US3058673A - Apparatus for pulverizing material - Google Patents

Apparatus for pulverizing material Download PDF

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Publication number
US3058673A
US3058673A US100679A US10067961A US3058673A US 3058673 A US3058673 A US 3058673A US 100679 A US100679 A US 100679A US 10067961 A US10067961 A US 10067961A US 3058673 A US3058673 A US 3058673A
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United States
Prior art keywords
grinding chamber
outlet
inlet
under pressure
particles
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
Application number
US100679A
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English (en)
Inventor
Peter C Firing
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
NL Industries Inc
Original Assignee
Nat Lead Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority to NL121906D priority Critical patent/NL121906C/xx
Priority to NL276708D priority patent/NL276708A/xx
Application filed by Nat Lead Co filed Critical Nat Lead Co
Priority to US100679A priority patent/US3058673A/en
Priority to GB11703/62A priority patent/GB943579A/en
Priority to FR893013A priority patent/FR1318990A/fr
Priority to FI0709/62A priority patent/FI40507B/fi
Priority to ES276123A priority patent/ES276123A1/es
Priority to AT275962A priority patent/AT260665B/de
Priority to DEC26657A priority patent/DE1223237B/de
Priority to CH411462A priority patent/CH405890A/de
Application granted granted Critical
Publication of US3058673A publication Critical patent/US3058673A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C19/00—Other disintegrating devices or methods
    • B02C19/06—Jet mills
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C19/00—Other disintegrating devices or methods
    • B02C19/06—Jet mills
    • B02C19/061—Jet mills of the cylindrical type

