US1822221A - Process and apparatus for pulverizing material - Google Patents

Process and apparatus for pulverizing material Download PDF

Info

Publication number
US1822221A
US1822221A US226543A US22654327A US1822221A US 1822221 A US1822221 A US 1822221A US 226543 A US226543 A US 226543A US 22654327 A US22654327 A US 22654327A US 1822221 A US1822221 A US 1822221A
Authority
US
United States
Prior art keywords
grinder
separator
gaseous fluid
grinding
pulverizing
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
US226543A
Inventor
Michael D Jones
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.)
Fuller Lehigh Co
Original Assignee
Fuller Lehigh 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
Application filed by Fuller Lehigh Co filed Critical Fuller Lehigh Co
Priority to US226543A priority Critical patent/US1822221A/en
Application granted granted Critical
Publication of US1822221A publication Critical patent/US1822221A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C21/00Disintegrating plant with or without drying of the material

Definitions

  • This invention relates to a process and apparatus for pulverizing material in such a manner that the material is obtained in a dry pulverulent state and the grinder is prevented from clogging or becoming stopped up.
  • the invention is 1 applicablev to the grinding of various sorts of ma erial. but is especially suitable for rinding coalthat may be in the moist or damp state-so as to produce powdered fuel.
  • reference character 1 indicates a storage bin or receptacle for coal or other material that is to bev ground;
  • a conduit 2 leads from the bin 1 to the grinder 3 that may be one of the well known types.
  • A'heater 4 may be interposed between the bin and the grinder to cause a preliminary heaing of'the material that is to be round, and the grinder may also be heated yv means of the heater 5, which may be heated from any convenient source of lieat6, that isdiagrammatically illustrated.
  • Air is forced into the grinder and servesto lift the fine particles in the well known manner, and the dust-laden air passes
  • the invention will be understood from the through the outlet 7 to a separator 8 that may,
  • the separator 8 is providedwith means for heating the same, which may be, for example, a heating coil 9 or the separator may be heated in any other convenient manner.
  • the lower portion 10 of the separator is shown as being funnel-shaped and'an outlet 11 therefrom may lead to a furnace or storage receptacle.
  • An outlet 12 extends from the upper por tion of the separator 8 to the grinder 3, and is provided with a vent 13 to permit aportion of the gaseous fluid to escape so that the concentration of moisture in the gaseous fluid will not become too great.
  • a fan 14 is provided for forcing the circulation of theair or gaseous fluid throughthe grinder and separator back to the grinder, and fresh air or other gaseous fluid may be admitted at any convenient point in the cyclone separator to replace that which is vented out through the same time the air is permitted to remain suf-i ficiently concentrated with moisture to preplace.
  • the heater 4 between the storage bin and the grinder, as well as the heater 5 for the grinder itself, may both be dispensed with when there is not too much moisture in the materialto be ground, since the heat generated by the grinding operation together with the heat applied in the separator 8 will be sufficient to produce thoroughly dried material that is collected in the separator,
  • the process of pulverizing materials which comprises grinding the material while passing a gaseous fluid through the grinding zone to remove fine. particles and thence through a separating zone where the fine particles and gaseous fluid are separated, said separating zone being maintained at .an elely of the material passing therethrough.
  • the process of pulverizing material which comprises grinding the material while .vatecl temperature by heating it independentpassing a gaseous fluid through the grinding zone to remove fine particles, thence through a separating zone where the fine particles and gaseous fluid are separated, said separating zone being maintained at an elevated temperature by heating it independently of the material passing therethrough, and returning terial passing therethrough, returning gaseous fluid from the separator to the grinding zone, and venting a portion of it to the atmosphere.
  • a grinder means for passinga gaseous fluid through said grinder to remove the fine particles, a separator through which the dust laden fluid passes, and means for heating the isiepllrator independently of said gaseous u1 7.
  • a grinder means for passing a gaseous fluid through said grinder to remove the fine particles, a separator through which the dust laden fluid passes, means for heating the separator independently of said gaseous fluid, and means for returning a portion of the gaseous fluid from said separator to said grinder.
  • a grinder means for passing a gaseous fluid through said grinder to remove the fine particles, a separator through which the dust laden fluid passes, means for heating the separator independently of said gaseous fluid and means for returning a portion of the gaseous fluid from said separator to said grinder, and for venting another portion thereof to the atmosphere.

