Patent Application
20230062299
The present invention is directed towards a process for making a powder or granule containing
Chelating agents of the aminocarboxylate type such as methyl glycine diacetic acid (MGDA) and glutamic acid diacetic acid (GLDA) and their respective alkali metal salts are useful sequestrants for alkaline earth metal ions such as Ca2+ and Mg2+. A lot of aminocarboxylates show good biodegradability and are thus environmentally friendly. For that reason, they are recommended and used for various purposes such as laundry detergents and for automatic dishwashing (ADW) formulations, in particular for so-called phosphate-free laundry detergents and phosphate-free ADW formulations.
Depending on the type of product—liquid home care and fabric care products versus solid home care and fabric care products—and the manufacturing process of solid home care and fabric care products care product manufacturers may either prefer to handle solutions of aminocarboxylates or solid arminocarboxylates, for example joint spray drying or solid mixing. Powders and granules of aminocarboxylates may be shipped economically due to their high active ingredient content that goes along with low water content.
However, the hygroscopicity of alkali metal salts of MGDA and especially of GLDA may create problems like stabilization of detergent ingredients that are susceptible to alkali or to each other, for example peroxides and enzymes.
Citric acid and its alkali metal salts are considered as an alternative for aminocarboxylates. However, their ability to remove alkali earth metal cations especially in hard water is limited.
Commonly ADW formulations contain up to 40% of MGDA builder and are packaged in single unit doses, in brief also “SUD”. The space in these SUD is limited and thus a higher bulk density is desired, because a higher bulk density allows for more active product per volume unit in these SUDs.
It was therefore an objective of the present invention to provide a process that yields powders or granules of chelating agents with an high bulk density and a high capability to remove water hardness. It was also an objective of the present invention to provide powders or granules of chelating agents with a high bulk density and a high capability to remove water hardness.
Accordingly, the process defined at the outset has been found, hereinafter also referred to as inventive process or as process according to the present invention. The inventive process comprises several steps that may be referred to as step (a) or step (b) etc. and that will be explained in more detail below.
The inventive process is a process for making a powder or granule, said powders and granules also being referred to as inventive powders and inventive granules, respectively. In the context of the present invention, the term “powder” refers to particulate materials that are solids at ambient temperature and that preferably have an average particle diameter in the range of from 1 μm to less than 0.1 mm, preferably 30 μm up to 75 μm. The average particle diameter of inventive powders can be determined, e.g., by LASER diffraction methods, for example with Malvern apparatus, and refers to the volume average.
The term “granule” in the context of the present invention refers to particulate materials that are solids at ambient temperature and that preferably have an average particle diameter (D50) in the range of from 0.1 mm to 2 mm, preferably 0.4 mm to 1.25 mm, even more preferably 400 μm to 1 mm. The average particle diameter of inventive granules can be determined, e.g., by optical or preferably by sieving methods. Sieves employed may have a mesh in the range of from 60 to 3,000 μm.
In one embodiment of the present invention, powders or granules made according to the inventive process have a broad particle diameter distribution. In another embodiment of the present invention, inventive powders or inventive granules have a narrow particle diameter distribution. The particle diameter distribution can be adjusted, if desired, by multiple sieving steps.
Powders or granules made by the inventive process contain at least 75% by weight of at least one least alkali metal salt of citric acid (A), hereinafter also referred to as citrate (A). The contents of citrate (A) may be determined, e.g., by potentiometric titration with FeCl3, preferred are at least 80% by weight and even more preferred at least 85% by weight. The percentage refers to the solids content of said powder or granule and may be determined by Karl-Fischer titration or by drying at 160 to 200° C. to constant weight with infrared light. It excludes crystal water.
Granules and powders made by the inventive process may contain residual moisture, moisture referring to water including water of crystallization and adsorbed water. The amount of water may be in the range of from 0.1 to 20% by weight, preferably 1 to 15% by weight, referring to the total solids content of the respective powder or granule, and may be determined by Karl-Fischer-titration or by drying at 160 to 200° C. to constant weight with infrared light.
Particles of powders and granules made by the inventive process may have regular or irregular shape. Preferred shapes of particles of powders and of granules made by the inventive process are spheroidal shapes.
Alkali metal salts of MGDA are selected from compounds according to general formula (I)
(OOC—CH2—C(OH)(COO)—CH2COO)M3−xHx (I)
wherein
M is selected from alkali metal cations, same or different, for example cations of lithium, sodium, potassium, rubidium, cesium, and combinations of at least two of the foregoing. Preferred examples of alkali metal cations are sodium and potassium and combinations of sodium and potassium.
x in formula (I) is in the range of from zero to 1.0, preferred are zero to 0.5. In a particularly preferred embodiment, x is zero.
In one embodiment of the present invention, alkali metal salt of citrate (A) may contain one or more impurities that may result from the synthesis of the respective citrate (A). In other embodiments, however, alkali metal salt of citrate (A) is of high purity, and impurities are below detection level with standard analytic tools such as NMR spectroscopy or HPLC.
In any way, minor amounts of citrate (A) may bear a cation other than alkali metal. It is thus possible that minor amounts, such as 0.01 to 5 mol-% of total citrate (A), respectively, bear alkali earth metal cations such as Mg2+ or Ca2+, or an Fe2+ or Fe3+ cation.
Particles of powders or granules made by the inventive process further contain at least one additive selected from
In a preferred embodiment of the present invention, particles of powders or granules made by the inventive process contain
(Co)polymer (B) is selected from polymers (B) of (meth)acrylic acid and of copolymers (B) of (meth)acrylic acid, preferably of acrylic acid, partially or fully neutralized with alkali. In the context of the present invention, copolymers (B) are those in which at least 50 mol-% of the comonomers are (meth)acrylic acid, preferably at least 75 mol-%, even more preferably 80 to 99 mol-%.
