Patent Application
20220372176
The present invention relates to polymer dispersions that are especially suitable as dispersing agents for hydrophobic monomers in a hydrophilic medium, especially in water, and to methods making use of such dispersions. In this connection, the invention notably relates to emulsion polymerization of hydrophobic monomers and preparation of fabric conditioning compositions.
More precisely, the instant invention relates to aqueous dispersions of bloc polymers comprising a hydrophilic bloc and a short hydrophobic bloc, said dispersions comprising the bloc polymers in the form of micelles, or micelle-like structures, and made of bloc polymers organized with an outer hydrophilic “shell” and an inner hydrophobic “core”.
The term “aqueous dispersion” herein refers to dispersion in water, or alternatively in a water soluble medium that preferably comprises at least 50% of water, by weight based on the total weight of the water soluble medium (it may be an aqueous solution of salt or it may comprise a water soluble solvent such as ethanol for example). In the instant description, for sake of concision, the dispersant medium of an aqueous dispersion will be referred as “aqueous medium” in all cases (whatever this dispersion medium is, pure water or a water soluble medium).
One aim of the invention is to provide aqueous dispersions of the aforementioned type, that, among other possible advantages, have the ability to maintain hydrophobic monomers, in a dispersed state, when such monomers are mixed with the dispersions.
To this end, according to a first aspect, one subject-matter of the instant invention is a process for preparing a dispersion (herein referred as “dispersion D0”), that comprises the following successive steps: (E1) a free radical polymerization is performed in an aqueous medium (M) in the presence of:
(R11)x—Z11—C(—S)—Z12-[A]-R12 (1)
According to another aspect, a subject-matter of the invention is the dispersion D0 as obtained according to the aforementioned process.
The step (E1) of the process of the invention is a specific radical polymerization process that makes use of a pre-polymer (p0) that has a so-called “living” character, due to the specific (R11)x—Z11—C(═S)—Z12— terminal group carried by this pre-polymer. This living character is well-known as such (for more details, reference may e.g. be made to the Handbook of RAFT Polymerisation, Weinheim, WILEY-VCH Verlag GmbH & Co. 2008. Concretely, the living character of the polymerization of step (E1) implies that the polymer chain [A] carried by the pre-polymers (p0) are schematically extended by incorporation of the monomers (m) implemented in step (E1), between the chain [A] and the terminal group, whereby copolymers are obtained, that are terminated by the same (R11)x—Z11—C(═S)—Z12— terminal group that imparts the same living character to the chains obtained at the end of step (E1).
Besides, the use of the specific pre-polymer (p0) carrying the specific (R1)x—Z11—C(═S)—Z12-terminal group also lead to a radical polymerization having a controlled character: during step (E1), in the ideal case, the polymer chains virtually grow at the same speed and schematically, only on the given sites constituted by the existing chain [A] present on the pre-polymer. This leads to a controlled incorporation of the monomers (m), and therefore the formation of bloc copolymers wherein the hydrophobic blocs have substantially the same length: in theory, a length corresponding to the ratio m/p0 as defined hereinabove. In practice, a population of distinct polymer is obtained, but the controlled character of the polymerization leads to a polydispersity index that remains low, with the thus obtained hydrophobic blocs that are very close to the theory in terms of targeted number average molar mass.
In addition, the specific use in step (E1) of, on the one hand, a pre-polymer (p0) soluble in the aqueous medium (M); and, on the other hand, a hydrophobic monomer significantly less soluble with this medium, leads to a specific polymerization, wherein the polymer becomes progressively less and less compatible with the medium (M) as the polymerisation progresses, since the polymer incorporates more and more hydrophobic constituents. As a result, a dispersion is obtained due to the fact that the hydrophobic blocs of the obtained copolymers tend to self-organize in order to decrease the contact of the hydrophobic bloc with the aqueous medium (M).
The step (E1) is specifically carried out with a sufficient quantity of monomers (m) to obtain such a dispersion, but with a limited length of the hydrophobic bloc, typically with a ratio m/p0 that is preferably below 10 000 g/mol. This m/p0 ratio of the mass of the monomers (m) to the quantity (in mole) of pre-polymer (p0) is more preferably between 5 000 and 10 000 g/mol, for example between 6 000 and 9 000 g/mol.
