CN105148556A - Regeneration method for aging P204 organic phase - Google Patents

Regeneration method for aging P204 organic phase Download PDF

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Publication number
CN105148556A
CN105148556A CN201510584169.0A CN201510584169A CN105148556A CN 105148556 A CN105148556 A CN 105148556A CN 201510584169 A CN201510584169 A CN 201510584169A CN 105148556 A CN105148556 A CN 105148556A
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organic phase
aging
regeneration
active carbon
regeneration method
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CN201510584169.0A
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CN105148556B (en
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钟学明
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Nanchang Hangkong University
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Nanchang Hangkong University
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Abstract

The invention discloses a regeneration method for an aging P204 organic phase. Spherical active carbon is used as a regeneration agent. The regeneration method comprises the following steps: transferring the aging P204 organic phase into a reaction pot, adding 40-50g of the spherical active carbon into each liter of the aging P204 organic phase, and stirring under room temperature for 6-8 hours for filtration, wherein filtrate is a regenerated P204 organic phase, and the yield thereof is 96-98 percent. The regeneration method has the advantages of short technical flow, high regeneration speed, small use amount of chemical engineering reagents, zero emission of waste liquid, simple equipment, operation simplicity and convenience, low regeneration cost and the like.

Description

A kind of renovation process of aging P204 organic phase
Technical field
The present invention relates to a kind of renovation process of aging P204 organic phase, particularly relating to a kind of is regenerative agent with spheric active carbon, recovers the method for aging P204 organic extractant phase performance and function.The present invention specifically belongs to solvent extraction technology field.
Background technology
The chemical name of P204 is di-(2-ethylhexyl)phosphoric acid, and this is a kind of essential industry extractant being widely used in the fields such as light rare earth separation, the separation of cobalt nickel, heavy metal element recovery, heavy metal containing wastewater treatment, the reparation of heavy metal pollution farmland.In actual use, usually P204 extractant be dissolved in kerosene or sulfonated kerosene and make organic phase, the mechanism normally cation exchange mechanism of its extracting metals ion.Because P204 organic phase for a long time, periodically goes through the cyclic process such as saponification, extraction, washing and back extraction, amass night day and tire out, therefore inevitably there is various change and occur aging phenomenon in P204 organic phase gradually.P204 organic phase aging is an extremely complicated process, and the open research report of so far there are no this respect, so the current agine mechaism also not understanding P204 organic phase.P204 organic phase after aging, extraction load capacity obviously declines, separative efficiency significantly reduces, phase-splitting time significant prolongation, serious emulsification not even phase-splitting.
Many professional and technical personnel in the field adopt the chemical reagent treatment of aged P204 organic phases such as hydrochloric acid, nitric acid, NaOH, oxalic acid, but all end in failure.End today, owing to not having process of regenerating, when aging P204 organic phase cannot use, the most frequently used Disposal Measures is discarded.Discarded aging P204 organic phase, not only can suffer greater loss economically, and serious environment pollution, impact ecology.
Summary of the invention
The object of the invention is the method for there is no rejuvenating aged P204 organic phase, overcoming the problem of discarded aging P204 organic phase contaminated environment, impact ecology, setting up a kind of method that is easy, rejuvenating aged P204 organic phase fast and efficiently.
The renovation process of a kind of aging P204 organic phase of the present invention, take spheric active carbon as regenerative agent, is transferred in reaction pot by aging P204 organic phase, and often liter of aging P204 organic phase adds that 40g ~ 50g average grain diameter is 0.4mm ~ 0.6mm, BET specific surface area is 500m 2/ g ~ 1000m 2the spheric active carbon of/g, stirred at ambient temperature process 6h ~ 8h, filters; Filtrate is regeneration P204 organic phase, and its yield is 96% ~ 98%.
Advantage of the present invention is: technological process is short, and reproduction speed is fast, and chemical reagent consumption is few, and without discharging of waste liquid, equipment is simple, and easy and simple to handle, regeneration cost is low.Used spheric active carbon, can adopt the processing steps such as salt acid soak, filtration, washing, oven dry and high-temperature activation and regenerate.
Detailed description of the invention
Be further described below in conjunction with the renovation process of specific embodiment to a kind of aging P204 organic phase of the present invention.
embodiment 1:
Aging for 600L P204 organic phase is transferred in 1000L reaction pot, adds that 27kg average grain diameter is 0.5mm, BET specific surface area is 750m 2the spheric active carbon of/g, stirred at ambient temperature process 7h, filters; Filtrate is regeneration P204 organic phase, and its yield is 97%.
embodiment 2:
Aging for 600L P204 organic phase is transferred in 1000L reaction pot, adds that 24kg average grain diameter is 0.4mm, BET specific surface area is 1000m 2the spheric active carbon of/g, stirred at ambient temperature process 8h, filters; Filtrate is regeneration P204 organic phase, and its yield is 98%.
embodiment 3:
Aging for 600L P204 organic phase is transferred in 1000L reaction pot, adds that 30kg average grain diameter is 0.6mm, BET specific surface area is 500m 2the spheric active carbon of/g, stirred at ambient temperature process 6h, filters; Filtrate is regeneration P204 organic phase, and its yield is 96%.

