EP0191372B1 - Active agent concentrates for alkaline cleaner having two constituents, method for their fabrication and their use - Google Patents
Active agent concentrates for alkaline cleaner having two constituents, method for their fabrication and their use Download PDFInfo
- Publication number
- EP0191372B1 EP0191372B1 EP86101199A EP86101199A EP0191372B1 EP 0191372 B1 EP0191372 B1 EP 0191372B1 EP 86101199 A EP86101199 A EP 86101199A EP 86101199 A EP86101199 A EP 86101199A EP 0191372 B1 EP0191372 B1 EP 0191372B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- alkali metal
- active
- substance concentrates
- contain
- silica
- 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.)
- Expired
Links
- 239000012141 concentrate Substances 0.000 title claims description 45
- 238000000034 method Methods 0.000 title claims description 21
- 239000013543 active substance Substances 0.000 title claims description 20
- 239000000470 constituent Substances 0.000 title claims description 7
- 238000004519 manufacturing process Methods 0.000 title claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical group O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 97
- 239000000243 solution Substances 0.000 claims description 51
- 239000000377 silicon dioxide Substances 0.000 claims description 41
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 30
- 239000006185 dispersion Substances 0.000 claims description 30
- 238000004140 cleaning Methods 0.000 claims description 28
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 22
- 239000002253 acid Substances 0.000 claims description 22
- 150000007513 acids Chemical class 0.000 claims description 18
- 229910052783 alkali metal Inorganic materials 0.000 claims description 15
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims description 15
- 239000007864 aqueous solution Substances 0.000 claims description 14
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 14
- 239000000203 mixture Substances 0.000 claims description 14
- 230000002378 acidificating effect Effects 0.000 claims description 13
- 239000003381 stabilizer Substances 0.000 claims description 13
- 239000004094 surface-active agent Substances 0.000 claims description 13
- 235000019353 potassium silicate Nutrition 0.000 claims description 12
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 11
- -1 builders Substances 0.000 claims description 11
- 239000007789 gas Substances 0.000 claims description 11
- 238000011065 in-situ storage Methods 0.000 claims description 11
- 239000002736 nonionic surfactant Substances 0.000 claims description 11
- 238000001556 precipitation Methods 0.000 claims description 11
- 150000001340 alkali metals Chemical class 0.000 claims description 10
- 238000006243 chemical reaction Methods 0.000 claims description 10
- 239000011707 mineral Substances 0.000 claims description 10
- 238000002360 preparation method Methods 0.000 claims description 9
- 150000003839 salts Chemical class 0.000 claims description 9
- 229910052910 alkali metal silicate Inorganic materials 0.000 claims description 8
- 239000000654 additive Substances 0.000 claims description 7
- 150000008044 alkali metal hydroxides Chemical class 0.000 claims description 7
- 239000002280 amphoteric surfactant Substances 0.000 claims description 7
- 239000003945 anionic surfactant Substances 0.000 claims description 7
- 239000008139 complexing agent Substances 0.000 claims description 7
- 239000011734 sodium Substances 0.000 claims description 7
- 125000000129 anionic group Chemical group 0.000 claims description 6
- 239000003755 preservative agent Substances 0.000 claims description 6
- 229920000388 Polyphosphate Polymers 0.000 claims description 5
- 239000004115 Sodium Silicate Substances 0.000 claims description 5
- 239000001205 polyphosphate Substances 0.000 claims description 5
- 235000011176 polyphosphates Nutrition 0.000 claims description 5
- 238000006386 neutralization reaction Methods 0.000 claims description 4
- 229910052708 sodium Inorganic materials 0.000 claims description 4
- 229910052911 sodium silicate Inorganic materials 0.000 claims description 4
- 230000003139 buffering effect Effects 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 239000011521 glass Substances 0.000 claims description 2
- 229910052751 metal Inorganic materials 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims 4
- 229910002092 carbon dioxide Inorganic materials 0.000 claims 4
- RAHZWNYVWXNFOC-UHFFFAOYSA-N sulfur dioxide Inorganic materials O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 claims 3
- 239000004111 Potassium silicate Substances 0.000 claims 2
- 229910000288 alkali metal carbonate Inorganic materials 0.000 claims 2
- 150000008041 alkali metal carbonates Chemical class 0.000 claims 2
- 229910052936 alkali metal sulfate Inorganic materials 0.000 claims 2
- 239000001569 carbon dioxide Substances 0.000 claims 2
- 229910052681 coesite Inorganic materials 0.000 claims 2
- 229910052906 cristobalite Inorganic materials 0.000 claims 2
- 229910052913 potassium silicate Inorganic materials 0.000 claims 2
- NNHHDJVEYQHLHG-UHFFFAOYSA-N potassium silicate Chemical compound [K+].[K+].[O-][Si]([O-])=O NNHHDJVEYQHLHG-UHFFFAOYSA-N 0.000 claims 2
- 229910052682 stishovite Inorganic materials 0.000 claims 2
- 229910052905 tridymite Inorganic materials 0.000 claims 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 claims 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 claims 1
- 229910052700 potassium Inorganic materials 0.000 claims 1
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 27
- 239000004480 active ingredient Substances 0.000 description 20
- 235000011121 sodium hydroxide Nutrition 0.000 description 9
- 150000001875 compounds Chemical class 0.000 description 7
- IGFHQQFPSIBGKE-UHFFFAOYSA-N Nonylphenol Natural products CCCCCCCCCC1=CC=C(O)C=C1 IGFHQQFPSIBGKE-UHFFFAOYSA-N 0.000 description 6
- 239000003599 detergent Substances 0.000 description 6
- 235000010755 mineral Nutrition 0.000 description 6
- SNQQPOLDUKLAAF-UHFFFAOYSA-N nonylphenol Chemical compound CCCCCCCCCC1=CC=CC=C1O SNQQPOLDUKLAAF-UHFFFAOYSA-N 0.000 description 6
- GJCOSYZMQJWQCA-UHFFFAOYSA-N 9H-xanthene Chemical compound C1=CC=C2CC3=CC=CC=C3OC2=C1 GJCOSYZMQJWQCA-UHFFFAOYSA-N 0.000 description 5
- 229910019142 PO4 Inorganic materials 0.000 description 5
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 5
- 239000012459 cleaning agent Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 235000021317 phosphate Nutrition 0.000 description 5
- 229920001285 xanthan gum Polymers 0.000 description 5
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 4
- 230000007935 neutral effect Effects 0.000 description 4
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910004298 SiO 2 Inorganic materials 0.000 description 3
- QYKIQEUNHZKYBP-UHFFFAOYSA-N Vinyl ether Chemical class C=COC=C QYKIQEUNHZKYBP-UHFFFAOYSA-N 0.000 description 3
- 239000002518 antifoaming agent Substances 0.000 description 3
- 125000004432 carbon atom Chemical group C* 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 229920001577 copolymer Polymers 0.000 description 3
- BNIILDVGGAEEIG-UHFFFAOYSA-L disodium hydrogen phosphate Chemical compound [Na+].[Na+].OP([O-])([O-])=O BNIILDVGGAEEIG-UHFFFAOYSA-L 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 150000004760 silicates Chemical class 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 239000000080 wetting agent Substances 0.000 description 3
- RGHNJXZEOKUKBD-SQOUGZDYSA-N D-gluconic acid Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C(O)=O RGHNJXZEOKUKBD-SQOUGZDYSA-N 0.000 description 2
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 2
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 150000001642 boronic acid derivatives Chemical class 0.000 description 2
- 239000000872 buffer Substances 0.000 description 2
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 2
- 238000005238 degreasing Methods 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 150000002191 fatty alcohols Chemical class 0.000 description 2
- UPBDXRPQPOWRKR-UHFFFAOYSA-N furan-2,5-dione;methoxyethene Chemical compound COC=C.O=C1OC(=O)C=C1 UPBDXRPQPOWRKR-UHFFFAOYSA-N 0.000 description 2
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 230000001376 precipitating effect Effects 0.000 description 2
- 238000005204 segregation Methods 0.000 description 2
- 235000019832 sodium triphosphate Nutrition 0.000 description 2
- 230000006641 stabilisation Effects 0.000 description 2
- 238000011105 stabilization Methods 0.000 description 2
- RLQWHDODQVOVKU-UHFFFAOYSA-N tetrapotassium;silicate Chemical compound [K+].[K+].[K+].[K+].[O-][Si]([O-])([O-])[O-] RLQWHDODQVOVKU-UHFFFAOYSA-N 0.000 description 2
- RYFMWSXOAZQYPI-UHFFFAOYSA-K trisodium phosphate Chemical compound [Na+].[Na+].[Na+].[O-]P([O-])([O-])=O RYFMWSXOAZQYPI-UHFFFAOYSA-K 0.000 description 2
- SZHQPBJEOCHCKM-UHFFFAOYSA-N 2-phosphonobutane-1,2,4-tricarboxylic acid Chemical compound OC(=O)CCC(P(O)(O)=O)(C(O)=O)CC(O)=O SZHQPBJEOCHCKM-UHFFFAOYSA-N 0.000 description 1
- RGHNJXZEOKUKBD-UHFFFAOYSA-N D-gluconic acid Natural products OCC(O)C(O)C(O)C(O)C(O)=O RGHNJXZEOKUKBD-UHFFFAOYSA-N 0.000 description 1
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 1
- DBVJJBKOTRCVKF-UHFFFAOYSA-N Etidronic acid Chemical compound OP(=O)(O)C(O)(C)P(O)(O)=O DBVJJBKOTRCVKF-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 229920001732 Lignosulfonate Polymers 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 229920001938 Vegetable gum Polymers 0.000 description 1
- YDONNITUKPKTIG-UHFFFAOYSA-N [Nitrilotris(methylene)]trisphosphonic acid Chemical compound OP(O)(=O)CN(CP(O)(O)=O)CP(O)(O)=O YDONNITUKPKTIG-UHFFFAOYSA-N 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 229940045714 alkyl sulfonate alkylating agent Drugs 0.000 description 1
- 150000008052 alkyl sulfonates Chemical class 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000007853 buffer solution Substances 0.000 description 1
