Process and apparatus for separating anthracite or bituminous from refuse

Abstract

A process for separating Anthracite and low quality carbon from refuse. Crushed refuse is admixed with water from a water storage source. The admixture is transferred to a first cyclone separator to divide the admixture into a refuse rich slurry stream and a carbonaceous rich slurry stream. The refuse rich slurry stream is dewatered through a vibrating screen and the water collected sent to the raw feed sump source. The carbonaceous rich slurry is directed to a second cyclone separator to separate low quality carbon from high quality carbon, the high quality carbon is transferred to a third cyclone separator used to separate the media water therefrom. The separated media water is returned via a siphon leg to the raw feed sump, and the dewatered high quality Anthracite is available for markets requiring higher quality carbon.

Claims

1. A process for separating Anthracite from refuse comprising the steps of: crushing Anthracite coal refuse into an approximate size less than ??0; admixing the crushed Anthracite coal refuse with water in a raw feed sump into an admixture; transferring the admixture to a first cyclone separator having a substantially cylindrical chamber further defined by an upper section of a first diameter, a middle section having a second diameter greater than said first diameter reducing the speed of the admixture rotation, and a conical shaped lower section diminishing in diameter from said middle section, said first cyclone separator constructed and arranged to divide said admixture into a refuse rich slurry stream of about 80 Ash content to be discharged from a first apex positioned at the bottom of said lower section and a carbonaceous rich slurry stream drawn from an outlet positioned at said second diameter; directing said refuse rich slurry stream through a vibrating screen, said vibrating screen dewatering said refuse rich slurry stream and directing water collected from said dewatering step to said raw feed sump; transferring said carbonaceous rich slurry drawn from said outlet positioned at said second diameter of said middle section of said first cyclone separator to a second cyclone separator constructed and arranged to separate low quality carbon of about 45 Ash content from a high quality Anthracite slurry; collecting the low quality carbon from a lower section of said second cyclone separator; transferring the high quality Anthracite slurry drawn from an intake positioned at an upper section of said second cyclone separator to a third cyclone separator constructed and arranged to separate media from high quality Anthracite slurry of about 12 Ash content; returning water separated from the high quality Anthracite slurry drawn from an intake positioned where an upper section defined by a uniform diameter meets a lower section defined by a diminishing diameter of said third cyclone separator to said raw feed sump; and collecting the high quality Anthracite from a lower section of said third cyclone separator.

2. The process according to claim 1 including the step of monitoring said water to maintain a density between a range of 1.35 and 1.45 specific gravity.

3. The process according to claim 2 wherein fresh water is added to said raw water feed sump to maintain said specific gravity range.

4. The process according to claim 2 wherein water exceeding said specific gravity range is directed to a vacuum press for clarification and the clarified water directed to said raw feed sump.

5. The process according to claim 2 wherein water exceeding said specific gravity is directed to a centrifuge to be clarified and the clarified water returned to said raw feed sump.

6. The process according to claim 2 wherein water exceeding said specific gravity range is directed to a tailing pond.

7. The process according to claim 1 wherein feedstock slurry is introduced into said upper section of said first cyclone separator.

8. The process according to claim 1 wherein said second cyclone separator has a substantially cylindrical chamber having an upper section of a first diameter, a middle section having a second diameter equal to said first diameter, and a conical shaped lower section diminishing in diameter from said second section to expel low quality Anthracite.

9. The process according to claim 1 wherein said third cyclone separator has a substantially cylindrical chamber having an upper section of a first diameter and a conical shaped lower section diminishing in diameter to an outlet for discharge of high quality Anthracite.

10. The process according to claim 1 wherein said first cyclone separator middle section includes an axial extent greater than said first section for imparting tangentially-admitted feedstock slurry, a reduction in acceleration followed immediately by increasing acceleration in a depending lower section conical portion.

11. The process according to claim 7 wherein said feedstock slurry is supplied at a static pressure in a range of about 10 psi to about 20 psi at a volumetric flow rate in a range of about 2,000 gpm.

