US238044A - luckenbach - Google Patents
luckenbach Download PDFInfo
- Publication number
- US238044A US238044A US238044DA US238044A US 238044 A US238044 A US 238044A US 238044D A US238044D A US 238044DA US 238044 A US238044 A US 238044A
- Authority
- US
- United States
- Prior art keywords
- pipes
- tubes
- mineral
- gases
- steam
- 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
- 239000000126 substance Substances 0.000 description 30
- 239000007789 gas Substances 0.000 description 22
- 229910052500 inorganic mineral Inorganic materials 0.000 description 22
- 239000011707 mineral Substances 0.000 description 22
- 239000000463 material Substances 0.000 description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- 238000010298 pulverizing process Methods 0.000 description 8
- 206010010254 Concussion Diseases 0.000 description 6
- -1 steam Substances 0.000 description 6
- 239000000843 powder Substances 0.000 description 4
- 210000001513 Elbow Anatomy 0.000 description 2
- 238000005299 abrasion Methods 0.000 description 2
- 125000004429 atoms Chemical group 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 230000001939 inductive effect Effects 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000005065 mining Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000003247 radioactive fallout Substances 0.000 description 2
- 239000002699 waste material Substances 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
- B02C19/00—Other disintegrating devices or methods
- B02C19/06—Jet mills
Definitions
- the objects of our invention are to provide a method and apparatus which is more simple in its construction, quicker and more effective in its action, of greater durability and less expense in its operation than has been heretofore known.
- the objects are accomplished with our improved method and means by concentrating and combining two or more currents of air, steam, or water, or other suitable gases or fluids, which are discharged under suitable high pressure through pipes or tubes arranged in such a manner that minerals or other substances to be pulverized will be drawn into the current, and discharged therewith into a 3 5 focal or converging point, when the abrasion ofthe particles from the opposing currents will instantaneously reduce them to a powdered condition.
- the pulverizing apparatus shown in Fig. 1 consists of two short sections of pipes or tubes, A A, placed in alignment with each other, the inner ends of each tube terminating ata suitable distance from each other.
- a A a soft metal or an elastic ferrule
- the two ports B B are connected with pipes 7 5 O U, which conduct the current of water, steam, air, or other gases from a receiver to the concentratin g pulverizer.
- the central port or inlet, B is provided with an induction-pipe, D.
- the inner end of this pipe is made tapering and slightly convex, and projects just beyond the junction of the two passages leading from the inlet 13 B and into the expanded end of pipe A, thus forming a nozzle through which currents of air, steam, or water are forced.
- This nozzle is made adjustable by means of a screw which is cut on the pipe and screwed into the end of the fitting. When adjusted to the required posit-ion it is held by a suitable lock-nut, a. 0
- the apparatus is securely fastened to a suitable frame-work.
- An incasement, F incloses the ends of the tubes A A to prevent the pulverized material from waste.
- An opening at the bottom allows its discharge into suitable receivers.
- Suitable valveconnections between the pipes G O and steam or gas generator or air-compressor are employed for controlling the currents emanating 5 from said generator or compressor, the power of which is raised to one hundred and fifty pounds per square inch, more or less, as circumstances require.
- the hoppers E E are charged with mineral or other substance, after which steam, water, or gases are turned in and are forced into the branch fittings K K and around the nozzles H H into and through the tubes A A, by the action of the current in passing through the branch fittings, and around I 5 and through the annular nozzle H H a partial vacuum is formed in the tubes D D, whereby the mineral or other substance in the hopper E E is drawn into and through the tubes D D and joins with the rapid current of steam or gases, and thence through tubes A A into the open space between the outlet of the two pipes, where, by the action of the two opposing currents, the granular material is brought in contact, and with sufficient velocity to reduce the 2 5 material to a powder by the concussion or abras1on.
- the distance between the two pipes A A should vary according to the nature of the material. That having the greater specific grav- 0 ity will require the greatest distance, consequently the pipes A A should be made adjustable to meet that requirement.
- the case F can be made of any suitable material; but to prevent too great wear upon the 5 inner surface it'should be lined with some semielastic material, or some material in which the fine particles of mineral substances will adhere, thus presenting a mineral surface for the succeedin g atoms to abrade against, thereby secur- 0 in g the case from Wearin g away too rapidly.
- the material which meets at the converging or focal point will not all be reduced to a powder on its first concussion, but will fall out of the current onto suitable screens and be conducted back to the hopper and again returned to the focal point, where it will receive another blow. Thus the operation will be repeated until the substance is all reduced to the required fineness.
- Fig. 2 represents a horizontal sectional view of our apparatus provided with four conducting or discharging pipes, A. These pipes are all arranged within the same plane and discharge their contents into one common center. By this means the reduction is accelerated.
