GB2464998A - Bacterial process for the preparation metal-doped magnetite nanoparticles - Google Patents

Bacterial process for the preparation metal-doped magnetite nanoparticles Download PDF

Info

Publication number
GB2464998A
GB2464998A GB0816119A GB0816119A GB2464998A GB 2464998 A GB2464998 A GB 2464998A GB 0816119 A GB0816119 A GB 0816119A GB 0816119 A GB0816119 A GB 0816119A GB 2464998 A GB2464998 A GB 2464998A
Authority
GB
United Kingdom
Prior art keywords
nanoparticles
iron
transition metal
magnetite
reducing bacteria
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.)
Withdrawn
Application number
GB0816119A
Other versions
GB0816119D0 (en
Inventor
Victoria S Coker
Richard S Cutting
Jonathan R Lloyd
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
University of Manchester
Original Assignee
University of Manchester
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 University of Manchester filed Critical University of Manchester
Priority to GB0816119A priority Critical patent/GB2464998A/en
Publication of GB0816119D0 publication Critical patent/GB0816119D0/en
Publication of GB2464998A publication Critical patent/GB2464998A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/40Catalysts, in general, characterised by their form or physical properties characterised by dimensions, e.g. grain size
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/20Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state
    • B01J35/23Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state in a colloidal state
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74Iron group metals
    • B01J23/745Iron
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/89Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
    • B01J23/8906Iron and noble metals
    • B01J35/006
    • B01J35/023
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/33Electric or magnetic properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/391Physical properties of the active metal ingredient
    • B01J35/393Metal or metal oxide crystallite size
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00Nanotechnology for materials or surface science, e.g. nanocomposites
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G1/00Methods of preparing compounds of metals not covered by subclasses C01B, C01C, C01D, or C01F, in general
    • C01G1/02Oxides
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G49/00Compounds of iron
    • C01G49/02Oxides; Hydroxides
    • C01G49/08Ferroso-ferric oxide [Fe3O4]
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C15/00Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts
    • C07C15/40Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts substituted by unsaturated carbon radicals
    • C07C15/50Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts substituted by unsaturated carbon radicals polycyclic non-condensed
    • C07C15/52Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts substituted by unsaturated carbon radicals polycyclic non-condensed containing a group with formula
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2/00Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
    • C07C2/86Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation between a hydrocarbon and a non-hydrocarbon
    • C07C2/861Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation between a hydrocarbon and a non-hydrocarbon the non-hydrocarbon contains only halogen as hetero-atoms
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/30Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group
    • C07C67/333Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group by isomerisation; by change of size of the carbon skeleton
    • C07C67/343Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group by isomerisation; by change of size of the carbon skeleton by increase in the number of carbon atoms
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C69/00Esters of carboxylic acids; Esters of carbonic or haloformic acids
    • C07C69/612Esters of carboxylic acids having a carboxyl group bound to an acyclic carbon atom and having a six-membered aromatic ring in the acid moiety
    • C07C69/618Esters of carboxylic acids having a carboxyl group bound to an acyclic carbon atom and having a six-membered aromatic ring in the acid moiety having unsaturation outside the six-membered aromatic ring
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/20Bacteria; Culture media therefor
    • C12N1/205Bacterial isolates
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P3/00Preparation of elements or inorganic compounds except carbon dioxide
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2002/00Crystal-structural characteristics
    • C01P2002/50Solid solutions
    • C01P2002/52Solid solutions containing elements as dopants
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2002/00Crystal-structural characteristics
    • C01P2002/70Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data
    • C01P2002/72Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data by d-values or two theta-values, e.g. as X-ray diagram
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2002/00Crystal-structural characteristics
    • C01P2002/80Crystal-structural characteristics defined by measured data other than those specified in group C01P2002/70
    • C01P2002/85Crystal-structural characteristics defined by measured data other than those specified in group C01P2002/70 by XPS, EDX or EDAX data
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/01Particle morphology depicted by an image
    • C01P2004/04Particle morphology depicted by an image obtained by TEM, STEM, STM or AFM
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/60Particles characterised by their size
    • C01P2004/64Nanometer sized, i.e. from 1-100 nanometer
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2521/00Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
    • C07C2521/06Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
    • C07C2523/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals of the platinum group metals
    • C07C2523/42Platinum
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
    • C07C2523/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals of the platinum group metals
    • C07C2523/44Palladium
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
    • C07C2523/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals of the platinum group metals
    • C07C2523/46Ruthenium, rhodium, osmium or iridium
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
    • C07C2523/48Silver or gold
    • C07C2523/50Silver
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
    • C07C2523/48Silver or gold
    • C07C2523/52Gold
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/74Iron group metals
    • C07C2523/755Nickel
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12RINDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
    • C12R2001/00Microorganisms ; Processes using microorganisms
    • C12R2001/01Bacteria or Actinomycetales ; using bacteria or Actinomycetales

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Wood Science & Technology (AREA)
  • Zoology (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Biotechnology (AREA)
  • Inorganic Chemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Genetics & Genomics (AREA)
  • Microbiology (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Nanotechnology (AREA)
  • Physics & Mathematics (AREA)
  • Composite Materials (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • General Physics & Mathematics (AREA)
  • Medicinal Chemistry (AREA)
  • Tropical Medicine & Parasitology (AREA)
  • Virology (AREA)
  • Biomedical Technology (AREA)
  • Compounds Of Iron (AREA)
  • Catalysts (AREA)

