SYSTEMS AND METHODS FOR DOSING SLURRIES TO REMOVE SUSPENDED SOLIDS

• US 20190330088A1
• Filed: 01/05/2018
• Published: 10/31/2019
• Est. Priority Date: 01/10/2017
• Status: Active Grant

• Current Assignee: Vermeer Manufacturing Company
• Original Assignee: Vermeer Manufacturing Company
• Inventors: Askelsen, Tayte, Lanoue, Corey, Strobel, Andy
• Granted Patent: US 11,130,686 B2
• Time in Patent Office: Days
• CPC Class Codes: C02F 1/5209 Regulation methods for flocculation or precipitation
• CPC Class Codes: C02F 1/5227 Processes for facilitating the dissolution of solid flocculants in water
• CPC Class Codes: C02F 11/14 with addition of chemical agents
• CPC Class Codes: C02F 2103/10 from quarries or from mining activities
• CPC Class Codes: C02F 2201/002 Construction details of the apparatus
• CPC Class Codes: C02F 2201/008 Mobile apparatus and plants, e.g. mounted on a vehicle for biological treatment C02F2203/008
• CPC Class Codes: C02F 2209/04 Oxidation reduction potential [ORP]

Abstract

Systems and methods for dosing slurries to remove suspended solids from the slurry are disclosed. The systems and methods may be used to dewater slurries having relatively high solids content such as earthen slurries. In some embodiments, the zeta potential of the slurry is monitored by an electroacoustic zeta potential sensor to control coagulant addition.

Claims

1. A system for dosing a slurry to remove suspended solids, the system comprising:

a batch mix tank;

an electroacoustic zeta potential sensor in fluid communication with the batch mix tank;

a coagulant feed system for adding coagulant to the batch mix tank; and

a coagulant control system, the coagulant control system comprising a controller communicatively coupled to the coagulant feed system and configured to terminate coagulant addition based on a zeta potential parameter.

2. The system as set forth in claim 1 wherein the zeta potential parameter is the sign or magnitude of the zeta potential, the controller being configured to terminate coagulant addition based on a change in the sign or magnitude of the zeta potential parameter.

7. The system as set forth in claim 1 wherein the coagulant feed system comprises a coagulant feed pump and valve to control coagulant addition, the coagulant control system being communicatively coupled to the coagulant feed pump to control coagulant addition to the batch mix tank.

9. The system as set forth in claim 1 wherein the system is a mobile system to allow the system to be transported to different sites, the mobile system:

comprising tires or tracks to move the system to different sites; and

/or

being supported by a frame or skid that allows the system to be loaded or unloaded from a transport vehicle.

12. The system as set forth in claim 1 comprising a mixing system within the batch mix tank for mixing the contents of the batch mix tank.

16. The system as set forth in claim 1 further comprising:

a flocculant feed system, the flocculant feed system comprising a flocculant pump in fluid communication with the batch mix tank;

a flocculant control system communicatively coupled to the flocculant feed system; and

an interface sensor for sensing a solid-liquid interface in the batch mix tank, the interface sensor being communicatively coupled to the flocculant control system to control the amount of flocculant added to the batch mix tank by the flocculant feed system.

18. The system as set forth in claim 1 comprising a water feed system for adding water to the batch mix tank to dilute the slurry.

21. The system as set forth in claim 1 wherein the batch mix tank includes an adjustable weir to allow supernatant water to be decanted.

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23. A system for dosing a slurry to remove suspended solids, the system comprising:

a coagulant feed system for adding coagulant to an infeed slurry, the coagulant feed system comprising;

a coagulant mixing vessel;

a first coagulant feed port formed in the coagulant mixing vessel;

a first zeta potential sensor downstream of the first coagulant feed port, a first mixing zone of the coagulant mixing vessel being defined between the first coagulant feed port and the first zeta potential sensor;

a second coagulant feed port formed in the coagulant mixing vessel; and

a second zeta potential sensor downstream of the second coagulant feed port, a second mixing zone of the coagulant mixing vessel being defined between the second coagulant feed port and the second zeta potential sensor;

one or more coagulant feed pumps in fluid communication with the first and second coagulant feed ports; and

a coagulant control system, the coagulant control system comprising a controller configured to control coagulant addition based on a zeta potential parameter sensed by the first and/or second zeta potential sensor.

24. The system as set forth in claim 23 wherein the coagulant feed system comprises:

a third coagulant feed port; and

a third zeta potential sensor downstream of the third coagulant feed port, a third mixing zone of the coagulant mixing vessel being defined between the third coagulant feed port and the third zeta potential sensor.

30. The system as set forth in claim 23 further comprising:

a flocculant feed system comprising a flocculant mix tank; and

a flocculant control system communicatively coupled to the flocculant feed system.

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31. A method for dewatering earthen slurries, the method comprising:

ejecting slurry from a slurry transport vehicle into a pretreatment system to remove an initial amount of solids from the slurry and produce a solids-depleted slurry;

introducing the solids-depleted slurry into a batch mix tank;

adding coagulant to the solids-depleted slurry in the batch mix tank to change the zeta potential of the slurry; and

adding flocculant to the solid-depleted slurry in the batch mix tank to agglomerate suspended solids and form an agglomerated suspension; and

separating solids from the agglomerated suspension.

33. The method as set forth in claim 31 wherein the slurry transport vehicle is a first vehicle and the slurry is a first slurry, the method further comprising:

ejecting a second slurry form a second slurry transport vehicle into the pretreatment system to remove an initial amount of solids from the slurry and produce a second solids-depleted slurry;

introducing the second solids-depleted slurry into the batch mix tank;

adding coagulant and flocculant to the second solids-depleted slurry in the batch mix tank to agglomerate suspended solids and form an agglomerated suspension; and

separating solids from the agglomerated suspension.

35. The method as set forth in claim 31 wherein the solids are separated by sedimentation, centrifugation, filtration or by thermal drying.

39. The method as set forth in claim 31 wherein the zeta potential parameter is the sign of the zeta potential or the magnitude of the zeta potential.

41. The method as set forth in claim 31 wherein coagulant is added in two or more doses, the method comprising measuring the zeta potential after each dose is added to determine if the zeta potential is reduced to an amount within a set point range, wherein coagulant addition is terminated after the zeta potential is within the set point range.

43. The method as set forth in claim 31 further comprising diluting the slurry by adding water to the mix tank.

44. The method as set forth in claim 31 wherein the tank is a batch tank, the slurry added to the mix tank is a first slurry and the coagulant added to mix tank is a coagulant first portion, the first slurry being added to the mix tank to form a first slurry batch, the method further comprising:

discharging a treated first slurry batch from the mix tank;

adding a second slurry to the mix tank to form a second slurry batch;

adding a coagulant second portion to the mix tank;

monitoring the magnitude of the zeta potential during addition of the coagulant second portion; and

terminating addition of coagulant second portion to the batch mix tank when the magnitude of the zeta potential is within a set point range.

46. The method as set forth in claim 31 further comprising:

monitoring a solid-liquid interface by an interface sensor during flocculant addition; and

terminating flocculant addition based on output from the interface sensor.

47. The method as set forth in claim 31 wherein the batch mix tank is mixed while adding coagulant and while adding flocculant, the batch mix tank being mixed at a higher speed during coagulant addition relative to the speed during flocculant addition.

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