- 235000019846 buffering salt Nutrition 0.000 description 1
- 150000001244 carboxylic acid anhydrides Chemical class 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 235000011180 diphosphates Nutrition 0.000 description 1
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000000174 gluconic acid Substances 0.000 description 1
- 235000012208 gluconic acid Nutrition 0.000 description 1
- 159000000011 group IA salts Chemical class 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 238000010327 methods by industry Methods 0.000 description 1
- MGFYIUFZLHCRTH-UHFFFAOYSA-N nitrilotriacetic acid Chemical compound OC(=O)CN(CC(O)=O)CC(O)=O MGFYIUFZLHCRTH-UHFFFAOYSA-N 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- HWGNBUXHKFFFIH-UHFFFAOYSA-I pentasodium;[oxido(phosphonatooxy)phosphoryl] phosphate Chemical compound [Na+].[Na+].[Na+].[Na+].[Na+].[O-]P([O-])(=O)OP([O-])(=O)OP([O-])([O-])=O HWGNBUXHKFFFIH-UHFFFAOYSA-I 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- 150000003009 phosphonic acids Chemical class 0.000 description 1
- 229940072033 potash Drugs 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- 235000015320 potassium carbonate Nutrition 0.000 description 1
- 235000011181 potassium carbonates Nutrition 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 230000001698 pyrogenic effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 235000019795 sodium metasilicate Nutrition 0.000 description 1
- 239000001488 sodium phosphate Substances 0.000 description 1
- 235000019351 sodium silicates Nutrition 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- 238000004448 titration Methods 0.000 description 1
- UNXRWKVEANCORM-UHFFFAOYSA-I triphosphate(5-) Chemical compound [O-]P([O-])(=O)OP([O-])(=O)OP([O-])([O-])=O UNXRWKVEANCORM-UHFFFAOYSA-I 0.000 description 1
- LWIHDJKSTIGBAC-UHFFFAOYSA-K tripotassium phosphate Chemical compound [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 description 1
- 229910000406 trisodium phosphate Inorganic materials 0.000 description 1
- 235000019801 trisodium phosphate Nutrition 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
- C11D3/02—Inorganic compounds ; Elemental compounds
- C11D3/04—Water-soluble compounds
- C11D3/08—Silicates
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
- C11D3/02—Inorganic compounds ; Elemental compounds
- C11D3/12—Water-insoluble compounds
- C11D3/124—Silicon containing, e.g. silica, silex, quartz or glass beads
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D2111/00—Cleaning compositions characterised by the objects to be cleaned; Cleaning compositions characterised by non-standard cleaning or washing processes
- C11D2111/10—Objects to be cleaned
- C11D2111/14—Hard surfaces
Definitions
- the invention relates to active ingredient concentrates for alkaline two-component cleaners, processes for their preparation and their use.
- alkaline cleaning agents which contain caustic soda, orthophosphates, condensed phosphates, silicates, complexing agents, wetting agents and optionally corrosion inhibitors, anti-foaming agents and preservatives.
- products containing these constituents are marketed as powdery mixtures and are fed discontinuously to the cleaning bath in powder form, the concentration of the cleaning agent in the bath depending on the application and degree of soiling being between 0.1 and 20% by weight.
- the prerequisite for the effectiveness of the cleaning solution is compliance with the optimal concentration of the cleaning agent components. This can be determined by titration or a conductivity measurement.
- the conductivity measurement for determining the concentration can be carried out in conjunction with an automatic metering of the powder mixture in order to set the desired detergent concentration.
- liquid alkaline detergent concentrates In addition to powder detergents, the use of liquid alkaline detergent concentrates is also known. According to DE-OS 1467605, the prolonged storage of these concentrates can result in losses of polymer phosphates due to hydrolysis and the poor compatibility of the nonionic wetting and antifoam agents and polymer phosphates contained therein with the remaining detergent concentrate in that the detergents are treated with non-ionic wetting agents and / or anti-foaming agents and water-soluble organic acids or active ingredient concentrate containing complexes which form complexes with the water. These acidic or neutral reacting active ingredient concentrates were then processed into alkaline reacting liquid cleaners by adding an excess of alkali. The disadvantage of such a procedure, however, is that silicate-containing cleaning agents could not be produced in this way, since the surfactants used have high builder concentrations, ie. H. large amounts of silicates in the solution are not compatible.
- cleaning concentrates have now been produced from two components, one of which consists essentially of sodium hydroxide solution and the second contains the other cleaning constituents.
- the latter solution can be adjusted to acidic or neutral pH values, an acidic setting having the advantage that all of its components, in particular the surfactants, are particularly readily soluble.
- the disclosed two-component cleaners are characterized in particular by the fact that the acidic or neutral component is an aqueous dispersion of silica which has been prepared from pyrogenic or precipitated silica and optionally contains further constituents, such as phosphoric acid, sulfuric acid, polyphosphates, surfactants, stabilizers and / or preservatives can.
- a silica obtained from water glass by precipitation with sulfuric acid, washing out and drying was used for the preparation of the silica dispersions.
- the process of precipitating silica by acid treatment of water glass and washing and drying the precipitate is very complex and difficult to carry out, especially on an industrial scale.
- the silica obtained in this way is relatively poorly soluble when used in two-component cleaners. Solubility disadvantages arise in particular when the Si0 2 / Na 2 0 ratio in the cleaning bath is greater than 0.3: 1.
- Another disadvantage of using precipitated and isolated silica is the fact that, due to the limited solubility of nonionic surfactants, relatively acidic concentrates have to be prepared in order to ensure adequate stabilization. The consequence of this is that large amounts of alkali metal hydroxide have to be added in order to neutralize or to set a preferably alkaline pH of cleaning solutions.
- the invention therefore relates to active substance concentrates B for alkaline cleaners consisting of two components A and B, one component A of which is a strongly alkaline, predominantly alkali metal hydroxide-containing and used in excess basic aqueous solution and the others re component B is an aqueous dispersion containing silica which, as further additives, comprises anionic, nonionic and / or amphoteric surfactants, builder substances, stabilizers and optionally inorganic mineral acids, complexing agents, preservatives and / or other agents customary in cleaner concentrates, which are characterized in that they contain a silica dispersion which has been adjusted to a pH in the range from 1 to 11 and has been obtained in situ by treating alkali metal silicate solutions with mineral acids or in aqueous solution of its reacting gases.
- the invention also relates to a process for the preparation of active ingredient concentrates B for alkaline cleaners consisting of two components A and B, one component A of which is a strongly alkaline aqueous solution which contains predominantly alkali metal hydroxides and is used in excess, and the other component B of which is an aqueous dispersion comprising silica is which contains, as further additives, anionic, nonionic and / or amphoteric surfactants, builders, stabilizers and optionally inorganic mineral acids, complexing agents, preservatives and / or other agents customary in cleaner concentrates, which is characterized in that alkali metal silicate solutions have a pH between 8 and 11 treated with mineral acids or gases reacting acidic in aqueous solution and the silica dispersions thus obtained, without removing the salts formed during the neutralization, with the active ingredient concentrates B necessary components.
- the invention also relates to the use of such active substance concentrates B in alkaline two-component cleaners for cleaning rigid materials.
- soda and potash water glass solutions are equally well suited.
- aqueous sodium water glass solutions are preferably used, since these are cheaper and accessible in larger quantities.
- undiluted technical water glass solutions are used. This has proven to be advantageous simply because a high active substance content is sought for the active substance concentrates that are formed, which, when using dilute solutions, further process steps to increase the active substance content, such as, for B. concentration of the dispersion by evaporation or filtration, required. These steps become unnecessary if concentrated solutions are used.
- the silica precipitated in situ is prepared by reacting the water glass solutions mentioned with any mineral acids or gases reacting acidic in aqueous solution, e.g. B. HCI, S0 2 and / or C0 2 .
- acidic gases precipitation with CO 2 is preferred.
- mineral acids phosphoric acid and sulfuric acid as well as a mixture of both acids in a weight ratio of 3: 1 to 1: 3 have proven their worth. A ratio of 1: 1 is particularly preferred.
- concentrated acids are advantageously used in order to achieve a high active ingredient content in the silica dispersions formed.
- the pH should be between 8 and 10 and the reaction temperature between 60 and 90 ° C. Under these conditions, silica grades are obtained which provide particularly stable dispersions.