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Disintegrating Or Milling (AREA)
Description
(No Model.) 2 Sheets-Sheet 1.
P. A. LUGKENBAGH & J. WOLFENDEN.
Method ofand Apparatus for Pulverizing Mineral and otherfiubstanoes.
238,044- Patented Feb. 223881..
MPEYERS. FUDTO-LITHOGRAPHER. WASHINGTON. D O
(No Model.) I 2Shees-Sheet 2. F. A. LUOKE'NBACH & J. WOLFENDEN.
Method ofjand Apparatus for Pulverizing Mineraland other Substances. No. 238,044. PatentedFeb. 22, i881.
WITNESSES lwmwmozz N. PETERS. PHOTD-LITHOGRAFNER. WASHINGTON. D:C.
UNITED STATES t tties.
FREDERIO A. LUOKENBAGH AND JOHN WOLFENDEN, OF NEW YORK, N. Y., ASSIGNORS TO LYMAN F1 HOLMAN, F SAME PLACE.
METHOD OF AND APPARATUS FOR PULVERIZING MINERAL AND OTHER SUBSTANCES.
SPECIFICATION forming part of Letters Patent No. 238,044, dated February 22, 1881.
Application filed August 13, 1880. (No model.)
To all whom it may concern:
Be it known that we, FREDERIC A. LUCK- ENBACH and J OHN WOLFENDEN, both of the city, county, and State of New York, have invented a certain new and Improved Method of and Apparatus for Pulverizin g Mineral and other Substances; and we do hereby declare that the following is a clear, full, and exact description thereof, reference being had to the" to accompanying drawings.
Heretofore mineral and other substances have been pulverized to varying degrees of fineness by crushing, stamping, and grinding, and also by forcing the mineral or other sub- 1: 5 stances against a metallic disk by means of a powerful current of air. These devices have proven to be inefficient and too expensive, owing to the rapid wear and destruction of the working parts of the apparatus.
The objects of our invention are to provide a method and apparatus which is more simple in its construction, quicker and more effective in its action, of greater durability and less expense in its operation than has been heretofore known.
The objects are accomplished with our improved method and means by concentrating and combining two or more currents of air, steam, or water, or other suitable gases or fluids, which are discharged under suitable high pressure through pipes or tubes arranged in such a manner that minerals or other substances to be pulverized will be drawn into the current, and discharged therewith into a 3 5 focal or converging point, when the abrasion ofthe particles from the opposing currents will instantaneously reduce them to a powdered condition.
In obtaining the power of compressed gases,
we do not confine ourselves to any kind in particular, as under varied conditions and circumstances certain gases are found to be better adapted and more economical than others. Butfor general use itiiiis lfound that steam 5 under high pressure ispreferable for some purposes, and in some cases it should be superheated priorto its use. Compressed air and other gases can be used whereabsolute dryness is required, and also water can be applied when obtained from natural sources and at high elevation, as is now done in hydraulic mining, or from high pressure derived from mechanical means. In carrying out our invention suitable reservoirs for storing compressed gases are placed in proper position, having pipes attached thereto, and connected with the pulverizin g apparatus for conducting the gases therein.
The pulverizing apparatus shown in Fig. 1 consists of two short sections of pipes or tubes, A A, placed in alignment with each other, the inner ends of each tube terminating ata suitable distance from each other. Upon the end of each tube a soft metal or an elastic ferrule, A A, is placed, in order to prevent the end of the tube being worn away by the rebound of the substance being pulverized. The
other ends of the tubes A A are finished on the inside next to the end in a convex form, which constitutes the part of an annularnozzle. These ends of the tubes are screwed to the outlet end of a branch fitting, K. This fitting is provided with three induction ports or inlets terminating in one passage leading to the exit.
The two ports B B are connected with pipes 7 5 O U, which conduct the current of water, steam, air, or other gases from a receiver to the concentratin g pulverizer. The central port or inlet, B, is provided with an induction-pipe, D. The inner end of this pipe is made tapering and slightly convex, and projects just beyond the junction of the two passages leading from the inlet 13 B and into the expanded end of pipe A, thus forming a nozzle through which currents of air, steam, or water are forced. 8 This nozzle is made adjustable by means of a screw which is cut on the pipe and screwed into the end of the fitting. When adjusted to the required posit-ion it is held by a suitable lock-nut, a. 0
To the outer ends of the tubes D elbows are attached,'which support suitable hoppers E E for holding the material to be powdered.
The apparatus is securely fastened to a suitable frame-work.
An incasement, F, incloses the ends of the tubes A A to prevent the pulverized material from waste. An opening at the bottom allows its discharge into suitable receivers.
