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AP1160A - Product for bactericidal treatment of fluids. - Google Patents

Product for bactericidal treatment of fluids. Download PDF

Info

Publication number
AP1160A
AP1160A APAP/P/1999/001694A AP9901694A AP1160A AP 1160 A AP1160 A AP 1160A AP 9901694 A AP9901694 A AP 9901694A AP 1160 A AP1160 A AP 1160A
Authority
AP
ARIPO
Prior art keywords
product
metal
porous support
silver
specific surface
Prior art date
Application number
APAP/P/1999/001694A
Other versions
AP9901694A0 (en
Inventor
Claude Charles Andre Laure
Laifa Boufendi
Original Assignee
Gallion Herve
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=25686156&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=AP1160(A) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Priority claimed from CH93497A external-priority patent/CH691592A5/en
Priority claimed from CH224297A external-priority patent/CH691683A5/en
Application filed by Gallion Herve filed Critical Gallion Herve
Publication of AP9901694A0 publication Critical patent/AP9901694A0/en
Application granted granted Critical
Publication of AP1160A publication Critical patent/AP1160A/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/50Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Chemical Or Physical Treatment Of Fibers (AREA)

Abstract

The invention concerns a product for the bacterial treatment of fluids, characterised in that it consists almost exclusively of a porous support with inner and outer specific surface determined according to needs, for instance activated carbon and of a metal, for instance silver, covering said specific surface in a thin layer substantially uniform over the whole specific, said metal being bound to the porous support by strong bonds such as covalent bonds. The product is obtainable in a cold plasma reactor.