- the specified range of the pH value can advantageously be maintained when working in a buffer system.
- the buffering salts can be placed in aqueous solution for the precipitation reaction or can form in the course of the precipitation reaction.
- the silica When the silica is precipitated from the alkali metal silicate solutions with sulfuric acid, it has proven to be advantageous to present the desired amount of phosphate in the active ingredient concentrate as an aqueous solution and to effect a silica precipitation by simultaneously metering in water glass solution and sulfuric acid.
- the dispersion can be adjusted to the desired pH in the acidic, neutral or alkaline range. With an excess of mineral acid, pH values around 1 can be achieved without this affecting the suitability of the dispersions for alkaline two-component cleaners.
- the dispersions are preferably adjusted alkaline to pH values from 8 to 11, for which purpose aqueous sodium hydroxide solution or potassium hydroxide solution, sodium orthophosphate or potassium orthophosphate, sodium carbonate or potassium carbonate and / or sodium silicates or potassium silicates can be used.
- builder salts which are formed during in-situ precipitation or are added as a buffer are advantageous.
- Builder salts are understood to mean salts which enhance the cleaning action of the surfactants, for example alkali metal orthophosphates and / or polyphosphates, carbonates, borates and / or sulfates.
- alkali metal polyphosphates i. H. Alkali metal pyrophosphate and / or tripolyphosphate.
- surfactants to the silica dispersion.
- Anionic, nonionic and / or amphoteric surfactants are suitable for this purpose.
- there are compounds such as alkylbenzenesulfonates, alkylsulfonates, fatty alcohol sulfates, addition products of ethylene oxide and / or propylene oxide to fatty alcohols, fatty amines and alkylphenols and surface-active ethylene oxide / propylene oxide block polymers.
- the chain lengths of the alkyl radicals are in the range of 8 to 20 C atoms for the compounds mentioned and in the case of the alkylphenols in the range of 6 to 18 C atoms.
- amphoteric surfactants are compounds such as alkyldimethylammonium betaines having 12 to 18 carbon atoms in the alkyl radical.
- the silicas can be precipitated from alkali metal silicate solutions by mineral acids, even in the presence of the surfactants mentioned. This procedure in particular facilitates the stabilization of alkaline dispersions containing nonionic surfactants.
- silica dispersions for the active ingredient concentrates according to the invention can also contain complexing agents, such as. B. alkali metal salts of nitrilotriacetic acid, ethylenediaminetetraacetic acid, gluconic acid, citric acid or phosphonic acids (e.g. hydroxyethane-1, 1-diphosphonic acid, aminotrimethylenephosphonic acid and 2-phosphono-1, 2,4-butanetricarboxylic acid).
- complexing agents such as. B. alkali metal salts of nitrilotriacetic acid, ethylenediaminetetraacetic acid, gluconic acid, citric acid or phosphonic acids (e.g. hydroxyethane-1, 1-diphosphonic acid, aminotrimethylenephosphonic acid and 2-phosphono-1, 2,4-butanetricarboxylic acid).
- Compounds are used as stabilizers which prevent the sedimentation of the silica in the dispersions.
- B. GANTREZ R AN types from GAF Corporation such as copolymers of polymethyl vinyl ethers and maleic anhydride.
- the active ingredient concentrate B contains 10 to 26% by weight, preferably 15 to 25% by weight, particularly preferably 18 to 22% by weight, of silica, calculated as SiO 2 ; 5 to 27% by weight, preferably 8 to 25% by weight, particularly preferably 13 to 24% by weight, builder; 0.5 to 12% by weight, preferably 1 to 10% by weight, particularly preferably 1 to 8% by weight of surfactants; 0.2 to 5% by weight, preferably 0.3 to 3% by weight, particularly preferably 0.5 to 2% by weight, of stabilizers; and 0.5 to 10% by weight, preferably 1 to 8% by weight, particularly preferably 2 to 7% by weight, of complexing agent.
- the alkaline component A for the alkaline two-component cleaners consists essentially of sodium hydroxide solution or potassium hydroxide solution.
- the aqueous alkali metal hydroxide solution is used in excess for two-component cleaners; this is to be understood as an amount of sodium hydroxide solution or potassium hydroxide solution which is sufficient to give the two-component cleaner concentrate a pH greater than 11, preferably greater than 12, after combining the alkaline and the silica dispersion components according to the invention.
- the active ingredient components A and B are mixed in water heated to at least 40 ° C., the silica being converted to water-soluble silicates. PH values greater than 12 are reached.
- the advantage of using the active ingredient concentrates B according to the invention which contain silica precipitated in situ is to be seen in the fact that the dispersions are substantially more soluble under the preparation conditions of a detergent bath than dispersions known from the prior art.
- the use of silica precipitated in situ offers greater freedom in the formulation of the active ingredient concentrates with regard to the other components. For example, the use of alkaline salts as a builder is made possible.
- silica precipitated in situ compared to commercially available precipitated silica
- a complete dissolution of the silica types a) silica precipitated in situ was obtained after 4 minutes at 60 ° C . (stored from Example 1, 3 months) b) Precipitated silica FK 320 after 7 min. DEGUSSA reached.
- Active ingredient concentrates are:
- Example 5 In comparison, the dispersion (f) of Example 5 was still homogeneous even after a long storage period (12 months) and segregation was not observed.
- Greased, deep-drawn steel parts stored for three months were degreased in an alkaline cleaner solution (I) prepared with the active ingredient component (B) according to the invention and, in comparison, with a similar alkaline cleaner solution (11) made from powdery cleaner.
- the cleaning solutions were composed as follows:
- the cleaning solutions (I) and (11) prepared with the specified components showed a cloud point of 62 ° C. at 80 ° C. at the same active ingredient concentrations (50 g / l).
- the degreasing time was 12 min with freshly prepared cleaning solution (I) and 13 min with freshly prepared cleaning solution (11).
- the storage of the cleaning solution (I) prepared with the active ingredient concentrate according to the invention had no influence on the degreasing time and cloud point of the cleaning agent.
- these properties changed with the solution that was produced with the powdered cleaner over a longer storage period.
- the nonionic surfactants contained therein were broken down into anionic surfactants in the presence of caustic alkalis and atmospheric oxygen. This degradation of the non-ionic surfactants was also associated with an increase in the foaming power, which had a disruptive effect in particular for sprayable cleaning solutions.
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Description
Die Erfindung betrifft Wirkstoffkonzentrate für alkalische Zweikomponenten-Reiniger, Verfahren zu ihrer Herstellung und ihre Verwendung.The invention relates to active ingredient concentrates for alkaline two-component cleaners, processes for their preparation and their use.
Zum Reinigen starrer Materialien, beispielsweise von Werkstücken aus Metall oder Glas werden alkalische Reinigungsmittel verwendet, die Ätznatron, Orthophosphate, kondensierte Phosphate, Silikate, Komplexbildner, Netzmittel und gegebenenfalls Korrosionsinhibitoren, Antischaummittel und Konservierungsmittel enthalten. Im allgemeinen werden diese Bestandteile enthaltende Produkte als pulvrige Gemische in den Handel gebracht und dem Reinigungsbad in Pulverform diskontinuierlich zugeführt, wobei die Konzentration des Reinigungsmittels im Bad je nach Anwendungszweck und Verschmutzungsgrad zwischen 0,1 und 20 Gew.-% liegen kann.To clean rigid materials, for example workpieces made of metal or glass, alkaline cleaning agents are used, which contain caustic soda, orthophosphates, condensed phosphates, silicates, complexing agents, wetting agents and optionally corrosion inhibitors, anti-foaming agents and preservatives. In general, products containing these constituents are marketed as powdery mixtures and are fed discontinuously to the cleaning bath in powder form, the concentration of the cleaning agent in the bath depending on the application and degree of soiling being between 0.1 and 20% by weight.
Voraussetzung für die Wirksamkeit der Reinigungslösung ist die Einhaltung der optimalen Konzentration der Reinigerbestandteile. Diese kann durch Titration oder über eine Leitfähigkeitsmessung festgestellt werden. Die Leitfähigkeitsmessung zur Konzentrationsbestimmung kann in Verbindung mit einer automatischen Zudosierung des Pulvergemischs zur Einstellung der gewünschten Reinigerkonzentration durchgeführt werden.The prerequisite for the effectiveness of the cleaning solution is compliance with the optimal concentration of the cleaning agent components. This can be determined by titration or a conductivity measurement. The conductivity measurement for determining the concentration can be carried out in conjunction with an automatic metering of the powder mixture in order to set the desired detergent concentration.
Ein Nachteil der Arbeitsweise mit pulverförmigen Produkten, insbesondere wenn diese hygroskopische Salze enthalten, ist es, dass eine kontinuierliche, störungsfreie Zudosierung nur schwer sichergestellt werden kann. Weiterhin sind gerade besonders wirksame nichtionische Tenside empfindlich gegenüber festem Ätznatron. Bei längerer Lagerzeit werden sie zu Ethercarbonsäuren oxidiert. Dadurch wird bei bestimmten Reinigungsvorgängen eine Verschlechterung der Wirksamkeit und bei einem Spritzauftrag der Reinigungslösung eine störende Schaumbildung verursacht.A disadvantage of working with powdered products, especially if they contain hygroscopic salts, is that it is difficult to ensure continuous, trouble-free metering. Furthermore, particularly effective nonionic surfactants are sensitive to solid caustic soda. If stored for a long time, they will be oxidized to ether carboxylic acids. This results in a deterioration in the effectiveness of certain cleaning processes and in a spray application of the cleaning solution causes an annoying foam formation.