Abstract

A process for preparing magnetite nanoparticles incorporating one of more transition elements comprising exposing a ferric iron source to a culture of dissimilatory iron-reducing bacteria (DIRB) and/or a sulphate-reducing bacteria (SRB) in the presence of a redox mediator. The preferred ferric iron source is ferrihydrite, the preferred bacterium is G. sulfurreducens, the preferred redox mediator is an electron shuttle such as anthraquinone-2,6-disulfonate (AQDS). The preferred source of the metal dopant is sodium tetrachloropalladate (Na2PdCl4). The resultant metal-doped magnetite nanoparticles may be coated with a biomolecular coating derived from the bacterium. The metal-doped magnetite nanoparticles are useful catalytically, especially in the Heck reaction between iodobenzene and either styrene or ethyl acrylate. For this reaction, the metal-doped magnetite nanoparticles are more effective catylysts than commercially available colloidal palladium catalysts.

Description

MAGNETICALLY RECOVERABLE CATALYSTS
The present invention provides a process for producing iron minerals, and in particular, magnetite from a ferric iron source. More particularly, the present invention provides a process for producing such minerals via a biological means. The invention is therefore concerned with the production of biogenic magnetic minerals produced by microbial activity. More particularly, magnetite produced by the process of the present invention is in the form of crystalline particles. These biogenic particles may have a diameter of approximately 1 nm to approximately 50 nm. When the biogenic magnetite particles have a diameter in the nanometre range, i.e. approximately 1 to approximately 50 nm, the particles may be referred to as "biogenic nanomagnetite particles" or simply as "nanomagnetite particles".
The present invention thus relates to the preparation and use of iron-based magnetic nanoparticles and their use in the preparation of catalysts. In one preferred variant, the invention is concerned with the preparation of nanoscale magnetite particles which are produced by culturing bacteria with an iron based mineral. The bacteria used in the process of the invention are dissimilatory iron-reducing bacteria. The resulting nanoparticulate iron mineral is then reacted with a solution of a transition metal compound to produce a nanoparticulate iron-based catalytic material. The resulting catalytic material can be used in a number of chemical reactions where transition metals and compounds thereof are conventionally used as catalysts. One such example is in the Heck coupling reaction. The catalytic material of the present invention is magnetic and hence can easily be recovered after use.
Throughout the description and claims of this specification, the words "comprise" and "contain" and variations of the words, for example "comprising" and "comprises", means "including but not limited to", and is not intended to (and does not) exclude other moieties, additives, components, integers or steps.
Throughout the description and claims of this specification, the singular encompasses the plural unless the context otherwise requires. In particular, where the indefinite article is used, the specification is to be understood as contemplating plurality as well as singularity, unless the context requires otherwise.
Features, integers, characteristics, compounds, chemical moieties or groups described in conjunction with a particular aspect, embodiment or example of the invention are to be understood to be applicable to any other aspect, embodiment or example described herein unless incompatible therewith.
Nanoparticles make highly desirable catalysts, often offering unique properties linked to their very high surface area. Magnetic nanoparticles are particularly useful support materials for catalysts as they can combine the advantages of a high dispersion through a liquid with ease of recovery. Palladium, and other platinum group metals, placed on a suitable support material, make exceptionally useful catalysts for mild reaction conditions that have excellent compatibility with many polar functional groups and a high degree of chemo-, regio-and even stereoselectivity.
Synthetic magnetite nanoparticles have been coated previously with precious metals such as palladium to give a catalyst which is potentially recoverable with a large reactive surface for use in the Heck Reaction and hydrogenation reactions.
Wang et al described the synthesis of palladium-coated magnetic nanoparticles and their application in the Heck Reaction in Colloids and Surfaces A: Physicochem. Eng.
Aspects 276, 116-121, 2006. Similarly, Rossi et al describe super paramagnetic nanoparticle-supported palladium as a highly stable magnetically recoverable and reusable catalyst which can be used in hydrogenation reactions in Green Chemistry, 9, 379-385, 2007.
Baruwati et al (Organic Letters, 2007, 9(26), 5377-5380 describes palladium on surface modified NiFe2O4 nanoparticles as a magnetically recoverable catalyst suitable for Suzuki and Heck reactions. The NiFe2O4 nanoparticles are synthesised by a hydrothermal route at 225°C. Anchoring of dopamine molecules on the surface of the as-synthesised NiFe2O4 nanoparticles was achieved by a ref luxing for 12 hours in aqueous medium. Pd(0) nanoparticles were then anchored on to the surface-modified NiFe2O4 nanoparticles by reducing Na2PdCI4 with hydrazine monohydrate. This process therefore requires extreme temperatures to produce the nanoparticles in the first place and also does not directly anchor the palladium metal to the magnetic substrate.
Attempts to make these materials using conventional chemical approaches have achieved varying degrees of success. In addition the protocols developed are relatively complicated, often including steps to functionalise the surface prior to the addition of precious metal coating. Additional problems have included loss of the precious metal during the recovery and recycling steps.
Thus, there are a number of problems with these prior art systems. The synthesis of such prior art catalysts is difficult, expensive, and may require the use of high temperatures. The resulting catalysts may not have a good turnover or lifetime.
There is therefore a need to provide a convenient route by which magnetic nanoparticulate catalysts can be produced. There is also a need for such catalysts to be able to be produced both economically and on a commercially viable scale if desired. In addition there is a need for a process which is robust, reliable and reproducible.
The present invention satisfies some or all of the above needs which are presently unmet by prior art processes. The present invention therefore provides a convenient route to magnetic nanoparticu late iron-based minerals which can then be converted to nanoparticulate catalytic materials following reaction with a transition metal compound.
We have found that biological routes can be harnessed to make nanoparticles of iron minerals, such as magnetite, efficiently and at low cost. This can be done with a degree of control regarding the rate of reduction, for example through the addition of redox mediators. We have also found that the magnetic properties of the end product are adequately retained despite substitution by transition metals. The resulting iron magnetic nanoparticles, otherwise referred to as the biogenic magnetic nanoparticles, bearing a catalyst have excellent activity.
