CN108690915A - A method of from platiniferous Sewage treatment platinum charcoal - Google Patents

A method of from platiniferous Sewage treatment platinum charcoal Download PDF

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Publication number
CN108690915A
CN108690915A CN201710220401.1A CN201710220401A CN108690915A CN 108690915 A CN108690915 A CN 108690915A CN 201710220401 A CN201710220401 A CN 201710220401A CN 108690915 A CN108690915 A CN 108690915A
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CN
China
Prior art keywords
biological reactor
anaerobic biological
platinum
platinum charcoal
platiniferous
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201710220401.1A
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Chinese (zh)
Inventor
张乐华
盖瑞哲
刘熠阳
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East China University of Science and Technology
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East China University of Science and Technology
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by East China University of Science and Technology filed Critical East China University of Science and Technology
Priority to CN201710220401.1A priority Critical patent/CN108690915A/en
Publication of CN108690915A publication Critical patent/CN108690915A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B11/00Obtaining noble metals
    • C22B11/04Obtaining noble metals by wet processes
    • C22B11/042Recovery of noble metals from waste materials
    • C22B11/046Recovery of noble metals from waste materials from manufactured products, e.g. from printed circuit boards, from photographic films, paper or baths
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/18Extraction of metal compounds from ores or concentrates by wet processes with the aid of microorganisms or enzymes, e.g. bacteria or algae
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Abstract

The present invention provides a kind of method for handling platiniferous waste water using anaerobic biological reactor and recycling platinum charcoal.This method specifically includes following steps:(1)It is passed through platiniferous waste water in anaerobic biological reactor anode;(2)Collect the biomembrane and excess sludge in anaerobic biological reactor;(3)Biomembrane in anaerobic biological reactor is obtained into platinum charcoal with excess sludge in the mixed gas protected lower charing of inertia and reproducibility.Compared with prior art, the present invention can recycle the platinum in platiniferous waste water and be fabricated to platinum charcoal, simple process and low cost is honest and clean, has a good application prospect under conditions of not causing secondary pollution.

Description

A method of from platiniferous Sewage treatment platinum charcoal
Technical field
The invention belongs to noble metal recovery technology fields, and in particular to the method for recycling platinum charcoal.
Technical background
Platinum is one kind of platinum group metal, chemical symbol Pt, atomic number 78, atomic weight 195.08, with silvery white Non-ferrous metal gloss, fusing point are 1772 DEG C, there is good ductility, thermal conductivity and electric conductivity.The chemical property torpescence of platinum, in sky Highly stable in gas, when less than 450 DEG C of heating, surface forms platinum dioxide film, can be with sulphur, phosphorus, halogen under high temperature Learn reaction.Platinum does not dissolve in hydrochloric acid, sulfuric acid, nitric acid and alkaline solution, but can be dissolved in chloroazotic acid and the alkali of melting.Platinum be in the earth's crust most Rare one of element, compound is varied, may be used as urging for the fields such as chemical industry, pharmacy, oil refining, purifying vehicle exhaust In agent.
Currently, the whole world has 50% platinum to be distributed in South Africa.And the platinum mineral resources wretched insufficiency of China.Therefore, secondary Platinum is recycled in resource just seems extremely important.The platiniferous electroplate liquid and platiniferous that platiniferous waste water is primarily present in electroplating industry are urged The waste liquid generated after agent dissolving.The characteristics of these platiniferous waste water is platinum content height, difficult to degrade.Conventional recovery method be to platinum or Platinum carbon catalyst, useless electric slurry are roasted, and are dissolved after roasting, later separating-purifying.The disadvantage of this method maximum It is that electric slurry and element will produce poisonous and hazardous flue gas during roasting, to the body of operator and neighbouring resident Body causes directly to injure, and secondly, will produce NO, NO when nitric acid dissolves fired slags2Equal pernicious gases, if without processing It is directly discharged in air that air pollution can be caused.Therefore, the method for finding a high-efficiency environment friendly recycling platinum is particularly significant.
Currently, having had been reported that the feasibility and actual effect for having studied microbial method recycling platinum.Its principle mainly passes through Absorption of the microorganism to platinum, makes it be attached to the surface of microorganism, by the redox of microorganism, platinum ion is made to restore For metal simple-substance.But pure bacterium bioreactor is selected in wherein most research, is unfavorable for actual popularization and application.The present invention uses Anaerobic biological reactor realizes that the resource utilization of platinum waste water utilizes as experimental provision.Anaerobic biological reactor method is recycling COD is reduced while platinum ion, is had a good application prospect.
Invention content
It is an object of the invention to overcome the deficiencies of the prior art and provide one kind under certain conditions, is given birth to using anaerobism The method of microorganism recycling platinum charcoal in object reactor, for handling platiniferous waste water and resource utilization using the platinum member in waste water Element.
The object of the present invention is achieved like this:The anaerobic biological reactor that domestication is completed is placed on magnetic stirring apparatus, The certain density platiniferous waste water of preparation is added in anaerobic biological reactor, after reacting a period of time, collects excess sludge It is carbonized, is obtained containing platinum and carbon simple substance mixture, i.e. platinum charcoal with the biomembrane to fall off.
Description of the drawings:
Fig. 1 is the structural diagram of the present invention:
It is in figure:Platiniferous waste water 1, anaerobic reactor 2, platiniferous excess sludge 3, carbonizing apparatus 4, platinum charcoal 5, water outlet 6.
Specific implementation mode
Below in conjunction with the accompanying drawings, the present invention is further illustrated:As shown in Figure 1, a kind of micro- life of anaerobic biological reactor The method that object recycles platinum charcoal, which is characterized in that including platiniferous waste water 1, anaerobic reactor 2, platiniferous excess sludge 3, carbonizing apparatus 4, platinum charcoal 5, water outlet 6.
Platiniferous waste water 1 is passed through in anaerobic reactor 2, reacts discharge platiniferous excess sludge 3 and water outlet 6 after a period of time, In, platiniferous excess sludge 3 carbonizes in carbonizing apparatus 4, obtains platinum charcoal 5.
Embodiment 1:As a concentration of 2.11 mg/L of the platinum ion that platiniferous waste water is added, anaerobic reactor is placed in magnetic agitation On device, rotating speed is 200 rpm, reacts 24 h, and aqueous concentration is 0.033 mg/L, removal rate 98.43%.
Embodiment 2:As a concentration of 4.22 mg/L of the platinum ion that platiniferous waste water is added, anaerobic reactor is placed in magnetic force On blender, rotating speed is 200 rpm, reacts 24 h, aqueous concentration 0.21mg/L, removal rate 95.02%.
Embodiment 3:As a concentration of 8.44 mg/L of the platinum ion that platiniferous waste water is added, anaerobic reactor is placed in magnetic force On blender, rotating speed is 200 rpm, reacts 24 h, and aqueous concentration is 0.67 mg/L, removal rate 92.06%.
Embodiment 4:As a concentration of 16.88 mg/L of the platinum ion that platiniferous waste water is added, anaerobic reactor is placed in magnetic force On blender, rotating speed is 200 rpm, reacts 24 h, and aqueous concentration is 1.58 mg/L, removal rate 90.63%.
Embodiment 5:After biomembrane and excess sludge charing in anaerobic reactor, simple substance platinum and platinic ratio are obtained About 2:3, wherein simple substance platinum ratio shared in total platinum is 41.34%.