The step (E2) of the process induces only a change in the the copolymers as obtained at the end of step (E1), namely they are reacted in order to deprive them of their living character. Such a “deactivation” of living polymer is well-known per se and examples of methods are given hereinafter.
Therefore, at the end of step (E2), a very specific dispersion is obtained, herein referred as “dispersion D0” that contains micelles or micelle-like objects with an outer hydrophilic shell and an inner hydrophobic core, these micelles or micelle-like objects being made of bloc polymers, that are not living, but which however have a controlled structure and notably a controlled length of their short hydrophobic bloc.
The dispersion D0 as obtained according to the instant invention may be useful as such (for example, it may acts as a fabric conditioning composition if the hydrophobic monomers (m) are properly chosen), but it is also useful for preparing a more complex dispersion.
In this connection, another subject-matter of the invention is the use of the dispersion D0 as described above for dispersing hydrophobic species in an aqueous medium.
When a dispersion D0 as obtained according to the aforementioned steps (E1) and (E2) is contacted with hydrophobic monomers (for example by adding such monomers to the dispersion D0), said hydrophobic monomers migrate in contact with the hydrophobic parts of the polymers dispersed within the aqueous medium of said dispersion, whereby a dispersion is obtained (referred as “dispersion D” hereinafter), that comprises the hydrophobic monomers, stabilized by the polymers of the dispersion D0. The dispersion (D) may optionally comprise other hydrophobic species in addition to the hydrophobic monomers.
In other words, according to another specific aspect, another specific subject-matter of the instant invention is a process for preparing a dispersion (D) of hydrophobic monomers in an aqueous medium. This process comprises the preparation of a aforementioned steps (E1) and (E2), whereby a first dispersion of bloc copolymers (D0) is obtained, and then an additional step (E3) wherein said dispersion D0 is contacted with the hydrophobic monomers. Another subject-matter of the invention is the so obtained dispersion (D).
The dispersion (D) is generally used for implementing a polymerization of the hydrophobic monomers. In this connection, the invention provide a process for preparing a polymer latex that comprises a step (E4) wherein all of part of the hydrophobic monomers contained in a dispersion (D) of the aforementioned type are polymerized. In that respect, a specific subject-matter of the invention is a process for preparing a polymer latex (Dp) that comprises: the preparation of a dispersion (D0) as described above; a step (E3) wherein said dispersion D0 is contacted with hydrophobic monomers leading to a dispersion (D) of said hydrophobic monomers; and then (E4) a polymerization of all or part of the hydrophobic monomers
The aforementioned successive steps (E1), (E2) and (E3) wherein the hydrophobic monomers are monomers and then a step (E4) of polymerization of the monomers, typically a radical polymerization carried out by adding a radical initiator in the dispersion (D) comprising the hydrophobic monomers as obtained in step (E3). A dispersion of polymer, referred herein as “dispersion (Dp)” or “latex (Dp)” which is a polymer latex is then obtained in step (E4), that is another specific subject-matter of the instant invention.
In the dispersion (Dp) as obtained in step (E4), the hydrophobic polymer chains are stabilized by the copolymers as obtained in step (E2). Unless any phenomenon of chain transfer occurs, the stabilizing copolymer does not interfere with the polymerization of the monomers used in step (E4) since these copolymers have lost their living character in step (E2).
According to a specific embodiment, the dispersions (Dp) prepared according to step (E4) may be used in a fabric conditioning compositions. In that case, the hydrophobic species present in the dispersion (D) are chosen among species able to impart a proper treatment of the fabrics, especially of cotton fibers. Examples of proper species are given herein below as non-limitative possible examples.
Specific features and advantageous embodiments of the invention are described in more details herein below.
Step (E1): Preparation of a Dispersion of Living Copolymers
The step (E1) is a polymerization step that leads to a living block copolymer having a controlled internal structure and in the form of a suspension. The step (E1) may be performed batch or semi-batch.
As discussed hereinabove, a dispersion in step (E1) is obtained due to the specific use of the soluble pre-polymer (p0) and the hydrophobic monomers (m). The step (E1) can therefore be implemented without any surfactant in addition to the pre-polymer (p0) and the monomers (m) which constitute an advantage of the suspension of the invention since additional surfactant often limit the domains where the dispersion may be used.
