BINDERS STABILIZED IN AN AQUEOUS PHASE

Abstract

Binders stabilized in an aqueous phase and capable of codeposition with ionogenic gel-formers are disclosed. The binder may be a resin or polymer, including polyacrylates, polyurethanes, polyepoxides, urethane acrylates, aromatic and (cyclo)-aliphatic epoxy acrylates, polyesters, and mixtures thereof. The binders are modified by reactions between reactive groups on the binder and hydrophilic, functional molecules. Reactive groups on the binder may include isocyanates, hydroxyls, carboxyls, oxiranes, vinyls and amines. A method of producing such dispersions is disclosed.

Claims

1. A carrier binder stabilized in an aqueous phase and capable of codeposition with ionogenic gel-formers, wherein a binder is modified by means of reactive groups on the binder with a hydrophilic, functional molecule.

2. The carrier binder according to claim 1, wherein a binder which with an ionogenic gel forms a rinse-resistant coating having a rinse resistance of at least 0.2 bar spraying pressure or after an immersive rinsing process, where the binder constitute a core of the carrier binder micelles, which form micelles by means of polyurethanes with ethylene glycol units which are equipped with hydrophobic end groups.

3. The carrier binder according to claim 2, wherein the binder is a resin or polymer.

4. The carrier binder according to claim 1, wherein the hydrophilic, functional molecule is a telomer which is provided with a hydrophobic end group and is composed of ethylene glycol units, the number of ethylene glycol units in the telomer being 1 to 20.

5. The carrier binder according to claim 1, wherein the hydrophilic, functional molecule has a molecular weight between 300 and 1000 g/mole.

6. The carrier binder according to claim 1, wherein the hydrophilic, functional molecule possesses a C.sub.1-C.sub.4 alkyl or a C.sub.6-C.sub.12 aryl end group.

7. The carrier binder according to claim 1, wherein the hydrophobic end group of the hydrophilic, functional molecule is reactive.

8. The carrier binder according to claim 1, which comprises inorganic particles having a particle size of 5 nm to 800 nm in an amount of 0.01 to 50 wt %.

9. The carrier binder according to claim 8, wherein the inorganic particles are selected from the group consisting of color-effect and luster-effect pigments, anticorrosion pigments, UV protection pigments, or particles having other functional properties, without causing premature gelling of the dispersion through formation of polyvalent cations.

10. The carrier binder according to claim 9, wherein the inorganic particles are surface-modified with silanes, aminosilanes, phosphorus-group-containing and/or amine-containing organic molecules, phosphates, or with conductive or nonconductive organic coatings, it being possible for the coatings to comprise reactive groups for covalent or interactional attachment to the carrier binder.

11. The carrier binder according to claim 10, wherein the reactive groups of the inorganic particles are primary, secondary, tertiary amine, epoxy, isocyanate or hydroxyl groups.

12. A method for producing a carrier binder stabilized in an aqueous phase according to claim 1, wherein the binder is modified by reaction of the reactive groups of the binder to form 1 to 9 chain units of the hydrophilic, functional molecule.

Description

EXAMPLE 1: PRODUCTION OF A POLYURETHANE ACRYLATE DISPERSION, HYDROXYETHYL METHYLACRYLATE-TERMINATED (PUD-HEMA)DISPERSION I

[0025] The experimental setup consists of a 500 mL glass reactor with reflux condenser, a stirring guide with gas inlet, an RPG stirring motor and a close-clearance anchor stirrer. Heating is carried out using a magnetic stirrer with heating function and temperature sensor and also a silicone oil bath. Operation is to take place in the absence of water and under a continual flow of nitrogen throughout the reaction. At the start, the polyester polyol Priplast 3192 or Priplast XL 101 from Croda) is introduced in butan-2-one and this initial charge is homogenized at 65 C. for 10 minutes (min) at a stirrer speed of 120 rpm. Subsequently the diol, neopentyl glycol (NPG), and the carboxyl-containing diol, 2,2-bis-hydroxymethyl-propionic acid (DMPA) as chain extender, are added and homogenization takes place for a further 15 min. Thereafter the diisocyanate, 4,4-diphenylmethane diisocyanate, is added.