Definitions

  • the present invention relates to a new and novel apparatus for pulverizing material, and more particularly to an arrangement wherein the material is fed into a treatment zone in a unique manner and relationship with respect to the outlet from the treatment zone.
  • the present invention is directed to arrangements for finely grinding material, such devices commonly being referred to as micronizers.
  • Such apparatus is employed for finely grinding various materials into a powder-like form and in typical applications, the apparatus may be used for grinding up coarse particles of silica sand, salt, calciner discharge pigment, and the like.
  • the grinding action in micronizer devices is produced by attrition grinding or in other words, the particles of the treated material actually impact upon one another so as to physically tear the particles apart and reduce the size thereof.
  • Conventional micronizers generally provide a grinding chamber into which is directed a plurality of streams of gas under pressure, these streams being directed in such a manner as to produce a vortex within the grinding chamber.
  • the material to be treated is fed into the chamber and the vortex action therewithin causes the particles to impact against one another, the larger particles being carried outwardly by centrifugal force and the finer particles drifting inwardly until they are withdrawn from the central'portion of the grinding chamber.
  • the present invention provides a unique and improved manner of feeding the material to be treated into the grinding chamber, and in this respect represents a radical departure from the manner in which material is fed into prior art devices.
  • the feed arrangement is so constructed that the material is introduced near the periphery of the grinding chamber or in any event at a point spaced radially outwardly or laterally of the outlet of the apparatus. This has beeen considered to be necessary in order to prevent the outlet vortex from entraining coarse particles as they enter the grinding chamber. It is, of course, evident that any coarse particles which might travel from the inlet directly to the outlet would not be properly processed, and accordingly, the device would not function in the desired manner. Any tendency of the coarse particles to prematurely be withdrawn through the outlet is commonly referred to as shortcircuiting.
  • prior art feeding arrangements generally introduce the material to be treated at an angle such that the direction of movement is forwardly in the direction of rotation maintained within the grinding chamber by the streams of gas under pressure. This arrangement further assists in reducing the tendency for the coarse particles to be shortcircuited through the apparatus.
  • the inlet to the grinding chamber is disposed axially of the apparatus, and is axially aligned with and directly opposite to the outlet from the grinding chamber.
  • Flow directing means is disposed adjacent the inlet for changing the direction of movement of the infiowing material.
  • This flow directing means is so "ice constructed that the material is directed substantially radially of the grinding chamber toward the outer periph cry of the grinding chamber and away from the outlet.
  • the construction of the flow directing means is such that the infiowing material is distributed in all directions so as to get a very uniform distribution thereof within the grinding chamber.
  • the particles of material are initially directed radially outwardly such that they must completely reverse their direction of travel in order to reach the outlet of the grinding chamber.
  • the outwardly directed force acting on the particles tends to cause the larger particles to move to the outer periphery of the chamber which is a desirable feature, and the inflowing material and the streams of gas under pressure are initially generally moving in directions normal one to the other.
  • An additional feature of the present invention is the constructionof the annular side wall of the grinding chamber.
  • This side wall is constructed so as tobe a re:
  • An object of the present invention is to provide a new and novel apparatus for pulverizing material which pro-,
  • a further object of the invention is to provide pulver izing apparatus wherein there is less wear on the side Wall and nozzle portions thereof.
  • Still another object of the invention is the provision of pulverizing apparatus which substantially reduces the consumption of gas under pressure utilized for producing the streams hereinabove referred to.
  • a still further object of the invention is to provide 'pul-- verizing apparatus which is quite simple and inexpensive in construction and yet efiicient and reliable in operation.
  • FIG. 1 is a top view partly broken away of pulverizing apparatus according to the present invention
  • FIG. 2 is a sectional view partly broken away along line 22 of FIG. 1 looking in the direction of the arrows;
  • FIG. 3 is an enlarged sectional view taken substantially along line 3-3 of FIG. 2 looking in the direction of the arrows;
  • FIG. 4 is an enlarged end view of an inlet nozzle means employed in the present invention.
  • FIG. 5 is a sectional view taken substantially along line 55 of FIG. 4 looking in the direction of the arrows;
  • FIG. 6 is a sectional view taken along line 66 of FIG. 4 looking in the direction of the arrows;
  • FIG. 7 is a sectional view taken along line 7-7 of FIG. 4 looking in the direction of the arrows;
  • FIG. 8 is a sectional view similar to FIG. 3 illustrating in a somewhat schematic manner a modified form of the invention
  • FIG. 9 is a view similar to FIG. 8 of a still further modified form of the invention.
  • FIG. 10 is a sectional view taken substantially along line 10 10 of FIG. 9 looking in the direction of the arrows.
  • FIG. 1 a system employing the micronizer apparatus of the present invention.
  • the body means within which the grinding chamber is disposed is indicated generally by reference numeral 10, and it should be noted that in the present invention, the wheel-like main body portion may be disposed vertically in contrast to prior art arrangements wherein the main body portion including the grinding chamber is usually disposed horizontally.
  • the main body portion is maintained in its operative position by suitable conventional brace means comprising a plurality of angle iron members indicated by reference numerals 11 which are suitably rigidly interconnected with one another.
  • An inlet conduit 12 is provided which is in communication with the central portion of the grinding chamber Within the body means, and an outlet conduit 13 disposed in axial alignment with conduit 12 is in communication with the opposite central portion of the grinding chamber within the body means.