Claims (1)

1. the renovation process of an aging P204 organic phase, it is characterized in that: described renovation process take spheric active carbon as regenerative agent, aging P204 organic phase is transferred in reaction pot, in often liter of aging P204 organic phase, adds that 40g ~ 50g average grain diameter is 0.4mm ~ 0.6mm, specific area is 500m 2/ g ~ 1000m 2the spheric active carbon of/g, filters after stirred at ambient temperature process 6h ~ 8h; Filtrate is regeneration P204 organic phase, and its yield is 96% ~ 98%.
CN201510584169.0A 2015-09-15 2015-09-15 Regeneration method for aging P204 organic phase Expired - Fee Related CN105148556B (en)

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CN105148556A true CN105148556A (en) 2015-12-16
CN105148556B CN105148556B (en) 2017-04-12

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110551895A (en) * 2018-06-04 2019-12-10 格林美(江苏)钴业股份有限公司 Separation method of aged P 507
CN113308603A (en) * 2021-05-26 2021-08-27 广西银亿新材料有限公司 Treatment method of interphase dirt in nickel-cobalt metallurgy P204 extraction system

Citations (6)

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Publication number Priority date Publication date Assignee Title
US4197195A (en) * 1976-11-16 1980-04-08 Gesellschaft Fur Kernforschung M.B.H. Method for minimizing the organic waste in aqueous product streams produced in liquid-liquid extraction processes
CN2126708Y (en) * 1992-04-16 1993-02-03 沈祖志 Comprehensive speed process device for wine
EP0862737A1 (en) * 1995-11-24 1998-09-09 Pharmacia Biotech AB Chromotographic method and device in which a continuous macroporous organic matrix is used
CN1936035A (en) * 2006-09-29 2007-03-28 金川集团有限公司 P204 deferrizing regeneration method
CN101215637A (en) * 2008-01-11 2008-07-09 昆明理工大学 Method for eluting nickel from nickel-carrying activated carbon by cleanser essence
CN101831547A (en) * 2010-05-26 2010-09-15 江苏凯力克钴业股份有限公司 Method for purifying cobalt solution

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4197195A (en) * 1976-11-16 1980-04-08 Gesellschaft Fur Kernforschung M.B.H. Method for minimizing the organic waste in aqueous product streams produced in liquid-liquid extraction processes
CN2126708Y (en) * 1992-04-16 1993-02-03 沈祖志 Comprehensive speed process device for wine
EP0862737A1 (en) * 1995-11-24 1998-09-09 Pharmacia Biotech AB Chromotographic method and device in which a continuous macroporous organic matrix is used
CN1936035A (en) * 2006-09-29 2007-03-28 金川集团有限公司 P204 deferrizing regeneration method
CN101215637A (en) * 2008-01-11 2008-07-09 昆明理工大学 Method for eluting nickel from nickel-carrying activated carbon by cleanser essence
CN101831547A (en) * 2010-05-26 2010-09-15 江苏凯力克钴业股份有限公司 Method for purifying cobalt solution

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
刘明华: "《水处理化学品》", 31 January 2010, 化学工业出版社 *
钟学明: "老化P507萃取剂再生研究", 《江西科学》 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110551895A (en) * 2018-06-04 2019-12-10 格林美(江苏)钴业股份有限公司 Separation method of aged P 507
CN113308603A (en) * 2021-05-26 2021-08-27 广西银亿新材料有限公司 Treatment method of interphase dirt in nickel-cobalt metallurgy P204 extraction system

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