Neben pulverförmigen Reinigungsmitteln ist auch die Verwendung flüssiger alkalischer Reinigungsmittelkonzentrate bekannt. Nach der DE-OS 1467605 lassen sich bei längerer Lagerung dieser Konzentrate auftretende Verluste an Polymerphosphaten durch Hydrolyse sowie die schlechte Kompatibilität von darin enthaltenen nichtionogenen Netz- und Antischaummitteln und Polymerphosphaten mit dem restlichen Reinigerkonzentrat dadurch ausgleichen, dass man die Reiniger mit einem flüssigen, sauren, nichtionogenen Netzmittel und/oder Antischaummittel und wasserlösliche, mit den Härtebildnern des Wassers Komplexe bildende organische Säuren oder deren saure Salze enthaltenden Wirkstoffkonzentrat ergänzt. Diese sauer oder neutral reagierenden Wirkstoffkonzentrate wurden dann durch Zugabe eines Überschusses Alkali zu alkalisch reagierenden flüssigen Reinigern verarbeitet. Der Nachteil eines derartigen Vorgehens ist jedoch, dass silikathaltige Reinigungsmittel auf diesem Wege nicht hergestellt werden konnten, da die verwendeten Tenside mit hohen Builderkonzentrationen, d. h. grossen Mengen an Silikaten in der Lösung, nicht verträglich sind.In addition to powder detergents, the use of liquid alkaline detergent concentrates is also known. According to DE-OS 1467605, the prolonged storage of these concentrates can result in losses of polymer phosphates due to hydrolysis and the poor compatibility of the nonionic wetting and antifoam agents and polymer phosphates contained therein with the remaining detergent concentrate in that the detergents are treated with non-ionic wetting agents and / or anti-foaming agents and water-soluble organic acids or active ingredient concentrate containing complexes which form complexes with the water. These acidic or neutral reacting active ingredient concentrates were then processed into alkaline reacting liquid cleaners by adding an excess of alkali. The disadvantage of such a procedure, however, is that silicate-containing cleaning agents could not be produced in this way, since the surfactants used have high builder concentrations, ie. H. large amounts of silicates in the solution are not compatible.
Nach der DE-OS 3246080 wurden nun Reinigungskonzentrate aus zwei Komponenten hergestellt, von denen die eine im wesentlichen aus Natronlauge besteht, die zweite die übrigen Reinigerbestandteile enthält. Die letztere Lösung kann dabei auf saure oder neutrale pH-Werte eingestellt werden, wobei eine saure Einstellung den Vorteil hat, dass alle ihre Komponenten, insbesondere die Tenside, besonders gut löslich sind. Die offenbarten Zweikomponentenreiniger sind insbesondere dadurch gekennzeichnet, dass die saure bzw. neutrale Komponente eine wässrige Dispersion von Kieselsäure ist, die aus pyrogener oder gefällter Kieselsäure hergestellt wurde und gegebenenfalls weitere Bestandteile, wie Phosphorsäure, Schwefelsäure, Polyphosphate, Tenside, Stabilisatoren und/oder Konservierungsmittel enthalten kann.According to DE-OS 3246080, cleaning concentrates have now been produced from two components, one of which consists essentially of sodium hydroxide solution and the second contains the other cleaning constituents. The latter solution can be adjusted to acidic or neutral pH values, an acidic setting having the advantage that all of its components, in particular the surfactants, are particularly readily soluble. The disclosed two-component cleaners are characterized in particular by the fact that the acidic or neutral component is an aqueous dispersion of silica which has been prepared from pyrogenic or precipitated silica and optionally contains further constituents, such as phosphoric acid, sulfuric acid, polyphosphates, surfactants, stabilizers and / or preservatives can.
Für die Herstellung der Kieselsäuredispersionen wurde eine aus Wasserglas durch Fällen mit Schwefelsäure, Auswaschen und Trocknen erhaltene Kieselsäure verwendet. Das Verfahren, Kieselsäure durch Säurebehandlung von Wasserglas auszufällen und den Niederschlag zu waschen und zu trocknen, ist jedoch sehr aufwendig und gerade in grosstechnischem Massstab schwierig durchzuführen. Zudem ist die auf diesem Wege erhaltene Kieselsäure bei der Anwendung in Zweikomponentenreinigern relativ schlecht löslich. Löslichkeitsnachteile ergeben sich insbesondere dann, wenn das Si02/Na20-Verhältnis im Reinigungsbad grösser als 0,3 : 1 ist. Ein weiterer Nachteil der Verwendung gefällter und isolierter Kieselsäure ist darin zu sehen, dass aufgrund der begrenzten Löslichkeit nichtionischer Tenside relativ saure Konzentrate hergestellt werden müssen, um eine ausreichende Stabilisierung zu gewährleisten. Dies hat zur Folge, dass zur Neutralisation bzw. zur Einstellung eines bevorzugt alkalischen pH-Wertes von Reinigerlösungen hohe Mengen an Alkalimetallhydroxid zugesetzt werden müssen.A silica obtained from water glass by precipitation with sulfuric acid, washing out and drying was used for the preparation of the silica dispersions. However, the process of precipitating silica by acid treatment of water glass and washing and drying the precipitate is very complex and difficult to carry out, especially on an industrial scale. In addition, the silica obtained in this way is relatively poorly soluble when used in two-component cleaners. Solubility disadvantages arise in particular when the Si0 2 / Na 2 0 ratio in the cleaning bath is greater than 0.3: 1. Another disadvantage of using precipitated and isolated silica is the fact that, due to the limited solubility of nonionic surfactants, relatively acidic concentrates have to be prepared in order to ensure adequate stabilization. The consequence of this is that large amounts of alkali metal hydroxide have to be added in order to neutralize or to set a preferably alkaline pH of cleaning solutions.
Es wurde nun gefunden, dass es keineswegs nötig ist, aus Wasserglas mit Hilfe von Säuren ausgefällte Kieselsäure zu isolieren und zu trocknen. Vielmehr liessen sich hochwirksame flüssige Zweikomponentenreinigersysteme mit Kieselsäuredispersionen erhalten, die in situ durch Fällen der Kieselsäure aus Natron- oder Kaliwasserglas mit Säuren erhalten und mit Stabilisatoren, Tensiden und möglicherweise anderen Buildersubstanzen versetzt wurden. Überraschend ist, dass bei der Neutralisation entstehende Salze die Stabilität der Suspension nicht beeinträchtigen. Zusätzlich ist es möglich, stabile und lagerfähige Wirkstoffkonzentrate auch mit pH-Werten im alkalischen Bereich (bis pH 11) herzustellen.It has now been found that it is in no way necessary to isolate and dry silica precipitated from water glass with the aid of acids. Rather, highly effective liquid two-component cleaner systems with silica dispersions could be obtained, which were obtained in situ by precipitating the silica from sodium or potassium water glass with acids and mixed with stabilizers, surfactants and possibly other builder substances. It is surprising that salts formed during neutralization do not impair the stability of the suspension. In addition, it is possible to produce stable and storable active ingredient concentrates with pH values in the alkaline range (up to pH 11).
Die Erfindung betrifft daher Wirkstoffkonzentrate B für aus zwei Komponenten A und B bestehende alkalische Reiniger, deren eine Komponente A eine stark alkalische, überwiegend Alkalimetallhydroxide enthaltende und im Überschuss eingesetzte basische wässrige Lösung und deren andere Komponente B eine Kieselsäure enthaltende wässrige Dispersion ist, die als weitere Zusätze anionische, nichtionogene und/oder amphotere Tenside, Buildersubstanzen, Stabilisatoren und gegebenenfalls anorganische Mineralsäuren, Komplexbildner, Konservierungsmittel und/oder weitere in Reinigerkonzentraten übliche Mittel aufweist, die dadurch gekennzeichnet sind, dass sie eine auf einen pH-Wert im Bereich von 1 bis 11 eingestellte, durch Behandlung von Alkalimetallsilikatlösungen mit Mineralsäuren oder in wässriger Lösung seiner reagierenden Gase in situ gewonnene Kieselsäuredispersion enthalten.The invention therefore relates to active substance concentrates B for alkaline cleaners consisting of two components A and B, one component A of which is a strongly alkaline, predominantly alkali metal hydroxide-containing and used in excess basic aqueous solution and the others re component B is an aqueous dispersion containing silica which, as further additives, comprises anionic, nonionic and / or amphoteric surfactants, builder substances, stabilizers and optionally inorganic mineral acids, complexing agents, preservatives and / or other agents customary in cleaner concentrates, which are characterized in that they contain a silica dispersion which has been adjusted to a pH in the range from 1 to 11 and has been obtained in situ by treating alkali metal silicate solutions with mineral acids or in aqueous solution of its reacting gases.
