System for the transport of an ore pulp in a line system located along a gradient, and components of such a system

Information

  • Patent Grant
  • 8461702
  • Patent Number
    8,461,702
  • Date Filed
    Thursday, January 8, 2009
    16 years ago
  • Date Issued
    Tuesday, June 11, 2013
    11 years ago
Abstract
A system for transporting an ore pulp (S) in a line system (2) located along a gradient, wherein the ore pulp (S) flows in the line system by the effect of gravity, has at least one generator station (8) located in the line system (2), the station comprising a flow machine (11) driven by the ore pulp (S) and a generator (14) coupled to the flow machine (11) for producing electrical energy as components of the transport system.
Description
CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a U.S. National Stage Application of International Application No. PCT/EP2009/050183 filed Jan. 8, 2009, which designates the United States of America, and claims priority to DE Application No. 10 2008 005 689.8 filed Jan. 23, 2008 and DE Application No. 10 2008 009 669.5 filed Feb. 18, 2008. The contents of which are hereby incorporated by reference in their entirety.


TECHNICAL FIELD

The invention relates to a system for the transport of an ore pulp in a line system located along a gradient. In addition, the invention relates to components of such a system.


BACKGROUND

In many mining countries such as Chile and Peru, the systems for extracting ore lie at high altitudes of 2000 m to 5000 m. In these systems, the ore, after initial processing, is transported further as aqueous sludge in line systems to plants in which the suspended ore, also called ore pulp, is subsequently processed. During this initial processing, the ore is concentrated as a rule. Thus, for example, copper ore in natural deposits has a metal content of 0.5% to 3%. For the transport to the plants for the subsequent processing, for example smelting plants, the copper ore is concentrated to values of 30% to 50% during the initial processing in concentrator plants which are located in the vicinity of the mine. The plants for the subsequent processing are as a rule not located in the vicinity of the mine but rather at sea level at home or abroad, and therefore the concentrate in this case has to be shipped and exported. What are known as “slurry pipelines” are being increasingly used in order to transport the concentrate to the smelting plants or to the harbor, in which slurry pipelines the concentrate, the ore pulp (slurry), which is enriched with water for the transport, flows from the mine located at a high altitude to the coast. More than six slurry pipelines of this kind are in operation in Chile, the length of which is on average 170 km and which overcome an average difference in altitude of 3000 m with an average transport capacity of 2.5 million tons per year.


SUMMARY

According to various embodiments, a system for the transport of an ore pulp in a line system located along a gradient can be specified, wherein the system works with high economic efficiency. In addition, components can be specified suitable for the operation of such a system.


According to an embodiment, a system for the transport of an ore pulp in a line system which is located along a gradient and in which the ore pulp flows under the effect of the gravitational force, may comprise at least one generator station arranged in the line system, said generator station having a continuous-flow machine driven by the ore pulp and a generator coupled to the continuous-flow machine for generating electrical energy.


According to a further embodiment, the continuous-flow machine may comprise a rotating shaft which is driven by the flowing ore pulp and is connected to the generator in a gearless manner. According to a further embodiment, the system may comprise a plurality of generator stations arranged at a distance from one another at different altitudes.


According to another embodiment, a continuous-flow machine for a system as described above may have a housing mounted such as to be rotatable about an axis and having an inlet for the ore pulp, said inlet being connected to an outlet of a pipeline, carrying the ore pulp, of the line system and opening into at least one curved pipe part, from which the ore pulp flows out at a distance from the axis and has, when flowing out, a flow direction which, in a plane oriented perpendicularly to the axis, has a velocity component oriented perpendicularly to this axis in such a way that a torque is exerted on the housing about this axis.


According to a further embodiment of the continuous-flow machine, the inlet can be formed by a pipe into which the outlet of the pipeline is inserted. According to a further embodiment of the continuous-flow machine, the pipe may form the rotating shaft.


According to yet another embodiment, a generator system may comprise a continuous-flow machine as described above and a generator driven by said continuous-flow machine, wherein the rotating shaft of the continuous-flow machine is at the same time the rotor of the generator.





BRIEF DESCRIPTION OF THE DRAWINGS

For further explanation, reference is made to the exemplary embodiment reproduced in the drawings, in which:



FIG. 1 shows a system according to various embodiments in a schematic diagrammatic illustration,



FIG. 2 shows a generator station, likewise in a schematic diagrammatic illustration,



FIGS. 3 and 4 show a continuous-flow machine used in a generator station, in a side view and a plan view, respectively.