When no additional surfactant is used, the polymerization of the hydrophobic monomers (m) can be performed directly in batch ab initio conditions using pre-polymer (p0) soluble in the specific medium (M). Amphiphilic block copolymers thereby form and self-assemble into self-stabilized dispersions within the course of the polymerization by polymerization-induced self-assembly (PISA). In other words, dispersions according to the instant invention are then made via a macro-molecular self-assembly of polymeric emulsifiers.
In some specific cases, the use of additional surfactants may however be contemplated in step (E1). Even if not compulsory, it may be of interest in some cases, to add surfactant in addition to the pre-polymer (p0) and the monomers (m), depending on the final application intended for the dispersion. The surfactants may then be chosen from, but not limited to, ionic, non-ionic and amphoteric surfactants, such as polyvinyl alcohols, fatty alcohols or alkylphenol sulfates or sulfonates, alkylbenzene sulfonates, for example dodecylbenzene sulfonate, sulfosuccinates, quaternary ammonium salts or ethylated fatty alcohol. When additional surfactants are used in step (E1), there are preferably present at a concentration below 10%, by weight based on the total weight of the reaction medium. Typically, from 0.1% to 10% of surfactant may be used, preferably less than 8%, notably less than 5%, by weight based on the total weight of the reaction medium.
The Pre-Polymer (p0)
The so-called “pre-polymer” (p0) used in step (E1) is in fact a relatively short polymer chain having specific terminal groups that allow an extension of the polymer chain during step (E1), thus leading to a compound carrying a longer polymer. The pre-polymer (p0) is typically used in step (E1) as a macro-transfer agent.
The pre-polymer (p0) used in step (E1) is specifically soluble in a medium (M), which means that the pre-polymer may be solubilized in the medium (M) without phase separation on the macroscopic scale at the pre-polymer concentration used in step (E1), in the absence of the monomer (m). Concretely, the pre-polymer (p0) is solubilized in medium (M) at the beginning of step (E1).
To this end, the polymer chain [A] included in the pre-polymer (p0) is soluble in the medium (M). The exact nature of the polymer chain [A] may vary to quite a large extent and it can be adjusted, case by case, according to the medium (M) used and the final application(s) contemplated for the prepared dispersion.
Typically, the polymer chain [A] included in the pre-polymer (p0) can be selected from the homo- and copolymers (random, gradient or block) resulting from the polymerization of at least one or more hydrophilic monomers (mAh) selected from:
Alternatively, the hydrophilic monomers (mAh) may comprise monomers selected from:
According to the present description, the term “(meth)acrylate” refers collectively and alternatively to the acrylate and methacrylate and the term “(meth)acrylamide” refers collectively and alternatively to the acrylamide and methacrylamide, so that, for example, “butyl (meth)acrylate” means butyl acrylate and/or butyl methacrylate.
According to a possible embodiment, the polymer chain [A] included in the pre-polymer (p0) is a polymer chain resulting from the polymerization of hydrophilic monomers (mAh) only, provided that the pre-polymer (p0) remains soluble in the medium (M).
According to an alternatively embodiment, the polymer chain [A] included in the pre-polymer (p0) comprises some units which are hydrophobic in nature, provided that the pre-polymer (p0) remains, overall, soluble in the medium (M). In that case, the polymer chain [A] generally results from a copolymerization (random or block) of at least one hydrophilic monomer (mAh) as defined above with at least one hydrophobic monomer (mAH).
Examples of hydrophobic monomers (mAH) that can be present in the polymer chain [A] of in the pre-polymer (p0) include for example styrene or its derivatives, butadiene, chloroprene, (meth)acrylic esters, vinyl esters of a carboxylic acid, for instance vinyl acetate, vinyl versatate or vinyl propionate, and vinyl nitriles.
The term “(meth)acrylic esters” denotes esters of acrylic acid and of methacrylic acid with hydrogenated or fluorinated C1-C12 and preferably C1-C8 alcohols. Among the compounds of this type that may be mentioned are: methyl acrylate, ethyl acrylate, propyl acrylate, n-butyl acrylate, isobutyl acrylate, 2-ethylhexyl acrylate, t-butyl acrylate, methyl methacrylate, ethyl methacrylate, n-butyl methacrylate, isobutyl methacrylate
The vinyl nitriles more particularly include those containing from 3 to 12 carbon atoms, such as, in particular, acrylonitrile and methacrylonitrile.