Suitable comonomers for copolymers (B) are ethylenically unsaturated compounds, such as styrene, isobutene, ethylene, α-olefins such as propylene, 1-butylene, 1-hexene, and ethylenically unsaturated dicarboxylic acids and their alkali metal salty and anhydrides such as but not limited to maleic acid, fumaric acid, itaconic acid disodium maleate, disodium fumarate, itaconic anhydride, and especially maleic anhydride. Further examples of suitable comonomers are C1-C4-alkyl esters of (meth)acrylic acid, for example methyl acrylate, methyl methacrylate, ethyl acrylate, ethyl methacrylate, n-butyl acrylate.
In one embodiment of the present invention, (co)polymer (B) is selected from copolymers of (meth)acrylic acid and a comonomer bearing at least one sulfonic acid group per molecule. Comonomers bearing at least one sulfonic acid group per molecule may be incorporated into copolymer (C) as free acid or least partially neutralized with alkali. Particularly preferred sulfonic-acid-group-containing comonomers are 1-acrylamido-1-propanesulfonic acid, 2-acrylamido-2-propanesulfonic acid, 2-acrylamido-2-methylpropanesulfonic acid (AMPS), 2-methacrylamido-2-methylpropanesulfonic acid, 3-methacrylamido-2-hydroxypropanesulfonic acid, allylsulfonic acid, methallylsulfonic acid, allyloxybenzenesulfonic acid, methallyloxyben -zenesulfonic acid, 2-hydroxy-3-(2-propenyloxy)propanesulfonic acid, 2-methyl-2-propene sulfonic acid, styrenesulfonic acid, vinylsulfonic acid, 3-sulfopropyl acrylate, 2-sulfoethyl meth-acrylate, 3-sulfopropyl methacrylate, sulfomethacrylamide, sulfomethylmethacrylamide, and salts of said acids, such as the sodium salts, potassium salts or ammonium salts thereof.
Copolymers (B) may be selected from random copolymers, alternating copolymers, block copolymers and graft copolymers, alternating copolymers and especially random copolymers being preferred.
Useful copolymers (B) are, for example, random copolymers of acrylic acid and methacrylic acid, random copolymers of acrylic acid and maleic anhydride, ternary random copolymers of acrylic acid, methacrylic acid and maleic anhydride, random or block copolymers of acrylic acid and styrene, random copolymers of acrylic acid and methyl acrylate. More preferred are homopolymers of methacrylic acid. Even more preferred are homopolymers of acrylic acid.
(Co)polymer (B) may constitute straight-chain or branched molecules. Branching in this context will be when at least one repeating unit of such polymer (C) is not part of the main chain but forms a branch or part of a branch. Preferably, (co)polymer (B) is not cross-linked.
In one embodiment of the present invention, (co)polymer (B) has an average molecular weight Mw in the range of from 1,200 to 30,000 g/mol, preferably from 2,500 to 15,000 g/mol and even more preferably from 3,000 to 10,000 g/mol, determined by gel permeation chromatography (GPC) and referring to the respective free acid.
(Co)polymer (B) is partially or fully neutralized with alkali, for example with lithium or potassium or sodium or combinations of at least two of the forgoing, especially with sodium. For example, in the range of from 10 to 95 mol-% of the carboxyl groups of (co)polymer (C) may be neutralized with alkali, especially with sodium, preferably in the range from 20-70 mole-% of the carboxyl groups, even more preferred in the range of from 25-60 mole-%. In embodiments wherein (co)polymer (B) is fully neutralized with alkali, 100 mol-% of the carboxyl groups of (co)polymer (B) is neutralized with alkali, especially with sodium, or even an excess of alkali metal hydroxide is present.
In one embodiment of the present invention, copolymer (B) is selected from a combination of at least one polyacrylic acid and at least one copolymer of (meth)acrylic acid and a comonomer bearing at least one sulfonic acid group per molecule, both polymers being partially or fully neutralized with alkali.
In one embodiment of the present invention, (co)polymer (B) is selected from sodium salts of polyacrylic acid with an average molecular weight Mw in the range of from 1,200 to 30,000 g/mol, preferably from 2,500 to 15,000 g/mol and even more preferably from 3,000 to 10,000 g/mol, determined by gel permeation chromatography (GPC) and referring to the respective free acid.
The weight ratio of (A):(B) is in the range of from 5:1 up to 100:1, preferably 10:1 up to 50:1.
Alkali metal silicates are hereinafter also referred to as alkali metal silicate (C). In the context of the present invention, the term “alkali metal silicate” refers to compounds comprising SiO2 and M2O, having a molar ratio from 1.0 to 3.5, wherein M is an alkali metal, preferably potassium and/or sodium, more preferably sodium. In the literature, such compounds are also referred to as alkaline silicate, such as sodium silicate or potassium silicate. Alkali metal silicate are soluble in water and are generally manufactured by digestion of silica sand in an aqueous alkaline medium such as NaOH or KOH solution or by dissolving silicate glass, made from the fusion of sand and soda ash or potash, in water.
A preferred example of alkali metal silicate (C) is the sodium salt of water glass.
In one embodiment of the present invention, the molar ratio of SiO2/Na2O in alkali metal silicate (C) is in the range from 1.0 to 3.5, preferably from 1.6 to 2.6.
In embodiments wherein both (co)polymer (B) and alkali metal silicate (C) are present, the weight ratio of (A):(B)+(C)] is in the range of from 5:1 up to 100:1, preferably 10:1 up to 50:1.
In one embodiment of the present invention, the weight ratio of (B)/(C) is in the range of from 10:1 to 1:10, preferably 1:1 to 1:5.
The inventive process comprises steps (a) and (b),
Mixing of citrate (A) with (co)polymer (B) and, optionally, with alkali metal silicate (C) is performed in the presence of water. Said mixing can be conducted in a way that an aqueous solution of an aqueous solution of citrate (A) and of (co)polymer (B) and, optionally, with alkali metal silicate (C) are being combined in a vessel, preferably under vigorous stirring. It is also possible to combine an aqueous solution of (co)polymer (C) and solid citrate (A), or to combine an aqueous solution of citrate (A) and with solid (co)polymer (C), or to combine aqueous slurries of citrate (A) and (co)polymer (B) with a solution of alkali metal silicate (C) and then dilute the resultant slurry with water. In a preferred embodiment, a solution of citrate (A) is provided that has a temperature of 35 to 50° C., and an aqueous solution of alkali metal silicate (C) is being added and (co)polymer (B), in bulk or in solution.
