EP0612347A1

EP0612347A1 - Method of manufacturing dense-granulate low-alkali washing agents, containing no active chlorine or phosphate, for washing-up machines

Info

Publication number: EP0612347A1
Application number: EP92923070A
Authority: EP
Inventors: Hans Kruse; Christiane Zeise; Jürgen Härer; Franz Hundgeburt; Jochen Jacobs
Original assignee: Henkel AG and Co KGaA
Current assignee: Henkel AG and Co KGaA
Priority date: 1991-11-14
Filing date: 1992-11-06
Publication date: 1994-08-31
Also published as: DE4137470A1; WO1993010210A1

Abstract

Procédé de fabrication pour adjuvant de lavage liant le calcium, comprenant des additifs détergents alcalins granulaires à base de sels de sodium d'acides méthacryliques ou acryliques homopolymères ou copolymères, d'autres adjuvants, des agents de blanchiment, de l'eau et, le cas échéant, des agents tensioactifs non ioniques faiblement moussants, des enzymes, des activateurs de blanchiment, des substances odoriférantes et des colorants, consistant à prémélanger avec de l'eau et, éventuellement, d'autres composants liquides, le polyacrylate ou polyméthacrylate en poudre et/ou les additifs détergents alcalins avec du carbonate de sodium comprimé et d'autres adjuvants de granulation agglomérante, à mélanger ensuite le granulé avec l'agent de blanchiment et éventuellement avec un activateur de blanchiment, une substance odoriférante, des enzymes et un colorant, à saupoudrer de carbonate de sodium pulvérulent le granulé encore légèrement collant et enfin, à asperger le produit avec des agents tensioactifs non ioniques, de manière à lier la poudre de carbonate en excès.A manufacturing process for a calcium-binding washing aid, comprising granular alkaline detergent additives based on sodium salts of methacrylic or acrylic acids homopolymers or copolymers, other builders, bleaches, water and, where appropriate, low-foaming nonionic surfactants, enzymes, bleach activators, odoriferous substances and dyes, consisting of premixing with water and, optionally, other liquid components, polyacrylate or polymethacrylate powder and/or alkaline detergent additives with compressed soda ash and other clumping granulation aids, then mixing the granulate with the bleach and optionally with a bleach activator, an odoriferous substance, enzymes and a dye , sprinkling the still slightly sticky granulate with powdered sodium carbonate and finally, spraying the product with agents. ts nonionic surfactants, so as to bind the excess carbonate powder.

Description

"Process for the production of low alkaline, active chlorine and phosphate-free machine dishwashing detergents in the form of heavy granules"

The invention relates to a new process for producing machine washable dishwasher detergents which are low in alkali, active chlorine and phosphate-free, in the form of storage-stable, free-flowing, dust-free granules with high bulk densities - in particular in the range from about 750 to 1,100 g / l.

In the course of the ecological renunciation of phosphates or polyphosphates in detergents and cleaning agents, new and substituting framework substances are constantly being developed and optimized.

A powdery, commercially available poly (meth) acrylate with an active substance content of 92-93% and / or a granular alkaline cleaning additive based on sodium salts of homopolymeric or copolymeric (meth) acrylic acids is used as the calcium-binding framework substance , which is the subject of German patent application P 3937469.6.

It consists of:

(a) 35 to 60% by weight of sodium salts of at least one homopolymeric or copolymeric (meth) acrylic acid,

(b) 25 to 50% by weight sodium carbonate (calculated as anhydrous),

(c) 4 to 20% by weight sodium sulfate (calculated as anhydrous) and

(d) 1 to 7 wt .-% water, preferably from

(a) 40 to 55% by weight, in particular 45 to 52% by weight,

(b) 30 to 45% by weight, in particular 30 to 40% by weight,

(c) 5 to 15% by weight, in particular 5 to 10% by weight and

(d) 2 to 6% by weight, in particular 3 to 5% by weight, of the abovementioned compounds. Component (a) consists of homopolymeric or copolymeric carboxylic acids in the form of the sodium salts. Suitable homopolymers are polymethacrylic acid and preferably polyacrylic acid, for example those with a molecular weight of 800 to 150,000 (based on acid). If only homopolymeric polyacrylic acids (in salt form) are used, their molecular weight is preferably 1000 to 80,000 (based on acid) in the interest of good flowability and storage stability.