DETAILED DESCRIPTION

According to various embodiments, the system for the transport of an ore pulp in a line system which is located along a gradient and in which the ore pulp flows under the effect of the gravitational force is provided with at least one generator station arranged in the line system, said generator station has a continuous-flow machine driven by the ore pulp and a generator coupled to said continuous-flow machine for generating electrical energy.


According to various embodiments, the high potential energy of the ore pulp can in principle also be used for generating electrical energy, since it is possible to also drive a continuous-flow machine with a viscous aqueous sludge. This high potential energy has hitherto been wasted in pressure reduction devices arranged in the line system.


If the continuous-flow machine comprises a shaft which is driven by the flowing ore pulp and is connected to a generator in a gearless manner, it is possible to generate electrical energy with especially high efficiency.


If the line system overcomes a very large difference in altitude over a considerable length, the potential energy of the ore pulp can be utilized especially effectively if a plurality of generator stations located at a distance from one another at different altitudes are arranged in the line system.


According to various embodiments, a continuous-flow machine suitable for driving the generator of the system can be specified as a component of the system.


Accordingly, the continuous-flow machine has a housing mounted such as to be rotatable about an axis and having an inlet for the ore pulp, said inlet being connected to an outlet of a pipeline, carrying the ore pulp, of the line system and opening into at least one curved pipe part, from which the ore pulp flows out at a distance from the axis.


In this case, the ore pulp has, when flowing out, a flow direction which, in a plane oriented perpendicular to the axis, has a velocity component oriented perpendicular to this axis in such a way that a torque is exerted on the housing about this axis. Such a continuous-flow machine acts like a centrifugal radial machine and converts the kinetic energy of the flowing ore pulp into a rotary motion in an especially effective manner.


If the inlet is formed by a pipe into which the outlet-side end of the pipeline is inserted, and the pipe at the same time in particular forms the rotating shaft, an especially compact construction of the continuous-flow machine is made possible.


An especially economical type of construction is achieved if a generator system is used in which the continuous-flow machine together with the generator driven by it form a structural unit by the rotating shaft of the continuous-flow machine being at the same time the rotor of the generator.


According to FIG. 1, a system for the transport of an ore pulp S comprises a line system 2 which is located along a gradient and in which the ore pulp S is transported from a concentrator plant 4 arranged in the region of a mine to a subsequent processing plant 6 situated at a lower level. Arranged in the line system 2 at different altitudes h are a plurality of generator stations 8 having a continuous-flow machine which is driven by the ore pulp and with which the potential energy of the ore pulp S flowing in the line system 2 is converted into electrical energy. The typical head Δh upstream of such a generator station 8 is about 500 to 1000 m.


The basic construction of such a generator station 8 is shown in FIG. 2. The ore pulp S flowing in a pipeline 10 of the line system 2 flows through a continuous-flow machine 11 and sets a shaft 12 of the continuous-flow machine 11 in rotary motion, as indicated by the arrow 13. The shaft 12 drives a generator 14, with which the kinetic energy of the ore pulp is converted into electrical energy. The ore pulp S flowing out of the continuous-flow machine 12 flows into a collecting basin 16, from which it flows further on to the next generator station 8 or to the subsequent processing plant 6.



FIG. 3 shows the basic construction of a continuous-flow machine 12 which is especially suitable for the generation of electricity using a flowing ore pulp S. The continuous-flow machine 12 has a housing 18 which is mounted such as to be rotatable about an axis 20. The housing 18 is provided with an inlet 22 for the ore pulp S, and this inlet 22 is connected to an outlet 24 of the pipeline 10 carrying the ore pulp. The inlet 22 opens into two curved pipe parts 26, from which the ore pulp S flows out, at a distance from the axis 20, into the collecting basin 16 (FIG. 2). The outflow is effected from end openings 28 of the pipe parts 26 in a direction which, in a plane 30 oriented perpendicularly to the axis 20 and perpendicularly to the drawing plane, has a velocity component oriented perpendicularly to this axis 20 in such a way that a torque is exerted on the housing 18 about this axis 20. The openings 28 are arranged with their cross-sectional areas in a common plane, such that the ore pulp S flowing out of them exerts no resultant overall force on the housing 18. Instead of the two curved pipe parts 26 shown in the figure, a larger number of curved pipe parts 26 can also be provided.