The resulting biogenic material may also be crystalline. Microbes can be used in accordance with the invention to lay down a number of mineral phases under ambient conditions. The process of the invention is applicable to a number of catalytically active transition metals.
According to a first aspect of the present invention, there is provided a process for preparing magnetite nanoparticles incorporating one or more transition metal elements, the process comprising the steps: (a) exposing a compound or mixture of compounds as a source of ferric iron to a microbial system in a culture comprising a dissimilatory iron reducing bacteria (DIRB) and/or a sulphate reducing bacteria (SRB) in the presence of a redox mediator, (b) incubating the resulting mixture in a culture under anaerobic conditions to produce biogenic nanoparticles of an iron-based mineral, (c) separating the nanoparticles from the culture and optionally purifying the nanoparticles, (d) adding a solution containing one or more transition metal salts to a suspension of the nanoparticles to produce catalytic nanoparticles, and (e) recovering the catalytic nanoparticles.
The nanoparticles are preferably magnetic.
The source of iron can be an iron-based compound or a mixture of iron-based compounds which are capable of reacting with the bacteria to form magnetic nanoparticles.
In an embodiment, the source of iron is ferrihydrite.
In another embodiment, the source of iron is a waste iron material that would otherwise be land filled at large commercial and environmental cost. Examples of sources of Fe(III)-rich waste include acid mine drainage (AMD) sites and also water polishing steps in the water industry.
In an embodiment, step (c) does not include purifying the nanoparticles. In other words, in this embodiment, the nanoparticles are simply separated from the culture and the solution containing one or more transition metal salts is added immediately to the nanoparticles. In another embodiment, step (c) includes purifying the nanoparticles by washing.
In an embodiment, the redox mediator is an electron donor and an electron acceptor.
In an embodiment, the magnetic nanoparticles produced on exposure to the bacterial culture is one or more selected from the group comprising Fe304 (magnetite), Fe3S4 (greigite) and Fe7S8 (pyrrhotite). In a preferred embodiment, the magnetic material is magnetite.
In another embodiment, the bacterium is preferably a DIRB.
In an alternative embodiment, the bacterium is preferably a sulphate-reducing bacteria.
A number of suitable bacteria are described in the reference Microbiology Monograph (3), D Schüler: Magneto Reception and Magneto Somes in Bacteria DOl 10.
1007/71 71_047/published on line: 8 September 2006. The contents of this document in relation to dissimilatory iron-reducing bacteria and sulphate-reducing bacteria are intended to be incorporated herein as part of the present invention and form part of the 1 5 disclosure of the present invention in relation to the microbial process. Thus, preferred bacteria of the present invention are described on pages 278 to 282 of that reference.
Fig 2 of the review by Coker et al on page 279 shows a phylogenetic tree which presents a range of dissimilatory iron-reducing bacteria that can be used to synthesise magnetic nanoparticles. These bacteria specifically form part of the process of the present invention. Bacteria of particular interest in the present invention include the Geobacter species, Shewanella species and Geothrix species. In addition archaea, eg hyperthermophiles could also be used.
Preferred dissim ilatory iron-reducing bacteria include Geobacter, Shewanella and Geothrix.
Preferred sulphate-reducing bacteria include Desulfovibrio, Desulfococcus, Desulfobacter, Desulfobulbus and Desulfobotulus.
The nanoparticulate matter is produced from the iron source at around room temperature, typically 20°C using a range of different iron (III) reducing bacteria.
However, the process can be carried out at temperatures between 10° and 40°C. There is no need for elevated pressure, unless a barophilic organism is used.
The resulting magnetic nanoparticles may be recovered from the bacterial solution after incubation and washed. The material is then introduced into a solution containing one or more transition metals in the form of their salts. The magnetic iron nanoparticles are able to absorb and reduce the metals from the transition metal solution thereby forming particles in the range of ito 10 nm and preferably in the range of 5 to 7 nm of the transition metal on the magnetic nanoparticles. The magnetic nanoparticles have a size in the range of 15 to 50 nm and are preferably of 20 to 30 nm in size.
The culture may be incubated with the transition metal solution under anaerobic or aerobic conditions depending on whether an oxide or a zero-valent metal is required. In such a case, there is no separate step of recovering and purifying the particles. This is done for a period of between 8 and 72 hours. More preferably the incubation period is from 12 to 48 hours.
1 5 In a preferred embodiment, the final concentration of the transition metal or transition metals is between 0.5 and 40% by mass of the magnetic nanoparticles, and is preferably in the range of 1 and 20%. More preferably the final concentration of the transition metal or metals is in the range of 2 to 10% by mass, and most preferably it is in the range of 5 to 10% by mass.
In an embodiment, the source of the catalytic material is one or more transition metal salts. The transition metal salt is in aqueous solution or an aqueous-based solution.
The transition metal salts are reduced in solution by the magnetite to the transition metal itself. The transition metal solution may contain a single transition metal salt or a mixture of transition metal salts. A mixture of transition metal salts may be reacted using a single solution containing more than one transition metal salt, or by using more than one solution each containing a single transition metal salt.
The transition metal salt is a salt of one or more metals selected from the group comprising: palladium, platinum, rhodium, iridium, silver, gold, ruthenium, osmium, nickel and titanium. More preferably the transition metal is one or more selected from palladium, platinum or iridium.
The catalysts of the present invention have a number of advantages. Experimental tests show that the catalysts are more active than transition metal catalysts deposited by anaerobic bacteria in the absence of magnetic nanoparticles or are more active than transition metal colloids. For example, it can be seen from the figures that the palladium-magnetite complex is more active in Heck coupling than palladium which has been deposited using anaerobic bacteria or palladium colloids.
The use of more than one transition metal salt allows the production of nanoparticle alloys on the surface of the magnetic particles. X-ray diffraction provides evidence that alloys are being created on the surface of the magnetic particles rather than simply effecting deposition of two individual metals.