Suitable copolymers are those of acrylic acid with methacrylic acid and preferably copolymers of acrylic acid or methacrylic acid with maleic acid. Copolymers of acrylic acid with maleic acid, as are characterized, for example, in EP 25991-B1, have proven particularly suitable. These are copolymers which contain 50 to 90% by weight of acrylic acid and 50 to 10% by weight of maleic acid. Copolymers in which 60 to 85% by weight of acrylic acid and 40 to 15% by weight of maleic acid are present are particularly preferred. Their molecular weight, based on free acids, is generally 5,000 to 200,000, preferably 10,000 to 120,000.

Mixtures of different homopolymers and copolymers can also advantageously be used, in particular mixtures of homopolymeric acrylic acid and the copolymers of 50 to 90% by weight of acrylic acid and 50 to 10% of maleic acid described above. Such mixtures, which are characterized by favorable grain properties and high storage stability, can consist, for example, of 10 to 50% by weight of homopolymeric acrylic acid and 90 to 50% by weight of acrylic acid-maleic acid copolymers. Highly polymeric polyacrylic acids can also be used in these mixtures, which, when used alone, have a slightly greater tendency to stick or melt than the low molecular weight polyacrylates.

The sodium carbonate (b) and the sodium sulfate (c) are used in anhydrous form. With proportions of sodium carbonate of approx. 40% by weight and more, it is advisable to reduce the water content (d) of the additives to less than 6% by weight or to choose a somewhat higher proportion of sodium sulfate, for example in the range 8 to 15% by weight. Proportions of sodium sulfate of over 10% by weight, preferably 15 to 20% by weight, fundamentally improve the grain properties and shelf life of the additives. On the other hand, sodium sulfate is ineffective ballast substance when the additives are used, which is why its proportion should be as small as possible. It is very surprising that fractions of 5 to 6% by weight (c) are sufficient to add additives with a content of approx. 50% by weight (a), approx. 40% by weight (b) and approx To stabilize 4% by weight (d) and to guarantee good pouring properties.

Furthermore, the cleaning additives can also contain minor constituents such as dyes and color pigments and can be colored uniformly or speckled. The proportion of such minor components is well below 1% by weight. The cleaning additives are obtained by spray drying an appropriate aqueous slurry. The bulk density of the powders or granules obtained in the spray drying is in the range from 350 to 550 g / 1, in the specific case bulk densities of the dry products in the range from 440 to 450 g / 1 are shown. In the abovementioned application it is stated that these cleaning additives are suitable as additional components for agents for cleaning hard surfaces, the area of application of the dishwashing agents being expressly mentioned. It also states there that these phosphate-free builder components are usually stored separately from granular detergents and cleaning agents and - depending on requirements - can be used together with these in washing or cleaning processes. It is also mentioned the possibility of mixing them in granular cleaning agents in special cases or processing them together with them.

Based on these cleaning additives, low-alkaline active chlorine and phosphate-free machine dishwashing detergents containing calcium-binding framework substances, soda, water glass, solid per-compounds, activators and surfactants as well as any other usual constituents of such agents in the form of storage-stable, free-flowing, dust-free granules are also used for the practical application required bulk densities above 650 g / 1 on the basis of a mixture of fine particulate solid components compacted by the mixing process with liquid components absorbed therein, containing about 15 to 30% by weight, based on the total weight of dishwashing detergent, a granular alkaline cleaning additive produced in a separate process step according to DE 3937469.6 from:

(b) 25 to 50% by weight of sodium carbonate (calculated as anhydrous),

(c) 4 to 20% by weight of sodium sulfate (calculated as anhydrous),

(d) 1 to 7% by weight of water have been developed which are premixed with at least a portion of the liquid components and, if desired, a portion of the finely divided solid components of the machine dishwashing detergent in a first sub-stage and subsequently with the remaining components of the Dishwasher detergents have been combined. They have bulk densities in the range from 750 to 1,000 g / l and are the subject of the older, unpublished German patent application P 4110510.9.