The inlet 22 is formed by a pipe 32 into which the outlet-side end of the pipeline 10 is inserted. This pipe 32 at the same time forms the rotating shaft 12 of the continuous-flow machine 11. The pipe 32 (the shaft 12) is provided with a winding 36 on its outer circumference and is at the same time the rotor of the generator 14 (only illustrated schematically), and so the continuous-flow machine 11 and the generator 14 driven by it form a structural unit.


The flow conditions within the continuous-flow machine are illustrated in the plan view according to FIG. 4. The ore pulp S flowing into the housing 18 of the continuous-flow machine vertically to the drawing plane is deflected there by 90° and undergoes a change in the direction of movement in the curved pipe parts 26, the result of which change is that the ore pulp, when flowing out of the openings 28, has a flow direction 38 with a flow component 40 which is oriented perpendicularly to the axis 20 and lies in a plane (the drawing plane) lying perpendicularly to this axis 20, such that a torque is exerted on the housing 18 about this axis 20. The reaction forces produced during the outflow at the two outflow openings 28 are opposite and equal, and therefore the total force transmitted to the housing 18 disappears.

Claims
  • 1. A system for the transport of an ore pulp in a line system which is located along a gradient and in which the ore pulp flows under the effect of the gravitational force, the system comprising: a plurality of generator stations arranged at a distance from one another at different altitudes along the gradient of the line system;the plurality of generator stations each including a continuous-flow machine driven by the ore pulp and a generator coupled to the associated continuous-flow machine for generating electrical energy;wherein each continuous-flow machine includes a housing rotatably mounted about an axis and having an inlet for the ore pulp;the inlet being connected to an outlet of a pipeline carrying the ore pulp and opening into at least two curved pipe parts;the outlet of the pipeline providing that the ore pulp flows out at a distance from the axis and has, when flowing out, a flow direction which, in a plane oriented perpendicularly to the axis, has a velocity component oriented perpendicularly to this axis in such a way that a torque is exerted on the housing about this axis; andwherein the continuous-flow machine comprises a rotating shaft which is driven by the flowing ore pulp and is connected to the generator in a gearless manner.
  • 2. The system according to claim 1, wherein there are two curved pipe parts, and the ore pulp flows out of the two curved pipe parts via two openings, wherein the two curved pipe parts are arranged in such a way that the reaction forces produced during the outflow of the ore pulp at the openings are opposite and equal.
  • 3. The system according to claim 1, wherein a head of the ore pulp upstream of a generator station is within the range of 500 to 1000 m.
  • 4. The system according to claim 1, wherein the inlet of the continuous-flow machine is formed by a pipe into which the outlet of the pipeline is inserted.
  • 5. The system according to claim 4, wherein the pipe forms the rotating shaft.
  • 6. The system according to claim 1, wherein the ore pulp discharging from the continuous-flow machine flows into a collecting basin, from which it flows further on to a subsequent processing plant or to the next generator station.
  • 7. A method for transporting of an ore pulp in a line system which is located along a gradient and in which the ore pulp flows under the effect of the gravitational force, the method comprising: arranging a plurality of generator stations at different altitudes along the gradient of the line system;the plurality of generator stations each including a continuous-flow machine driven by the ore pulp and a generator coupled to the continuous-flow machine for generating electrical energy;wherein each continuous-flow machine has a housing mounted such as to be rotatable about an axis and having an inlet for the ore pulp;connecting the inlet to an outlet of a pipeline carrying the ore pulp;wherein the inlet opens into at least two curved pipe parts, from which the ore pulp flows out at a distance from the axis and has, when flowing out, a flow direction which, in a plane oriented perpendicularly to the axis, has a velocity component oriented perpendicularly to this axis in such a way that a torque is exerted on the housing about this axis; anddriving a rotating shaft of the continuous-flow machine by the flowing ore pulp wherein the rotating shaft is connected to the generator in a gearless manner.