Two routes are possible for the biological synthesis of nano-scale magnetite. First, magnetotactic bacteria are able to synthesise intracellular crystals of single domain magnetite which are used to orientate the cell with the Earth's magnetic field, helping the organism guide itself to the sediment water interface. Although minor levels of substitution can be achieved using these organisms, growth yields and indeed the final yields of intracellular magnetite are generally low. In contrast, dissimilatory Fe(lll)-reducing bacteria such as Geobacter species make copious quantities of extracellular nano-scale magnetite through the respiration of poorly crystalline Fe(lll) oxides and oxyhydroxides. These specialist anaerobic bacteria live in environments depleted of oxygen and therefore conserve energy for growth by transferring electrons from the oxidation of simple carbon sources such as acetate to Fe(lll) and Mn(IV)-bearing minerals.
The mechanism of this transformation involves the formation of magnetite through the extracellular reduction of the Fe(lll) mineral phase causing the release of soluble Fe(ll), and ultimately resulting in complete recrystallization of the amorphous mineral into a new potentially high-value magnetic phase. Most importantly these enzyme-driven reactions take place rapidly at ambient pressures and temperatures, using inexpensive feedstocks.
Previously Fe(lll)-oxyhydroxides converted to magnetite by Geobacter sulfurreducens have also been altered to include significant quantities of additional transition metals such as Co and Ni forming nano-ferrites thus optimising magnetic properties for different commercial applications and also for bioremediation through the reduction of toxic metals and radionuclides such as Cr(Vl) and Tc(Vll), and reductive dehalogenations of xenobiotic organics contaminants. These nano-scale biomagnetite crystals could also be very useful as support materials in accordance with the present invention for industrial catalysts.
The present invention enables biomagnetic nanoparticles based on iron minerals to be prepared by microbial reduction which can then be functionalised with one or more transition metals to produce a nanoscale magnetic catalytic particle. For example, using palladium and magnetite we are able to produce bio-magnetite functionalised with palladium nanoparticles with a minimal level of downstream processing.
The catalyst can then be used in the Heck coupling of a range of materials such as, for example, iodobenzene with styrene or ethyl acrylate. Heck chemistry is of wide-ranging industrial importance as it provides one of the simplest routes to substituted olefins, more traditionally via a palladium-phosphine catalyst although a large amount of literature is devoted to the study of a variety of different catalysts for these reactions.
We also believe that this simple, energy efficient route to novel biologically-derived heterostructures can be harnessed to make a wide range of functionalised nanocatalysts for contrasting applications.
The following Figures are illustrative of the invention. Fig 1 shows images of palladium nanoparticles on biomagnetite. Fig 2 is a XPS trace that shows that the palladium is metallic and that any oxide component is negligible. Fig 3 shows the results for Heck coupling of iodobenzene and styrene using palladium-magnetite. Fig 4 shows the Heck coupling of iodobenzene and ethyl acrylate using palladium magnetite. Fig 5 shows the size and shape of gold nanoparticles supported on biogenic magnetite. Fig 6 shows XRD results for nanoparticle alloys on the surface of magnetite. The alloy is a palladium gold alloy. Fig 7 shows the X-ray diffraction results which are indicative of the formation of a palladium gold alloy rather than the deposition of palladium and gold as separate entities. Figure 8. TEM images of Pd-coated biogenic magnetite. Image b contains annotation indicating where EDX spectra were taken. Figure 9. (a) X-ray diffraction (XRD) and (b) selected area diffraction (SAD) pattern for Pd-coated biogenic magnetite with reflections labelled in black (magnetite) and grey (palladium). Figure 10. X-ray magnetic circular dichroism spectra for (a) biogenic magnetite and (b) Pd-coated biogenic magnetite. Figure 11. XPS of Pd 3d of biogenic Pd-magnetite before (a) and after (b) use as a catalyst in the Heck coupling of iodobenzene and styrene.
The basic ingredients required for operation of the process of the present invention include a suitable buffer. A redox system is also required to biosynthesise the magnetite and this includes an electron donor (acetate or hydrogen for Geobacter, lactate/f ormate or hydrogen for She wane/Ia and an electron shuttle such as AQDS, humic materials or flavins such as riboflavin. It is also preferable for the microbial cells to be pre-grown to a suitable density. This can be done using conventional procedures and usually takes place on fumarate-containing media (fumarate is an electron acceptor).
Mineral phases that have been successfully used in the process of the present invention can be referred to as iron (III) oxides, oxyhydroxides and oxyhydroxy sulphates, including poorly crystalline phases such as ferrihydrite. Other substrates that have also been used include schwertmannite lepidocrocite akaganeite and feroxyhyte.
Separation techniques used to isolate the magnetic nanoparticles include the use of magnetic separating devices, centrifugation or filtration.
In accordance with another aspect of the present invention, the invention provides magnetic nanoparticles including a conditioning film. The conditioning film helps support the transition metal functionalisation. Thus, the magnetic nanoparticles of the present invention also include a biomolecular coating on the particle which provide the particles with a number of advantageous properties. We have conducted studies using XPS that demonstrate the presence of the biomolecular film. It is possible to show, for example, the presence of nitrogen in the biomolecular film using this technique.
Magnetic nanoparticles that include a conditioning film may be manufactured by a method according to a first aspect of the present invention wherein step (c) does not include purifying the nanoparticles or wherein step (c) does not include extensive purification of the nanoparticles. In other words, the nanoparticles are separated from the culture and the solution containing one or more transition metal salts is added immediately to the nanoparticles.
Alternatively, magnetic nanoparticles that include a conditioning film may be manufactured by a method according to a first aspect of the present invention which further includes an additional step (ci) in between steps (c) and (d). Step (ci) may include the addition of a conditioning film to purified or non-purified nanoparticles.
The principle described below specifically in relation to magnetite can be applied to a number of different sources of iron, including iron waste. In the case of the exemplary preparation of magnetite, the iron source is iron ferrihydrite (amorphous iron (Ill) oxyhdroxide).
Biogenic nano-magnetite was produced by anoxic washed cell suspensions of G. sulfurreducens challenged with Fe(lll)-oxyhydroxide, and electron donor (acetate) and a redox mediator (AQDS). After approximately 24 hours, the Fe(lll)-oxyhydroxide had converted completely to magnetite. Production of a Pd-coated magnetite was completed by adding a solution of NaPdCI4 to the magnetite suspension. Optimization studies suggested that removal of soluble palladium, presumably by Fe(ll)-mediated reduction to Pd(0) on the surface of the magnetite nanoparticles, was rapid and efficient at a range of Pd(ll) concentrations. For further detailed analyses of the material, a bionanomagnetite suspension was prepared to give a 5% Pd loading, by mixing the Pd(ll) solution and magnetite for 12 hours prior to washing in deionised water. No additional ligands were used to functionalise the surface of the magnetite prior to the addition of the solution of Pd(ll). For example, the common and costly practise of first modifying the surface of the carrier with a ligand such as 3-aminopropyl triethoxysilane (APTS) to aid attachment before adding a reducing agent such as hydrogen to convert the Pd to the metallic form was not required in accordance with the process of the invention.