[0026] The temperature of the solution is maintained at 82 C., corresponding to an outer jacket temperature of 94 C., for 6 h.

[0027] After 6 h, the partially hydrophilic building blocks for the end group are added, in the form of 2-hydroxyethyl methacrylate (HEMA). After about 80 min, dimethylethanolamine is added in order to neutralize the carboxyl functions. When this has taken place, ethylene glycol monobutyl ether is added to the reaction. Finally, the DI water is added, cooling takes place with continual stirring, and the solvent is removed on a rotary evaporator.

[0028] Determination of the solids fraction gave a value of 22.71 wt %. The particle size of the polymer is around 73 nm, determined using a Nano Zetasizer.

EXAMPLE 2: PRODUCTION OF A POLYURETHANE ACRYLATE DISPERSION, POLYETHYLENE GLYCOL METHACRYLATE-TERMINATED (PUD-PEGMA500)DISPERSION II

[0029] In a 500 mL glass reactor with reflux condenser, a stirring guide with gas inlet, an RPG stirring motor and a close-clearance anchor stirrer, the polyester polyol Priplast 3192 from Croda is introduced in butan-2-one and this initial charge is homogenized at 65 C. for 10 min at a stirrer speed of 120 rpm. Subsequently the diol, neopentyl glycol (NPG), and the carboxyl-containing diol, 2,2-bis-hydroxymethyl-propionic acid (DMPA) as chain extender, are added, and homogenization takes place for a further 15 min. Thereafter the diisocyanate, 4,4-diphenylmethane diisocyanate, is added. The temperature of the solution is held at 82 C., corresponding to an outer jacket temperature of 94 C., for 6 h. After 6 h, the partially hydrophilic building blocks for the end group are added in the form of poly(ethylene glycol) methacrylate having an average numerical mean of the molecular weight Mn=500 g/mole (PEGMA-500). After about 80 min, dimethylethanolamine is added in order to neutralize the carboxyl functions. When this has taken place, ethylene glycol monobutyl ether is added to the reaction. Finally, the DI water is added, and the reaction is subsequently cooled for 30 minutes with continual stirring, and the solvent is removed on a rotary evaporator. The solids fraction of PUD-PEGMA500 is 25 wt %. The particle size of the polymer is around 73 nm, as measured using a Nano Zetasizer and with a solids content (SC) of 24.80 wt %.

[0030] Formulation Priplast-3192-PUD-PEGMA-500 is indicated below

TABLE-US-00001 Compound Structure Initial mass [g] Polyester polyol [00001] 321.6 Methyl ethyl ketone [00002] 800.01 4,4-Diphenylmethane diisocyanate [00003] 100.12 Neopentyl glycol [00004] 2.9157 2,2-Bis-hydroxymethyl- propionic acid [00005] 19.2087 2-Hydroxyethyl methacrylate [00006] Poly(ethylene glycol) methacrylate [00007] 32.2031 Dimethylethanolamine [00008] 10.2109 Ethylene glycol monobutyl ether [00009] 28.0333 Double-distilled water [00010] 1000.01

[0031] A formulation of a coating material which withstands a spraying pressure of 0.5 bar is obtained from the following mixture:

[0032] Formulation consisting of 2.5 g of dispersion I, 2.5 g dispersion II and 5 g of blocked isocyanate crosslinker with polyethylene glycol units as carrier dispersion and is mixed by means of an Ultraturrax (IKA T 10 basic ULTRA-TURRAX-IKA with S 10 N-10 G dispersing tool) on level 4 for 10 min. Introduction takes place with a shearing forces such as to form a uniform micelle, so that the overall mixture is sufficiently stable on pH reduction.

[0033] Alternatively, in the case of larger amounts of the mixture (1 kg), it is also possible, for example, to use laboratory dispersers with low viscosity blades, which are engaged at 2000 rpm for around 30 min in order to generate a correspondingly homogeneous distribution of the constituents.

[0034] Particularly high corrosion protection is additionally generated with the addition of around 1-2 g of bisphenol A-diglycidyl ether (BADGE) or with bisphenol F diglycidyl ether.