It should be noted that the styrene may be totally or partially replaced with derivatives such as α-methylstyrene or vinyltoluene or tertbutylstyrene.
Other ethylenically unsaturated monomers (mAH) that may be used, alone or as mixtures, or that are copolymerizable with the above monomers include especially:
The polymer chain [A] of the pre-polymer (p0) has preferably a number-average molar mass of less than 10 000 g/mol, for example, less than 5 000 g/mol, and typically more than the ratio m/p0 used in step (E1). This number-average molar mass can be for example measured by steric exclusion chromatography, using polyethylene glycol as standard or triple detection (GPC).
According to an interesting embodiment, that reveals especially suitable when the dispersion prepared according to steps (E1) and (E2) is intended to be used for the preparation of fabric conditioning composition, the polymer chain [A] of the pre-polymer (p0) comprises cationic monomers Ac and non-ionic monomers An.
The polymer chain [A] may e.g. be a statistical copolymer including monomers Ac and An.
Alternatively, the polymer chain [A] may be a bloc copolymer including a hydrophilic block [Ac] deriving from cationic monomers Ac; and a non-ionic block [An] deriving from non-ionic monomers An
Pre-polymers (p0) having such a bloc structure may typically be obtained by implementing the aforementioned step (E0) and making use of:
Suitable cationic monomers Ac especially include quaternary ammonium monomers or salts thereof, e.g. selected from the group consisting in:
The (3-acrylamidopropyl)trimethylammonium salts are especially suitable monomers Ac.
As regards nonionic monomers An, they are preferably selected from (meth)acrylamides and derivatives or (meth)acrylic acids and derivatives, more preferably from (meth)acrylamides.
A suitable pre-polymer (p0), exemplified hereinafter, is a pre-polymer wherein the chain [A] is a statistical copolymer of acrylamide (AM) and (3-acrylamidopropyl)trimethylammonium chloride (APTAC).
Whatever its exact composition, the pre-polymer (p0) used in step (E1) may typically be obtained by a preparation step (E0) of controlled radical polymerization of a composition comprising:
The group (R11)x-Z11—C(═S)—Z12— of pre-polymer (p0), which may especially be a thiocarbonylthio group, is typically introduced via the control agent used in the controlled radical polymerization performed in the above-mentioned step (E0), which is typically a RAFT or MADIX control agent.
The radical polymerization control agent used in step (E0) may advantageously have the formula (F) below:
wherein:
According to one particular embodiment, R, is a substituted or unsubstituted, preferably substituted, alkyl group.
The optionally substituted alkyl, acyl, aryl, aralkyl or alkyne groups to which reference is made in the present description generally contain 1 to 20 carbon atoms, preferably 1 to 12 and more preferentially 1 to 9 carbon atoms. They may be linear or branched. They may also be substituted with oxygen atoms, in particular in the form of esters or sulfur or nitrogen atoms.
Among the alkyl radicals, mention may be made especially of methyl, ethyl, propyl, butyl, pentyl, isopropyl, tert-butyl, pentyl, hexyl, octyl, decyl or dodecyl radicals.
For the purposes of the present description, the alkyne groups are radicals generally containing from 2 to 10 carbon atoms, and contain at least one acetylenic unsaturation, such as the acetylenyl radical.
For the purposes of the present description, the acyl groups are radicals generally containing from 1 to 20 carbon atoms with a carbonyl group.
Among the aryl radicals which may be used according to the invention, mention may be made in particular of the phenyl radical, optionally substituted especially with a nitro or hydroxyl function.
Among the aralkyl radicals, mention may be made in particular of the benzyl or phenethyl radical, optionally substituted especially with a nitro or hydroxyl function.
When R, is a polymer chain, this polymer chain may be derived from a radical or ionic polymerization or derived from a polycondensation.
Advantageously, in step (E0), the radical polymerization control agent is a xanthate compound, for instance O-ethyl-S-(1-methoxycarbonyl ethyl) xanthate of formula (CH3CH(CO2CH3))S(C═S)OCH2CH3.