Transmission electron microscope (TEM) images of the material produced by precipitating Pd onto the surface of biogenic magnetite are shown in Fig. 8(a-b). Fig. 8a showed the sample to contain particles of two contrasting sizes while Energy Dispersive X-ray (EDX) analysis of the general area showed the sample to contain approx 3.3 at% Pd. The high-resolution image in Fig. 8b shows a representative sample of two different size particles with the smaller ( 5 nm) attached to the larger (20 nm).
Using spot EDX elemental analysis (labelled on Fig. 8b) on both these particles, and other similar clusters, the larger particles (point 1) were found to contain less than 1 at% Pd whereas the smaller contained 9-10 at% Pd (point 2). Since the Pd-rich particles were smaller than the spot size used for EDX it is thought that the small particles were pure Pd and the larger were the magnetite crystals, indicating that Pd formed smaller nanoparticles on the larger nanoparticles of magnetite. Both small and large particles showed continuous lattice fringes, indicative of well-crystalline single crystals of both materials.
X-ray Diffraction (XRD) and Selected Area Diffraction (SAD) in Fig. 9(a-b) confirmed the presence of magnetite alongside faint reflections due to Pd metal, with no reflections from any other phase. The reflections in the XRD due to Pd are broader than those due to magnetite most likely as the particle size is smaller, as confirmed by TEM analyses (e.g. Fig. 8b). Crystallite size was estimated by applying the Scherrer equation to the (311) peak of magnetite and the (111) peak of Pd in Fig. 9 and the results gave a mean crystallite size of 27.2 nm for magnetite and 5.4 nm for Pd, again in good agreement with the TEM images.
The Fe L-edge and K-edges of magnetite were collected to give the X-ray Magnetic Circular Dichroism (XMCD) and Extended X-ray Absorption Fine Structure (EXAFS), respectively, before and after addition of Pd. It is speculated that either the amount of Pd bonded directly to Fe is too low for detection or the Pd is bonded to magnetite via an 0 bridging atom rather than directly to Fe. XMCD, a technique that can differentiate between Fe2 and Fe3 as well as between Td and Oh coordinated Fe in magnetite, was used to analyse the surface of the magnetite (top 4.5 nm). Fig. lOa shows the Fe L-edge difference spectrum for biogenic magnetite with and without Pd that after fitting gives Fe2/Fe3 ratio of 0.55, indicating an excess of Fe2 compared to stoichiometric magnetite which would give a ratio of 0.50. After the addition of Pd it was found that there was a small reduction in the amount of Fe2 at the surface, forming a spinel that was closer to stoichiometric magnetite with an Fe2/Fe3 ratio of 0.53. This indicates that the magnetite was partially oxidised during Pd(0) nanoparticle formation, possibly during reduction of the Pd(ll) by Fe(ll) at the surface in agreement with the EXAFS data. Fe 2p spectra (Fig. 11 b) collected using X-ray Photoelectron spectroscopy (XPS) before and after addition of Pd to the magnetite also indicates that the surface Fe2:Fe3 ratio decreases as Pd(ll) is introduced, indicating that the sample was oxidised at the surface.
In addition an XPS wide scan indicates that the surface of these nanoparticles has an Fe:Pd ratio of 1:0.22 (Fig. 11 a).
EXAFS and XPS were also used to investigate the structure of the Pd particles deposited on the surface of the magnetite. These show the main peak to be Pd(0) and the weak peak to indicate a second phase that is possibly PdO or Pd02. The Pd-oxide could be due to either partial oxidation of the surface of the metallic Pd clusters or could be from the bonding of the Pd nanoparticles to the magnetite via oxygen, which supports the hypothesis that the Pd is attached to the magnetite by a bond to the nearest 0 and not Fe ion.
This sample was then tested in the Heck Reaction for coupling iodobenzene to styrene and ethyl acrylate and found to be better than commercially available colloidal palladium catalyst. ICP-AES analysis of the supernatant from the Heck reaction found that there was negligible loss of Pd or Fe to the solution.
The experimental results show a simple method for producing highly catalytically active 1 0 nanoparticles using a low-cost synthesis route.
G. sulfurreducens was obtained from our laboratory culture collection and grown under strictly anaerobic conditions at 30°C in modified fresh water medium as described previously in [quote ref 14]. Sodium acetate (20 mM) and fumarate (40 mM) were provided as the electron donor and acceptor, respectively. However, a range of electron donors and acceptors could be used. All manipulations were done under an atmosphere of N2-C02 (80:20). Late log-phase cultures of G. sulfurreducens was harvested by centrifugation at 4920 g for 20 minutes and washed twice in carbonate buffer (NaHCO3; mM, pH 7.1) under N2-C02 (80:20) gas prior to use. Aliquots of the washed cell suspension (1.5 ml) were added to sealed anaerobic bottles containing 28.5 ml bicarbonate buffer (30 mM), poorly crystalline Fe(lll) oxide (50 mM) (prepared according to [quote ref 15]), sodium acetate (20 mM) and an electron shuttling compound anthraquinone-2,6-disulfonate (10 tiM) to increase the rate of Fe(lll) reduction. The final concentration of bacteria corresponded to 0.2 mg protein per mL. Bottles were incubated in the dark at 20°C for two days after which magnetite had been produced. The resultant magnetite was washed twice in degassed deionised water and then resuspended in water using magnetic separation to remove the supernatant. An aliquot of a solution of sodium tetrachloropalladate (Na2PdCI4, Sigma-Aldrich CAS no. 13820-53-6) was then added so that the final concentration of Pd was 5% by mass of the magnetite. The magnetite suspension was left overnight in a shaking incubator at 150 rpm and 20°C.
The sample was then washed again using degassed, distilled deionised water twice before drying under anoxic conditions.
X-ray absorption spectra (XAS) were collected for the Fe and Pd Kedges on beamline 9.3 at the Synchrotron Radiation Source (SRS), Daresbury Laboratory.
XAS for X-ray magnetic circular dichroism (XMCD) were collected on beamline 4.0.2 at the Advanced Light Source (ALS), Berkeley, CA, using the octopole magnet endstation.
Transmission electron microscopy (TEM) was conducted using a commercial instrument (Phillips/FEI CM200) equipped with a Field Emission Gun (FEG), EDX system (Oxford Instruments UTW ISIS) and a Gatan Imaging Filter (GIF). All TEM images presented here are bright-field images obtained using an operating beam voltage of 200 keV.
Selected Area Electron Diffraction (SAED) patterns were acquired using an appropriate diffraction aperture.
X-ray photoelectron spectroscopy (XPS) data were recorded using a commercial system (Kratos Axis Ultra) employing a monochromated Al Ka X-ray source and an analyser pass energy of 20eV, resulting in a total energy resolution of ca. 0.9eV.