Die Erfindung betrifft ausserdem ein Verfahren zur Herstellung von Wirkstoffkonzentraten B für aus zwei Komponenten A und B bestehende alkalische Reiniger, deren eine Komponente A eine stark alkalische, überwiegend Alkalimetallhydroxide enthaltende und im Überschuss eingesetzte basische wässrige Lösung und deren andere Komponente B eine Kieselsäure enthaltende wässrige Dispersion ist, die als weitere Zusätze anionische, nichtionogene und/oder amphotere Tenside, Buildersubstanzen, Stabilisatoren und gegebenenfalls anorganische Mineralsäuren, Komplexbildner, Konservierungsmittel und/oder weitere in Reinigerkonzentraten übliche Mittel aufweist, das dadurch gekennzeichnet ist, dass man Alkalimetallsilikatlösungen bei einem pH-Wert zwischen 8 und 11 mit Mineralsäuren oder in wässriger Lösung sauer reagierenden Gasen behandelt und die dadurch erhaltenen Kieselsäuredispersionen, ohne die bei der Neutralisation entstehenden Salze zu entfernen, mit den zur Herstellung der Wirkstoffkonzentrate B erforderlichen Bestandteilen versetzt.The invention also relates to a process for the preparation of active ingredient concentrates B for alkaline cleaners consisting of two components A and B, one component A of which is a strongly alkaline aqueous solution which contains predominantly alkali metal hydroxides and is used in excess, and the other component B of which is an aqueous dispersion comprising silica is which contains, as further additives, anionic, nonionic and / or amphoteric surfactants, builders, stabilizers and optionally inorganic mineral acids, complexing agents, preservatives and / or other agents customary in cleaner concentrates, which is characterized in that alkali metal silicate solutions have a pH between 8 and 11 treated with mineral acids or gases reacting acidic in aqueous solution and the silica dispersions thus obtained, without removing the salts formed during the neutralization, with the active ingredient concentrates B necessary components.
Die Erfindung betrifft ausserdem die Verwendung derartiger Wirkstoffkonzentrate B in alkalischen Zweikomponentenreinigern zum Reinigen starrer Materialien.The invention also relates to the use of such active substance concentrates B in alkaline two-component cleaners for cleaning rigid materials.
Für die Zwecke der Erfindung geeignet sind wässrige Alkalimetallsilikatlösungen, deren Si02-/ M20-Verhältnis (M=Alkalimetall) im Bereich von 2 bis 3,5 liegt. Dabei sind Natron- und Kaliwasserglaslösungen prinzipiell gleichermassen gut geeignet. Es werden jedoch bevorzugt wässrige Natronwasserglaslösungen verwendet, da diese billiger und in grösseren Mengen zugänglich sind.Suitable for the purposes of the invention are aqueous alkali metal silicate solutions whose Si0 2 - / M 2 0 ratio (M = alkali metal) is in the range from 2 to 3.5. In principle, soda and potash water glass solutions are equally well suited. However, aqueous sodium water glass solutions are preferably used, since these are cheaper and accessible in larger quantities.
In einer bevorzugten Ausführungsform der Erfindung werden unverdünnte technische Wasserglaslösungen eingesetzt. Dies hat sich allein schon deshalb als vorteilhaft erwiesen, weil für die entstehenden Wirkstoffkonzentrate ein hoher Wirkstoffgehalt angestrebt wird, der bei Einsatz verdünnter Lösungen weitere Verfahrensschritte zur Steigerung des Wirkstoffgehaltes, wie z. B. Einengen der Dispersion durch Eindampfen oder Filtration, erforderlich machte. Diese Schritte werden entbehrlich, wenn konzentrierte Lösungen eingesetzt werden.In a preferred embodiment of the invention, undiluted technical water glass solutions are used. This has proven to be advantageous simply because a high active substance content is sought for the active substance concentrates that are formed, which, when using dilute solutions, further process steps to increase the active substance content, such as, for B. concentration of the dispersion by evaporation or filtration, required. These steps become unnecessary if concentrated solutions are used.
Die Herstellung der in situ gefällten Kieselsäure erfolgt durch Umsetzung der genannten Wasserglaslösungen mit beliebigen Mineralsäuren oder in wässriger Lösung sauer reagierenden Gasen, z. B. HCI, S02 und/oder C02. Bei Einsatz saurer Gase wird die Fällung mit C02 bevorzugt. Bei Verwendung von Mineralsäuren haben sich Phosphorsäure und Schwefelsäure sowie ein Gemisch beider Säuren im Gewichtsverhältnis 3 : 1 bis 1 : 3 bewährt. Besonders bevorzugt ist ein Verhältnis von 1 : 1. In der Praxis werden mit Vorteil konzentrierte Säuren eingesetzt, um einen hohen Wirkstoffgehalt in den entstehenden Kieselsäuredispersionen zu erzielen.The silica precipitated in situ is prepared by reacting the water glass solutions mentioned with any mineral acids or gases reacting acidic in aqueous solution, e.g. B. HCI, S0 2 and / or C0 2 . When using acidic gases, precipitation with CO 2 is preferred. When using mineral acids, phosphoric acid and sulfuric acid as well as a mixture of both acids in a weight ratio of 3: 1 to 1: 3 have proven their worth. A ratio of 1: 1 is particularly preferred. In practice, concentrated acids are advantageously used in order to achieve a high active ingredient content in the silica dispersions formed.
Während der Fällungsreaktion soll der pH-Wert zwischen 8 und 10 und die Reaktionstemperatur zwischen 60 und 90°C liegen. Unter diesen Bedingungen werden Kieselsäurequalitäten erhalten, die besonders stabile Dispersionen liefern. Der angegebene Bereich des pH-Wertes lässt sich in vorteilhafter Weise einhalten, wenn in einem Puffersystem gearbeitet wird. Als Puffer sind insbesondere Alkalimetallsalze von Säuren geeignet, deren Anionen im pH-Bereich von 8 bis 10 puffernd wirken, beispielsweise Phosphate, Carbonate und/oder Borate. Die puffernden Salze können sowohl in wässriger Lösung für die Fällungsreaktion vorgelegt werden als auch sich im Verlauf der Fällungsreaktion bilden.During the precipitation reaction, the pH should be between 8 and 10 and the reaction temperature between 60 and 90 ° C. Under these conditions, silica grades are obtained which provide particularly stable dispersions. The specified range of the pH value can advantageously be maintained when working in a buffer system. Alkali metal salts of acids whose anions have a buffering action in the pH range from 8 to 10, for example phosphates, carbonates and / or borates, are particularly suitable as buffers. The buffering salts can be placed in aqueous solution for the precipitation reaction or can form in the course of the precipitation reaction.
Bei der Fällung der Kieselsäure aus den Alkalimetallsilikatlösungen mit Schwefelsäure hat es sich als vorteilhaft erwiesen, die im Wirkstoffkonzentrat gewünschte Menge an Phosphat als wässrige Lösung vorzulegen und durch gleichzeitiges Zudosieren von Wasserglaslösung und Schwefelsäure eine Kieselsäurefällung zu bewirken.When the silica is precipitated from the alkali metal silicate solutions with sulfuric acid, it has proven to be advantageous to present the desired amount of phosphate in the active ingredient concentrate as an aqueous solution and to effect a silica precipitation by simultaneously metering in water glass solution and sulfuric acid.
Am Ende der Fällung kann die Dispersion auf den gewünschten pH-Wert im sauren, neutralen oder alkalischen Bereich eingestellt werden. Durch einen Überschuss an Mineralsäure sind pH-Werte um 1 erreichbar, ohne dass dies die Eignung der Dispersionen für alkalische Zweikomponentenreiniger beeinträchtigen würde. Vorzugsweise werden die Dispersionen jedoch alkalisch auf pH-Werte von 8 bis 11 eingestellt, wozu wässrige Natronlauge oder Kalilauge, Natriumorthophosphat oder Kaliumorthophosphat, Natriumcarbonat oder Kaliumcarbonat und/oder Natriumsilicate oder Kaliumsilicate verwendet werden können.At the end of the precipitation, the dispersion can be adjusted to the desired pH in the acidic, neutral or alkaline range. With an excess of mineral acid, pH values around 1 can be achieved without this affecting the suitability of the dispersions for alkaline two-component cleaners. However, the dispersions are preferably adjusted alkaline to pH values from 8 to 11, for which purpose aqueous sodium hydroxide solution or potassium hydroxide solution, sodium orthophosphate or potassium orthophosphate, sodium carbonate or potassium carbonate and / or sodium silicates or potassium silicates can be used.
Für die vorgesehene Verwendung der erfindungsgemässen Wirkstoffkonzentrate in alkalischen Zweikomponentenreinigern ist ein gewisser Gehalt an Buildersalzen vorteilhaft, die bei der in-situ-Fällung entstehen oder als Puffer zugesetzt werden. Unter Buildersalzen werden dabei Salze verstanden, die die Reinigungswirkung der Tenside verstärken, beispielsweise Alkalimetall-orthophosphate und/oder -polyphosphate, -carbonate, -borate und/oder -sulfate. Insbesondere kommen hierfür Alkalimetallpolyphosphate, d. h. Alkalimetallpyrophosphat und/oder -tripolyphosphat, in Betracht.For the intended use of the active compound concentrates according to the invention in alkaline two-component cleaners, a certain content of builder salts which are formed during in-situ precipitation or are added as a buffer is advantageous. Builder salts are understood to mean salts which enhance the cleaning action of the surfactants, for example alkali metal orthophosphates and / or polyphosphates, carbonates, borates and / or sulfates. In particular, alkali metal polyphosphates, i. H. Alkali metal pyrophosphate and / or tripolyphosphate.