12. The process according to claim 1 wherein said process is use for concentrating rare earth elements.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 is a flow chart depicting the staging of the three cyclone separators;

(2) FIG. 2 is a frontal pictorial view of the three cyclone separators per the instant invention; and

(3) FIG. 3 is a side pictorial view thereof.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT

(4) Detailed embodiments of the instant invention are disclosed herein; however, it is to be understood that the disclosed embodiments are merely exemplary of the invention, which may be embodied in various forms. Therefore, specific functional and structural details disclosed herein are not to be interpreted as limiting, but merely as a basis for the claims and as a representation basis for teaching one skilled in the art to variously employ the present invention in virtually any appropriately detailed structure.

(5) A typical pile of tailings comprises coal and refuse. For instance, a typical pile may comprise up to 20% by weight of coal with the balance being refuse. As used herein, the term coal is intended to mean Anthracite or Bituminous coal, and the term refuse is intended to mean a variety of inorganic matter such as rocks, shale, slate, clay, and the like, which is mined along with the coal. Referring to the figures in general, in the processes, refuse 10 which may comprise less than 20% coal by weight, is crushed and screened to an approximate size range of less than ??0, The crushed refuse is admixed with water 14 drawn from a water source forming an admixture 16. The admixture 16 is transferred into a first cyclone separator 18 constructed and arranged to divide the admixture 16 into a refuse rich slurry stream 20 and a carbonaceous rich slurry stream 22. Preferably, as further described herein, the cylindrical shaped cyclone separators have a continuous sidewall shaped to adjust acceleration/centrifugal force of the slurry stream. A first cyclone separator 18 has a continuous sidewall 30 depending from a top wall 32 forming a chamber 34 therein. An upper section 36 formed by the sidewall 30 expanding from a first diameter, as measured by the size of the top wall 32 expanding outwardly to a middle section 38 forming a second diameter 40, as measured along the widest portion of the sidewall 30. The admixture 16 is admitted through an inlet 42 formed tangentially in the sidewall 30, wherein acceleration is slowed and then rapidly increased upon entering a third section 44, wherein the sidewall 30 is formed into a conical shape diminishing in diameter from the middle section 38 to a first apex 46 to expel a refuse rich slurry 50 containing inert rock. The refuse rich slurry 50 is passed over a vibrating screen 52 for dewatering. Water 54 collected from the dewatering step is directed to the raw feed sump 12 for reuse, and the inert rock 51 with about 80% ash content is discharged. Because of the cylindrical shape, a substantial deceleration and acceleration is imparted to the solids as they circulate in the chamber at any given radius.

(6) The carbonaceous rich slurry stream 22 is drawn from an outlet 60 through a transfer line 62 to a second cyclone separator 68. The second cyclone separator 68 has a continuous sidewall 70 depending from top wall 72 forming a chamber 74 therein. An upper section 76 is formed by the sidewall 70 depending from a first diameter, as measured by the size of the top wall 72, with a uniform diameter to a lower section 78. The admixture, being a carbonaceous rich slurry stream 22, is admitted through an inlet 80 formed tangentially in the sidewall 70, wherein acceleration maintained and then rapidly increased upon entering the lower section 78, wherein the sidewall 70 is formed into a conical shape, diminishing in diameter along the length of the lower section 78 to a second apex 82 for expelling a low quality carbon 84 with about 45% ash content. The high quality Anthracite slurry 90 is drawn from the vortex. The high quality carbon exits the second cyclone separator 68 through an intake 92 and transfer line 94. A cylindrical type of cyclone is to be contrasted with a tapered or variable acceleration type, wherein the shell has a depending frusto-conical or tapered portion of substantial length and a relatively small included cone angle. Because of the conical shape, the acceleration forces increase on the particles as they circulate and advance.

