Material reducing apparatus and method of operating the same

• US 4,061,274 A
• Filed: 07/26/1976
• Issued: 12/06/1977
• Est. Priority Date: 07/26/1976
• Status: Expired due to Term

• Current Assignee: Williams Patent Crusher and Pulverizer Company
• Original Assignee: Williams Patent Crusher and Pulverizer Company
• Inventors: Williams, Robert M.
• Primary Examiner(s): Custer, Jr., Granville Y.
• Application Number:
  US05/708,889
• Time in Patent Office: 498 Days
• Field of Search: 241/23, 241/24, 241/48, 241/52, 241/53, 241/57, 241/59, 241/65, 241/79.1, 241/80
• US Class Current: 241/19
• CPC Class Codes: B02C 21/00 Disintegrating plant with or without drying of the material for grain B02C9/04
• CPC Class Codes: B02C 23/30 the applied gas acting to effect material separation B02C23/34 takes precedence
• CPC Class Codes: B02C 23/32 with return of oversize material to crushing or disintegrating zone B02C23/34 takes precedence

Abstract

Method of and apparatus for reducing material by grinding and for handling the ground product in a system that minimizes the production of a product containing a high percentage of extreme fines so that the product is more uniform in size and the apparatus is more efficient in producing that product.

Claims

1. A method of reducing the size of a moisture carrying friable material while reducing regrinding of the finer fractions comprising the steps of:

connecting up in a first air circulating system and in series order a material grinding mill, a fluid bed separator chamber, a first cyclone separator and a blower;

introducing the friable material to the first system at the grinding mill, passing the output of said grinding mill through the fluid bed separator chamber to separate the finer fraction from the coarser and heavier fraction which returns to the grinding mill for further reduction, and discharging ground material from the first system at the cyclone separator while returning the air from the blower to the grinding mill;

connecting up in a second air circulating system and in series order a material classifier, a second cyclone separator and a second blower;

introducing to the second system at the material classifier the material discharged at the first cyclone separator from the first system;

classifying the material introduced from the first system in the second system into acceptable and oversize fractions; and

discharging the acceptable fraction at the second system cyclone separator while returning the oversize fraction to the first system at the grinding mill.

2. The method in accordance with claim 1 and comprising introducing an oxygen deficient hot gas into the first system between said blower and said grinding mill to supply the hot gas into the grinding mill to lower the moisture content of the material reduced therein, and supplying a portion of the oxygen deficient gas from the first system into the second system between said second blower and said material classifier.

3. The method in accordance with claim 1 and comprising operating the grinding mill to produce initially regrindable oversize material larger than approximately a size to pass a 200 mesh screen, and utilizing the fluid bed separator chamber to separate by specific gravity said regrindable material from the portion of smaller material responsive to the circulating air.

4. Apparatus for reducing the size of a moisture carrying friable material while reducing the sticking of fines on the material subject to regrinding comprising, a material reducing mill having an inlet for the moisture carrying friable material to be reduced in size and an outlet for reduced material;

a fluid bed material separator connected to said mill outlet in position to receive the material reduced in said mill and separate it according to weight, said heavier fractions returning to said mill through said outlet;

cyclonic separator means connected in material flow relationship to receive material from said fluid bed separator and deliver it to an outlet;

blower means having a suction inlet connection with said cyclonic separator means and an outlet connected into said mill, said blower circulating air through said mill, fluid bed separator and cyclonic separator means to transport the reduced material from said mill and fluid bed separator to said cyclonic separator means and to return air substantially free of material to said mill;

a source of oxygen deficient hot gases connected into blower means outlet, whereby the moisture carrying material is, at least, partially dried to avoid the finer fractions sticking to the heavier fractions and returning to said mill for subjection to regrinding, material classifier means connected to receive material from said cyclonic separator means outlet, a second cyclonic separator means and a second blower means connected in series relation with said classifier means, said second blower means creating a flow of air to carry reduced material from said classifier means to said second cyclonic separator means, said second cyclonic separator means having an outlet for reduced material of substantially desired size, and a material transfer connection between said material classifier means for said mill for the return of coarse material to said mill for regrinding.

5. The apparatus set forth in claim 4 wherein there is a flow connection from the outlet of the first mentioned blower means to the outlet of said second blower means for the transfer of heated air into said classifier means.

6. The apparatus set forth in claim 4 wherein there is a hot gas connection from said blower means outlet into said material classifying means, whereby the returned oversize material is further subject to moisture reduction in advance of return to said reducing mill inlet.