WO2002100534A1 - Verfahren zum abbau biologischer und/oder organischer substanzen - Google Patents
Verfahren zum abbau biologischer und/oder organischer substanzen Download PDFInfo
- Publication number
- WO2002100534A1 WO2002100534A1 PCT/EP2002/006260 EP0206260W WO02100534A1 WO 2002100534 A1 WO2002100534 A1 WO 2002100534A1 EP 0206260 W EP0206260 W EP 0206260W WO 02100534 A1 WO02100534 A1 WO 02100534A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- group
- metal catalyst
- catalyst
- temperature
- alloy element
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 20
- 239000000126 substance Substances 0.000 title claims abstract description 18
- 230000015556 catabolic process Effects 0.000 title claims abstract description 7
- 238000006731 degradation reaction Methods 0.000 title claims abstract description 7
- 239000003054 catalyst Substances 0.000 claims abstract description 43
- 229910052751 metal Inorganic materials 0.000 claims abstract description 32
- 239000002184 metal Substances 0.000 claims abstract description 32
- 239000000956 alloy Substances 0.000 claims abstract description 18
- 229910045601 alloy Inorganic materials 0.000 claims abstract description 18
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000001301 oxygen Substances 0.000 claims abstract description 14
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 14
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 229910052802 copper Inorganic materials 0.000 claims abstract description 9
- 229910052742 iron Inorganic materials 0.000 claims abstract description 9
- 229910052759 nickel Inorganic materials 0.000 claims abstract description 9
- 239000007800 oxidant agent Substances 0.000 claims abstract description 9
- 229910052804 chromium Inorganic materials 0.000 claims abstract description 7
- 239000007789 gas Substances 0.000 claims abstract description 7
- 229910052748 manganese Inorganic materials 0.000 claims abstract description 7
- 229910052750 molybdenum Inorganic materials 0.000 claims abstract description 6
- 230000003647 oxidation Effects 0.000 claims abstract description 6
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 6
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 5
- 229910052721 tungsten Inorganic materials 0.000 claims abstract description 5
- 229910052788 barium Inorganic materials 0.000 claims abstract description 4
- 229910052796 boron Inorganic materials 0.000 claims abstract description 4
- 229910052791 calcium Inorganic materials 0.000 claims abstract description 4
- 229910052738 indium Inorganic materials 0.000 claims abstract description 4
- APFVFJFRJDLVQX-UHFFFAOYSA-N indium atom Chemical compound [In] APFVFJFRJDLVQX-UHFFFAOYSA-N 0.000 claims abstract description 4
- 239000007791 liquid phase Substances 0.000 claims abstract description 4
- 229910052749 magnesium Inorganic materials 0.000 claims abstract description 4
- 229910052712 strontium Inorganic materials 0.000 claims abstract description 4
- 229910052720 vanadium Inorganic materials 0.000 claims abstract description 4
- 229910052733 gallium Inorganic materials 0.000 claims abstract description 3
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 27
- 238000004659 sterilization and disinfection Methods 0.000 claims description 12
- 230000008569 process Effects 0.000 claims description 11
- 238000005275 alloying Methods 0.000 claims description 10
- 239000000203 mixture Substances 0.000 claims description 4
- 229910052783 alkali metal Inorganic materials 0.000 claims description 2
- 150000001340 alkali metals Chemical class 0.000 claims description 2
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims 1
- 229910052792 caesium Inorganic materials 0.000 claims 1
- 150000001875 compounds Chemical class 0.000 claims 1
- 229910052744 lithium Inorganic materials 0.000 claims 1
- 229910052700 potassium Inorganic materials 0.000 claims 1
- 229910052701 rubidium Inorganic materials 0.000 claims 1
- 229910052708 sodium Inorganic materials 0.000 claims 1
- 239000000470 constituent Substances 0.000 abstract description 3
- 230000001954 sterilising effect Effects 0.000 abstract description 2
- 230000001590 oxidative effect Effects 0.000 abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 18
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 12
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 12
- 239000003139 biocide Substances 0.000 description 9
- 238000006243 chemical reaction Methods 0.000 description 8
- 244000052616 bacterial pathogen Species 0.000 description 7
- 239000010949 copper Substances 0.000 description 7
- RBTBFTRPCNLSDE-UHFFFAOYSA-N 3,7-bis(dimethylamino)phenothiazin-5-ium Chemical compound C1=CC(N(C)C)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 RBTBFTRPCNLSDE-UHFFFAOYSA-N 0.000 description 6