A control agent that is particularly suited to the implementation of step (E0) is the compound sold by the company Solvay under the name Rhodixan® A1.
The Free-Radical Polymerization Initiator
Any source of free radicals which is known per se as being suitable for polymerization processes in a medium comprising water miscible solvent may be used in steps (E0) and (E1) of the polymerization of the invention.
The radical polymerization initiator may, for example, be selected from the following initiators:
According to one advantageous embodiment, use may be made of a radical initiator of redox type, which has the advantage of not requiring specific heating of the reaction medium (no thermal initiation). It is typically a mixture of at least one water-soluble oxidizing agent with at least one water-soluble reducing agent.
The oxidizing agent present in the redox system may be selected, for example, from peroxides such as: hydrogen peroxide, tert-butyl hydroperoxide, cumene hydroperoxide, t-butyl peroxyacetate, t-butyl peroxybenzoate, t-butyl peroxyoctoate, t-butyl peroxyneodecanoate, t-butyl peroxyisobutyrate, lauroyl peroxide, t-amyl peroxypivalate, t-butyl peroxypivalate, dicumyl peroxide, benzoyl peroxide, sodium persulfate, potassium persulfate, ammonium persulfate or potassium bromate.
The reducing agent present in the redox system may typically be selected from sodium formaldehyde sulfoxylate (in particular in dihydrate form, known under the name Rongalit, or in the form of an anhydrite), ascorbic acid, erythorbic acid, sulfites, bisulfites or metasulfites (in particular alkali metal sulfites, bisulfites or metasulfites), nitrilotrispropionamides, and tertiary amines and ethanolamines (which are preferably water-soluble).
Possible redox systems comprise combinations such as:
mixtures of water-soluble persulfates with water-soluble tertiary amines,
mixtures of water-soluble bromates (for example alkali metal bromates) with water-soluble sulfites (for example alkali metal sulfites),
mixtures of hydrogen peroxide, alkyl peroxide, peresters, percarbonates and the like and any iron salts, titanous salts, zinc formaldehyde sulfoxylate or sodium formaldehyde sulfoxylate, and reducing sugars,
alkali metal or ammonium persulfates, perborate or perchlorate in combination with an alkali metal bisulfite, such as sodium metabisulfite, and reducing sugars, and
alkali metal persulfates in combination with an arylphosphinic acid, such as benzenephosphonic acid and the like, and reducing sugars.
An advantageous redox system comprises (and preferably consists of) for example a combination of ammonium persulfate and sodium formaldehyde sulfoxylate.
Another advantageous initiator is or comprises sodium persulfate NaPS.
The Monomers (m) Used in Step (E1)
The ethylenically unsaturated hydrophobic monomer (m) used in step (E1) may advantageously be selected from the group consisting of:
More preferably, the ethylenically unsaturated hydrophobic monomers (m) comprise alkyl (meth)acrylates containing less than 30, for example from 4 to 30 carbon atoms, notably between 8 to 24, carbon atoms, and mixtures thereof. For example it may be selected from the group consisting of butyl acrylate; 2-ethylhexyl acrylate; and their mixtures.
According to a specific embodiment, the step (E1) may be a copolymerization step using co-monomers (m′) in addition to one or more monomers (m). In that case, co-monomers (m′) may be selected from the list consisting of:
These co-monomers (m′) may be chosen depending on the specific use of the polymer dispersion of the invention. Typically, the ratio by weight (m)/(m′) of the monomer(s) (m) to the co-monomer(s) (m′) present in the polymer dispersion is at least 50:50, for example at least 55:45, e.g. at least 60:40 or 75:25 in some cases.
According to one embodiment of the invention, only one kind of monomers is used in the medium (M) to form a homopolymer.
According to one embodiment of the invention, at least two monomers (namely at least two kinds of monomers) are used to form a random, gradient or block copolymer.
The Step (E2)
Step (E2) is a deactivation step: during this step, the terminal group that imparts the living character of the polymer chains obtained in step (E1) are converted into another terminal group that do not impart this living properties.
This deactivation of the terminal group (R11)x—Z11—C(═S)—Z12— may be made by any method known per se, for example according to one of the method described in patent applications WO 02/090397, FR 2 829 140, WO 03/065803 or WO 2005/040233.