  • a feed hopper 15 is provided through which material to be treated is fed into the inlet conduit 12, and a conduit 16 is connected with a suitable source of gas under pressure such as steam, which is employed for forcing the feed material under pressure into the grinding chamber of the apparatus.
  • Conduit 20 is suitably connected with a source of gas under pressure such as steam, this conduit being connected with a steam chest 21 which extends annularly about the side wall portion of the grinding chamber as will hereinafter more clearly appear.
  • a source of gas under pressure such as steam
  • the steam chest 21 includes therewithin an annularly extending recess or manifold 25 which is adapted to distribute gas under pressure such as steam received through the conduit 20 to various jet nozzles disposed about the grinding chamber and in communica-.
  • member 32 forms the side wall of the grinding chamber and in combination with the steel ring 31 serves to provide a rigid outer framework for the body means.
  • the inner surface 35 of side wall 32 is provided with a central annular recess by forming the inner surface of a substantially V- shaped cross-sectional configuration such that it will provide a pair of sloping surfaces completely around the grinding chamber which is indicated by the reference numeral 36.
  • the sloping walls of the inner surface 35 may also be curved if desired, as long as the net effect is to cause particles thrown out by centrifugal force to move along the walls to the central portion of the side wall 32.
  • the grinding chamber is defined by the side wall 32 and also is axially confined between a first end wall portion 40 and a second end wall portion 41.
  • End wall portions 40 and 41 may each be provided with a suitable liner 40' and 41' respectively formed of stainless steel or the like to reduce wear thereon.
  • end wall portions 40 and 41 are suitably rigidly secured to the side wall and ring assembly 31, 32 as by clamping and the like to provide a rigid unit.
  • a plurality of stud and nut assemblies 45 serve to connect end wall portion 40 with a radially extending flange formed on the outlet conduit 13.
  • An annular ring 46 is suitably secured as by welding within a central opening 47 provided through end wall 40, and it will be noted that ring 46 includes an outer portion 48 which extends axially within the grinding chamber. This portion 48 serves as an annular barrier which will block the movement of particles along liner 40 to the outlet opening 50 formed through the ring 46.
  • Some relatively heavy particles may tend to move along liner 40 without being sufliciently comminuted in the vortex within the chamber, and accordingly, there is a tendency for some relatively large particles to move inwardly very closely adjacent to the liner 40' out of the main vortex flow and thence to the outlet.
  • Portion 48 prevents this movement of relatively large particles along the liner 40' and ensures that such particles will not be short circuited through the device without being swept up into the vortex and sufliciently comminuted. It is apparent that a large space is provided between the annular barrier 48 and the remaining components of the device which permits a ready flow of fine particles into the outlet of the apparatus.
  • a plurality of stud and nut assemblies 51 connect a fitting 52 to the other end wall portion 41, and a gasket 53 is mounted between fitting 52 and end wall 41.
  • Fitting 52 includes an axially extending hollow boss 55 having an internal thread 56 formed in the bore thereof.
  • a first tubular member 57 having a thread on the outer surface thereof is threaded within boss 55 and includes a radially extending flange 58.
  • a second tubular member 59 has a radially extending flange 60 formed thereon, and the feed hopper '15 is formed integral with tubular member 59 and extends upwardly therefrom as seen in FIG. 3.
  • a hollow member 61 has a venturi-shaped bore 62 formed therewithin and the radially extending flange 63 thereof is clamped between flanges 58 and 60, the entire assembly being held in this clamped position by nut and bolt assembly 65.
  • a radially extending flange 66 is formed at the outer end of tubular member 59 and is connected by nut and bolt assembly 67 to a radially extending flange 68 formed on the adjacent end of conduit 16.
  • a steam nozzle 69 is mounted within tubular member 59' adjacent the flange 66 thereof, the inner surface of tubular member 59 and the outer surface of steam nozzle 69 being provided with cooperating threads for mounting the steam nozzle in position.
  • the feeding arrangement thus far described is fairly conventional since the material to be treated is fed downwardly through the hopper portion as indicated by arrow A. Gas under pressure such as steam flowing through conduit 16 as indicated by arrow B then passes out through the open end of the steam nozzle 69.
  • the open end of the steam nozzle is disposed beneath the forward end of the hopper A and as the steam escapes from nozzle 69, it will entrain material flowing down through the hopper, and in cooperation with the venturi bore portion 62 will carry the material under pressure into the grinding chamber.
  • the inlet opening into the grinding chamber is indicated at 70, this inlet opening being formed through the central portion of an annular member 72 having an arcuate inner surface 73 of the configuration shown.
  • a flow directing means in the form of an inlet nozzle indicated generally by reference numeral 75 is supported in position as hereinafter more fully described adjacent to member 72 and is provided with an arcuate surface 76 which in cooperation with arcuate surface 73 on member 72 defines an annular passageway 80 which discharges at 81 in such a direction that particles of material leaving the discharge portion 81 are directed substantially radially outwardly toward the side wall of the grinding chamber and away from the outlet thereof.
  • a tapered recess portion 85 is formed in the end wall portion 41 adjacent the outlet of the inlet nozzle means to ensure that there is sufiicient clearance for the particles to smoothly flow into the grinding chamber. 7
  • the inlet nozzle means 75 has a substantially circular outer configuration, and as seen in FIG. 5, the outer surface 83 may be substantially flat, while the inner surface 84 tapers from the discharge portion 81 substantially uniformly to a point 85 whereupon the arcuate surface 76 slopes upwardly to an apex or point 86. It will thus be seen that as the stream of inflowing material passes through the inlet opening 70, it will be diverted gradually by the arcuate surface 76 and the sloping surface 85 to a direction substantially normally to the axial inflow whereby the material will be directed radially outwardly of the nozzle means within the grinding chamber.