In one embodiment of the present invention, mixing according to step (a) is performed in a nozzle, for example a three-fluid nozzle, immediately before or simultaneously with step (b).
The resultant aqueous formulation is preferably in the form of an emulsion or microemulsion.
Step (a) can be performed at ambient temperature. In other embodiments, step (a) is being performed at 20° C. or at elevated temperature, for example at a temperature in the range of from 25 to 90° C., preferably 60 to 75° C.
The water used in step (a) may be present in an amount that all citrate (A) and (co)polymer (B) and, and, optionally, alkali metal silicate (C) are dissolved. However, it is also possible to use less amounts of water and mix citrate (A) and (co)polymer (B) and, optionally, alkali metal silicate (C)in a way that a slurry is being formed, with the continuous phase having the appearance of a solution or an emulsion.
In one embodiment of the present invention, the total solids content of such solution or slurry formed as result of step (a) is in the range of from 20 to 75%, preferably 35 to 50%.
In one embodiment of the present invention, such solution or slurry has a pH value in the range of from 2.5 to 13, preferably from 7 to 12 and even more preferably at least 8 up to 12.
Mixing may be performed with mechanical support, for example shaking or stirring.
In step (b), a spray-drying or spray granulation is performed, using a gas with an inlet temperature of at least 125° C. Said gas, hereinafter also being referred to as “hot gas”, may be nitrogen, a rare gas or preferably air. In the course of step (b), most of the water used in step (a) will be removed, for example at least 55%, preferably at least 65% of the water. In one embodiment of the present invention, 99% of the water at most will be removed.
Spray-drying and spray granulation will be described in more detail below.
The aqueous slurry or aqueous solution according to step (a) may have a temperature in the range of from 15 to 95° C., preferably 20 to 90° C. and even more preferably 50 to 90° C.
In step (b), said aqueous slurry or aqueous solution is introduced into a spray tower or spray granulator. A spray granulator usually contains a fluidized bed, in the context of the present invention it is a fluidized bed of citrate (A), or of inventive granule. Such fluidized bed of citrate (A) is preferably in the form of chelating agent in crystalline form, for example at least 66% crystal-line form, determined by X-Ray diffraction. In one embodiment of the present invention, the fluidized bed may have a temperature in the range of from 75 to 150° C., preferably 80 to 110° C. Spray towers usually do not contain any fluidized bed.
Spraying is being performed through one or more nozzles per spray tower or spray granulator. Suitable nozzles are, for example, high-pressure rotary drum atomizers, rotary atomizers, three-fluid nozzles, single-fluid nozzles, three-fluid nozzles and two-fluid nozzles, single-fluid nozzles and two-fluid nozzles and three-fluid nozzles being preferred. The first fluid is the aqueous slurry or aqueous solution or emulsion, respectively, the second fluid is compressed hot gas, also referred to as hot gas inlet stream, for example with a pressure of 1.1 to 7 bar. The hot gas inlet stream may have a temperature in the range of from at least 125° C. to 250° C., preferably 150 to 250° C., even more preferably 160 to 220° C.
In step (b), the aqueous slurry or aqueous solution obtained from step (a) is introduced in the form of droplets. In one embodiment of the present invention, the droplets formed during the spray-granulating or spray-drying have an average diameter in the range of from 10 to 500 82 m, preferably from 20 to 180 μm, even more preferably from 30 to 100 μm.
In one embodiment of the present invention, the off-gas departing the spray tower or spray granulator, respectively, may have a temperature in the range of from 40 to 140° C., preferably 80 to 110° C. but in any way colder than the hot gas stream. Preferably, the temperature of the off-gas departing the drying vessel and the temperature of the solid product present in the drying vessel are identical.
In one embodiment of the present invention, the pressure in the spray tower or spray granulator in step (b) is normal pressure ±100 mbar, preferably normal pressure ±20 mbar, for example one mbar less than normal pressure.
In one embodiment of the present invention, especially in a process for making an inventive granule, the average residence time of citrate (A) in step (b) is in the range of from 2 minutes to 4 hours, preferably from 30 minutes to 2 hours.
In another embodiment of the present invention, spray-granulation is being performed by performing two or more consecutive spray-drying processes, for example in a cascade of at least two spray dryers, for example in a cascade of at least two consecutive spray towers or a combination of a spray tower and a spray chamber, said spray chamber containing a fluidized bed. In the first dryer, a spray-drying process is being performed in the way as follows.
Spray-drying may be preferred in a spray dryer, for example a spray chamber or a spray tower. An aqueous slurry or solution with a temperature preferably higher than ambient temperature, for example in the range of from 50 to 95° C. is introduced into the spray dryer through one or more spray nozzles into a hot gas inlet stream, for example nitrogen or air, the solution or slurry being converted into droplets and the water being vaporized. The hot gas inlet stream may have a temperature in the range of from 125 to 350° C. The second spray dryer is charged with a fluidized bed with solid from the first spray dryer and solution or slurry obtained according to the above step is sprayed onto or into the fluidized bed, together with a hot gas inlet stream. The hot gas inlet stream may have a temperature in the range of from 125 to 350° C., preferably 160 to 220° C.
In embodiments wherein an aged slurry is used, such aging may take in the range of from 2 hours to 24 hours at the temperature preferably higher than ambient temperature.
In the course of step (b), most of the water is removed. Most of the water shall mean that a residual moisture content of 0.1 to 20% by weight, referring to the powder or granule, remains in embodiments that start of from a solution, about 51 to 75% by weight of the water present in the aqueous solution is removed in step (b).
A powder or granule is obtained.
In one embodiment of the inventive process, the inventive process may contain further steps, for example separating off fines or lumps, milling down lumps, and/or returning fines and milled down lumps into the inventive process, for example by directly returning them into a spray granulator—or dissolving them in water and then spray-drying.
Such optional additional steps are hereinafter also referred to step (c), and they are briefly discussed hereinafter.