The excellent dishwashing detergents according to P 4110510.9 can be easily produced in technical quantities. On a large scale, however, there can be unexpected complications in that the granules, due to their own weight, cake together during storage and cannot always be separated easily. The present invention therefore represents an advantageous further development of the older method for improving the storage stability.

A process was then found which also used for low-alkali, active chlorine and phosphate-free cleaning agents for machine dishwashing containing granular, alkaline cleaning additives according to German patent application P 3937469.6, further builders, bleaches, water and optionally low-foam nonionic surfactants, enzymes, bleach activators, fragrances and / or dyes, if powdery poly (meth) acrylate and / or the granular, alkaline cleaning additives are premixed with compressed sodium carbonate and other builders, with water and, if appropriate, with further liquid Components agglomerated granulated in a conventional manner, the granules then with the bleach, and optionally a bleach activator, fragrance, enzymes and / or Mixed dye, dusted the still slightly sticky granules with powdered sodium carbonate, and finally sprayed with the proportion of nonionic surfactants.

Excess sodium carbonate portions were bound by the subsequent addition of the portions of nonionic surfactant, which resulted in product dedusting. The addition of sodium carbonate in turn prevented the granules from quickly caking in the pile. As a result, the granulate structure was preserved on the way into the vortex channel. Dusting with sodium carbonate powder also increased the liter weight by 850 to 1,000 g. A further increase in the liter weight was achieved if the granulation was first carried out with the addition of liquid water glass and then water or water alone, if the sodium carbonate introduced in the granulation step was partially hydrated or if the batch size was increased.

The cleaning agents according to the invention contain about 10 to 30, preferably about 15 to 25% by weight of the granular alkali cleaning additive according to DE 39 37 469 and / or poly (meth) acrylate powder, about 15 to 35, preferably about 20 to 30% by weight of compressed sodium carbonate, about 0.5 to 10, preferably about 2 to 4% by weight of powdered sodium carbonate, about 5 to 30, preferably about 10 to 25% by weight of powdered sodium disilicate, about 2 to 30, preferably about 5 to 25% by weight of further framework substances, preferably sodium citrate dihydrate, about 2 to 15, preferably about 5 to 10% by weight sodium perborate, about 0.5 to 10, preferably about 1 up to 5% by weight of an activator for sodium perborate, about 0.1 to 10, preferably about 0.5 to 5% by weight of nonionic surfactants, optionally about 0.1 to 10, preferably about 0.5 to 5% by weight % Water glass solution and up to about 2% by weight of other customary components of such agents. The poly (meth) acrylates are used as powder, but preferably as granules. The usable polyacrylates include Alcoxperse D from Alco: Alcosperse® 102, 104, 106, 404, 406), Acrylsole® from Norsohaas: Acrysole ® A IN, LMW 45 N, LMW 10 N, LMW 20 N, SP 02N, Degapasv-R from Degussa: Degapas iv from Goodrich: Good-Rite ^ K-XP 18. Copolymers (polyacrylic acid and maleic acid) can also be used, for example Sokalanew from BASF: SokalanCB) CP 5, CP 7, Acrysole (From Norsohaas: AcrysolWQR 1014, Alcosperse B) from Alco: AlcosperseCjy 175. Anhydrous trisodium citrate or trisodium citrate dihydrate are suitable as sodium citrate. The preferred phosphate is the tetrasodium salt of l-hydroxyethane-l, l-di-phosphonic acid (Turpinal jy 4 NZ from Henkel). Sodium carbonate of any quality is preferably used as the alkali carbonate, such as, for example, calcined soda or compressed soda. Dried water glass with the module SiOz: Na ₂ 0 = 1: 2 - 2.5 is suitable as a disilicate (for example Porti1 ® A or AW from Henkel, Britesil ^R H 24 or C 24 from Akzo).

Compacted sodium carbonate is to be understood as granular calcined sodium carbonate which is commercially available (for example V-soda from Matthes & Weber). It is anhydrous. The powdered sodium carbonate used is also anhydrous. It has an average grain size of <0.1 mm on average. The sodium disilicate is used in powder form. The SiÜ2: Na ₂ 0 ratio can be 2 to 3.4: 1.