  • 8. The method according to claim 7, wherein there are two curved pipe parts, and the ore pulp flows out of the two curved pipe parts via two openings, and the method comprising: arranging the two curved pipe parts in such a way that the reaction forces produced during the outflow of the ore pulp at the openings are opposite and equal.
  • 9. The method according to claim 7, wherein a head of the ore pulp upstream of a generator station is within the range of 500 to 1000 m.
  • 10. The method according to claim 7, wherein the inlet of the continuous-flow machine is formed by a pipe into which the outlet of the pipeline is inserted.
  • 11. The method according to claim 10, wherein the pipe forms the rotating shaft.
  • 12. The method according to claim 7, wherein the ore pulp discharging from the continuous-flow machine flows into a collecting basin, from which it flows further on to a subsequent processing plant or to the next generator station.
Priority Claims (2)
Number Date Country Kind
10 2008 005 689 Jan 2008 DE national
10 2008 009 669 Feb 2008 DE national
PCT Information
Filing Document Filing Date Country Kind 371c Date
PCT/EP2009/050183 1/8/2009 WO 00 9/15/2010
Publishing Document Publishing Date Country Kind
WO2009/092633 7/30/2009 WO A
US Referenced Citations (75)
Number Name Date Kind
3153 Whitelaw et al. Jul 1843 A
3943 Black Mar 1845 A
5039 Galvani Mar 1847 A
24740 Hughes Jul 1859 A
31217 Armstrong Jan 1861 A
36164 Monson Aug 1862 A
37841 Megay Mar 1863 A
63148 Ely Mar 1867 A
75011 Hainsworth Mar 1868 A
103162 Duvall May 1870 A
110912 Gibson Jan 1871 A
211572 Hinden Jan 1879 A
214159 Langevin Apr 1879 A
499121 Kales Jun 1893 A
523734 Shaw Jul 1894 A
634969 Wahle Oct 1899 A
700224 McRae May 1902 A
709242 Prescott et al. Sep 1902 A
715152 Roeske Dec 1902 A
768884 O'Brien Aug 1904 A
890392 Adams Jun 1908 A
935046 McLaren Sep 1909 A
982035 Clapp Jan 1911 A
999776 Gill Aug 1911 A
1049213 Dresser Dec 1912 A
1050410 Wainwright Jan 1913 A
1287049 Kramer Dec 1918 A
1329626 Oman Feb 1920 A
2060414 Fladeland Nov 1936 A
2569997 Kollsman Oct 1951 A
2690809 Kerry Oct 1954 A
3304051 Thomas Feb 1967 A
3383805 Powell May 1968 A
3813043 Mordehai May 1974 A
3879152 Eskeli Apr 1975 A
3984698 Brewer Oct 1976 A
3999711 Katzman Dec 1976 A
4027483 Wahl, III Jun 1977 A
4059772 Wilkerson Nov 1977 A
4132901 Crausbay Jan 1979 A
4272685 Toyama Jun 1981 A
4274814 Rylewski Jun 1981 A
4298311 Ritzi Nov 1981 A
4302683 Burton Nov 1981 A
4332520 House Jun 1982 A
4336693 Hays et al. Jun 1982 A
4363341 Powell Dec 1982 A
4391102 Studhalter et al. Jul 1983 A
4430042 House Feb 1984 A
4438638 Hays et al. Mar 1984 A
4452566 Kardas Jun 1984 A
4651765 Beth Mar 1987 A
4741154 Eidelman May 1988 A
4893986 Catterfeld et al. Jan 1990 A
D307044 Johnston et al. Apr 1990 S
5236349 Fabris Aug 1993 A
5263814 Jang Nov 1993 A
5307993 Simonetti et al. May 1994 A
5408824 Schlote Apr 1995 A
5525034 Hays Jun 1996 A
5560196 Schlote Oct 1996 A
5738249 Kikuchi et al. Apr 1998 A
5905312 Liou May 1999 A
6029688 Kaufman Feb 2000 A
6668539 Schlote Dec 2003 B2
6783320 Johnson Aug 2004 B2
6929444 Bomski Aug 2005 B1
6996971 Schlote Feb 2006 B2
7222487 Hinkley May 2007 B1
7722313 Dilorio May 2010 B1
8342364 Bertucci et al. Jan 2013 B2
20050147493 Vorobiev et al. Jul 2005 A1
20060230742 Witteveen Oct 2006 A1
20080272601 Newman Nov 2008 A1
20130008522 Bertucci et al. Jan 2013 A1
Foreign Referenced Citations (4)
Number Date Country
4265 Apr 2001 AT
2412583 Jun 2004 CA
130466 Apr 1978 DE
2006028377 Mar 2006 WO
Non-Patent Literature Citations (2)
Entry
International PCT Search Report, PCT/EP2009/050183, 15 pages, Mailed Apr. 15, 2010.
Walker, C.I; “Slurry Turbine Energy Recovery Systems”, in Liu, H. and Round, GF: Freight Pipelines, Proceedings of the 6th International Symposium on Freight Pipelines, Hemisphere Publishing Corporation, XP002576115, pp. 51-56, 1990.
Related Publications (1)
Number Date Country
20110012370 A1 Jan 2011 US