends longitudinally through the mill 102 and is enclosed by the screen shaft 101. Thehollow shaft 104 has anangle disc flange 106 that is received in a compartment 107 in the chamber 100. The widened and centrally open end of the mill 102 has received therein a directingring 108, and the said ring has arranged thereon or has secured thereto a hopper 109. The passage through the hopper 109 communicates with the upper portion of the mill 102.
Centrally received through thehollow shaft 104 there is a flow pipe 110. Thisflow pipe merges into acentral partition 11 that divides the compartment 107 and the chamber 100 from a second compartment 112 in the said chamber. Received in the compartment 112 is adisc flange 113 that is formed on one end of a flow pipe 114 the same size as the flow pipe 110. The flow-pipe 114 passes centrally through the hollow screen pipe 97 and has its second end formed with a disc flange 115 that is received in acompartment 116 in the chamber 91. The second compartment in the chamber 91 is indicated by the numeral 117 and is divided from thechamber 116 by only a ring flange 118. In the compartment 117 there is re ceived a disc flange 119 formed on the inner end of a flow pipe 120. The flow pipe 120 extends centrally through thetubular screen 93 in the mill 86. In all of the mills and in the compartment 103 in the mill 102 there are weighted breaker elements, such as steel balls or the like. The balls in the several compartments vary in size and consequently in weight. The several mills are revolved in a manner as willbe presently described and the material is acted upon by the weights,
the centrifugal force incident to the turning of the mills and the act of attrition as well as by the impellers and the air drawn into the mills by the impellers. The arrows indicate the directions taken by the material in the pulverizing thereof in the mills.
In Figure 10 the body of the mill 121 is of cylindrical shape. The mill is centrally divided by a screen partition 122 into compartments 123 and 124, respectively. The compartment 123 has communicating therewith the intake opening of a hopper 125, and the hopper has an opening below its inlet in which is arranged a'flow pipe 126. In the compartment 124 there are impeller blades 127. Similar fan or impeller blades may be arranged in the compartn'ient 123. The mill has central hollowshafts upon its opposite faces and the powdered material finds an outlet through thehollow shaft 128. The operation of the device is similar to that previously described.
It is to be noted that the parts of my improvement are assembled for repairing and facility in performing such repairs and that one end of the mill can be operated without the other end and one motor can operate all of the mills.
The motive power for driving the mills is preferably electrical and preferably by induction, and preferably in a motor generating set. The poles for the motor to operate the mill may be located at any convenient face of the body portion of the mill most available and suitable for such application. In the showing of, the drawings thepoles 129 are located on the peripheryof the rotating or impelling portion of the apparatus and the generator is invariably located near the center of rotation of the mill or impeller as is possible and convenient for its application. The motor poles can be located as desired to perform their functions electrically and in this case around the periphery of the rotor, the same being elec-' trically applied and connected electrically to the generator in the condition which will permit of the motor receiving its current from and through the generator, and as the motor operates the mill it also causes the generator to generate to the limit of the distance the motor is located from the generator center or from the generator to the motor peripherally. Thus it will be noted that the power current will be controlled so that the supply of power current will be permitted to supply only the amount of power current necessary to keep up the speed to its required degree of rotation and load or in other words the power current will be regulated in quantity to only the amount necessary between the current needed by the motor which is not supplied to it by the generator. It will be understood also that although some impellers and ball mills are small others may be larger in diameter and sufficiently contracted 1 in width to curtail the use of power current,
both as to a bill mill and its impeller for the application of the principle involved in this application and the use of power generally as applied to various constructions of appliances in general.
' screen forinin nee-mas changes in form, design, material employed etc. Therefore, I do not wish to be confined to the structural embodiments herein set forth and hold myself entitled to make such .Having described the invention, I,
1. A ball mill for pulverizing coal and like combustible material and for delivering the powdered material to aburner,comprising a. plurality of mill chambers, a hollow shaft for-the mills, bearings for the shaft, weighted balls in each mill chamber, a screen In each mill chamber, hoppers communicating with the chambers outward of the screens and through which the material is introduced, an im ller chamber in each mill, impellers int e chambers comprising oppositely directed curved fan blades, a partition associated with the hollow shaft and arranged between the fan blades, the outer series, of fan blades communicating with the hollow shaft, oppositel directed tubes communicating with the ollow shaft, and means for simultaneously or independently revolving the mills, as and for the purpose set forth.
2. Means for pulverizing coal or like combustible material, comprising a mill having hollow shafts projecting from the sides thereof, bearings for the shaft, said mill'having an impe er chamber therein, a
the inner wall of the chamber a secon screen arranged longitudin y in the mill chamber and connected with the first mentioned screen, attrition balls in the mill chamber, an impeller in the impeller chamber comprising a disc mem ber connected with the hollow shaft and oppositely curved fan blades on the sides ofthe disc, as and for the purpose set forth.
3. Means for pulverizmg coal or like combustible material, comprising a plurality of revoluble mills, a hollow shaft for the mills, bearings for the shaft, said shaft and the portions thereof received in the respective mills, being apertured to.prov1de screens, casings formed on the confronting ends of the shaft between the mills, a second hollow shaft arranged centrally in-the first mentioned hollow shaft and projecting through a closed end of the said first men- 'tioned shaft, said second mentioned shaft having angle flanges extending in the cas- A ings and provided with impeller blades, certam of said mills being divided by rin discs into separate compartments, weighte balls of different sizes in the respective compartments and means for independently or simultaneously imparting circumferential movement to the mills, as and for the purpose set forth.
4. A revoluble ball mill, for pulverizing coal or like combustible material, havlng hollow shafts, bearing 'members for the shafts, said mill being divided by a screen into a ball compartment and into an impeller chamber, a, fan impeller in the chamber, a core disc arranged around the mill, and poles for an induction motor extending iron;1 the core, as and for the purpose set ort ' 5. A. revoluble ball mill for pulverizing.
ing the mill, comprisin peripheral poles for an electric motor and poles at the center of the mill connected to the generator for the motor.
In testimony whereof I aflix my signature.
PAUL L. oRoWE,
US59542A1925-09-301925-09-30Ball millExpired - LifetimeUS1627488A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US2681210A (en)*1953-02-091954-06-15Alfred J SchaeferMixer and blender
US2708075A (en)*1952-05-291955-05-10Bath Iron Works CorpPeripheral feed breaker
US2853244A (en)*1956-05-151958-09-23John A PlimptonContinuous feeder for dual drum type breaker mills
US3537658A (en)*1968-12-101970-11-03Polysius GmbhAutogenous airswept mill
US20070007372A1 (en)*2000-07-072007-01-11Symyx Technologies, Inc.Methods and apparatus for mechanical treatment of materials such as catalysts

Cited By (6)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US2708075A (en)*1952-05-291955-05-10Bath Iron Works CorpPeripheral feed breaker
US2681210A (en)*1953-02-091954-06-15Alfred J SchaeferMixer and blender
US2853244A (en)*1956-05-151958-09-23John A PlimptonContinuous feeder for dual drum type breaker mills
US3537658A (en)*1968-12-101970-11-03Polysius GmbhAutogenous airswept mill
US20070007372A1 (en)*2000-07-072007-01-11Symyx Technologies, Inc.Methods and apparatus for mechanical treatment of materials such as catalysts
US7503515B2 (en)*2000-07-072009-03-17Symyx Technologies, Inc.Methods and apparatus for mechanical treatment of materials such as catalysts

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