  • FIG. 4 four similar attaching abutments 90 are provided for securing the inlet nozzle means in operative position as shown in FIG. 3 for example.
  • These four abutments 90 are equally angularly spaced from one another and terminate at apex portions 91 from which they extend outwardly from the sharply tapered portions of surface 76.
  • the inner portions of the abutments adjacent to the apex portions 91 are substantially triangular in cross-section as seen in FIG. 7 thereby defining a pair of oppositely sloping side surfaces 92.
  • the rear portions 93 of the abutments which extend to the outer periphery of the inlet nozzle means are substantially rectangular in cross-section, and two sloping surfaces 95 connect the surfaces 92 with the rectangular rear portion 93.
  • each of the abutments 90 provides a minimum of resistance to flow of the material passing through the inlet opening 70 and impinging upon the inlet nozzle means.
  • a hardened sleeve 100 is provided in an opening formed through each of the abutrnents 90, the bore within the insert sleeves being threaded.
  • Aligned counter bored openings 101 are provided in member 72 and four cap screws 102 extend through openings 101 and are threaded within the sleeves 100. In this manner, the four cap screws securely retain the inlet means in operative position, and at the same time the four spaced abutments still permit ready flow of the material thereabout and thence radially outwardly within the grinding chamber.
  • the flow directing means thus far described is in the form of an inlet nozzle means. It is apparent that the construction of the flow directing means can be wisely varied as long as the end result is to change the direction of the axially flowing material so as to direct it substantially radially outwardly within the grinding chamber.
  • the body means within which the grinding chamber is disposed and the surrounding steam chest 121 may be identical with the previously disclosed arrangement.
  • the inlet opening is indicated by reference numeral 122 and the outlet opening is indicated by reference numeral 123.
  • the flow directing means in this modification may take the form of a flat plate or baflle 126 which may be suitably supported in position as shown, the baflle being, of course, disposed between the inlet and the outlet of the grinding chamber. It is evident that as indicated by the arrows in FIG. 8 the flow of material under pressure will be deflected by the plate 125, and since the material is flowing in under pressure, it will thereby be directed substantially radially outwardly within the grinding chamber.
  • the modification shown in FIG. 8 will obtain the desired end result, although it is considered preferable to gradually change the direction of flow with a construction as shown for example in FIG. 3.
  • FIGS. 9 and 10 a further modification of the invention is illustrated wherein the body means 130 and steam chest 131 associated therewith may be identical with the previously discussed structure.
  • the inlet conduit 135 may terminate in a closed end 136.
  • the cylindrical portion 137 of the conduit which extends within the grinding chamber may be provided with a plurality of radially extending openings 138 as seen most clearly in FIG. 10 of the drawings. As shown, these openings are eight in number, it being apparent that the number of openings may be varied as desired.
  • a plurality of streams of gas under pressure are also discharged into an outer portion of the treatment zone, and the treated material is Withdrawn from the central portion of the zone.
  • the method may be carried out with many different structural arrangements and the flow directing means may be widely varied as will be apparent to one skilled in the art, the essential feature being that the inflowing material is radially directed outwardly from a central portion of the grinding chamber opposite to the outlet of the grinding chamber.
  • Pulverizing apparatus including a substantially cylindrical grinding chamber, means for admitting a plurality of angularly spaced streams of gas under pressure into an outer portion of said chamber, said grinding chamber being defined between opposite end wall portions and a side wall portion, one end wall portion having an outlet formed thcrethrough, the opposite end wall portion having an inlet formed therethrough substantially aligned with said outlet, and flow directing means adjacent said inlet for directing material flowing through said inlet under pressure outwardly toward the outer periphery of the chamber and away from said outlet, said side wall portion including a centrally recessed annular portion, said means for admitting a plurality of streams of gas under pressure opening through said recessed portion.
  • Pulverizing apparatus comprising a body means including a first end wall portion and a second end wall portion and an annularly extending side wall portion disposed between said end wall portions to define a substantially cylindrical grinding chamber, said first end wall portion having an outlet formed through the central portion thereof, said second end wall portion having an inlet formed through the central portion thereof and being axially aligned with said outlet, and flow directing means disposed adjacent said inlet and between said inlet and said outlet for directing a stream of material flowing through said inlet under pressure radially outwardly of u the chamber toward the outer periphery of the chamber and away from said outlet.
  • Apparatus as defined in claim 2, wherein said fie directing means comprises an arcuate deflecting surface for deflecting and changing the direction of an infiowing stream of material.
  • Apparatus as defined in claim 2 including an annular barrier extending into said chamber from said first end wall portion for defining an annular barrier about said outlet.
  • Pulverizing apparatus comprising a body means including a first end wall portion and a second end wall portion joined by an annular side wall portion, said side wall portion including an inner surface the central portion of which is recessed, a plurality of jets mounted in said side wall and opening through said recessed portion of the side wall for admitting gas under pressure into an outer portion of said chamber, said first end wall portion having an outlet formed through the central portion thereof, said second end wall portion having an inlet formed through the central portion thereof directly opposite to and axially aligned with said outlet, flow directing means disposed adjacent said inlet, said flow directing means including a surface for directing an inflowing stream of material under pressure radially outwardly of the flow directing means toward said side wall and away from said outlet to thereby prevent short-circuiting of material to be treated through the apparatus.