Description

Product for the bactericidal treatment of fluids
Products are known for the bactericidal treatment of water, consisting · of active carbon impregnated with silver in the form of salts obtained by immersing the carbon in a solution of silver nitrates .
Such a product has drawbacks: salting-out of nitrates and salting-out of silver. This is because the impregnation does not make it possible to obtain sufficient bonding between the silver and the carbon and salting-out is inevitable.
The use of this product in the field of potable O water is therefore limited because the concentration of dissolved silver is limited to 0.01 ppm.
In the laboratory, it is known for active ? carbon to be hot metallized with metallic silver in a £“*· chamber in which a very high vacuum has been created.
In this chamber, the silver is evaporated in order to be able to penetrate the carbon. This process allows good diffusion of the silver into the pores of the carbon but the poor bonding of the silver to the carbon results in salting-out of the dissolved silver. The internal structure of the active carbon is completely upset and exhibits significant pollution. This product obtained is more friable and becomes spent with the passage of water. This application does not allow a stable product to be obtained and the manufacture of this product is very difficult, since it takes a long time to obtain the vacuum, and therefore not industrializable.
APO 0 116 0
The object of the present invention is to propose a product which, after treatment, has a much greater bactericidal and bacteriostatic power than the known products and is virtually free of any pollution. Since the bactericidal power depends on the effective surface area of the product, the latter must have a very high useable active surface area.
The product for the bactericidal treatment according to the invention is distinguished by the fact that it consists almost exclusively, on the one hand, of a porous support of defined external and internal specific surface depending on the requirements and, on the other hand, of a metal covering said specific surface as a thin film of approximately ' uniform thickness over the entire specific surface, this metal being bonded to the porous support by strong bonding of the covalent-bond type.
Since the metal is strongly bonded to the porous body, there is no risk of it becoming detached and it may be present as a very thin film of the order of 5 to 10 A. The product is very pure.
The porous support may be inorganic or organic, especially synthetic. It may, for example, consist of active carbon, pumice stone, rock, synthetic resin, etc .
The product has a remanence, that is to say a preservability, inhibiting any subsequent contamination of the fluid treated.
The metal may, for example, be pure metallic silver, or copper, nickel or any other metal having the desired effects.
APO01160
Such a product is obtained by injecting the metal, particularly silver, in atomic form into a porous body, for example active carbon powder immersed in a plasma.
Two examples of how to obtain a product according to the invention, consisting of active carbon and of silver, will be described below.
Example 1:
The active carbon, in powder form, was treated in a radiofrequency (13.56 MHz) capacitively coupled discharge in a reactor. The configuration was chosen so as to obtain a high self-polarization voltage across the space-charge sheath.
The gas used in the reactor is argon - with a flow rate of 20 seem corresponding to a pressure of 1 Pa - and the RF electric power coupled to the gas is 400 W. This coupling takes place through an L-type impedance-matching box. Since the space-charge sheath has a width of approximately 1.5 cm, the intensity of the electric field in the sheath is 5.3 104 Vm1. Under these conditions, the density of the plasma is estimated to be 10-10 cm'3.
·*— o
The active carbon powder particles are immersed in the plasma where they are consequently subjected to continuous ion bombardment. The effect of this bombardment is to heat the carbon within the actual plasma. The ion flux reaching the surface of the carbon powder particles is estimated to be 7.3 χ 1012 ions. s'1.
The silver is injected in atomic form into the gas phase. The effect of the plasma is to create anchoring sites for the silver atoms. This anchoring
APO01160 therefore results in strong C-Ag atomic bonding of the covalent-bond type. Thus, the silver aggregates observed in a scanning electronic microscope are firmly bonded to the carbon support and cannot be salted-out.
The physico-chemical analyses carried out on the carbon powder particles thus treated show a proportion of silver of 57% on the external surface of the carbon. As regards the proportion of silver which diffuses into the volume of the carbon, through the pores of the powder particles, this may be modulated by varying the physical parameters of the discharge. In addition, X-ray fluorescence analyses reveal a very negligible, if not zero, level of pollution compared with that of powder particles treated by chemical impregnation means. This result is due to the fact that the carbon powder particles are exposed to a controlled gaseous environment - in the example in question an inert gas - serving only as a carrier for the metallization. Consequently, any pollution is reduced as far as possible.
It should furthermore be pointed out that this process is integrated: no post-treatment, for example thermal post-treatment, is necessary. The powder particles are treated in one go for a well-defined time, for example 20 minutes.
Example II:
Argon is injected via the base of the reactor, by pumping at the top of the reactor. The virgin active carbon, coming from calcined coconuts, and the N6-grade pure silver (that is to say silver having a purity equal to 99.9999%) are placed in powder form in a rotary drum allowing these powders to be bathed in a
AP O 0 116 0 plasma remote from the pumping valve. A high-intensity electric field is created in the reactor in order to levitate the powder particles in the plasma. Under these conditions, the plasma density is approximately 10’9 cm’3 and the electron and ion temperatures are 3 eV and 0.03 eV, respectively.
The active carbon granules are immersed in the plasma and, consequently, subjected to continuous bombardment by silver ions. The effect of this bombardment is to raise the temperature of the carbon to approximately 900°C.
The working parameters are as follows:
- argon flow rate: approx. 9 seem minute);
- working pressure: 2 Pa;
- plasma excitation power: 100 W;
- self-polarization voltage: 1.2 χ 105
- deposition time: 25 minutes
- deposited thickness: 5 to 10 A.
The deposited thickness is nanometric. It corresponds to an internal density of Ag of greater than 4%.
<0 ©
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therefore

Claims (8)