At the end of step (b), powder or granule, respectively, is removed from the spray tower or spray granulator. Said powder or granule has been at least partially formed in the course of step (b) of the inventive process. Said removal may be performed through one or more openings in the spray tower or spray granulator. Preferably, such one or more openings are at the bottom of the respective spray tower or spray granulator. Powder or granules, respectively, are removed including fines and lumps.
In embodiments in which a powder is made preferably 70 to 95% by weight of the solid formed are withdrawn from the spray tower per hour. In embodiments in which a granule is made, 20 to 60% of the fluidized bed are withdrawn per hour, for example with an extruder screw. Additional solids, especially fines, may be collected in the off-gas purification.
In one embodiment of the inventive process, in the course of step (c) fines may be separated off from said powder or granules, wherein said fines have a maximum particle diameter of 350 μm. Preferably, fines in processes wherein granules are desired may have a particles diameter in the range of from 1 to 150 μm. The act of separating off the fines may be performed by sieving or by air classification, preferably by sieving.
In embodiments wherein spray-drying is performed, fines have a particles diameter of 30 μm or less, for example 1 to 30 μm.
In one embodiment of the present invention, in step (b) 40 to 100% of the fines present in the respective material withdrawn at the end of step (b) are separated off. In a preferred embodiment, in step (c) 80 to 99% by weight of the fines are separated off, and the residual 1 to 20% are left in the respective powder or granule. It is tedious to try to remove the fines quantitatively.
In step (c) of the inventive process, so-called lumps or “overs” may be separated off from said powder or granules.
In embodiments wherein granules are desired, said lumps to be separated off are particles that have a minimum particle diameter of 1,000 μm, for example, 1,500 μm to 2 mm or even more. In a preferred embodiment, lumps are particles that have a minimum particle diameter of 1,250 μm or more, even more preferably 900 μm to 2 mm.
In embodiments wherein powders are desired, said lumps or overs have a minimum particle diameter of 250 μm or more, for example 250 to 1,000 μm.
Overs or lumps may be removed, e.g., with the help of a discharge screw or a rotary valve, usually together with desired product, and then classified.
It is observed that in connection with the recycling, the smaller the maximum size of the lumps to be separated off in step (c) the better the hygroscopicity behavior of the later chelating agent, and the better the peroxide stability.
Separating off lumps and fines may be performed in any order, consecutively or simultaneously.
In one embodiment of the present invention, the amount of powder or granule, respectively, other than fines and overs is in the range of from 55 to 70% by weight, referring to total amount of material removed at the end of step (b).
The lumps separated of in step (c) may be milled down to a smaller size, for example to maximum particle diameter of 500 μm, preferably to a maximum particle diameter of 400 μm. The milling may be performed in any type of mills. Examples of particularly useful mills are jet mills, pin mills and bolting machines (German: Stiftmühlen). Further examples are roller mills and ball mills.
In one embodiment, said fines from step (c) and milled lumps from step (c) are reintroduced into a spray-dryer or spray-granulator. Such reintroducing may be performed by pneumatically transporting said fines milled lumps from step (c) into the spray tower or spray granulator, respectively, preferably through an extra opening rather than together with solution or slurry from step (a).
The share of fines withdrawn in step (c) may be in the range of from 0.5 to 20% by weight of the total citrate (A) withdrawn in step (b), preferably 4 to 18% by weight. The share of lumps is in the range of from 5 to 60% by weight of the total citrate (A) withdrawn in step (b), preferably 20 to 40% by weight and even more preferably 25 to 35% by weight. With a higher share of lumps, the inventive process becomes economically unfavorable because it is too much recycling. With a lower share of lumps the hygroscopicity may become too high.
By performing the inventive process, powders and granules may be obtained. Such powders and granules have a particularly high bulk density (German: Schüttdichte), for example 800 to 950 g/l, preferably 850 to 920 g/l and more preferably 875 to 910 g/l, determined according to DIN ISO 697-1984-01.
A further aspect of the present invention is related to granules and powders, hereinafter also referred to as inventive granules and inventive powders, respectively. Inventive powders and inventive granules contain
In this weight ratio, impurities of citrate (A) that stem from the synthesis, see above, are neglected.
In the context of the present invention, the term “in molecularly disperse form” implies that all or a vast majority, for example at least 80% of the particles of inventive powder and of inventive granules contain citrate (A) and (co)polymer (C) or preferably citrate (A) and alkali metal silicate (C) and (co)polymer (B). The term “in molecularly disperse form” implies as well that citrate (A) and (co)polymer (C) or all three of the foregoing are distributed over the diameter of the particle in an almost homogeneous way.
In a preferred embodiment of the present invention, the weight ratio of (A):[(B)+(C)] is in the range of from 10:1 up to 50:1.
In one embodiment of the present invention, the weight ratio of (B)/(C) is in the range of from 10:1 to 1:10, preferably 1:1 to 1:5.
In one embodiment of the present invention, inventive powders are selected from powders having an average particle diameter in the range of from 1 μm to less than 0.1 mm.
In one embodiment of the present invention, inventive granules are selected from granules with an average particle diameter in the range of from 0.1 mm to 2 mm, preferably 0.75 mm to 1.25 mm.
In one embodiment of the present invention, inventive powder or inventive granule contains in the range of from 95 to 99.8% by weight citrate (A) and 0.1 to 4.5% by weight of (co)polymer (B), and, optionally, 0.1 to 2% by weight salt of alkali metal silicate (C), percentages referring to the solids content of said powder or granule.
Inventive powders and inventive granules exhibit overall advantageous properties including but not limited to an excellent yellowing behavior, especially in the presence of bleaching agents. They are therefore excellently suitable for the manufacture of cleaning agents that contain at least one bleaching agent, such cleaning agent hereinafter also being referred to as bleach. In particular inventive powders and inventive granules are suitable for the manufacture cleaning agent for fibers or hard surfaces wherein said cleaning agent contains at least one peroxy compound.
Inventive granules and especially inventive powders may easily be converted into compactates and into agglomerates.