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 6
- 229960000907 methylthioninium chloride Drugs 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- 239000002351 wastewater Substances 0.000 description 6
- 239000011651 chromium Substances 0.000 description 5
- 239000011572 manganese Substances 0.000 description 5
- 230000008859 change Effects 0.000 description 4
- 230000007797 corrosion Effects 0.000 description 4
- 238000005260 corrosion Methods 0.000 description 4
- 150000002500 ions Chemical class 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 3
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229910001385 heavy metal Inorganic materials 0.000 description 3
- TUJKJAMUKRIRHC-UHFFFAOYSA-N hydroxyl Chemical compound [OH] TUJKJAMUKRIRHC-UHFFFAOYSA-N 0.000 description 3
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 3
- 239000011733 molybdenum Substances 0.000 description 3
- 150000002894 organic compounds Chemical class 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- 238000002835 absorbance Methods 0.000 description 2
- 239000013543 active substance Substances 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 239000008346 aqueous phase Substances 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 230000000149 penetrating effect Effects 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 229910052709 silver Inorganic materials 0.000 description 2
- 239000004332 silver Substances 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- 230000007306 turnover Effects 0.000 description 2
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 208000001348 Chloracne Diseases 0.000 description 1
- 241001101998 Galium Species 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 239000012736 aqueous medium Substances 0.000 description 1
- 239000003899 bactericide agent Substances 0.000 description 1
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 1
- 238000003287 bathing Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000003115 biocidal effect Effects 0.000 description 1
- 230000008033 biological extinction Effects 0.000 description 1
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 1
- 229910052794 bromium Inorganic materials 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000000249 desinfective effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 210000001654 germ layer Anatomy 0.000 description 1
- 238000005324 grain boundary diffusion Methods 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 239000011133 lead Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000002609 medium Substances 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 150000004965 peroxy acids Chemical class 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 238000007669 thermal treatment Methods 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 239000002759 woven fabric Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/889—Manganese, technetium or rhenium
- B01J23/8892—Manganese
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/86—Chromium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/58—Fabrics or filaments
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/722—Oxidation by peroxides
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/42—Nature of the water, waste water, sewage or sludge to be treated from bathing facilities, e.g. swimming pools
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
Definitions
- the invention relates to a process for the degradation of biological and / or organic substances in the liquid phase, in particular for the disinfection of liquids, by bringing an all-metal catalyst into active connection with an oxidizing agent.
- biocides are added, which may contain phosphorus, bromine, chlorine or the like, among other things. These raw materials are considered toxic.
- targeted water poisoning is initially accepted, the residual water remaining after the wastewater purification, or its thickened solid components, having a high potential for pollution.
- DE-C 195 03 865 is a catalyst containing manganese, nickel and copper for the oxidation of water constituents in the presence of hydrogen peroxide and oxygen, which is obtained by thermal treatment of one of 10 to 30 wt .-% copper and 5 to 15 wt .-% % Nickel and 60 to 80% by weight of manganese existing alloy at temperatures of 400 to 1000 ° C in an oxygen-containing atmosphere for a time of 0.25 to 5 hours.
- the catalyst can additionally contain at least one of the elements iron, chromium, silicon, titanium, aluminum, molybdenum, phosphorus or nitrogen in an amount up to a total of 5% by weight.