Claims (4)

1. the present invention relates to a kind of methods that anaerobic biological reactor method recycles platinum charcoal, it is characterised in that:This method specifically includes Following steps:(1)It is passed through platiniferous waste water in anaerobic biological reactor anode;(2)Collect the biomembrane in anaerobic biological reactor And excess sludge;(3)By in anaerobic biological reactor biomembrane and excess sludge it is mixed gas protected in inertia and reproducibility Lower charing obtains platinum charcoal.
2. a kind of method of microbial method recycling platinum charcoal according to claim 1, which is characterized in that step(1)Described Anaerobic biological reactor is pure bacterium or mixed bacterium anaerobic biological reactor.
3. a kind of method of microbial method recycling platinum charcoal according to claim 1, which is characterized in that step(2)Described Biomembrane and excess sludge collection method include gravity concentration method, floatation thickening method, centrifugal concentrating method.
4. a kind of method of microbial method recycling platinum charcoal according to claim 1, which is characterized in that step(3)Described Inertia and reproducibility mixed gas include nitrogen, argon, helium, vapor or hydrogen.
CN201710220401.1A 2017-04-06 2017-04-06 A method of from platiniferous Sewage treatment platinum charcoal Pending CN108690915A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710220401.1A CN108690915A (en) 2017-04-06 2017-04-06 A method of from platiniferous Sewage treatment platinum charcoal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710220401.1A CN108690915A (en) 2017-04-06 2017-04-06 A method of from platiniferous Sewage treatment platinum charcoal

Publications (1)

Publication Number Publication Date
CN108690915A true CN108690915A (en) 2018-10-23

Family

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Family Applications (1)

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CN201710220401.1A Pending CN108690915A (en) 2017-04-06 2017-04-06 A method of from platiniferous Sewage treatment platinum charcoal

Country Status (1)

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CN (1) CN108690915A (en)

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002192178A (en) * 2000-12-22 2002-07-10 Fuji Photo Film Co Ltd Heavy metal trapping method and heavy metal recovering method
CN201737770U (en) * 2010-03-22 2011-02-09 南京加德绿色能源研发有限公司 Microbial response system for waste water treatment and clean energy production at the same time
CN102674544A (en) * 2012-05-28 2012-09-19 苏州苏水环境工程有限公司 Upflow blanket filter (UBF) anaerobic reactor with filter layer at top and for treating chemical wastewater
CN102869618A (en) * 2010-04-27 2013-01-09 西门子工业公司 Ballasted anaerobic system and method for treating wastewater
CN103153883A (en) * 2011-05-04 2013-06-12 Rm泰科株式会社 Method for heavy metal elimination or precious metal recovery using microbial fuel cell
CN103663860A (en) * 2013-10-30 2014-03-26 郭强 Treatment method of high-concentration wastewater
JP2015058401A (en) * 2013-09-19 2015-03-30 パナソニック株式会社 Wastewater treatment apparatus

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002192178A (en) * 2000-12-22 2002-07-10 Fuji Photo Film Co Ltd Heavy metal trapping method and heavy metal recovering method
CN201737770U (en) * 2010-03-22 2011-02-09 南京加德绿色能源研发有限公司 Microbial response system for waste water treatment and clean energy production at the same time
CN102869618A (en) * 2010-04-27 2013-01-09 西门子工业公司 Ballasted anaerobic system and method for treating wastewater
CN103153883A (en) * 2011-05-04 2013-06-12 Rm泰科株式会社 Method for heavy metal elimination or precious metal recovery using microbial fuel cell
CN102674544A (en) * 2012-05-28 2012-09-19 苏州苏水环境工程有限公司 Upflow blanket filter (UBF) anaerobic reactor with filter layer at top and for treating chemical wastewater
JP2015058401A (en) * 2013-09-19 2015-03-30 パナソニック株式会社 Wastewater treatment apparatus
CN103663860A (en) * 2013-10-30 2014-03-26 郭强 Treatment method of high-concentration wastewater

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
马世昌主编: "《化学物质辞典》", 30 April 1999, 陕西科学技术出版社 *

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