Um eine gute Reinigungswirkung zu erzielen, ist es ausserdem zweckmässig, der Kieselsäuredispersion Tenside zuzusetzen. Für diesen Zweck sind anionische, nichtionische und/oder amphotere Tenside geeignet. Im einzelnen kommen Verbindungen wie Alkylbenzolsulfonate, Alkylsulfonate, Fettalkoholsulfate, Anlagerungsprodukte von Ethylenoxid und/oder Propylenoxid an Fettalkohole, Fettamine und Alkylphenole sowie oberflächenaktive Ethylenoxid/Propylenoxid-Blockpolymerisate in Frage. Die Kettenlängen der Alkylreste liegen bei den genannten Verbindungen im Bereich von 8 bis 20 C-Atomen und im Fall der Alkylphenole im Bereich von 6 bis 18 C-Atomen. Weiterhin kommen als amphotere Tenside Verbindungen wie Alkyldimethylammoniumbetaine mit 12 bis 18 C-Atomen im Alkylrest in Betracht.In order to achieve a good cleaning effect, it is also expedient to add surfactants to the silica dispersion. Anionic, nonionic and / or amphoteric surfactants are suitable for this purpose. Specifically, there are compounds such as alkylbenzenesulfonates, alkylsulfonates, fatty alcohol sulfates, addition products of ethylene oxide and / or propylene oxide to fatty alcohols, fatty amines and alkylphenols and surface-active ethylene oxide / propylene oxide block polymers. The chain lengths of the alkyl radicals are in the range of 8 to 20 C atoms for the compounds mentioned and in the case of the alkylphenols in the range of 6 to 18 C atoms. Also suitable as amphoteric surfactants are compounds such as alkyldimethylammonium betaines having 12 to 18 carbon atoms in the alkyl radical.
In einer bevorzugten Ausführungsform der vorliegenden Erfindung kann die Fällung der Kieselsäuren aus Alkalimetallsilikatlösungen durch Mineralsäuren auch in Gegenwart der genannten Tenside erfolgen. Durch diese Verfahrensweise wird insbesondere die Stabilisierung von alkalischen niotensidhaltigen Dispersionen erleichtert.In a preferred embodiment of the present invention, the silicas can be precipitated from alkali metal silicate solutions by mineral acids, even in the presence of the surfactants mentioned. This procedure in particular facilitates the stabilization of alkaline dispersions containing nonionic surfactants.
Zusätzlich können die Kieselsäuredispersionen für die erfindungsgemässen Wirkstoffkonzentrate auch Komplexbildner enthalten, wie z. B. Alkalimetallsalze der Nitrilotriessigsäure, Ethylendiamintetraessigsäure, Gluconsäure, Citronensäure oder Phosphonsäuren (z. B. Hydroxyethan-1, 1-diphosphonsäure, Aminotrimethylenphosphonsäure und 2-Phosphono-1, 2,4-butantricarbonsäure).In addition, the silica dispersions for the active ingredient concentrates according to the invention can also contain complexing agents, such as. B. alkali metal salts of nitrilotriacetic acid, ethylenediaminetetraacetic acid, gluconic acid, citric acid or phosphonic acids (e.g. hydroxyethane-1, 1-diphosphonic acid, aminotrimethylenephosphonic acid and 2-phosphono-1, 2,4-butanetricarboxylic acid).
Als Stabilisatoren werden Verbindungen verwendet, die die Sedimentation der Kieselsäure in den Dispersionen verhindern. Es werden z. B. Reinsubstanzen oder Gemische aus der Gruppe Pflanzengummi, d. h. Xanthan, und der Copolymeren aus Polyalkylvinylethern und Carbonsäureanhydriden verwendet, z. B. GANTREZR AN-Typen der Firma GAF-Corporation wie Copolymere aus Polymethylvinylethern und Maleinsäureanhydrid.Compounds are used as stabilizers which prevent the sedimentation of the silica in the dispersions. There are e.g. B. pure substances or mixtures from the group vegetable gum, ie xanthan, and the copolymers of polyalkyl vinyl ethers and carboxylic acid anhydrides, for. B. GANTREZ R AN types from GAF Corporation such as copolymers of polymethyl vinyl ethers and maleic anhydride.
Das Wirkstoffkonzentrat B enthält 10 bis 26Gew.-%, bevorzugt 15 bis 25Gew.-%, besonders bevorzugt 18 bis 22 Gew.-%, Kieselsäure, berechnet als Si02; 5 bis 27 Gew.-%, bevorzugt 8 bis 25Gew.-%, besonders bevorzugt 13 bis 24 Gew.-%, Builder; 0,5 bis 12Gew.-%, bevorzugt 1 bis 10 Gew.-%, besonders bevorzugt 1 bis 8Gew.- % Tenside; 0,2 bis 5 Gew.-%, bevorzugt 0,3 bis 3 Gew.-%, besonders bevorzugt 0,5 bis 2 Gew.-%, Stabilisatoren; und 0,5 bis 10 Gew.-%, bevorzugt 1 bis 8Gew.-%, besonders bevorzugt 2 bis 7 Gew.-%, Komplexbildner.The active ingredient concentrate B contains 10 to 26% by weight, preferably 15 to 25% by weight, particularly preferably 18 to 22% by weight, of silica, calculated as SiO 2 ; 5 to 27% by weight, preferably 8 to 25% by weight, particularly preferably 13 to 24% by weight, builder; 0.5 to 12% by weight, preferably 1 to 10% by weight, particularly preferably 1 to 8% by weight of surfactants; 0.2 to 5% by weight, preferably 0.3 to 3% by weight, particularly preferably 0.5 to 2% by weight, of stabilizers; and 0.5 to 10% by weight, preferably 1 to 8% by weight, particularly preferably 2 to 7% by weight, of complexing agent.
Die alkalische Komponente A für die alkalischen Zweikomponentenreiniger besteht im wesentlichen aus Natronlauge bzw. Kalilauge. Als weitere Bestandteile können gegebenenfalls solche Verbindungen in Betracht kommen, die mit den Bestandteilen der erfindungsgemässen Kieselsäuredispersions-Komponente nicht verträglich sind, wie beispielsweise Ligninsulfonate. Die wässrige Alkalimetallhydroxidlösung wird für Zweikomponentenreiniger im Überschuss verwendet; darunter ist eine solche Menge an Natronlauge oder Kalilauge zu verstehen, die ausreichend ist, um dem Zweikomponentenreiniger-Konzentrat nach der Zusammengabe der alkalischen und der erfindungsgemässen Kieselsäuredispersions-Komponente einen pH-Wert grösser als 11, vorzugsweise grösser als 12 zu geben.The alkaline component A for the alkaline two-component cleaners consists essentially of sodium hydroxide solution or potassium hydroxide solution. Compounds which are incompatible with the constituents of the silica dispersion component according to the invention, such as, for example, lignin sulfonates, may optionally be considered as further constituents. The aqueous alkali metal hydroxide solution is used in excess for two-component cleaners; this is to be understood as an amount of sodium hydroxide solution or potassium hydroxide solution which is sufficient to give the two-component cleaner concentrate a pH greater than 11, preferably greater than 12, after combining the alkaline and the silica dispersion components according to the invention.
Zur Herstellung einer Zweikomponentenreinigerlösung werden die Wirkstoffkomponenten A und B in auf wenigstens 40°C erwärmtem Wasser vermischt, wobei die Kieselsäure zu wasserlöslichen Silikaten umgesetzt wird. Dabei werden pH-Werte grösser als 12 erreicht.To prepare a two-component cleaning solution, the active ingredient components A and B are mixed in water heated to at least 40 ° C., the silica being converted to water-soluble silicates. PH values greater than 12 are reached.
Der Vorteil der Verwendung der erfindungsgemässen, in situ gefällte Kieselsäure enthaltenden Wirkstoffkonzentrate B ist darin zu sehen, dass die Dispersionen unter den Ansatzbedingungen eines Reinigerbades wesentlich besser löslich sind als aus dem Stand der Technik bekannte Dispersionen. Daneben bietet der Einsatz der in situ gefällten Kieselsäure grössere Freiheiten bei der Formulierung der Wirkstoffkonzentrate bezüglich der weiteren Komponenten. So wird beispielsweise die Verwendung alkalischer Salze als Builder ermöglicht. Im Vergleich zu aus dem Stand der Technik bekannten Systemen kann ausserdem bei der Zusammengabe der beiden Komponenten für das Reinigungsbad ein Teil der Alkalimetall-Lauge eingespart werden, wenn die erfindungsgemässen Wirkstoffkonzentrate schon auf einen ph-Wert von 8 bis 11 eingestellt wurden und damit eine Neutralisation stark saurer Komponenten mit grossen Überschüssen an Alkalimetallhydroxiden nicht mehr erforderlich ist.The advantage of using the active ingredient concentrates B according to the invention which contain silica precipitated in situ is to be seen in the fact that the dispersions are substantially more soluble under the preparation conditions of a detergent bath than dispersions known from the prior art. In addition, the use of silica precipitated in situ offers greater freedom in the formulation of the active ingredient concentrates with regard to the other components. For example, the use of alkaline salts as a builder is made possible. In comparison to systems known from the prior art, a part of the alkali metal alkali can also be saved when the two components for the cleaning bath are combined, if the active compound concentrates according to the invention have already been adjusted to a pH of 8 to 11 and thus neutralization strongly acidic components with large excesses of alkali metal hydroxides is no longer required.