Landscapes

  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Cyclones (AREA)

Description

Sept. 8, 1931. M. D.- JoNEs PROCESS MD APPARATUS FOR PULVERIZING MATERIAL I W Filed 001;. 17, 1927 M INVENTOR;
J 4 Qqrrogezxusnm.
Patented Sept 8,1931
UNITED STATES- PATENT OFFICE MICHAEL D. JONES, OFIALLENTOWN, IENNSYLVANIA, assmnon TO FULLER Lenten coMrANY, or FULLERTON, rENnsYLvANIA, A CORPORATION or DELAWABE' PROCESS AND APPARATUS FOR PULVERIZING MATERIAL Application filed October 17, 1927. Serial No. 226,543.
This invention relates to a process and apparatus for pulverizing material insuch a manner that the material is obtained in a dry pulverulent state and the grinder is prevented from clogging or becoming stopped up. The invention is 1 applicablev to the grinding of various sorts of ma erial. but is especially suitable for rinding coalthat may be in the moist or damp state-so as to produce powdered fuel.
Ithas been found heretofore that in pulverizing or grinding materials that contain excessive amounis of moisture, that the moisture interferes with the proper pulverization of the material or retards the pulverization because the dampmaterial coats the surfaces of the grinding elements and does not permit proper functioning of the various parts. fT he amount of heat generated by the process of pulverization is not suflicient to furnish enough heat for drying the material especially if a considerable amount of moisture is present.
By the present invention, difiiculties here-' tofore encountered in grinding or pulverizmg processes and apparatus are overcome and the pulverization is suitably accom-- plished by using grinders or pulverizers of,
vent explosions from accidentally taking different t es.
description in connection with the accompanying drawing, in which a diagrammatic arrangement of apparatus is indicated for carrying out the invention. In the drawing reference character 1 indicates a storage bin or receptacle for coal or other material that is to bev ground; A conduit 2 leads from the bin 1 to the grinder 3 that may be one of the well known types. A'heater 4 may be interposed between the bin and the grinder to cause a preliminary heaing of'the material that is to be round, and the grinder may also be heated yv means of the heater 5, which may be heated from any convenient source of lieat6, that isdiagrammatically illustrated. I
Air is forced into the grinder and servesto lift the fine particles in the well known manner, and the dust-laden air passes The invention will be understood from the through the outlet 7 to a separator 8 that may,
be of the cyclone type or of the well known sort that is suitable for separating gaseous and solid particles from each other. The separator 8 is providedwith means for heating the same, which may be, for example, a heating coil 9 or the separator may be heated in any other convenient manner. The lower portion 10 of the separator is shown as being funnel-shaped and'an outlet 11 therefrom may lead to a furnace or storage receptacle. An outlet 12 extends from the upper por tion of the separator 8 to the grinder 3, and is provided with a vent 13 to permit aportion of the gaseous fluid to escape so that the concentration of moisture in the gaseous fluid will not become too great. A fan 14 is provided for forcing the circulation of theair or gaseous fluid throughthe grinder and separator back to the grinder, and fresh air or other gaseous fluid may be admitted at any convenient point in the cyclone separator to replace that which is vented out through the same time the air is permitted to remain suf-i ficiently concentrated with moisture to preplace. The heater 4 between the storage bin and the grinder, as well as the heater 5 for the grinder itself, may both be dispensed with when there is not too much moisture in the materialto be ground, since the heat generated by the grinding operation together with the heat applied in the separator 8 will be sufficient to produce thoroughly dried material that is collected in the separator,
I claim: o
1. The process of pulverizing materials which comprises grinding the material while passing a gaseous fluid through the grinding zone to remove fine. particles and thence through a separating zone where the fine particles and gaseous fluid are separated, said separating zone being maintained at .an elely of the material passing therethrough.
:2. The process of pulverizing material which comprises grinding the material while .vatecl temperature by heating it independentpassing a gaseous fluid through the grinding zone to remove fine particles, thence through a separating zone where the fine particles and gaseous fluid are separated, said separating zone being maintained at an elevated temperature by heating it independently of the material passing therethrough, and returning terial passing therethrough, returning gaseous fluid from the separator to the grinding zone, and venting a portion of it to the atmosphere.
4. The process of pulverizing material which comprises forcing air through the grinding zone and thence through a separating zone Where the air is separated from. the solid particles, said separating zone being maintained at an elevated temperature by heating it independently of the material passing therethrough.
5. The process of. pulverizing material which comprises forcing air through the grinding zone, thence through a separating zone wherethe air is separated from the solid particles, said separating zone being maintained at an elevated temperature by heating it independently of the material passing therethrough, and returning a portion of the air to the grinding zone.
6. In an apparatus for pulverizing material, a grinder, means for passinga gaseous fluid through said grinder to remove the fine particles, a separator through which the dust laden fluid passes, and means for heating the isiepllrator independently of said gaseous u1 7. In an apparatus for pulverizing material, a grinder, means for passing a gaseous fluid through said grinder to remove the fine particles, a separator through which the dust laden fluid passes, means for heating the separator independently of said gaseous fluid, and means for returning a portion of the gaseous fluid from said separator to said grinder.
8. In an apparatus for pulverizing material, a grinder, means for passing a gaseous fluid through said grinder to remove the fine particles, a separator through which the dust laden fluid passes, means for heating the separator independently of said gaseous fluid and means for returning a portion of the gaseous fluid from said separator to said grinder, and for venting another portion thereof to the atmosphere.
9. In an apparatus for pulverizing mate rial, a grinder, means for passing a gaseous MICHAEL D. JONES.
US226543A 1927-10-17 1927-10-17 Process and apparatus for pulverizing material Expired - Lifetime US1822221A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US226543A US1822221A (en) 1927-10-17 1927-10-17 Process and apparatus for pulverizing material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US226543A US1822221A (en) 1927-10-17 1927-10-17 Process and apparatus for pulverizing material