Another aspect of the present invention is therefore the use of an inventive powder or an inventive granule according for the manufacture of a cleaning agent that may contain at least one bleaching agent, and in particular for the manufacture of cleaning agent for fibers or hard surfaces, wherein said cleaning agent contains at least one peroxy compound. Another aspect of the present invention is a process for making at a cleaning agent by combining at least one inventive powder or at least one inventive granule with at least one bleaching agent, preferably at least one peroxy compound. Another aspect of the present invention is a cleaning agent, hereinafter also being referred to as inventive cleaning agent.
Inventive cleaning agents may contain at least one bleaching agent and at least one inventive powder or at least one inventive granule. Inventive cleaning agents show a reduced tendency for yellowing and therefore have an extended shelve-life.
Examples of suitable peroxy compounds are sodium perborate, anhydrous or for example as monohydrate or as tetrahydrate or so-called dihydrate, sodium percarbonate, anhydrous or, for example, as monohydrate, hydrogen peroxide, persulfates, organic peracids such as peroxylauric acid, peroxystearic acid, peroxy-α-naphthoic acid, 1,12-diperoxydodecanedioic acid, per-benzoic acid, peroxylauric acid, 1,9-diperoxyazelaic acid, diperoxyisophthalic acid, in each case as free acid or as alkali metal salt, in particular as sodium salt, also sulfonylperoxy acids and cationic peroxy acids.
In a preferred embodiment, peroxy compound is selected from inorganic percarbonates, persulfates and perborates. Examples of sodium percarbonates are 2 Na2CO3.3 H2O2. Examples of sodium perborate are (Na2[B(OH)2(O2)]2), sometimes written as NaBO2.O2.3H2O instead. Most preferred peroxy compound is sodium percarbonate.
The term “cleaning agents” includes compositions for dishwashing, especially hand dishwash and automatic dishwashing and ware-washing, and compositions for hard surface cleaning such as, but not limited to compositions for bathroom cleaning, kitchen cleaning, floor cleaning, descaling of pipes, window cleaning, car cleaning including truck cleaning, furthermore, open plant cleaning, cleaning-in-place, metal cleaning, disinfectant cleaning, farm cleaning, high pressure cleaning, and in addition, laundry detergent compositions.
Such cleaning agents may be liquids, gels or preferably solids at ambient temperature, solids cleaning agents being preferred. They may be in the form of a powder or in the form of a unit dose, for example as a tablet.
In one embodiment of the present invention, inventive cleaning agents may contain in the range of from 2 to 50% by weight of inventive powder or inventive granule, in the range of from 0.5 to 15% by weight of bleach. Percentages are based on the solids content of the respective inventive cleaning agent.
Inventive cleaning agents may contain further ingredients such as one or more surfactants that may be selected from non-ionic, zwitterionic, cationic, and anionic surfactants. Other ingredients that may be contained in inventive cleaning agents may be selected from bleach activators, bleach catalysts, corrosion inhibitors, sequestering agents other than citrate (A), enzymes, fragrances, dyestuffs, antifoams, and builders.
Particularly advantageous inventive cleaning agents may contain one or more complexing agents selected from alkali metal salts of methylglycine diacetic acid (“MGDA”) or of glutamic acid diacetic acid (“GLDA”). Advantageous detergent compositions for cleaners and advantageous laundry detergent compositions may contain one or more sequestrant (chelating agent) other than a mixture according to the present invention. Examples for sequestrants other than a mixture according to the present invention are IDS (iminodisuccinate), phosphonic acid derivatives, for example the disodium salt of hydroxyethane-1,1-diphosphonic acid (“HEDP”), and polymers with complexing groups like, for example, polyethyleneimine in which 20 to 90 mole-% of the N-atoms bear at least one CH2COO− group, and their respective alkali metal salts, especially their sodium salts, for example IDS-Na4, and trisodium citrate, and phosphates such as STPP (sodium tripolyphosphate). Due to the fact that phosphates raise environmental concerns, it is preferred that advantageous inventive cleaning agents are free from phosphate. “Free from phosphate” should be understood in the context of the present invention, as meaning that the content of phosphate and polyphosphate is in sum in the range from 10 ppm to 0.2% by weight, determined by gravimetric methods and referring to the respective inventive cleaning agent.
Inventive cleaning agents may contain one or more surfactant, preferably one or more non-ionic surfactant.
Preferred non-ionic surfactants are alkoxylated alcohols, di- and multiblock copolymers of ethylene oxide and propylene oxide and reaction products of sorbitan with ethylene oxide or propylene oxide, alkyl polyglycosides (APG), hydroxyalkyl mixed ethers and amine oxides.
Preferred examples of alkoxylated alcohols and alkoxylated fatty alcohols are, for example, compounds of the general formula (II)
in which the variables are defined as follows:
In one embodiment, compounds of the general formula (I) may be block copolymers or random copolymers, preference being given to block copolymers.
Other preferred examples of alkoxylated alcohols are, for example, compounds of the general formula (II)
in which the variables are defined as follows:
The sum a+b+d is preferably in the range of from 5 to 100, even more preferably in the range of from 9 to 50.
Preferred examples for hydroxyalkyl mixed ethers are compounds of the general formula (IV)
in which the variables are defined as follows:
The variables m and n are in the range from zero to 300, where the sum of n and m is at least one, preferably in the range of from 5 to 50. Preferably, m is in the range from 1 to 100 and n is in the range from 0 to 30.
Compounds of the general formula (II) and (III) may be block copolymers or random copolymers, preference being given to block copolymers.
Further suitable nonionic surfactants are selected from di- and multiblock copolymers, composed of ethylene oxide and propylene oxide. Further suitable nonionic surfactants are selected from ethoxylated or propoxylated sorbitan esters. Amine oxides or alkyl polyglycosides, especially linear C4-C16-alkyl polyglucosides and branched C8-C14-alkyl polyglycosides such as compounds of general average formula (V) are likewise suitable.
wherein the variables are defined as follows:
An overview of suitable further nonionic surfactants can be found in EP-A 0 851 023 and in DEA 198 19 187.
Mixtures of two or more different nonionic surfactants may also be present.
Other surfactants that may be present are selected from amphoteric (zwitterionic) surfactants and anionic surfactants and mixtures thereof.