Ein weiterer Vorteil der erfindungsgemässen Vorgehensweise ist darin zu sehen, dass der zumindest für grössere Substanzmengen verfahrenstechnisch aufwendige Schritt des Auswaschens der gefällten Kieselsäure sowie die Schritte des Abtrennens von der Fällungslösung und des Trocknens der isolierten Kieselsäure überflüssig werden. Ausserdem ist es als vorteilhaft anzusehen, dass höhere Salzgehalte weder die Stabilität der Kieselsäuredispersionen noch die Wirksamkeit der entstehenden Zweikomponentenreiniger beeinträchtigen.Another advantage of the procedure according to the invention can be seen in the fact that the step of washing out the precipitated silica, which is complex in terms of process engineering, at least for larger amounts of substance, and the steps of separating from the precipitation solution and drying the isolated silica, are superfluous. In addition, it is to be regarded as advantageous that higher salt contents do not impair the stability of the silica dispersions or the effectiveness of the two-component cleaners that arise.
Das Verfahren wird durch die nachfolgenden Beispiele näher erläutert.The process is explained in more detail by the examples below.
Zu 8 Litern einer 2%igen Dinatriumhydrogenphosphatlösung wurden bei 80°C mit Hilfe von zwei Dosierpumpen gleichzeitig 35 kg Natronwasserglas, das auf ein Si02/Na20-Gewichtsverhältnis von 3,3 und einen Gesamtfeststoffgehalt von 35% eingestellt wurde, und 4,7 kg einer Mischung aus 98%iger Schwefelsäure und 85%iger Phosphorsäure im Gewichtsverhältnis 1 : 1 so zudosiert, dass der pH-Wert immer im Bereich von 8 bis 9 gehalten wurde. Der Suspension wurden 1,0% Xanthan als Stabilisator, 2% eines Additionsproduktes von 14 EO an Nonylphenol und 1% Alkylbenzolsulfonsäure zugesetzt. Die Dispersion wies einen pH-Wert von 8,5 auf. Durch Zugabe von 5 kg Natronwasserglas stieg der pH-Wert auf 10,4. Die Dispersion blieb dabei stabil.To 8 liters of a 2% disodium hydrogenphosphate solution were added at 80 ° C with the help of two metering pumps simultaneously 35 kg of sodium water glass, which was adjusted to a Si0 2 / Na 2 0 weight ratio of 3.3 and a total solids content of 35%, and 4. 7 kg of a mixture of 98% sulfuric acid and 85% phosphoric acid in a weight ratio of 1: 1 are metered in such that the pH is always kept in the range from 8 to 9. 1.0% xanthan as a stabilizer, 2% of an addition product of 14 EO with nonylphenol and 1% alkylbenzenesulfonic acid were added to the suspension. The dispersion had a pH of 8.5. By adding 5 kg of soda water glass, the pH rose to 10.4. The dispersion remained stable.
Zu 8 Litern einer 10%igen Natriumtriphosphatlösung wurden bei 70°C gleichzeitig 40 kg Kaliwasserglas mit einem Si02/K20-Gewichtsverhältnis von 2,1 und einem Gesamtfeststoffgehalt von 40% und 6kg 98%iger Schwefelsäure zudosiert, so dass ein pH-Wert zwischen 8 und 9 eingehalten wurde. Der Suspension wurden ausserdem 1,5% Xanthan als Stabilisator, 2% eines Additiosproduktes von 14 EO an C,2-18-Fettalkohol und 1% Alkylbenzolsulfonsäure zugesetzt.To 8 liters of a 10% sodium triphosphate solution, 40 kg of potassium water glass with an SiO 2 / K 2 0 weight ratio of 2.1 and a total solids content of 40% and 6 kg of 98% sulfuric acid were simultaneously metered in at 70 ° C., so that a pH Value between 8 and 9 observed has been. 1.5% xanthan as a stabilizer, 2% of an additive of 14 EO to C, 2-18 fatty alcohol and 1% alkylbenzenesulfonic acid were also added to the suspension.
In einem Rührbehälter wurden zu 5 Litern einer 2%igen Dinatriumhydrogenphosphatlösung 60g Alkylbenzolsulfonsäure und 240g Nonylphenol + 14 EO gegeben und auf 80°C aufgeheizt. Zu dieser Lösung wurden gleichzeitig 3,8 kg einer Mischung aus 98%iger Schwefelsäure und 85%iger Phosphorsäure im Gewichtsverhältnis 5 : 1 und 40 kg Natronwasserglas mit einem Si02/Na20-Gewichtsverhältnis von 3,3 und einer Dichte von 1,35g/cm3 so zudosiert, dass der pH-Wert im Bereich von 8,8 bis 9,2 gehalten wurde. Nach vollständiger Umsetzung bildete sich eine Dispersion mit einem pH-Wert von 9,1. Der Dispersion wurden 0,3% eines Stabilisatorgemisches aus Xanthan und eines Copolymeren auf der Basis Polymethylvinylether/Maleinsäureanhydrid (GAN-TREZ R AN 149) zugesetzt.60 g of alkylbenzenesulfonic acid and 240 g of nonylphenol + 14 EO were added to 5 liters of a 2% disodium hydrogenphosphate solution in a stirred container and heated to 80.degree. 3.8 kg of a mixture of 98% sulfuric acid and 85% phosphoric acid in a weight ratio of 5: 1 and 40 kg of sodium silicate with an SiO 2 / Na 2 O weight ratio of 3.3 and a density of 1 were simultaneously added to this solution. 35g / cm 3 metered in such a way that the pH was kept in the range from 8.8 to 9.2. After the reaction was complete, a dispersion with a pH of 9.1 was formed. 0.3% of a stabilizer mixture of xanthan and a copolymer based on polymethyl vinyl ether / maleic anhydride (GAN-TREZ R AN 149) was added to the dispersion.
Das bessere Löseverhalten der in situ gefällten Kieselsäure gegenüber handelsüblichen Fällungskieselsäuren wird durch das folgende Beispiel erläutert: In einem Reinigungsbad, das 5% Natronlauge und 1% Kieselsäure enthielt, wurde bei 60°C eine vollständige Auflösung der Kieselsäurearten a) in situ gefällte Kieselsäure nach 4min. (aus Beispiel 1, 3 Monate gelagert) b) Fällungskieselsäure FK 320 nach 7 min. Fa. DEGUSSA erreicht.The better dissolution behavior of the silica precipitated in situ compared to commercially available precipitated silica is illustrated by the following example: In a cleaning bath containing 5% sodium hydroxide solution and 1% silica, a complete dissolution of the silica types a) silica precipitated in situ was obtained after 4 minutes at 60 ° C . (stored from Example 1, 3 months) b) Precipitated silica FK 320 after 7 min. DEGUSSA reached.
Der Vorteil der in situ gefällten Kieselsäure im Hinblick auf die gleichmässige und stabile Verteilung von Tensiden in flüssigen builderhaltigen Wirkstoffkonzentraten gegenüber Lösungen ohne Kieselsäure wird durch den Vergleich von Lösungen und Dispersionen deutlich: Wie die Wirkstoffkonzentrate a, b, c, d in Tabelle 1 zeigen, konnten in Gegenwart von Tensiden (hier z. B. Nonylphenyl + 14 EO) nur begrenzte Builderkonzentrationen gewählt werden, um eine bei Raumtemperatur gerade noch stabile Lösung zu erhalten. Im Falle der Dispersionen e und f dagegen waren Tenside auch bei hohen Builderkonzentrationen homogen verteilbar und über lange Zeit lagerstabil.The advantage of silica precipitated in situ with regard to the uniform and stable distribution of surfactants in liquid builder-containing active ingredient concentrates compared to solutions without silica is clear from the comparison of solutions and dispersions: As the active ingredient concentrates a, b, c, d in Table 1 show In the presence of surfactants (here e.g. nonylphenyl + 14 EO), only limited builder concentrations could be selected in order to obtain a solution that was just stable at room temperature. In contrast, in the case of dispersions e and f, surfactants were homogeneously distributable even at high builder concentrations and had a long shelf life.
Der Vorteil der in situ gefällten Kieselsäure gegenüber herkömmlicher, durch saure Fällung hergestellter, handelsüblicher Kieselsäure in Hinblick auf eine gleichmässige und stabile Verteilung von Tensiden in flüssigen builderhaltigen Wirkstoffkonzentraten wird durch den Vergleich der Dispersion (f) des Beispiels 5 mit der nachfolgend formulierten Dispersion deutlich:
- 20 % Fällungskieselsäure Degussa FK 320
- 5 % Nonylphenol + 14 EO
- 11 % Trinatriumphosphat
- 0,05% Stabilisator
- 20% precipitated silica Degussa FK 320
- 5% nonylphenol + 14 EO
- 11% trisodium phosphate
- 0.05% stabilizer
Diese Dispersion zeigte schon nach zwei Monaten eine messbare Entmischung; an der Konzentratoberfläche schied sich sichtbar das Netzmittel ab.This dispersion showed measurable segregation after only two months; The wetting agent separated visibly on the surface of the concentrate.