Typically, step (E2) comprise the addition of a peroxide or a peracid to the dispersion obtained in step (E1). At low pH, a peracid will be typically used, for example peracetic acid.
At high pH, hydrogen peroxide would be preferable.
Use of the Dispersion (D0)
The dispersions (D0) of the invention are typically used for dispersing hydrophobic monomers (leading to dispersion (D) comprising said hydrophobic monomers), leading after polymerization to dispersion of polymers (Dp). Hydrophobic species such as e.g. perfumes may be added to the obtained dispersion (D) and (Dp).
In the specific domain of fabric conditioning composition, the dispersions (D0) and (Dp) may be potentially used:
According to a specifically interesting mode, illustrated in the appended examples, a dispersion (Dp) may be used. In this connection, the dispersion (Dp) is preferably prepared by polymerizing in step (E4) of a dispersion (D) prepared in step (E3) by mixing a dispersion (D0) with hydrophobic species that are hydrophobic similar or identical to the monomers (m) used for preparing the dispersion (D0).
Preferably, both the monomers (m) used in step (E1) and the hydrophobic species used in step (E3) are monomers including alkyl (meth)acrylates containing less than 30, preferably from 8 to 24, carbon atoms, for example butyl acrylate and/or 2-ethylhexyl acrylate. As illustrated in the examples, the polymer dispersions (Dp) obtained accordingly exhibit very good softening properties.
The following examples are given as an illustration of possible interesting embodiments of the invention.
In a 2000 mL glass bottle were introduced: 441.7 g of 50% wt water solution of Acrylamide (AM) 105.7 g of a 75% wt water solution of (3-acrylamidopropyl)trimethylammonium chloride (APTAC); and 448.3 g of demineralized water. The pH (initially equal to 6.49) was then adjusted to pH=3.03, by addition of H2SO4 (10% wt water solution).
12.5272 g of Rhodixan® A1 (Solvay) and 195.9 g of ethanol were then added, that turns the obtained mixture to be cloudy. After 10 min of strong agitation, 1.6254 g of V50 initiator were added.
The obtained mixture was introduced in a 2000 mL double-jacketed glass vessel equipped with an agitation anchor, a nitrogen inlet, a temperature sensor and a condensor.
Nitrogen was introduced (bubbling) during 30 min at room temperature (25° C.) and then the reaction medium was heated at 63° C. within 30 min. A marked exothermicity was observed around 50° C. The nitrogen was then used a nitrogen blanket and the temperature of 63° C. was maintained during 10 h.
The reaction medium was then cooled down to 23° C. within 30 min and let at room temperature overnight. A viscous liquid was then obtained, having a dry extract of 29.84%.
Ethanol and a part of the water were evaporated (rotavapor—55° C., 50 mbar), leading to a composition MCTA1, having a dry extract of 48.3% (measured with a thermobalance—1 h, 130° C.).
The awaited molar composition of the polymer (90/10 in mol for AM/APTAC) has been confirmed by RMN 1H, that also indicates a Mn of about 6 700 g/mole.
In a 2000 mL double-jacketed glass vessel equipped with an agitation mobile, a nitrogen inlet, a temperature sensor and a condensor, 29.45 g of a 50% wt water solution of AM; 7.03 g of a 75% wt water solution of APTAC; and 248 g of demineralized water were introduced. The pH (initially equal to 3.66) was then adjusted to pH=2.92, by addition of H2SO4 (10% wt water solution). 41.66 g of Rhodixan® A1 (Solvay) and 166.63 g of ethanol were then added.
Nitrogen was introduced (bubbling) during 45 min at room temperature (25° C.) and then the reaction medium was heated at 63° C. within 60 min.
When the temperature has reached 63° C., 5.42 g of a 5% water solution of V50 was added and the following parallel injections were started:
The temperature of 63° C. was maintained during 8 h. A very marked exothermicity was observed. The reaction medium was cooled down to 20° C. within 60 min and let at this temperature overnight.