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  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Disintegrating Or Milling (AREA)
  • Preliminary Treatment Of Fibers (AREA)
  • Treatment Of Fiber Materials (AREA)
  • Nozzles (AREA)
US100679A 1961-04-04 1961-04-04 Apparatus for pulverizing material Expired - Lifetime US3058673A (en)

Priority Applications (10)

Application Number Priority Date Filing Date Title
NL121906D NL121906C (ja) 1961-04-04
NL276708D NL276708A (ja) 1961-04-04
US100679A US3058673A (en) 1961-04-04 1961-04-04 Apparatus for pulverizing material
GB11703/62A GB943579A (en) 1961-04-04 1962-03-27 Method of and apparatus for pulverizing material
FR893013A FR1318990A (fr) 1961-04-04 1962-04-02 Procédé de broyage fin et appareils pour sa mise en oeuvre
FI0709/62A FI40507B (ja) 1961-04-04 1962-04-03
ES276123A ES276123A1 (es) 1961-04-04 1962-04-03 Un aparato y un método para la pulverización de materiales
AT275962A AT260665B (de) 1961-04-04 1962-04-04 Strahlmühle
DEC26657A DE1223237B (de) 1961-04-04 1962-04-04 Strahlmuehle mit flachzylindrischer Mahlkammer
CH411462A CH405890A (de) 1961-04-04 1962-04-04 Verfahren und Einrichtung zum Pulverisieren von Material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US100679A US3058673A (en) 1961-04-04 1961-04-04 Apparatus for pulverizing material

Publications (1)

Publication Number Publication Date
US3058673A true US3058673A (en) 1962-10-16

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US100679A Expired - Lifetime US3058673A (en) 1961-04-04 1961-04-04 Apparatus for pulverizing material

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US (1) US3058673A (ja)
AT (1) AT260665B (ja)
CH (1) CH405890A (ja)
DE (1) DE1223237B (ja)
ES (1) ES276123A1 (ja)
FI (1) FI40507B (ja)
FR (1) FR1318990A (ja)
GB (1) GB943579A (ja)
NL (2) NL121906C (ja)

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3168989A (en) * 1962-05-02 1965-02-09 Allis Chalmers Mfg Co Process and equipment for the production of granulated material
US3184169A (en) * 1963-03-29 1965-05-18 Lawrence S Friedman Apparatus for pneumatically pulverizing material
US3223333A (en) * 1963-09-24 1965-12-14 Fluid Energy Proc And Equipmen Method for preparing liquid slurries and for dispersement thereof in polymeric substances
US3348779A (en) * 1964-10-02 1967-10-24 Norwood H Andrews Method and apparatus for comminuting materials
US3837583A (en) * 1972-05-13 1974-09-24 Kronos Titan Gmbh Multi-stage jet mill
US4018388A (en) * 1976-05-13 1977-04-19 Andrews Norwood H Jet-type axial pulverizer
US4515317A (en) * 1982-02-01 1985-05-07 Thiokol Corporation Method of and apparatus for grinding solid organic waste material encountered in sewage waste and waste water reclamation
WO2001024935A2 (en) * 1999-10-06 2001-04-12 Cornerstone Technologies, L.L.C. High pressure mill and method of creating ultra-fine particles of materials using the same
US20020054995A1 (en) * 1999-10-06 2002-05-09 Marian Mazurkiewicz Graphite platelet nanostructures
US20080277264A1 (en) * 2007-05-10 2008-11-13 Fluid-Quip, Inc. Alcohol production using hydraulic cavitation
CN105665104A (zh) * 2016-04-12 2016-06-15 苏州金宁纳米科技有限公司 一种超细颗粒破碎装置及破碎方法
CN112604799A (zh) * 2020-11-28 2021-04-06 韩寒 一种石英砂滤料制备方法
US11634865B2 (en) 2016-02-11 2023-04-25 Structured I, Llc Belt or fabric including polymeric layer for papermaking machine