1. A product for the bactericidal treatment of fluids, consisting of a porous support coated with a metal, the metal covering the internal and external specific surface of the porous body wherein the layer is thin and of approximately uniform thickness over the entire specific surface, that is to say also the internal surface of the pores, the metal being bonded to the porous support by strong bonding of the covalent-bond type.
ΑΡ»01160
2. The product as claimed in claim 1, wherein the metal is pure metal silver (Ag°), copper or nickel.
3. The product as claimed in claim 1 or 2, wherein the porous support consists of active carbon, or any other organic or inorganic or synthetic material.
o
4. The product according to one of claims 1 to 3, wherein the thickness of the layer may be modulated.
5. The product as claimed in one of claims 1 to 4, which has a remanence inhibiting any subsequent contamination of the fluid treated.
a
6. A process for obtaining the product as claimed in one of claims 1 to 5, consisting in depositing a metal as a thin film on a porous support by treating the porous support in a cold-plasma reactor by immersing the porous body in an inert-gas plasma, wherein the metal is injected in atomic form into the gas plasma, subjecting the porous support to an electric filed of greater than 5,3 104 Vm'1.
7. The process as claimed in claim 6, wherein the porous support is treated in a reactor having a space-charge sheath with a width equal to approximately 1.5 cm.
8.
The process as claimed in claim 6, wherein the inert gas is argon.
APAP/P/1999/001694A 1997-04-22 1998-04-22 Product for bactericidal treatment of fluids. AP1160A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
CH93497A CH691592A5 (en) 1997-04-22 1997-04-22 Process for obtaining carbon granules impregnated with silver.
CH224297A CH691683A5 (en) 1997-09-23 1997-09-23 Stable bactericidal product for water treatment
PCT/IB1998/000610 WO1998047819A1 (en) 1997-04-22 1998-04-22 Product for bactericidal treatment of fluids

Publications (2)

Publication Number Publication Date
AP9901694A0 AP9901694A0 (en) 1999-12-31
AP1160A true AP1160A (en) 2003-06-30

Family

ID=25686156

Family Applications (1)

Application Number Title Priority Date Filing Date
APAP/P/1999/001694A AP1160A (en) 1997-04-22 1998-04-22 Product for bactericidal treatment of fluids.

Country Status (10)

Country Link
EP (1) EP0979212B1 (en)
CN (1) CN1108994C (en)
AP (1) AP1160A (en)
AT (1) ATE329883T1 (en)
AU (1) AU6848698A (en)
DE (1) DE69834912T2 (en)
ES (1) ES2270512T3 (en)
OA (1) OA11208A (en)
PT (1) PT979212E (en)
WO (1) WO1998047819A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20120138526A1 (en) * 2009-07-13 2012-06-07 Serigne Dioum Product for removing pollutants from a fluid, and method for producing same

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4407865A (en) * 1981-06-09 1983-10-04 Atlantic Richfield Company Process for coating a sterilizing filter material with silver and product formed thereby
FR2585694A1 (en) * 1982-10-15 1987-02-06 Someya Nobuo Water sterilising agent

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2205515Y (en) * 1994-12-23 1995-08-16 国营华北光学仪器厂 Low temperature plasma air purifier
JPH09108654A (en) * 1995-10-16 1997-04-28 Nisshin Steel Co Ltd Activated carbon for purifying water
WO1998015337A2 (en) * 1996-10-10 1998-04-16 Marcel Huder Solid filter

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4407865A (en) * 1981-06-09 1983-10-04 Atlantic Richfield Company Process for coating a sterilizing filter material with silver and product formed thereby
FR2585694A1 (en) * 1982-10-15 1987-02-06 Someya Nobuo Water sterilising agent

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20120138526A1 (en) * 2009-07-13 2012-06-07 Serigne Dioum Product for removing pollutants from a fluid, and method for producing same
US10118838B2 (en) * 2009-07-13 2018-11-06 Serigne Dioum Product for removing pollutants from a fluid, and method for producing same

Also Published As

Publication number Publication date
CN1257463A (en) 2000-06-21
WO1998047819A1 (en) 1998-10-29
ES2270512T3 (en) 2007-04-01
EP0979212A1 (en) 2000-02-16
CN1108994C (en) 2003-05-21
DE69834912T2 (en) 2007-02-15
AU6848698A (en) 1998-11-13
DE69834912D1 (en) 2006-07-27
EP0979212B1 (en) 2006-06-14
PT979212E (en) 2006-11-30
AP9901694A0 (en) 1999-12-31
OA11208A (en) 2003-05-16
ATE329883T1 (en) 2006-07-15

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