Methods of enhancing fine particle dewatering

• US 7,820,058 B2
• Filed: 08/03/2007
• Issued: 10/26/2010
• Est. Priority Date: 06/07/1999
• Status: Expired due to Fees

• Current Assignee: Mineral Technologies Pty Ltd. (Downer EDI Limited)
• Original Assignee: Mineral Technologies Pty Ltd. (Downer EDI Limited)
• Inventors: Yoon, Roe Hoan
• Primary Examiner(s): Hruskoci; Peter A
• Application Number:
  US11/833,402
• Publication Number:
  US 20080053914A1
• Time in Patent Office: 1,180 Days
• Field of Search: 210/727
• US Class Current: 210/727
• CPC Class Codes: B03D 1/08 Subsequent treatment of concentrated product froth dispersion B01D19/02
• CPC Class Codes: C02F 1/26 by extraction
• CPC Class Codes: C02F 11/147 using organic substances C02F11/148 takes precedence
• CPC Class Codes: C02F 2103/10 from quarries or from mining activities
• CPC Class Codes: C02F 2301/063 Underpressure, vacuum
• CPC Class Codes: C10L 5/04 Raw material of mineral origin to be used; Pretreatment thereof pretreatment of fuels of non-mineral origin C10L5/40
• CPC Class Codes: F26B 2200/18 Sludges, e.g. sewage, waste, industrial processes, cooling towers
• CPC Class Codes: F26B 5/005 by dipping them into or mixing them with a chemical liquid, e.g. organic; chemical, e.g. organic, dewatering aids F26B3/005 takes precedence; using chemical vapours or gases F26B21/14

Abstract

A new method of improving the process of dewatering fine particulate materials is disclosed. In this method, an aqueous slurry of fine particles is treated with appropriate hydrophobizing reagents so that the particulate material becomes moderately hydrophobic with its water contact angle considerably below 90°. A low hydrophile-lipophile balance (HLB) number surfactant is then added to the slurry, so that the surfactant molecules adsorb on the moderately hydrophobic surface primarily by hydrophobic attraction and, thereby, increase its contact angle close to or above 90°. By virtue of the greatly enhanced hydrophobicity, the water molecules adhering to the surface are destabilized and removed more readily by a mechanical dewatering process. Any nonionic surfactant with its HLB number below about 15 may be used for the hydrophobicity enhancement. The surfactants may be used in conjunction with appropriate solvents such as light hydrocarbon oils and short-chain alcohols. The moisture reduction can be further improved by using appropriate electrolytes in conjunction with the low HLB surfactants, spraying surface tension lowering reagents onto the filter cake, subjecting the cake to a suitable vibratory means, and by using combinations thereof.

Claims

1. A process for dewatering a slurry of hydrophobic coal particulate material comprising:

i) forming a layer of hydrophobes on the surface of said hydrophobic coal particulate material and initially increasing the hydrophobicity of said hydrophobic coal particulate material by adding hydrocarbon oil to said slurry, wherein the hydrophobicity of said coal particulate material is increased;

ii) adding a nonionic surfactant of hydrophile-lipophile balance (HLB) number less than 15 dissolved in at least one organic solvent;

iii) allowing said nonionic surfactant to adsorb on less hydrophobic parts of the surface of said hydrophobic coal particulate material to further increase hydrophobicity of said hydrophobic coal particulate material having increased hydrophobicity from the addition of said hydrocarbon oil; and

iv) effecting separation of water from said slurry of hydrophobic coal particulate material by subjecting said slurry to a mechanical method of dewatering.

2. The process of claim 1, further comprising agitating said slurry.

3. The process of claim 1, wherein said particulate material comprises particles of less than 2 mm in size.

4. The process of claim 1, wherein said nonionic surfactant is selected from the group consisting of:

fatty acids, fatty esters, phosphate esters, hydrophobic polymers, ethers, glycol derivatives, sarcosine derivatives, silicon-based surfactants and polymers, sorbitan derivatives, sucrose and glucose esters and derivatives, lanolin-based derivatives, glycerol esters, ethoylated fatty esters, ethoxylated amines and amides, ethoxylated linear alcohols, ethoxylated tryglycerides, ethoylated vegetable oils, and ethoxylated fatty acids.

5. The process of claim 1, wherein said nonionic surfactant is dissolved in an oil of vegetable origin.

6. The process of claim 1, wherein said organic solvent includes a solvent selected from the group consisting of:

light hydrocarbon oils and short-chain alcohols.

7. The process of claim 6, wherein said light hydrocarbon oils are selected from diesel oil, kerosene, gasoline, petroleum distillate, turpentine, naphtanic oils, and oils of vegetable origins.

8. The process of claim 6, wherein said short-chain alcohols have carbon atom numbers less than eight.

9. The process of claim 1, wherein said mechanical method of dewatering is selected from the group consisting of:

vacuum filtration, pressure filtration, centrifugal filtration, and centrifugation.

10. A process for dewatering a slurry of hydrophobic coal particulate material comprising:

forming a layer of hydrophobes on the surface of said hydrophobic coal particulate material and initially increasing the hydrophobicity of said hydrophobic coal particulate material by adding hydrocarbon oil to said slurry, wherein said hydrophobic coal particulate material exhibits a contact angle and the contact angle of said hydrophobic coal particulate material is below 45°

;

dissolving a nonionic surfactant of hydrophile-lipophile balance (HLB) number less than 15 in at least one organic solvent;

adding said dissolved nonionic surfactant and said at least one organic solvent to said slurry; and

allowing said nonionic surfactant to adsorb on less hydrophobic parts of the surface of said hydrophobic coal particulate material, to further increase the hydrophobicity of said material having increased hydrophobicity from the addition of said hydrocarbon oil, wherein said contact angle of said hydrophobic coal particulate material is above 45°

; and

effecting separation of water from said slurry of hydrophobic coal particulate material by subjecting said slurry to a mechanical method of dewatering.

11. The process according to claim 10, further comprising agitating said slurry.

12. The process of claim 10, wherein said organic solvent includes a solvent selected from the group consisting of:

light hydrocarbon oils and short-chain alcohols.

13. The process of claim 12, wherein said light hydrocarbon oils are selected from diesel oil, kerosene, gasoline, petroleum distillate, turpentine, naphtanic oils, and oils of vegetable origins.

14. The process of claim 12, wherein said short-chain alcohols have carbon atom numbers less than eight.

15. The process of claim 10, wherein said coal particulate material comprises particles of less than 2 mm in size.

16. A process for dewatering a slurry of superficially oxidized coal particles, comprising:

i) initially regenerating the hydrophobic surface of said oxidized coal particles,

ii) forming a layer of hydrophobes on the surface of said hydrophobic coal particulate material and increasing the hydrophobicity of said coal particles by adding hydrocarbon oil to said slurry,

ii) adding a non-ionic surfactant of hydrophile-lipophile balance (HLB) number less than 15 dissolved in at least on organic solvent;

iii) allowing said non-ionic surfactant to adsorb on less hydrophobic parts of the surface of said coal particles, to further increase the hydrophobicity of said coal particles having increased hydrophobicity from the addition of said hydrocarbon oil; and

iv) effecting separation of water from said slurry of hydrophobic particulate material by subjecting said slurry to a mechanical method of dewatering.

17. The process of claim 16, wherein said superficially oxidized coal particles are wet ground in a ball mill to regenerate the hydrophobic surface.