Im Vergleich dazu war die Dispersion (f) des Beispiels 5 auch nach langer Lagerzeit (12 Monaten) noch homogen, und eine Entmischung wurde nicht beobachtet.In comparison, the dispersion (f) of Example 5 was still homogeneous even after a long storage period (12 months) and segregation was not observed.
Herstellung und Verwendung der ZweikomponentenreinigerManufacture and use of two-component cleaners
Befettete, drei Monate gelagerte, tiefgezogene Stahlteile wurden in einer mit der erfindungsgemässen Wirkstoffkomponente (B) hergestellten alkalischen Reinigerlösung (I) und im Vergleich dazu mit einer gleichartigen, aus pulvrigem Reiniger hergestellten alkalischen Reinigerlösung (11) entfettet.Greased, deep-drawn steel parts stored for three months were degreased in an alkaline cleaner solution (I) prepared with the active ingredient component (B) according to the invention and, in comparison, with a similar alkaline cleaner solution (11) made from powdery cleaner.
Die Reinigerlösungen waren wie folgt zusammengesetzt:The cleaning solutions were composed as follows:
- 25 g/l Kieselsäuredispersion (siehe unten) und25 g / l silica dispersion (see below) and
- 50 g/I Natronlauge, 50%ig50 g / l sodium hydroxide solution, 50%
- 20 % Si02 20% Si0 2
- 10 % Na3P04 10% Na 3 P0 4
- 6 % Nonylphenol + 14 EO6% nonylphenol + 14 EO
- 1 % Stabilisator (Xanthan)1% stabilizer (xanthan)
- 50 g/I eines pulverförmigen Reinigers folgender50 g / l of a powdered cleaner following
- 20 % Natriummetasilikat20% sodium metasilicate
- 5 % Na3P04 5% Na 3 P0 4
- 25 % Ätznatron25% caustic soda
- 47 % Soda und47% soda and
- 3 % Nonylphenol + 14 EO3% nonylphenol + 14 EO
Die mit den angegebenen Komponenten hergestellten Reinigerlösungen (I) und (11) zeigten bei gleichen Wirkstoffkonzentrationen (50g/I) bei 80°C einen Trübungspunkt von 62°C. Die Entfettungszeit betrug mit frisch hergestellter Reinigerlösung (I) 12 min, mit frisch hergestellter Reinigerlösung (11) 13 min.The cleaning solutions (I) and (11) prepared with the specified components showed a cloud point of 62 ° C. at 80 ° C. at the same active ingredient concentrations (50 g / l). The degreasing time was 12 min with freshly prepared cleaning solution (I) and 13 min with freshly prepared cleaning solution (11).
Wie die nachfolgende Tabelle 2 zeigt, hatte die Lagerung der mit dem erfindungsgemässen Wirkstoffkonzentrat hergestellten Reinigerlösung (I) keinen Einfluss auf Entfettungszeit und Trübungspunkt des Reinigers. Hingegen veränderten sich diese Eigenschaften bei der Lösung, die mit dem pulverförmigen Reiniger hergestellt wurde, bei längerer Lagerzeit. Die darin enthaltenen Niotenside wurden in Gegenwart von Ätzalkalien und Luftsauerstoff zu anionischen Tensiden abgebaut. Dieser Abbau der Niotenside war ausserdem mit einer Verstärkung des Schaumvermögens verbunden, die sich insbesondere für spritzbare Reinigerlösungen störend auswirkte.
Claims (23)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19853504172 DE3504172A1 (en) | 1985-02-07 | 1985-02-07 | ACTIVE CONCENTRATES FOR ALKALINE TWO-COMPONENT CLEANERS, METHOD FOR THEIR PRODUCTION AND THEIR USE |
DE3504172 | 1985-02-07 |
Publications (2)
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EP0191372A1 EP0191372A1 (en) | 1986-08-20 |
EP0191372B1 true EP0191372B1 (en) | 1988-10-26 |
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EP86101199A Expired EP0191372B1 (en) | 1985-02-07 | 1986-01-30 | Active agent concentrates for alkaline cleaner having two constituents, method for their fabrication and their use |
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Country | Link |
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US (1) | US4695396A (en) |
EP (1) | EP0191372B1 (en) |
JP (1) | JPS61183400A (en) |
AU (1) | AU578794B2 (en) |
DE (2) | DE3504172A1 (en) |
ZA (1) | ZA86891B (en) |
Cited By (1)
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EP3156475B1 (en) | 2015-10-16 | 2018-06-06 | Hans Georg Hagleitner | Liquid cleaning concentrate |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
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US5145608A (en) * | 1986-02-06 | 1992-09-08 | Ecolab Inc. | Ethoxylated amines as solution promoters |
IL82648A0 (en) * | 1986-05-27 | 1987-11-30 | Lilly Co Eli | Human protein s,a plasma protein regulator of hemostasis |
SE500387C2 (en) * | 1989-11-09 | 1994-06-13 | Eka Nobel Ab | Silica sols, process for making silica sols and using the soles in paper making |
IE910108A1 (en) * | 1990-01-15 | 1991-07-17 | S B Chemicals Ltd | Stabilised gel system and production thereof |
GB9000833D0 (en) * | 1990-01-15 | 1990-03-14 | S B Chemicals Limited | Detergent and production thereof |
US5145597A (en) * | 1990-08-31 | 1992-09-08 | Shell Oil Company | Cleaning composition and method of use |
GB9513110D0 (en) * | 1995-06-28 | 1995-08-30 | Laporte Esd Ltd | Dairy system cleaning preparation and method |
WO1999038942A1 (en) | 1998-01-30 | 1999-08-05 | Rhodia Inc. | Low foaming surfactant compositions useful in highly alkaline caustic cleaners |
CN115386434B (en) * | 2022-07-14 | 2024-08-23 | 广州市人和清洗有限公司 | Bi-component cleaning agent for cleaning pipeline and preparation method thereof |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
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US2992997A (en) * | 1955-05-25 | 1961-07-18 | Purex Corp Ltd | Method for derusting and removing heat scale from ferrous bodies and compositions of matter useful therefor |
CA777770A (en) * | 1964-12-24 | 1968-02-06 | Henkel And Cie., G.M.B.H. | Continuous cleansing of rigid materials |
US3553016A (en) * | 1967-06-02 | 1971-01-05 | Lithcote Corp | Method and composition for treating stainless steel |
US3823094A (en) * | 1969-01-08 | 1974-07-09 | Colgate Palmolive Co | Two part liquid car wash system |
US3715324A (en) * | 1971-10-18 | 1973-02-06 | G Krall | Insoluble polymeric diazonium salt chromogen |
FR2193874B1 (en) * | 1972-07-25 | 1977-04-01 | Colgate Palmolive Co | |
US3997460A (en) * | 1975-04-10 | 1976-12-14 | The Clorox Company | Liquid abrasive cleaner |
US4200548A (en) * | 1976-08-02 | 1980-04-29 | Elektrokemiska Aktiebolaget | Silicic acid detergent product for microdeposition of silicic acid on textiles |
FR2380986A1 (en) * | 1977-02-16 | 1978-09-15 | Rhone Poulenc Ind | NEW PROCESS FOR STABILIZING ANHYDROUS SODIUM METASILICATE AND THUS OBTAINED PRODUCT |
US4521332A (en) * | 1981-03-23 | 1985-06-04 | Pennwalt Corporation | Highly alkaline cleaning dispersion |
DE3246080A1 (en) | 1982-12-13 | 1984-06-14 | Henkel KGaA, 4000 Düsseldorf | CLEANING PROCEDURE |
US4597888A (en) * | 1985-06-19 | 1986-07-01 | Parker Chemical Company | Cleaner for steel cans |
-
1985
- 1985-02-07 DE DE19853504172 patent/DE3504172A1/en not_active Withdrawn
-
1986
- 1986-01-30 EP EP86101199A patent/EP0191372B1/en not_active Expired
- 1986-01-30 DE DE8686101199T patent/DE3661024D1/en not_active Expired
- 1986-02-06 AU AU53252/86A patent/AU578794B2/en not_active Ceased
- 1986-02-06 ZA ZA86891A patent/ZA86891B/en unknown
- 1986-02-07 JP JP61026645A patent/JPS61183400A/en active Pending
- 1986-02-07 US US06/827,291 patent/US4695396A/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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EP3156475B1 (en) | 2015-10-16 | 2018-06-06 | Hans Georg Hagleitner | Liquid cleaning concentrate |
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Publication number | Publication date |
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JPS61183400A (en) | 1986-08-16 |
DE3504172A1 (en) | 1986-08-07 |
DE3661024D1 (en) | 1988-12-01 |
AU578794B2 (en) | 1988-11-03 |
US4695396A (en) | 1987-09-22 |
AU5325286A (en) | 1986-08-14 |
EP0191372A1 (en) | 1986-08-20 |
ZA86891B (en) | 1986-09-24 |
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