- CH-A 605 421 is a method for disinfecting bathing, drinking and industrial water with hydrogen peroxide by adding hydrogen peroxide to the water and activating it or catalyzing its decomposition.
- the catalysis is to be carried out by means of a current cell, the electrodes of which are made of copper, iron, graphite, nickel, platinum or silver. A surface treatment of the metal electrodes is not provided. It is also proposed that the addition of at least one substance which contains copper, palladium, iron, nickel, cobalt, lead, cadmium or silver be catalyzed, as a result of which the water to be treated is contaminated with heavy metal ions.
- DE-C 196 10 345 describes a catalyst for the oxidation of waste water contaminants by means of peracids and / or hydrogen.
- An alloy consisting of 10 - 60 mass% Co, 5 - 50 mass% Ni, 5 - 20 mass% W and 5 - 25 mass% Cr is used for Temperatures in the range of 250 ° C to 1250 ° C for a time 0.5 to 3 hours in an oxygen-containing atmosphere thermally treated.
- DE-A 196 30 043 discloses a catalyst containing manganese for the oxidation of impurities in acidic waste water.
- An alloy consisting of (in mass%) 10 - 40% Mn, 10 - 25% Cr and 50 - 70% Fe as the rest is in the temperature range of 300 - 1200 ° C for 0.3 to 3 hours in an oxygen-containing atmosphere thermally treated.
- the catalyst obtained in this way is brought into contact with the waste water containing hydrogen peroxide to be treated for 1 to 60 minutes in that the waste water passes over or through it several times.
- the object of the invention is to provide a method for the degradation of biological and / or organic substances, in particular for the disinfection of liquids, which manages with at least equally good cleaning of the substances, in particular the liquids, without the addition of environmentally harmful biocides.
- heavy metal ions should also be prevented from penetrating into the aqueous phase.
- the full metal catalyst is produced from the following components:
- At least one alloy element of a group I at least one alloy element of a group II, at least one alloy element of a group IM,
- group I includes the alloying elements Ni, Mg, Ba, Ca, Sr, which form divalent oxides below the Tammant temperature in an oxygen-containing atmosphere
- group II includes the alloying elements Cr, B, Al, Ga, indium, which only form trivalent oxides below the Tammant temperature in an oxygen-containing atmosphere
- group III includes the alloying elements Fe, Cu, Mn, Mo, W, V, which in Dependence on temperature and gas atmosphere, especially that
- Oxygen partial pressure form oxides in different oxidation levels, that the full metal catalyst is annealed, and that the full metal catalyst thus obtained is in operative connection with the
- Oxidizing agent and the substance is brought.
- the subject of the invention deals with solid reactions and their interfaces. Reactions in which one or more solid phases are involved have peculiarities due to the relatively rigid fixation of their particles, in the periodic as well as the aperiodic lattice, compared to reaction between gases or liquids that are miscible with one another. In contrast to liquids and gases, solids are rarely in the normal state of thermodynamic equilibrium. Understanding solid reactions requires the elucidation of a whole Sequence of steps, whereby physical processes of substance energy and impulse transport are just as important as the actual chemical reactions. The mass transport takes place as a change of location of individual lattice building blocks either through the lattice or volume diffusion, the grain boundary diffusion and the surface diffusion or through chemical transport via the gas phase.
- the reaction rate is determined by the respective diffusion mechanism and the associated activation energy of the place change process. It is generally only worth mentioning at relatively high temperatures, so that the solid reactions, at least those which take part in the exclusively solid phases, have their domain in the case of thermally stable organic compounds. However, this does not mean that changes of location are not detectable even at relatively low temperatures.
- Tamman defined the temperature of the noticeably beginning change of location, with the Tammant temperatures for metals around one third, for oxides around two thirds and for organic compounds below three quarters of the melting temperature of these substances.
- the degradation of biological and / or organic substances in the liquid phase in particular the disinfection of liquids, can take place without the use of biocides, which in addition to an at least equally good cleaning of the substances, in particular the liquids to be disinfected, thus occurs the use of any biocides can be dispensed with.