A liquid (=composition MCTA2) was then obtained, having the following features:
192.8 g of the composition MCTA1 of example 1.1, 27.96 g of butyl acrylate (ABu), 414.3 g of demineralized water and 0.71 g of an aqueous solution of sodium persulfate (NaPS) having a NaPS concentration of 10% wt were mixed in a 600 mL glass beaker and then transferred in a 1000 mL double-jacketed glass vessel equipped with an lightning type agitation, a nitrogen inlet and a condensor.
Nitrogen was introduced (bubbling) during 1 h at room temperature (25° C.) and then the reaction medium was heated at 75° C. within 1 h. After 20 minutes of heating, 56.7 g of the composition MCTA1 of example 1.1 and 21.6 g of demineralized water were added to the reaction medium.
When the temperature has reached 75° C., 6.22 mL of a 10% wt water solution of NaPS are added from a syringe pump within 2 hours, and 162.46 mL d'ABu are added from a second syringe pump within 2.5 hours.
At the end of the injections, the reaction medium is let during 2 hours at 75° C. and then cooled down overnight.
The glass vessel is unloaded and an homogeneous white latex having a pH of about 3-4 is obtained, referred herein as D0-1-Xa, without any crusts visible on the stirring blade.
517.9 g of the obtained D0-1-Xa latex are re-introduced in the glass vessel and then heated to 70° C. within 1 h, and then 9.68 g of peracetic acid (35% wt aqueous solution) are added within 1 h. The reaction medium is let 1 h at 70° C. after the end of the addition of the peracetic acid.
A white latex is then obtained, referred herein as D0-1, having the same visual appearance as D0-1-Xa.
UV analysis indicates that a complete dexanthatation occurred. And a light scattering measure confirms that the particle size is unchanged in comparison to D0-1-Xa.
The latex D0-1 exhibits the following features:
675.7 g of the composition MCTA2 of example 1.2, 41.92 g of butyl acrylate (ABu), 685 g of demineralized water and 1.03 g of an aqueous solution of sodium persulfate (NaPS) having a NaPS concentration of 10% wt were introduced in a 2000 mL double-jacketed glass vessel equipped with an agitation mobile, a nitrogen inlet, a temperature sensor and a condensor.
Nitrogen was introduced (bubbling) during 1 h at room temperature (25° C.) and then the reaction medium was heated at 75° C. within 1 h.
When the temperature has reached 75° C., 9.345 g of a 10% wt water solution of NaPS are added from a syringe pump within 2.5 hours, and 237.56 g of ABu are added from a second syringe pump within 2 hours.
At the end of the injections, the reaction medium is let during 2 hours at 75° C. and then cooled down overnight.
The glass vessel is unloaded and an homogeneous white latex having a pH of about 3-4 is obtained, referred herein as D0-2-Xa.
1621.97 g of the obtained D0-2-Xa are re-introduced in the glass vessel and then heated to 70° C. within 1 h, and then 35.98 g of peracetic acid (35% wt aqueous solution) are added within 1 h The reaction medium is let 1 h at 70° C. after the end of the addition of the peracetic acid.
A white latex is then obtained, referred herein as D0-2, having the same visual appearance as D0-2-Xa.
This latex D0-2 exhibits the following features:
78.5 g of the dispersion D0-1 of example 2.1 and 191 g of demineralized water were mixed in a 600 mL glass beaker and then transferred in a in a 500 mL double-jacketed glass vessel equipped with an lightning type agitation, a nitrogen inlet and a condenser Nitrogen was introduced (bubbling) during 1 h at room temperature (25° C.) and then the reaction medium was heated at 70° C. within 1 h.
When the temperature has reached 70° C., 2.8970 g of a 10% wt water solution of NaPS and 86.406 mL of ABu are added from a syringe pump within 4 hours. The reaction medium is then cured 2 h at 70° C. after the end of the addition.
An homogeneous latex Dp-1 is then obtained, having the following features:
252.65 g of the dispersion D0-2 of example 2., 530.52 g of demineralized water and 3.36 g of tert-dodecylmercaptan (TDM) were introduced in a 2000 mL double-jacketed glass vessel equipped with an agitation mobile, a nitrogen inlet, a temperature sensor and a condensor.
Nitrogen was introduced (bubbling) during 1 h at room temperature (25° C.) and then the reaction medium was heated at 70° C. within 1 h.