Claims (13)

  1. CLAIMS1. A process for preparing magnetite nanoparticles incorporating one or more transition metal elements, the process comprising the steps: (a) exposing a compound or mixture of compounds as a source of ferric iron to a microbial system in a culture comprising a dissimilatory iron reducing bacteria (DIRB) and/or a sulphate reducing bacteria (SRB) in the presence of a redox mediator, (b) incubating the resulting mixture in a culture under anaerobic conditions to produce biogenic nanoparticles of an iron-based mineral, (c) separating the nanoparticles from the culture and optionally purifying the nanoparticles, (d) adding a solution containing one or more transition metal salts to a suspension of the nanoparticles to produce catalytic nanoparticles, and (e) recovering the catalytic nanoparticles.
  2. 2. A process as claimed in claim 1, wherein the nanoparticles are magnetic.
  3. 3. A process as claimed in claim 1 or 2, wherein the source of iron can be an iron-based compound or a mixture of iron-based compounds which are capable of reacting with the bacteria to form magnetic nanoparticles.
  4. 4. A process as claimed in any of claims I to 3, wherein the source of iron is ferrihydrite.
  5. 5. A process as claimed in any preceding claim, wherein step (c) does not include purifying the nanoparticles.
  6. 6. A process as claimed in any preceding claim, wherein the redox mediator is an electron donor and an electron acceptor.
  7. 7. A process as claimed in any preceding claim, wherein the bacterium is a DIRB, or wherein the bacterium is preferably a sulphate-reducing bacteria.
  8. 8. A process as claimed in claim 7, wherein the dissimilatory iron-reducing bacteria is Geobacter, Shewanella or Geothrix, or wherein the sulphate-reducing bacteria is Desulfovibrio, Desulfococcus, Desulfobacter, Desulfobulbus or Desulfobotulus.
  9. 9. A process as claimed in any preceding claim, wherein the transition metal solution may contain a single transition metal salt or a mixture of transition metal salts.
  10. 10. A process as claimed in claim 9, wherein the transition metal salt is a salt of one or more metals selected from the group comprising: palladium, platinum, rhodium, iridium, silver, gold, ruthenium, osmium, nickel and titanium.
  11. 11. A process substantially as hereinbefore described.
  12. 12. A magnetic nanoparticle including a conditioning film, which is a biomolecular coating on the particle derived from the bacterium. a)Q
  13. 13. A magnetic nanoparticle substantially as hereinbefore described. a)
GB0816119A 2008-09-04 2008-09-04 Bacterial process for the preparation metal-doped magnetite nanoparticles Withdrawn GB2464998A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB0816119A GB2464998A (en) 2008-09-04 2008-09-04 Bacterial process for the preparation metal-doped magnetite nanoparticles