The apparatus thus described is operated in- 10g the following manner, to wit: Suitable valveconnections between the pipes G O and steam or gas generator or air-compressor are employed for controlling the currents emanating 5 from said generator or compressor, the power of which is raised to one hundred and fifty pounds per square inch, more or less, as circumstances require. The hoppers E E are charged with mineral or other substance, after which steam, water, or gases are turned in and are forced into the branch fittings K K and around the nozzles H H into and through the tubes A A, by the action of the current in passing through the branch fittings, and around I 5 and through the annular nozzle H H a partial vacuum is formed in the tubes D D, whereby the mineral or other substance in the hopper E E is drawn into and through the tubes D D and joins with the rapid current of steam or gases, and thence through tubes A A into the open space between the outlet of the two pipes, where, by the action of the two opposing currents, the granular material is brought in contact, and with sufficient velocity to reduce the 2 5 material to a powder by the concussion or abras1on.
The distance between the two pipes A A should vary according to the nature of the material. That having the greater specific grav- 0 ity will require the greatest distance, consequently the pipes A A should be made adjustable to meet that requirement.
The case F can be made of any suitable material; but to prevent too great wear upon the 5 inner surface it'should be lined with some semielastic material, or some material in which the fine particles of mineral substances will adhere, thus presenting a mineral surface for the succeedin g atoms to abrade against, thereby secur- 0 in g the case from Wearin g away too rapidly. We
do not limit ourselves to the form of the case. for the form may, from necessity, be required to change to meet the Varying conditions of the substance to be pulverized.
The material which meets at the converging or focal point will not all be reduced to a powder on its first concussion, but will fall out of the current onto suitable screens and be conducted back to the hopper and again returned to the focal point, where it will receive another blow. Thus the operation will be repeated until the substance is all reduced to the required fineness.
Fig. 2 represents a horizontal sectional view of our apparatus provided with four conducting or discharging pipes, A. These pipes are all arranged within the same plane and discharge their contents into one common center. By this means the reduction is accelerated.
What we claim, and desire to secure by Letters Patent, is-
1. The herein-described method of pulverizin g mineral or other substances, by introducin g them into two or more opposing currents, by which said substances are discharged into a convergent or focal point, where, by their extreme velocity, the substance becomes pulverized by the concussion.
2. In combination with the case F, two or more pipes, A, for conducting opposing currents of water, steam, or gases under pressure, fitting K, pipe D, and hoppers E, from which the substance to be pulverized is drawn into the current in pipes A and discharged at .the focal point.
FREDERIO A. LUOKENBAOH. JOHN WOLFENDEN. Witnesses:
JONATHAN MARsHALL, JAMES M. TULLY.
Publications (1)
Publication Number | Publication Date |
---|---|
US238044A true US238044A (en) | 1881-02-22 |
Family
ID=2307400
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US238044D Expired - Lifetime US238044A (en) | luckenbach |
Country Status (1)
Country | Link |
---|---|
US (1) | US238044A (en) |
Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2478461A (en) * | 1946-03-16 | 1949-08-09 | Nichols Eng & Res Corp | Apparatus and method for treating foundry sand |
US2538340A (en) * | 1945-11-14 | 1951-01-16 | Arthur O Tomek | Sand scrubbing device and method |
US2704635A (en) * | 1951-06-02 | 1955-03-22 | Conrad M Trost | Pulverizing mill having opposed jets and circulatory classification |
US2766496A (en) * | 1952-02-02 | 1956-10-16 | Robert W Ward Company | Method and apparatus for cleaning foundry sand |
US3186648A (en) * | 1963-05-27 | 1965-06-01 | Grace W R & Co | Fluid energy mill |
US3675858A (en) * | 1970-06-18 | 1972-07-11 | Hewlett Packard Co | Angular impact fluid energy mill |
US3876156A (en) * | 1971-12-29 | 1975-04-08 | Bayer Ag | Method of and apparatus for the jet-pulverisation of fine grained and powdered solids |
US4261521A (en) * | 1980-03-13 | 1981-04-14 | Ashbrook Clifford L | Method and apparatus for reducing molecular agglomerate sizes in fluids |
US4875629A (en) * | 1988-09-02 | 1989-10-24 | Air Powder Systems | Particle pulverizer injection nozzle |