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2275213B (en) * 1993-02-16 1996-03-20 Atritor Ltd Micronising mill

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US90097A (en) * 1869-05-18 Improved apparatus for purifying-, screening
US2474314A (en) * 1944-11-28 1949-06-28 Johns Manville Method and apparatus for size reduction and fiberizing of crude fibrous materials
US2690880A (en) * 1951-04-10 1954-10-05 Freeport Sulphur Co Rectilinear pulverizer
US2917386A (en) * 1955-09-09 1959-12-15 Aeroprojects Inc Homogenizing method and apparatus

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB432191A (en) * 1933-10-09 1935-07-22 Internat Pulverizing Corp Improvements in or relating to the pulverizing of minerals and similar materials
DE674661C (de) * 1935-12-22 1939-04-22 Benjamin Graemiger Dipl Ing Einrichtung zum Zerkleinern von festem Gut
GB756791A (en) * 1953-06-08 1956-09-12 Texaco Development Corp Improvements in or relating to method and apparatus for disintegrating solid materials

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US90097A (en) * 1869-05-18 Improved apparatus for purifying-, screening
US2474314A (en) * 1944-11-28 1949-06-28 Johns Manville Method and apparatus for size reduction and fiberizing of crude fibrous materials
US2690880A (en) * 1951-04-10 1954-10-05 Freeport Sulphur Co Rectilinear pulverizer
US2917386A (en) * 1955-09-09 1959-12-15 Aeroprojects Inc Homogenizing method and apparatus

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3168989A (en) * 1962-05-02 1965-02-09 Allis Chalmers Mfg Co Process and equipment for the production of granulated material
US3184169A (en) * 1963-03-29 1965-05-18 Lawrence S Friedman Apparatus for pneumatically pulverizing material
US3223333A (en) * 1963-09-24 1965-12-14 Fluid Energy Proc And Equipmen Method for preparing liquid slurries and for dispersement thereof in polymeric substances
US3348779A (en) * 1964-10-02 1967-10-24 Norwood H Andrews Method and apparatus for comminuting materials
US3837583A (en) * 1972-05-13 1974-09-24 Kronos Titan Gmbh Multi-stage jet mill
US4018388A (en) * 1976-05-13 1977-04-19 Andrews Norwood H Jet-type axial pulverizer
US4515317A (en) * 1982-02-01 1985-05-07 Thiokol Corporation Method of and apparatus for grinding solid organic waste material encountered in sewage waste and waste water reclamation
US6318649B1 (en) 1999-10-06 2001-11-20 Cornerstone Technologies, Llc Method of creating ultra-fine particles of materials using a high-pressure mill
WO2001024935A2 (en) * 1999-10-06 2001-04-12 Cornerstone Technologies, L.L.C. High pressure mill and method of creating ultra-fine particles of materials using the same
US20020054995A1 (en) * 1999-10-06 2002-05-09 Marian Mazurkiewicz Graphite platelet nanostructures
WO2001024935A3 (en) * 1999-10-06 2002-05-10 Cornerstone Technologies L L C High pressure mill and method of creating ultra-fine particles of materials using the same
US6824086B1 (en) 1999-10-06 2004-11-30 Cornerstone Technologies, L.L.C. Method of creating ultra-fine particles of materials using a high-pressure mill
US20080277264A1 (en) * 2007-05-10 2008-11-13 Fluid-Quip, Inc. Alcohol production using hydraulic cavitation
US11634865B2 (en) 2016-02-11 2023-04-25 Structured I, Llc Belt or fabric including polymeric layer for papermaking machine
CN105665104A (zh) * 2016-04-12 2016-06-15 苏州金宁纳米科技有限公司 一种超细颗粒破碎装置及破碎方法
CN112604799A (zh) * 2020-11-28 2021-04-06 韩寒 一种石英砂滤料制备方法
CN112604799B (zh) * 2020-11-28 2022-04-08 安康市翔泽油田材料有限公司 一种石英砂滤料制备方法

Also Published As

Publication number Publication date
AT260665B (de) 1968-03-11
FI40507B (ja) 1968-10-31
FR1318990A (fr) 1963-02-22
CH405890A (de) 1966-01-15
NL276708A (ja)
GB943579A (en) 1963-12-04
NL121906C (ja)
DE1223237B (de) 1966-08-18
ES276123A1 (es) 1962-06-16

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