- biocides which in addition to an at least equally good cleaning of the substances, in particular the liquids to be disinfected, thus occurs the use of any biocides can be dispensed with.
- CH-A 605 421 also prevents heavy metal ions from penetrating into the aqueous phase.
- the full metal catalyst consists of alloys that are thermodynamically capable of releasing electrons in aqueous systems. This creates a positively charged surface.
- the decisive feature of the full metal catalyst according to the invention is that, despite the positively charged surface, no metal cations leave the metallic composite. This is achieved by forming a special surface structure that only allows electrons to pass through.
- the full metal catalyst according to the invention reacts with hydrogen peroxide.
- a hydroxide anion and a hydroxyl radical are formed from one molecule of hydrogen peroxide by taking up an electron.
- the full metal catalyst is charged positively, with negatively charged germs now accumulating on the catalyst surface.
- Germs interact with the positively charged catalyst surface.
- the germ layers are disassembled on the catalyst surface with the help of hydrogen peroxide. This releases a large amount of surface-active substances.
- the germ dies and disappears from the catalyst surface within a short time.
- the full metal catalyst according to the invention recovers the previously released electrons and the cycle can start again.
- the surface-active substances are now able to replace the biofilms in the water cycle.
- the metabolic processes in the biofilm are considerably disturbed, whereby the detached components die off or are removed from the circuit by filter stages or blowdown.
- Group I forming the full metal catalyst is based on the following alloying elements: nickel, magnesium, barium, calcium, strontium.
- the group II forming the full metal catalyst is based on the following alloying element: chromium, boron, aluminum, galium, indium.
- Group III is essentially based on the following alloying elements: iron, copper, manganese, molybdenum, tungsten and vanadium.
- the alloying elements on which the latter group III is based can form oxides of different valences depending on the temperature and gas atmosphere, in particular the oxygen partial pressure.
- iron can be bivalent or trivalent
- manganese can be bivalent, trivalent or tetravalent
- molybdenum can be trivalent, tetravalent, pentavalent or hexavalent.
- the full metal catalyst which is present in tempered form, can be doped on the surface with alkali metals.
- the full metal catalyst is in the form of wire, sheet metal, foil or foam, in the form of knitted fabrics, woven fabrics, honeycomb moldings, structured packings or the like.
- the number of bacteria is determined before the start and after the 3 h.
- the disinfection rate is:
- KZ ° KZi number of bacteria after 30 min
- the catalysts of the invention consistently showed activities in the methylene blue test of over 90% and in the disinfection test a disinfection rate of at least 3 powers of ten (99.9%).
- the correspondingly selected comparison samples also showed a certain effect in both tests, but both samples showed a tendency to corrosion that was too high for practical use. But while with Copper had the intended tests carried out, the corrosion stresses in the normal steel were so pronounced after only a few hours that the tests could only be evaluated to a limited extent.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Catalysts (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10128129A DE10128129B4 (de) | 2001-06-09 | 2001-06-09 | Verfahren zum Abbau biologischer und/oder organischer Substanzen sowie Vollmetallkatalysator |