Sodium citrate dihydrate is used as a powder. It has an average grain size of 0.2 mm. Anhydrous sodium citrate can also be used.

Nitri-triacetate and phosphonates can serve as further framework substances. They bind together with the polycarboxylate Reinigungsaddi¬ tivanteil by complexing or dispersion hardening ^{constituents'} as calcium and magnesium ions cium- from the water or from the food particles, and thus prevent the formation of limescale in the dishwasher and on the dishes. They can be used as anhydrous and / or as hydrate salts, whereby in the agglomerating granulation from about 5 to 10, preferably about 6 to 8 parts by weight of water and anhydrous salts, hydrate salts can also be formed. For some time now, active oxygen carriers have been the preferred bleaching agent components of detergents for machine dishwashing (HGSM). These primarily include sodium perborate mono- and tetra- hydrate as well as sodium percarbonate. As active oxygen only develops its full effect at elevated temperatures, so-called bleach activators are used to activate it at approx. 60 ° C, the temperatures of the cleaning process in the HGSM. Preferred bleach activators are TAED (tetraacetylenediamine), PAG (pentaacetylglucose), DADHT (1,5-diacetyl-2,2-dioxo-hexahydro-1,3,5-triazine) and ISA (isatoic acid anhydride).

Extremely low-foaming compounds are preferably used as nonionic surfactants, which serve to better remove fatty food residues and as pressing aids. These preferably include Ci2-Ci8-alkyl-polyethylglycol-polypropylene glycol ethers, each with up to 8 moles of ethylene oxide and propylene oxide units in the molecule. Their share in the total weight of the finished tablets is generally 0.2 to 5, preferably 0.5 to 3% by weight. However, other nonionic surfactants known as low-foaming can also be used, such as e.g. C 1 -C 4 -alkylpolyethylene glycol -polybutylene glycol ether, each with up to 8 moles of ethylene oxide and butylene oxide units in the molecule and then optionally 0.2 to 2, preferably 0.2 to 1% by weight, based on the entire tablet , on defoaming agents such as Add silicone oils, mixtures of silicone oil and hydrophobicized silica, paraffin oil / Guerbet alcohols and hydrophobicized silica.

For better detachment of protein or starch-containing food residues, enzymes such as proteases and amylases, for example proteases such as BLAP ^R from Henkel, Opitmase® -M-440, Optimase® -M -330, Opticlean®- M-375, Opticlean (j -M-250 from Solvay Enzymes, Maxacal ® CX 450,000, Maxapem üv from Ibis, Savinase® T from Novo or Experase® T from Ibis and amylases such as Termamyl ® 60 T, 90 T from Novo, A ylase-LT® from Solvay Enzymes or Maxamyl® P 5000 from Ibis, and customary dyes and fragrances can also be added. The following areas can be considered for frame formulations of virtually all possible constituents of the granular detergents produced according to the invention:

Components area preferred area

In the production of the detergent granules, it was necessary to use larger amounts of liquid, in which case even larger amounts of the components to be combined, together with the granular cleaning additive and / or the poly (meth) acrylate, can be subjected to the premix. Here, for example, the polyacrylate components can be mixed together with the compressed sodium carbonate, at least a portion of finely divided solid water glass and sodium citrate and agglomerated in a densifying manner by adding limited amounts of water and / or aqueous water glass solutions. If, for example, a knife ring is used in a Lödige ploughshare mixer, heavy granules with bulk densities in the range of up to 950 g / l are obtained in the procedure described in detail in the examples below.

The following process modification can lead to the setting of particularly high bulk densities: in a preparatory process step, the water-free soda is mixed with about 5 to. 20, preferably 10 to 15 wt .-% water anhydrated and added to the granulation process in this form.

The ultimate bulk weights can then be in the range of 1000 g / 1.

If water is used as auxiliary liquid in such amounts in the course of this granulation process that residual moisture in the finished product exceeds the range of about 4 to 7% by weight, it may be expedient to subject the pre-granules formed to intermediate drying. Drying in the fluidized bed is suitable for this purpose, for example. As a rule, such a drying treatment with product temperatures in the range of approximately 80 ° C. for a limited period of time - for example 10 to 15 minutes - is sufficient to set the desired residual moisture in the product within the range of approximately 4 to 7% by weight.