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB0816119A GB2464998A (en) 2008-09-04 2008-09-04 Bacterial process for the preparation metal-doped magnetite nanoparticles

Publications (2)

Publication Number Publication Date
GB0816119D0 GB0816119D0 (en) 2008-10-15
GB2464998A true GB2464998A (en) 2010-05-12

Family

ID=39888762

Family Applications (1)

Application Number Title Priority Date Filing Date
GB0816119A Withdrawn GB2464998A (en) 2008-09-04 2008-09-04 Bacterial process for the preparation metal-doped magnetite nanoparticles

Country Status (1)

Country Link
GB (1) GB2464998A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EA018956B1 (en) * 2011-03-24 2013-12-30 Федеральное Государственное Автономное Образовательное Учреждение Высшего Профессионального Образования "Сибирский Федеральный Университет" Method of producing stable aqueous sol based on ferrihydrite nanoparticles
CN105780067A (en) * 2016-02-01 2016-07-20 中国科学院生态环境研究中心 Method for in-situ synthesis of three-dimensional nanometer palladium catalyst layer through electrode activity biological membrane and application
WO2016203121A1 (en) * 2015-06-17 2016-12-22 Nanobacterie Apyrogenic preparation containing nanoparticles synthesised by magnetotactic bacteria for medical or cosmetic applications.
CN107287129A (en) * 2016-04-01 2017-10-24 兰州大学 One plant can make heavy metal settle sulfate reducing bacteria and its application
CN109811011A (en) * 2019-01-31 2019-05-28 内蒙古科技大学 A kind of method of the hollow micro-nano ferroso-ferric oxide of biosynthesis

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106865935A (en) * 2017-01-13 2017-06-20 大连理工大学 Using anthraquinone 2,6 disulfonic acid salt(AQDS)The method for promoting excess sludge methane phase
CN115528262A (en) * 2022-09-29 2022-12-27 中南大学 Microorganism-sodium alginate-based porous composite palladium-carbon catalyst and preparation method thereof
CN115608376B (en) * 2022-10-14 2024-02-20 中南大学 Palladium-iron nanomaterial based on saccharomycete residues as well as preparation method and application thereof
CN117904212A (en) * 2024-03-01 2024-04-19 中山大学 Biological preparation method and application of zero-valent iron sulfide

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060014261A1 (en) * 1999-10-28 2006-01-19 Phelps Tommy J Fermentative process for making inorganic nanoparticles

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060014261A1 (en) * 1999-10-28 2006-01-19 Phelps Tommy J Fermentative process for making inorganic nanoparticles