[0035] Thereafter, 12 g of a 1 wt % strength solution of the gel-former are added and incorporated by stirring overnight. The solids content of dispersion I and II is adjusted for this application to 20 wt %-25 wt %.

EXAMPLE 3: SYNTHESIS METHOD FOR CARRIER DISPERSION

[0036] A further preferred mixing variant with high rinse resistance and high corrosion protection is the mixture of two as carrier dispersions, consisting of a polyacrylate-DPE carrier dispersions with a further carrier dispersion, which as hydrophilic isocyanate crosslinker is equipped with a polyethylene glycol methyl ether, such as, for example, the product BL 5335 from Covestro+BADGE, which form a rinse-resistant coating.

[0037] The two-stage synthesis is carried out in a 5 L glass reactor with close-clearance double anchor stirrer. Also mounted are reflux condenser, nitrogen inlet and outlet, bubble counter, heating jacket with thermostat, and the Gravidos feed. In the first stage, the reactor is charged with 1300 g of water, and heated to 40 C. with a stirrer speed of 120 rps and a full stream of nitrogen. When the 40 C. has been reached, the nitrogen stream is reduced to 1 bubble/s. Subsequently 25 g of styrene, 21.8 g of polyethylene glycol methyl ether methacrylate Mn 500 g/mole, and 2.055 g of 1,1-diphenylethylene are added. 100 g of water are added for subsequent rinsing. Leave the solution with stirring for around 5 min, then dissolve 4.056 g of ammonium peroxodisulfate in 100 g of water and add. The solution is then heated to 90 C. within a temperature-time ramp of around 45 min.

[0038] In the second stage, a mixture of 500 g of butyl methacrylate and 25 g of hydroxyethyl methacrylate is added dropwise from a Gravidos container by means of the Gravidos system over the course of 4 hours at a metering rate of around 2.188 g/min. From a second Gravidos container, 50 g of an epoxy acrylic acid in 50 g of butanone is metered in with a metering rate of 0.416 g over 4 hours. The epoxy acrylic acid is prepared as described below. The butanone is removed from the reactor again partly via the nitrogen stream. Alternatively it may be removed almost completely afterward, on a rotary evaporator. Following the complete addition of the monomers, stirring is continued at 90 C. for 2 hours. The dispersion is cooled, filtration takes place, and then determinations are made of the particle size of the solids and pH and also of the solids content (SC).

[0039] To this dispersion, which accordingly has approximately a SC of 40 wt %, it is then possible to add 10-50 wt % of BL 5335. In that case it is necessary to prepare approximately the 1-1.2-fold amount of polysaccharide solution with an SC of 1 wt % and to mix it with the dispersion for around 24 h.

EXAMPLE 4: SYNTHESIS METHOD, CARRIER BINDER WITH EMULSIFIER PROPERTIES

[0040] The experimental setup consists of a 500 mL glass rector with reflux condenser, a stirring guide with gas inlet, an RPG stirring motor and a close-clearance anchor stirrer. Heating is carried out using a magnetic stirrer with heating function and temperature sensor and also a silicone oil bath. Operation is to take place in the absence of water and under a continual stream of nitrogen throughout the reaction.

[0041] At the start, polyethylene glycol methyl ether Mn 750 g/mole and 79.8 g of a polycyclic methyldiphenyl isocyanate (MDI) such as Desmodur VL from Covestro or Bayer are introduced and this initial charge is heated at 70 C. for 2 hours with continual stirring at 120 rpm using an anchor stirrer. Then 17.4 g of butoxime are added with stirring and the components react at an internal reactor temperature of 70 C. for 2 h. Thereafter 20.21 g of diisopropylamine are added and stirring is carried out at 70 C. for 40 min. The complete conversion in the reaction can be monitored with the aid of infrared spectra (IR spectra) from the decrease in the isocyanate bands at a wavenumber between 2200 and 2400 cm.sup.1. The binder is subsequently adjusted to a solids fraction of 35-40 wt % using double-distilled water, and, with continual stirring and also with introduction of shearing forces, a dispersion is produced which has an emulsifying action for various types of resin such as, for example, bisphenol A diglycidyl ether or PUD resins.