DE10128129.3 | 2001-06-09 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2002100534A1 true WO2002100534A1 (de) | 2002-12-19 |
Family
ID=7687815
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2002/006260 WO2002100534A1 (de) | 2001-06-09 | 2002-06-07 | Verfahren zum abbau biologischer und/oder organischer substanzen |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE10128129B4 (de) |
WO (1) | WO2002100534A1 (de) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP4122894A1 (de) | 2021-07-22 | 2023-01-25 | Newtec Water Systems NV | Verfahren und system zur wasserreinigung |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102005062337B4 (de) * | 2005-12-24 | 2009-04-16 | Mol Katalysatortechnik Gmbh | Verfahren zur Erzeugung von arteigenen, biofilmlösenden Stoffen (Biotensiden) |
DE102006022892B8 (de) * | 2006-05-15 | 2008-04-03 | Mol Katalysatortechnik Gmbh | Verfahren zur Herstellung von Papier |
DE102007061965A1 (de) * | 2007-12-21 | 2009-06-25 | Guggenbichler, Joseph Peter | Reduzierung der mikrobiellen Kontamination in Kühltürmen |
DE102010019389B4 (de) * | 2010-05-04 | 2014-03-13 | Mol Katalysatortechnik Gmbh | Verfahren zur Sanierung von Trinkwasserversorgungssystemen |
CN111558371B (zh) * | 2020-04-20 | 2023-12-15 | 上海海庭环境工程有限公司 | 一种基于陶瓷基与碳基混合体作为载体的催化剂制备方法及配套的平板式臭氧氧化反应器 |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57105287A (en) * | 1980-12-22 | 1982-06-30 | Chiyoda Chem Eng & Constr Co Ltd | Purification of waste water containing polyvinyl alcohol |
JPS58112088A (ja) * | 1981-12-25 | 1983-07-04 | Chiyoda Chem Eng & Constr Co Ltd | ヒドラジン含有廃水の処理法 |
DE19503865C1 (de) * | 1995-02-07 | 1996-04-04 | Krupp Vdm Gmbh | Katalysator zur Oxidation von Abwasserinhaltsstoffen |
DE19610345C1 (de) * | 1996-03-18 | 1997-11-20 | Krupp Vdm Gmbh | Katalysator zur Oxidation von Abwasserverunreinigungen mittels Persäuren und/oder Wasserstoffperoxid |
DE19630043A1 (de) * | 1996-07-25 | 1998-01-29 | Krupp Vdm Gmbh | Manganhaltiger Katalysator zur Oxidation von Verunreinigungen in sauren Abwässern |
DE19634527A1 (de) * | 1996-08-27 | 1998-03-05 | Krupp Vdm Gmbh | Verfahren zur Reinigung schadstoffhaltiger Abwässer mittels Zugabe von organischen Persäuren und/oder Peroxoverbindungen |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CH605421A5 (en) * | 1976-04-02 | 1978-09-29 | Schweizerische Sodafabrik | Disinfecting water using hydrogen peroxide |
DE19700164C2 (de) * | 1997-01-07 | 1999-01-07 | Krupp Vdm Gmbh | Verwendung eines Vollmetallkatalysators für den oxidativen Abbau von organischen Verbindungen |
-
2001
- 2001-06-09 DE DE10128129A patent/DE10128129B4/de not_active Expired - Fee Related
-
2002
- 2002-06-07 WO PCT/EP2002/006260 patent/WO2002100534A1/de not_active Application Discontinuation
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57105287A (en) * | 1980-12-22 | 1982-06-30 | Chiyoda Chem Eng & Constr Co Ltd | Purification of waste water containing polyvinyl alcohol |
JPS58112088A (ja) * | 1981-12-25 | 1983-07-04 | Chiyoda Chem Eng & Constr Co Ltd | ヒドラジン含有廃水の処理法 |
DE19503865C1 (de) * | 1995-02-07 | 1996-04-04 | Krupp Vdm Gmbh | Katalysator zur Oxidation von Abwasserinhaltsstoffen |
DE19610345C1 (de) * | 1996-03-18 | 1997-11-20 | Krupp Vdm Gmbh | Katalysator zur Oxidation von Abwasserverunreinigungen mittels Persäuren und/oder Wasserstoffperoxid |