(7) The high quality Anthracite slurry stream 90 is drawn through the transfer line 94 to a third cyclone separator 100. The third cyclone separator 100 has a continuous sidewall 102 depending from a top wall 104 forming a chamber 106 therein. An upper section 108 is formed by the side all 102 depending along a first diameter, as measured by the size of the top wall 104 maintaining a uniform diameter to a lower section 110. The high quality Anthracite slurry 90 is admitted through an inlet 96 formed tangentially in the sidewall 102, wherein acceleration is maintained and then rapidly increased upon entering the lower section 110. The sidewall 102 is formed into a conical shape, diminishing in diameter along the length of the lower section 110 to a third apex 114 used for expelling dewatered high quality Anthracite 118 with about 12% ash content. The third cyclone 100 operates to separate the high quality Anthracite slurry 90 from the media water 120 drawn from an intake 112 of the cyclone separator 100 through a transfer line 122 for recycling to the raw feed sump 12 with about 90% return of the media water 120. According to this preferred embodiment of the present invention, the above-described process will operate efficiently in a continuous manner to separate carbon of different qualities from refuse provided certain process conditions are observed. For instance, for Anthracite coal it is important that the specific gravity of the water is measured through the water storage source. For Anthracite coal having a specific gravity of about 1.75, the density of the water should be maintained in a range of about 1.35 and 1.45 specific gravity.

(8) The specific gravity of the medium tends to increase after the process has been operating in the steady state for a period of time. In order to control the specific gravity of the medium within the desired range upstream of the first cyclone separator, the recirculating media is constantly monitored with a density gauge so that appropriate action can be taken to maintain the specific gravity within the desired range. For instance, if the specific gravity should increase beyond the desired limit, it can be reduced by bleeding media water out of the system and adding fresh water. If the specific gravity should drop below the desired lower level, it can be increased by increasing the particulate matter in the crushed Anthracite material make up.

(9) In a preferred embodiment, the feedstock slurry is supplied at a static pressure in a range of about 10 psi to about 20 psi at a volumetric flow rate in a range of about 2,000 gpm.

(10) The process disclosed herein is directed to separating Anthracite coal and a low quality carbon from refuse. Since Anthracite coal separation is known to be more difficult than Bituminous coal separation, the process should be effective on Bituminous coal. While some adjustments in operating conditions will have to be made to compensate for the different specific gravity of bituminous coal, such adjustments should be apparent to those skilled in the art in light of the present disclosure.

(11) The term coupled is defined as connected, although not necessarily directly, and not necessarily mechanically. The use of the word a or an when used in conjunction with the term comprising in the claims and/or the specification may mean one, but it is also consistent with the meaning of one or more or at least one. The term about means, in general, the stated value plus or minus 5%. The use of the term or in the claims is used to mean and/or unless explicitly indicated to refer to alternatives only or the alternative are mutually exclusive, although the disclosure supports a definition that refers to only alternatives and and/or.

(12) The terms comprise (and any form of comprise, such as comprises and comprising), have (and any form of have, such as has and having), include (and any form of include, such as includes and including) and contain (and any form of contain, such as contains and containing) are open-ended linking verbs. As a result, a method or device that comprises, has, includes or contains one or more steps or elements, possesses those one or more steps or elements, but is not limited to possessing only those one or more elements. Likewise, a step of a method or an element of a device that comprises, has, includes or contains one or more features, possesses those one or more features, but is not limited to possessing only those one or more features. Furthermore, a device or structure that is configured in a certain way is configured in at least that way, but may also be configured in ways that are not listed.

(13) All patents and publications mentioned in this specification are indicative of the levels of those skilled in the art to which the invention pertains. It is to be understood that while a certain form of the invention is illustrated, it is not to be limited to the specific form or arrangement herein described and shown. It will be apparent to those skilled in the art that various changes may be made without departing from the scope of the invention and the invention is not to be considered limited to what is shown and described in the specification and figures included herein.

(14) One skilled in the art will readily appreciate that the present invention is well adapted to carry out the objectives and obtain the ends and advantages mentioned, as well as those inherent therein. The embodiments, methods, procedures and techniques described herein are presently representative of the preferred embodiments, are intended to be exemplary, and are not intended as limitations on the scope. Changes therein and other uses will occur to those skilled in the art which are encompassed within the spirit of the invention and are defined by the scope of the appended claims. Although the invention has been described in connection with specific preferred embodiments, it should be understood that the invention as claimed should not be unduly limited to such specific embodiments. Indeed, various modifications of the described modes for carrying out the invention which are obvious to those skilled in the art are intended to be within the scope of the following claims.