Examples of amphoteric surfactants are those that bear a positive and a negative charge in the same molecule under use conditions. Preferred examples of amphoteric surfactants are so-called betaine-surfactants. Many examples of betaine-surfactants bear one quaternized nitrogen atom and one carboxylic acid group per molecule. A particularly preferred example of amphoteric surfactants is cocamidopropyl betaine (lauramidopropyl betaine).
Examples of amine oxide surfactants are compounds of the general formula (VI)
R7R8R9N→O (VI)
wherein R7, R5 and R9 are selected independently from each other from aliphatic, cycloaliphatic or C2-C4-alkylene C10-C20-alkylamido moieties. Preferably, R7 is selected from C8-C20-alkyl or C2-C4-alkylene C10-C20-alkylamido and R5 and R9 are both methyl.
A particularly preferred example is lauryl dimethyl aminoxide, sometimes also called lauramine oxide. A further particularly preferred example is cocamidylpropyl dimethylaminoxide, sometimes also called cocamidopropylamine oxide.
Examples of suitable anionic surfactants are alkali metal and ammonium salts of C8-C18-alkyl sulfates, of C8-C18-fatty alcohol polyether sulfates, of sulfuric acid half-esters of ethoxylated C4-C12-alkylphenols (ethoxylation: 1 to 50 mol of ethylene oxide/mol), C12-C18 sulfo fatty acid alkyl esters, for example of C12-C18 sulfo fatty acid methyl esters, furthermore of C12-C18-alkylsulfonic acids and of C10-C18-alkylarylsulfonic acids. Preference is given to the alkali metal salts of the aforementioned compounds, particularly preferably the sodium salts.
Further examples for suitable anionic surfactants are soaps, for example the sodium or potassium salts of stearoic acid, oleic acid, palmitic acid, ether carboxylates, and alkylether phosphates.
Preferably, laundry detergent compositions contain at least one anionic surfactant.
In one embodiment of the present invention, inventive cleaning agents that are determined to be used as laundry detergent compositions may contain 0.1 to 60% by weight of at least one surfactant, selected from anionic surfactants, amphoteric surfactants and amine oxide surfactants.
In one embodiment of the present invention, inventive cleaning agents that are determined to be used for hard surface cleaning may contain 0.1 to 60% by weight of at least one surfactant, selected from anionic surfactants, amphoteric surfactants and amine oxide surfactants.
In a preferred embodiment, inventive cleaning agents do not contain any anionic detergent.
Inventive cleaning agents may comprise one or more bleach catalysts. Bleach catalysts can be selected from bleach-boosting transition metal salts or transition metal complexes such as, for example, manganese-, iron-, cobalt-, ruthenium- or molybdenum-salen complexes or carbonyl complexes. Manganese, iron, cobalt, ruthenium, molybdenum, titanium, vanadium and copper complexes with nitrogen-containing tripod ligands and also cobalt-, iron-, copper- and ruthenium-amine complexes can also be used as bleach catalysts.
Inventive cleaning agents may comprise one or more bleach activators, for example N-methylmorpholinium-acetonitrile salts (“MMA salts”), trimethylammonium acetonitrile salts, N-acylimides such as, for example, N-nonanoylsuccinimide, 1,5-diacetyl-2,2-dioxohexahydro -1,3,5-triazine (“DADHT”) or nitrile quats (trimethylammonium acetonitrile salts).
Further examples of suitable bleach activators are tetraacetylethylenediamine (TAED) and tetraacetylhexylenediamine.
Inventive cleaning agents may comprise one or more corrosion inhibitors. In the present case, this is to be understood as including those compounds which inhibit the corrosion of metal. Examples of suitable corrosion inhibitors are triazoles, in particular benzotriazoles, bisbenzotriazoles, aminotriazoles, alkylaminotriazoles, also phenol derivatives such as, for example, hydroquinone, pyrocatechol, hydroxyhydroquinone, gallic acid, phloroglucinol or pyrogallol. In one embodiment of the present invention, inventive cleaning agents comprise in total in the range from 0.1 to 1.5% by weight of corrosion inhibitor.
Inventive cleaning agents may comprise one or more additional builders, selected from organic and inorganic builders. Examples of suitable inorganic builders are sodium sulfate or sodium carbonate, zeolites, sheet silicates, in particular those of the formula α-Na2Si2O5, β-Na2Si2O5, and δ-Na2Si2O5, also fatty acid sulfonates, α-hydroxypropionic acid, alkali metal malonates, fatty acid sulfonates, alkyl and alkenyl disuccinates, tartaric acid diacetate, tartaric acid monoacetate, oxidized starch, and polymeric builders, for example polycarboxylates and polyaspartic acid. Examples of organic builders are especially polymers and copolymers other than (co)polymer (B), or one additional copolymer (B). In one embodiment of the present invention, organic builders are selected from polycarboxylates, for example alkali metal salts of (meth)acrylic acid homopolymers or (meth)acrylic acid copolymers, partially or completely neutralized with alkali.
Suitable comonomers for (meth)are monoethylenically unsaturated dicarboxylic acids such as maleic acid, fumaric acid, maleic anhydride, itaconic acid and citraconic acid. A suitable polymer is in particular polyacrylic acid, which preferably has an average molecular weight Mw in the range from 2000 to 40 000 g/mol, preferably 3,000 to 10,000 g/mol.
It is also possible to use copolymers of at least one monomer from the group consisting of monoethylenically unsaturated C3-C10-mono- or C4-C10-dicarboxylic acids or anhydrides thereof, such as maleic acid, maleic anhydride, acrylic acid, methacrylic acid, fumaric acid, itaconic acid and citraconic acid, with at least one hydrophilic or hydrophobic monomer as listed below.
Suitable hydrophobic monomers are, for example, isobutene, diisobutene, butene, pentene, hexene and styrene, olefins with 10 or more carbon atoms or mixtures thereof, such as, for example, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene, 1-octadecene, 1-eicosene, 1-docosene, 1-tetracosene and 1-hexacosene, C22-α-olefin, a mixture of C20-C24-α-olefins and polyisobutene having on average 12 to 100 carbon atoms per molecule.