The pre-granules are then mixed with the still missing components of the dishwashing detergent to form the finished product. In all the cases shown here, the mixing time is both in the preliminary stage of the compacting mixture under the influence of liquid components and in the subsequent final mixture with the other components in the range of a few minutes, for example in the range of 1 to 5 minutes. The mixing took place, for example, in a Lödige mixer or in mixers from I atec, Unimix, Drais or Papenmeier.

The fine, but slightly sticky granules are dried by adding sodium carbonate powder to the surface of the granules formed, and excess sodium carbonate powder is bound by spraying on nonionic surfactants which are liquid at room temperature or their concentrated aqueous solutions.

B e i s i e l e

The bulk weights of the essential individual components used in the examples below were as follows:

Sodium carbonate, compressed 1080 g / 1

Tri-sodium citrate x 2 H ₂ 0 870 g / 1

Sodium perborate x H ₂ 0 540 g / 1

Water glass (Porti! A), powder 840 g / 1 granular cleaning additive 395 g / 1

Plurafac ^R LF 403: alkyl (Cι ₂ -Ci8) -polyethylene glycol (<8 E0) -pol propylene-glycol - (<8 P0) -ether (BASF)

Example 1:

219 kg of granular cleaning additive, 358 kg of compressed sodium carbonate and 254 kg of powdered water glass were mixed in succession in a 3000 l discontio mixer with 57 kg of a 37% strength aqueous water glass solution (water glass N (3.0)) and 59 kg of water while doing so granulated. 25 kg of light sodium carbonate powder were then mixed into the moist granules. The granules were sprayed with 28 kg of Dlucafy R LF 403 in order to bind dust off carbonate powders not required for moisture binding. The granules thus obtained were emptied from the mixer and treated in a fluidized bed.

Further processing of the granules was possible within 30 minutes in the pile. Slight caking disintegrated into the original granulate structure when falling into the swirl channel. After drying and sieving, the granules had a bulk density of 990 g / l. Without the addition of sodium carbonate powder, the granules caked directly under the internal load in such a way that further processing was impossible.

Example 2:

If 358 kg of compressed sodium carbonate were first introduced and hydrated with 5% water and then proceeded as described in Example 1, granules were obtained which were still processable after 1 hour. It had a bulk density of 1,040 g / l.

Example 3:

A further preparation was carried out as described in Example 1, but a premix of water glass and water was used for the granulation. The granules obtained after drying and sieving had a bulk density of 950 g / l. The granules obtained in this way were mixed with the remaining constituents of the detergent while increasing the bulk density. Bulk weights of up to 1,050 g / l were then achieved.

Claims

Patent claims

1. A process for the preparation of low-alkaline, active chlorine and phosphate-free cleaning agents for automatic dishwashing containing granular, alkaline cleaning additives according to German patent application P 3937469.6, further builders, bleaching agents, water and possibly low-foam nonionic surfactants , Enzymes, bleach activators, fragrances and / or dyes, characterized in that powdered poly (meth) acrylate and / or the granular, alkaline cleaning additives are premixed with compressed sodium carbonate and other structural substance, with water and optionally other liquid constituents in a manner known per se granulated in agglomerating form, the granules are then mixed with the bleaching agent and, if appropriate, a bleach activator, fragrance, enzymes and / or dye, the granules obtained, which are still slightly sticky, are dusted with powdered sodium carbonate, and finally sprayed with the proportion of nonionic surfactants.

2. The method according to claim 1, characterized in that the compressed sodium carbonate is anhydrated before mixing with about 5 - 20% preferably about 10 - 15% water.

3. Process according to claims 1 and 2, characterized in that the liquid components are added in the order of water glass solution-water in the graining step or that the total amount of water glass in the form of solid is mixed with the solid components before the addition of water .

4. Process according to claims 1 to 3, characterized in that the granules are pre-dried for about 10 to 15 minutes at about 80 ° C to a residual moisture of about 3 to 10, preferably 4 to 7% by weight before the addition of bleaching agents .