Publications (1)

Publication Number Publication Date
US1822221A true US1822221A (en) 1931-09-08

Family

ID=22849340

Family Applications (1)

Application Number Title Priority Date Filing Date
US226543A Expired - Lifetime US1822221A (en) 1927-10-17 1927-10-17 Process and apparatus for pulverizing material

Country Status (1)

Country Link
US (1) US1822221A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2437294A (en) * 1942-09-08 1948-03-09 Dalin David Dust separator
US2622341A (en) * 1948-09-25 1952-12-23 James F Finnegan Pneumatic grain conveyer and drier
DE861495C (en) * 1943-02-11 1953-01-05 Basf Ag Centrifugal dust collector
US3013734A (en) * 1957-04-11 1961-12-19 Hischmann Maschinenfabrik Fa G Method of and apparatus for the drying of goods to be ground in a grinding and sifting apparatus
US3160490A (en) * 1959-08-14 1964-12-08 Commissariat Energie Atomique Apparatus for the continuous purification of uranium hexafluoride
FR2439028A1 (en) * 1978-10-21 1980-05-16 Kloeckner Humboldt Deutz Ag METHOD AND DEVICE FOR MAKING A MIXTURE OF FLAMMABLE FUEL / OXYGEN INERT, INSIDE A PLANT, PARTICULARLY IN A GRINDING PLANT
US4913711A (en) * 1982-07-16 1990-04-03 Foster Wheeler Energy Corporation Spiral coil cool wall construction for high temperature cylindrical furnaces, vessels, cyclones, etc.
US20050109209A1 (en) * 2003-11-26 2005-05-26 Lee David B. Air purification system and method

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2437294A (en) * 1942-09-08 1948-03-09 Dalin David Dust separator
DE861495C (en) * 1943-02-11 1953-01-05 Basf Ag Centrifugal dust collector
US2622341A (en) * 1948-09-25 1952-12-23 James F Finnegan Pneumatic grain conveyer and drier
US3013734A (en) * 1957-04-11 1961-12-19 Hischmann Maschinenfabrik Fa G Method of and apparatus for the drying of goods to be ground in a grinding and sifting apparatus
US3160490A (en) * 1959-08-14 1964-12-08 Commissariat Energie Atomique Apparatus for the continuous purification of uranium hexafluoride
FR2439028A1 (en) * 1978-10-21 1980-05-16 Kloeckner Humboldt Deutz Ag METHOD AND DEVICE FOR MAKING A MIXTURE OF FLAMMABLE FUEL / OXYGEN INERT, INSIDE A PLANT, PARTICULARLY IN A GRINDING PLANT
US4270466A (en) * 1978-10-21 1981-06-02 Klockner-Humboltd-Deutz AG Method and apparatus for rendering an ignitable fuel-oxygen mixture inert
US4913711A (en) * 1982-07-16 1990-04-03 Foster Wheeler Energy Corporation Spiral coil cool wall construction for high temperature cylindrical furnaces, vessels, cyclones, etc.
US20050109209A1 (en) * 2003-11-26 2005-05-26 Lee David B. Air purification system and method
US7077892B2 (en) * 2003-11-26 2006-07-18 Lee David B Air purification system and method

Similar Documents

Publication Publication Date Title
US1822221A (en) Process and apparatus for pulverizing material
US4061274A (en) Material reducing apparatus and method of operating the same
US3078048A (en) Means and methods of supplying heat to grinding mills
US2106869A (en) Drier for granular and like materials
US1538192A (en) Apparatus for conditioning crushed material
US2956347A (en) Drying method and apparatus
CA1183113A (en) Apparatus for reducing friable materials into course and fine fractions
US2174630A (en) Classification system for pulverized materials
US2180804A (en) Process of electrostatic separation
US2235683A (en) Drying process
USRE17212E (en) Mokinley stockton
US3524544A (en) Milling plant for sifting damp material
US2080059A (en) Drying system and method
US2090187A (en) Manufacture of starch
US1892233A (en) Method of and apparatus for drying casein
US1611791A (en) Process of and apparatus for treating minerals
GB764127A (en) Apparatus for the comminution of coal
US1394294A (en) Grinding in ball-mills
US2446140A (en) Apparatus for pneumatically separating relatively moist comminuted material
US2213059A (en) Process for treating carbon black
US2939411A (en) Drying apparatus and process
CN104525341A (en) Flash dryer
GB184870A (en) Improvements in purifiers or separators for granular materials in the process of milling
US2592348A (en) Process of producing animal feeds
US2296159A (en) Drying apparatus