Suitable hydrophilic monomers are monomers with sulfonate or phosphonate groups, and also nonionic monomers with hydroxyl function or alkylene oxide groups. By way of example, mention may be made of: allyl alcohol, isoprenol, methoxypolyethylene glycol (meth)acrylate, methoxypolypropylene glycol (meth)acrylate, methoxypolybutylene glycol (meth)acrylate, methoxypoly(propylene oxide-co-ethylene oxide) (meth)acrylate, ethoxypolyethylene glycol (meth)acrylate, ethoxypolypropylene glycol (meth)acrylate, ethoxypolybutylene glycol (meth)acrylate and ethoxypoly(propylene oxide-co-ethylene oxide) (meth)acrylate. Polyalkylene glycols here may comprise 3 to 50, in particular 5 to 40 and especially 10 to 30 alkylene oxide units per molecule.
Particularly preferred sulfonic-acid-group-containing monomers here are 1-acrylamido -1-propanesulfonic acid, 2-acrylamido-2-propanesulfonic acid, 2-acrylamido -2-methylpropanesulfonic acid, 2-methacrylamido-2-methylpropanesulfonic acid, 3-methacrylamido-2-hydroxypropanesulfonic acid, allylsulfonic acid, methallylsulfonic acid, allyloxybenzenesulfonic acid, methallyloxybenzenesulfonic acid, 2-hydroxy -3-(2-propenyloxy)propanesulfonic acid, 2-methyl-2-propene-1-sulfonic acid, styrenesulfonic acid, vinylsulfonic acid, 3-sulfopropyl acrylate, 2-sulfoethyl methacrylate, 3-sulfopropyl methacry-late, sulfomethacrylamide, sulfomethylmethacrylamide, and salts of said acids, such as sodium, potassium or ammonium salts thereof.
Particularly preferred phosphonate-group-containing monomers are vinylphosphonic acid and its salts.
Moreover, amphoteric polymers can also be used as builders.
Inventive cleaning agents may comprise, for example, in the range from in total 10 to 50% by weight, preferably up to 20% by weight, of builder.
In one embodiment of the present invention, inventive cleaning agents according to the invention may comprise one or more cobuilders.
Inventive cleaning agents may comprise one or more antifoams, selected for example from silicone oils and paraffin oils.
In one embodiment of the present invention, inventive cleaning agents comprise in total in the range from 0.05 to 0.5% by weight of antifoam.
Inventive cleaning agents may comprise one or more enzymes. Examples of enzymes are lipases, hydrolases, amylases, proteases, cellulases, esterases, pectinases, lactases and peroxidases.
In one embodiment of the present invention, inventive cleaning agents may comprise, for example, up to 5% by weight of enzyme, preference being given to 0.1 to 3% by weight. Said enzyme may be stabilized, for example with the sodium salt of at least one C1-C3-carboxylic acid or C4-C10-dicarboxylic acid. Preferred are formates, acetates, adipates, and succinates.
In one embodiment of the present invention, inventive cleaning agents may comprise at least one zinc salt. Zinc salts can be selected from water-soluble and water-insoluble zinc salts. In this connection, within the context of the present invention, water-insoluble is used to refer to those zinc salts which, in distilled water at 25° C., have a solubility of 0.1 g/l or less. Zinc salts which have a higher solubility in water are accordingly referred to within the context of the present invention as water-soluble zinc salts. In one embodiment of the present invention, zinc salt is selected from zinc benzoate, zinc gluconate, zinc lactate, zinc formate, ZnCl2, ZnSO4, zinc acetate, zinc citrate, Zn(NO3)2, Zn(CH3SO3)2 and zinc gallate, preferably ZnCl2, ZnSO4, zinc acetate, zinc citrate, Zn(NO3)2, Zn(CH3SO3)2 and zinc gallate.
In another embodiment of the present invention, zinc salt is selected from ZnO, ZnO.aq, Zn(OH)2 and ZnCO3. Preference is given to ZnO.aq.
In one embodiment of the present invention, zinc salt is selected from zinc oxides with an average particle diameter (weight-average) in the range from 10 nm to 100 μm. The cation in zinc salt can be present in complexed form, for example complexed with ammonia ligands or water ligands, and in particular be present in hydrated form. To simplify the notation, within the context of the present invention, ligands are generally omitted if they are water ligands.
Depending on how the pH value of mixture according to the invention is adjusted, zinc salt can change. Thus, it is for example possible to use zinc acetate or ZnCl2 for preparing formulation according to the invention, but this converts at a pH of 8 or 9 in an aqueous environment to ZnO, Zn(OH)2 or ZnO.aq, which can be present in non-complexed or in complexed form.
Zinc salt may be present in those inventive cleaning agents that are solid at room temperature. In such inventive cleaning agents zinc salts are preferably present in the form of particles which have for example an average diameter (number-average) in the range from 10 nm to 100 μm, preferably 100 nm to 5 μm, determined for example by X-ray scattering.
Zinc salt may be present in those inventive cleaning agents that are liquid at room temperature. In such inventive cleaning agents zinc salts are preferably present in dissolved or in solid or in colloidal form.
In one embodiment of the present invention, inventive cleaning agents comprise in total in the range from 0.05 to 0.4% by weight of zinc salt, based in each case on the solids content of the cleaning agent in question.
Here, the fraction of zinc salt is given as zinc or zinc ions. From this, it is possible to calculate the counterion fraction.
In one embodiment of the present invention, inventive cleaning agents are free from heavy metals apart from zinc compounds. Within the context of the present, this may be understood as meaning that inventive cleaning agents are free from those heavy metal compounds which do not act as bleach catalysts, in particular of compounds of iron and of bismuth. Within the context of the present invention, “free from” in connection with heavy metal compounds is to be understood as meaning that the content of heavy metal compounds which do not act as bleach catalysts is in sum in the range from 0 to 100 ppm, determined by the leach method and based on the solids content. Preferably, inventive cleaning agents has, apart from zinc, a heavy metal content below 0.05 ppm, based on the solids content of the formulation in question. The fraction of zinc is thus not included.