When the temperature has reached 70° C., 7.78 g of a 10% wt water solution of NaPS was added as a shot and then 209.28 g of ABu were added within 4 hours. The reaction medium is then cured 2 h at 70° C. after the end of the addition of ABu.
An homogeneous latex Dp-2 is then obtained, having the following features:
252.65 g of the dispersion D0-2 of example 2., 517.30 g of demineralized water and 16.80 g of TDM were introduced in a 2000 mL double-jacketed glass vessel equipped with an agitation mobile, a nitrogen inlet, a temperature sensor and a condensor.
Nitrogen was introduced (bubbling) during 1 h at room temperature (25° C.) and then the reaction medium was heated at 70° C. within 1 h.
When the temperature has reached 70° C., 7.78 g of a 10% wt water solution of NaPS was added as a shot and then 209.28 g of ABu were added within 4 hours. The reaction medium is then cured 2 h at 70° C. after the end of the addition of ABu.
An homogeneous latex Dp-3 is then obtained, having the following features:
The dispersions of latex as obtained in Example 3 were used for a fabric treatment.
Each of the dispersions Dp-1, Dp-2 and Dp-3 of example 3 was first diluted with water to a concentration of 0.2 wt. %, and then left for 12 hours at 25° C. Then, each of the obtained diluted dispersions was again diluted down with water to a concentration of 0.004 wt. % for the fabric treatment, thus leading to three fabric treatment compositions referred as C1, C2 and C3 (C1 correspond to the twice diluted dispersion Dp-1, C2 correspond to the twice diluted dispersion Dp-2, and C3 correspond to the twice diluted dispersion Dp-3).
The composition were used for treating 40 g Fabric (with 1000 ml of composition) in the conditions described herein-after.
For sake of comparison, the softening performance of the compositions C1, C2 and C3 were compared to a positive Benchmark (PBM) and to a negative benchmark (NBM), defined herein-after, used in the same conditions.
Cotton terry towels with approximate size 20×20 cm were used
A fabric treatment composition was used as a positive benchmark containing the commercially available quat Fentacare® TEP-88 of formula:
at the same weight concentration as in the compositions C1, C2 and C3.
Pure water (without any additive) was used as the negative Benchmark
The fabrics were treated in a two-part procedure
(A) Treatment with the Tested Composition (C1, C2, C3, PBM or NBM).
(B) Drying and Conditioning.
The softness was assessed in a panel of 6 people. The panellists assign a number from 1 to 5 characterizing the softness, higher score corresponds to better softness.
The panels included 4 samples:
Each fabric is touched only 3 times. The number of touches has to be limited as touching the fabric can lead to increase in softness. We have a total of 18 determinations of the softness for each system. The softness is calculated as an average of the 18 values. The standard deviation of the measurement is calculated in the following manner
Here SDP is the so-called pooled standard deviation; SD1, SD2, SDK are the standard deviations for each group; n1, n2, nk are the number of fabrics in each group. In our case we have 3 groups each containing the same number of fabrics (6). SD1, SD2 and SD3 are the standard deviations of the determination of the score from the 1st, 2nd and 3rd touch, respectively. The above equation can be written as follows:
The standard error for each system is calculated via the following equation:
Here N=18 is the total number of the measurements (or touches here).
The softness score assigned to a studied sample is not an absolute value, and makes sense only when compared to the values of the positive and negative benchmark. However the values of the softness score of the PBM and NBM vary in a certain range. Therefore a direct comparison between the softness scores of samples studied in different panels is misleading. A correct comparison would reflect the degree in which the compared samples differ from the PBM and the NBM. In order to be able to compare systems studied in different panels we introduced a parameter called softness degree, SDG:
The SDG is measured in percent. The NBM and PBM have 0% and 100% SDG, respectively. The majority of the studied systems have SDG in the range 0÷100%, some exceptionally well performing systems have SDG>100%.
The standard error of the softness degree is calculated via the standard rules for error propagation:
Δ(a±b)=√{square root over (Δa2+Δb2)}
Δ(a/b)=(a/b)√{square root over ((Δa/a)2+(Δb/b)2)}
Softness degree of the studied latexes at the working concentration (1×CW).
| Number | Date | Country | Kind |
|---|---|---|---|
| 19306273.4 | Oct 2019 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2020/076627 | 9/23/2020 | WO |