US5385640A (en) * | 1993-07-09 | 1995-01-31 | Microcell, Inc. | Process for making microdenominated cellulose |
US5487419A (en) * | 1993-07-09 | 1996-01-30 | Microcell, Inc. | Redispersible microdenominated cellulose |
US5732893A (en) * | 1995-04-06 | 1998-03-31 | Nied; Roland | Device for fluidized-bed jet milling |
US20040016835A1 (en) * | 2002-07-23 | 2004-01-29 | Xerox Corporation | Particle entraining eductor-spike nozzle device for a fluidized bed jet mill |
US20080257411A1 (en) * | 2007-04-18 | 2008-10-23 | Kelsey Robert L | Systems and methods for preparation of emulsions |
US20090152212A1 (en) * | 2007-04-18 | 2009-06-18 | Kelsey Robert L | Systems and methods for treatment of groundwater |
US7651621B2 (en) | 2007-04-18 | 2010-01-26 | Vrtx Technologies, Llc | Methods for degassing one or more fluids |
US7651614B2 (en) | 2007-02-13 | 2010-01-26 | Vrtx Technologies, Llc | Methods for treatment of wastewater |
-
0
- US US238044D patent/US238044A/en not_active Expired - Lifetime
Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2538340A (en) * | 1945-11-14 | 1951-01-16 | Arthur O Tomek | Sand scrubbing device and method |
US2478461A (en) * | 1946-03-16 | 1949-08-09 | Nichols Eng & Res Corp | Apparatus and method for treating foundry sand |
US2704635A (en) * | 1951-06-02 | 1955-03-22 | Conrad M Trost | Pulverizing mill having opposed jets and circulatory classification |
US2766496A (en) * | 1952-02-02 | 1956-10-16 | Robert W Ward Company | Method and apparatus for cleaning foundry sand |
US3186648A (en) * | 1963-05-27 | 1965-06-01 | Grace W R & Co | Fluid energy mill |
US3675858A (en) * | 1970-06-18 | 1972-07-11 | Hewlett Packard Co | Angular impact fluid energy mill |
US3876156A (en) * | 1971-12-29 | 1975-04-08 | Bayer Ag | Method of and apparatus for the jet-pulverisation of fine grained and powdered solids |
US4261521A (en) * | 1980-03-13 | 1981-04-14 | Ashbrook Clifford L | Method and apparatus for reducing molecular agglomerate sizes in fluids |
US4875629A (en) * | 1988-09-02 | 1989-10-24 | Air Powder Systems | Particle pulverizer injection nozzle |
US5385640A (en) * | 1993-07-09 | 1995-01-31 | Microcell, Inc. | Process for making microdenominated cellulose |
US5487419A (en) * | 1993-07-09 | 1996-01-30 | Microcell, Inc. | Redispersible microdenominated cellulose |
US5732893A (en) * | 1995-04-06 | 1998-03-31 | Nied; Roland | Device for fluidized-bed jet milling |
US20040016835A1 (en) * | 2002-07-23 | 2004-01-29 | Xerox Corporation | Particle entraining eductor-spike nozzle device for a fluidized bed jet mill |
US6951312B2 (en) * | 2002-07-23 | 2005-10-04 | Xerox Corporation | Particle entraining eductor-spike nozzle device for a fluidized bed jet mill |
US7651614B2 (en) | 2007-02-13 | 2010-01-26 | Vrtx Technologies, Llc | Methods for treatment of wastewater |
US20080257411A1 (en) * | 2007-04-18 | 2008-10-23 | Kelsey Robert L | Systems and methods for preparation of emulsions |
US20090152212A1 (en) * | 2007-04-18 | 2009-06-18 | Kelsey Robert L | Systems and methods for treatment of groundwater |
US7651621B2 (en) | 2007-04-18 | 2010-01-26 | Vrtx Technologies, Llc | Methods for degassing one or more fluids |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US238044A (en) | luckenbach | |
US4390131A (en) | Method of and apparatus for comminuting material | |
US2515542A (en) | Method for disintegration of solids | |
US1935344A (en) | Impact pulverizer | |
US3741485A (en) | Fluid energy grinder for increasing bulk density of materials | |
US2515541A (en) | Apparatus for disintegration of solids | |
US3895760A (en) | Method and apparatus for shattering shock-severable solid substances | |
US2636688A (en) | Method for treating coal and the like | |
KR910004253A (en) | Impingement air pulverizer and pulverization method | |
US1279804A (en) | Concrete-mixer. | |
US1708123A (en) | Method and apparatus for grinding fibrous rubber scrap or the like | |
US2119887A (en) | Apparatus for disintegrating solids | |
US251803A (en) | starkey | |
US4875629A (en) | Particle pulverizer injection nozzle | |
US1096623A (en) | Ash-conveyer. | |
US1885645A (en) | Cement gun nozzle | |
US253344A (en) | chiohester | |
AU2008202342A1 (en) | Center-feed nozzle in a contained cylindrical feed-inlet tube for improved fluid-energy mill grinding efficiency | |
SU1477236A3 (en) | Disintegrating apparatus with pressure chamber | |
US1597656A (en) | Pulverizing device | |
US2765122A (en) | Jet mill | |
JP2012161722A (en) | Pulverizing apparatus | |
JP2006514883A (en) | Crusher | |
US291367A (en) | luckenbach | |
US5683039A (en) | Laval nozzle with central feed tube and particle comminution processes thereof |