Within the context of the present invention, “heavy metals” are deemed to be all metals with a specific density of at least 6 g/cm3 with the exception of zinc. In particular, the heavy metals are metals such as bismuth, iron, copper, lead, tin, nickel, cadmium and chromium. Preferably, inventive cleaning agents comprise no measurable fractions of bismuth compounds, i.e. for example less than 1 ppm.
Inventive cleaning agents are excellent for cleaning hard surfaces and fibres.
The present invention is further illustrated by working examples.
General remarks: The bulk density was determined in accordance with ISO 697 (2nd edition 1981-03-01).
NI: Norm liter, liters under normal conditions; Nm3: norm cubic meter, cubic meter under normal conditions. Unless expressly indicated otherwise, percentages are % by weight.
Starting Materials:
The molecular weight of polymers (B.1) and (B.2) was determined by GPC. Said measurements were performed at a pH value of 7.4 (phosphate buffer), stationary phase: cross-linked poly-acrylate, mobile phase: water, pH value 7.4, phosphate buffer with 0.01 M NaN3.
The calcium binding capacity was determined by titration with CaCl2 solution: a glass beaker is charged with 1 g of granule dissolved in 100 ml demineralized water. Then, 2 ml of the 10% by weight sodium carbonate solution are added and set to a pH value of 11 ±0.2 with NaOH (1 mol/L) or HCI (1 mol/L). Standard titration parameters for polymers are at 25° C. and pH 11. The solution was clear and colorless. The optrode is set to 660 nm and put into the glass beaker.
I. Manufacture of Spray Liquors
I.1 Manufacture of Spray Liquor SL.1, Step (a.1)
A vessel was charged with 14.629 kg of an aqueous solution of (A.1) (40% by weight). An amount of 124 g of a 48.5% by weight aqueous solution of (C.1) and 246 g of a 49% by weight aqueous solution (B.1) was added. The spray liquor SL.1 so obtained was stirred vigorously and then heated to 70° C. for 3 hours and then subjected to spray granulation.
I.2 Manufacture of Spray Liquor SL.2, Step (a.2)
A vessel was charged with 15.28 kg of an aqueous solution of (A.1) (40% by weight) and 720 g of an aqueous solution of (B.1) (45% by weight). The spray liquor SL.2 so obtained was stirred vigorously and then heated to 70° C. and subjected to spray granulation.
I.3 Manufacture of Spray Liquor SL.3, Step (a.3)
A vessel was charged with 15.5 kg of an aqueous solution of (A.1) (40% by weight) and 750 g of an aqueous solution of (B.2) (40% by weight). The spray liquor SL.3 so obtained was stirred and then heated to 70° C. and subjected to spray granulation.
II Spray Granulation
II.1 Spray Granulation of Spray Liquor SL.1, Step (b.1)
A lab scale granulator, commercially available as Glatt Procell Lab System with Vario 3 Insert, is charged with 0.9 kg of solid trisodium citrate spherical particles, diameter 350 to 1000 μm, and 600 g of milled trisodium citrate particles. An amount of 200 Nm3/h of air with a temperature of 165 to 168° C. is blown from the bottom. A fluidized bed of trisodium citrate particles is obtained. The above spray liquor SL.1 is introduced by spraying 6 kg of SL.1 (70° C.) per hour into the fluidized bed from the bottom through a two-fluid nozzle, absolute pressure in the nozzle: 4 bar. Granules are formed, and the bed temperature, which corresponds to the surface temperature of the solids in the fluidized bed, is 95 to 101° C.
Particles that were large (heavy) enough fall through the zigzag air classifier (operated at 1.8 to 2 bar relative pressure) are continuously transferred into a sample bottle. The smaller (lighter) granules are blown through the recycle back into the fluidized bed by the air classifier.
When about 1 L of granules were collected in the sample bottle, the bottle is replaced by a new sample bottle. The collected granules were subjected to a sieving step, mesh size 1 mm. Two fractions were obtained: coarse particles (diameter>1 mm) and value fraction (<1 mm). Coarse particles (diameter>1 mm), were milled down together with small amounts of value fraction using a hammer mill (Kinetatica Polymix PX-MFL 90D) at 4000 rounds per minute (rpm), 2 mm mesh. The powder so obtained was returned into the fluidized bed. The major part of the value fraction, which was not milled down, left the process and was collected.
After consumption of 12 kg of SL.1 a steady state is reached. Then, the fraction <1 mm is collected as inventive granules Gr.1.
The residual moisture of Gr.1 is determined to be 11.5%, referring to the total solids content of the granule and determined by Karl-Fischer titration.
In the above example, hot air of 170° C. can be replaced by hot N2 having a temperature of
The inventive granule Gr.1 has an excellent iron and calcium binding capacity combined with low hygroscopicity and low tendency of yellowing.
II.2 Spray Granulation of Spray Liquor SL.2, Step (b.2)
When experiment under II.1 is essentially repeated but with SL.2 instead of SL.1 and under similar parameter for the spray granulation, inventive granule Gr.2 is obtained, with low hygroscopicity and low tendency of yellowing but high iron and calcium binding capacity.
II.3 Spray Granulation of Spray Liquor SL.3, Step (b.3)
When experiment under II.1 is essentially repeated but with SL.3 instead of SL.1 and under similar parameter for the spray granulation, inventive granule Gr.3 is obtained, with low hygroscopicity and low tendency of yellowing but high iron and calcium binding capacity.
II.4 Spray Granulation of an Aqueous Solution of (A.1)
When experiment under II.1 is essentially repeated but with an aqueous solution of (A.1) with a concentration as in SL.1—but neither (B.1) nor (B.1) nor (B.2)—instead of SL.1 and under similar parameter for the spray granulation, comparative granule C-Gr.4 is obtained, with comparatively low iron and calcium binding capacity.
From inventive granules, example detergent compositions for automatic dishwashing detergents can be formulated by mixing the respective components according to Table 1.
| Number | Date | Country | Kind |
|---|---|---|---|
| 19217607.1 | Dec 2019 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2020/084607 | 12/4/2020 | WO |