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EA018956B1 (en) * 2011-03-24 2013-12-30 Федеральное Государственное Автономное Образовательное Учреждение Высшего Профессионального Образования "Сибирский Федеральный Университет" Method of producing stable aqueous sol based on ferrihydrite nanoparticles
WO2016203121A1 (en) * 2015-06-17 2016-12-22 Nanobacterie Apyrogenic preparation containing nanoparticles synthesised by magnetotactic bacteria for medical or cosmetic applications.
FR3037581A1 (en) * 2015-06-17 2016-12-23 Nanobacterie APYROGEN PREPARATION CONTAINING NANOPARTICLES SYNTHESIZED BY MAGNETOTACTIC BACTERIA FOR MEDICAL OR COSMETIC APPLICATIONS
CN107708735A (en) * 2015-06-17 2018-02-16 纳米细菌公司 The apyrogenetity preparation for being used for medical treatment or cosmetic applications comprising the nano-particle synthesized by magnetotactic bacteria
US10391122B2 (en) 2015-06-17 2019-08-27 Nanobacterie Non-pyrogenic preparation comprising nanoparticles synthesized by magnetotactic bacteria for medical or cosmetic applications
US10980833B2 (en) 2015-06-17 2021-04-20 Nanobacterie Non-pyrogenic preparation comprising nanoparticles synthesized by magnetotactic bacteria for medical or cosmetic applications
US11759478B2 (en) 2015-06-17 2023-09-19 Nanobacterie Non-pyrogenic preparation comprising nanoparticles synthesized by magnetotactic bacteria for medical or cosmetic applications
CN105780067A (en) * 2016-02-01 2016-07-20 中国科学院生态环境研究中心 Method for in-situ synthesis of three-dimensional nanometer palladium catalyst layer through electrode activity biological membrane and application
CN107287129A (en) * 2016-04-01 2017-10-24 兰州大学 One plant can make heavy metal settle sulfate reducing bacteria and its application
CN107287129B (en) * 2016-04-01 2021-05-28 兰州大学 Sulfate reducing bacteria capable of settling heavy metals and application thereof
CN109811011A (en) * 2019-01-31 2019-05-28 内蒙古科技大学 A kind of method of the hollow micro-nano ferroso-ferric oxide of biosynthesis
CN109811011B (en) * 2019-01-31 2021-07-23 内蒙古科技大学 Method for biologically synthesizing hollow micro-nano ferroferric oxide

Also Published As

Publication number Publication date
GB0816119D0 (en) 2008-10-15

Similar Documents

Publication Publication Date Title
GB2464998A (en) Bacterial process for the preparation metal-doped magnetite nanoparticles
Ali et al. Overview of microbes based fabricated biogenic nanoparticles for water and wastewater treatment
Li et al. Porous Fe2O3 microcubes derived from metal organic frameworks for efficient elimination of organic pollutants and heavy metal ions
Chen et al. Enhanced removal of lead ions from aqueous solution by iron oxide nanomaterials with cobalt and nickel doping
Wu et al. Preferential growth of the cobalt (200) facet in Co@ N–C for enhanced performance in a Fenton-like reaction
Anantharaj et al. Enhancing electrocatalytic total water splitting at few layer Pt-NiFe layered double hydroxide interfaces
Liu et al. Recent advances in removal techniques of vanadium from water: A comprehensive review
Xia et al. Phosphorus removal from diluted wastewaters using a La/C nanocomposite-doped membrane with adsorption-filtration dual functions
Hua et al. Effect of bicarbonate on aging and reactivity of nanoscale zerovalent iron (nZVI) toward uranium removal
Sargazi et al. Ultrasound assisted reverse micelle efficient synthesis of new Ta-MOF@ Fe3O4 core/shell nanostructures as a novel candidate for lipase immobilization
EP2892853B1 (en) Particle for recovering an anion from an aqueous solution
US9138727B2 (en) Iron—nickel core-shell nanoparticles
Wen et al. Amorphous FeNiPt nanoparticles with tunable length for electrocatalysis and electrochemical determination of thiols
Zhou et al. Effect of natural organic matter on the fate of cadmium during microbial ferrihydrite reduction
Qafoku Terrestrial nanoparticles and their controls on soil-/geo-processes and reactions
Paladini et al. The role of cobalt hydroxide in deactivation of thin film Co-based catalysts for sodium borohydride hydrolysis
Kim et al. Conventional and photoinduced radioactive 137Cs removal by adsorption on FeFe, CoFe, and NiFe Prussian blue analogues
JPWO2015049959A1 (en) Method for producing alloy nanoparticles, alloy nanoparticles produced using the same, and catalyst comprising the same
CN114522687B (en) Multicomponent mesogenic nanoparticles, method for the production and use thereof
WO2012161216A1 (en) Complex and uses thereof
Yao et al. Nonprecious bimetallic (Mo, Fe)-N/C nanostructures loaded on PVDF membrane for toxic CrVI reduction from water
Bi et al. Microwave-assisted synthesis of hollow microspheres with multicomponent nanocores for heavy-metal removal and magnetic sensing
Zhang et al. SiO2-assisted synthesis of Fe3O4@ SiO2@ C-Ni nanochains for effective catalysis and protein adsorption
Kumar et al. Functionalized Cu-based metal oxide nanoparticles with enhanced Cd+ 2 adsorption capacity and their ecotoxicity assessment by molecular docking
Okuda et al. Structural analysis of hydroxyapatite coating on magnetite nanoparticles using energy filter imaging and electron tomography

Legal Events

Date Code Title Description
WAP Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1)