DE19630043A1 (de) * | 1996-07-25 | 1998-01-29 | Krupp Vdm Gmbh | Manganhaltiger Katalysator zur Oxidation von Verunreinigungen in sauren Abwässern |
DE19634527A1 (de) * | 1996-08-27 | 1998-03-05 | Krupp Vdm Gmbh | Verfahren zur Reinigung schadstoffhaltiger Abwässer mittels Zugabe von organischen Persäuren und/oder Peroxoverbindungen |
Non-Patent Citations (2)
Title |
---|
PATENT ABSTRACTS OF JAPAN vol. 006, no. 191 (C - 127) 30 September 1982 (1982-09-30) * |
PATENT ABSTRACTS OF JAPAN vol. 007, no. 213 (C - 187) 20 September 1983 (1983-09-20) * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP4122894A1 (de) | 2021-07-22 | 2023-01-25 | Newtec Water Systems NV | Verfahren und system zur wasserreinigung |
Also Published As
Publication number | Publication date |
---|---|
DE10128129A1 (de) | 2002-12-19 |
DE10128129B4 (de) | 2012-07-19 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE69730433T2 (de) | Selbstregulierende zusammensetzung zur wasserreinigung | |
DE3030476A1 (de) | Verfahren zur desinfektion eines bakterien enthalt enden waessrigen mediums | |
EP0113060B2 (de) | Verfahren zur Entfernung von manganhaltigen Inkrustationen aus zur Wasserversorgung betriebenen Einrichtungen | |
EP0604904A1 (de) | Verfahren zur Abwasserbehandlung durch chemische Oxidation | |
DE2728106A1 (de) | Mikrobiozides produkt | |
WO1984003274A1 (en) | Method for producing a modified aqueous chlorite solution, solution produced thereby and utilization thereof | |
DE10201089A1 (de) | Verfahren zum Entkeimen und Reinigen von wasserführenden Systemen, insbesondere in Schwimm- und Badebeckenanlagen, und Vorrichtung für dessen Durchführung | |
DE102019216111A1 (de) | Konversionsmaterialien zur elektrochemischen wasserenthärtung | |
DE102008036369B4 (de) | Verfahren zur Eliminierung von Biofilmen | |
CH605421A5 (en) | Disinfecting water using hydrogen peroxide | |
DE10128129B4 (de) | Verfahren zum Abbau biologischer und/oder organischer Substanzen sowie Vollmetallkatalysator | |
EP1006085A2 (de) | Verfahren zur Schwimmbadwasseraufbereitung | |
DE69212736T2 (de) | Verfahren und Anlage für die Denitrifikation von Wasser mit metallischem Eisen | |
DE3610061A1 (de) | Verfahren zur aktivierung von wasserstoffperoxid auf elektrochemischem wege | |
DE60128342T2 (de) | Verwendung von ozonierten lösungen von tetrasilber tetraoxide | |
DE3687269T2 (de) | Verfahren zur behandlung von fluessigkeiten. | |
DE2222853A1 (de) | Verfahren zur Behandlung von phenolhaltigen Industrieabwaessern | |
DE102005050806A1 (de) | Verfahren zur katalysierten oxidativen Abwasserbehandlung | |
WO2002100540A1 (de) | Vollmetallischer oxidationskatalysator | |
DE10015453C2 (de) | Verfahren und Vorrichtung zum Erzeugen von Reinstwasser | |
DE102006022892B3 (de) | Verfahren zur Herstellung von Papier | |
DE2226434A1 (de) | Verfahren zum herstellen von wasserstoffperoxid | |
EP0423137B1 (de) | Wässrige lösung zur oxidation, entkeimung und desodorierung sowie verfahren zur herstellung dieser lösung | |
DE10154665A1 (de) | Verfahren zum Abbau biologischer und/oder organischer Substanzen | |
EP4112565A1 (de) | Verfahren zur kontrolle des wachstums von mikroorganismen |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ OM PH PL PT RO RU SD SE SG SI SK SL TJ TM TN TR TT TZ UA UG US UZ VN YU ZA ZM ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
REG | Reference to national code |
Ref country code: DE Ref legal event code: 8642 |
|
122 | Ep: pct application non-entry in european phase | ||
NENP | Non-entry into the national phase |
Ref country code: JP |
|
WWW | Wipo information: withdrawn in national office |
Country of ref document: JP |