AU722023B2 - Process for making substantially homogenous copolymers for personal care applications - Google Patents

Description

ll I S F Ref: 376291D1

AUSTRALIA

PATENTS ACT 1990 COMPLETE SPECIFICATION FOR A STANDARD PATENT

ORIGINAL

Name and Address of Applicant: Actual Inventor(s): Address for Service: Invention Title: ISP Investments Inc.

818 Washington Street Wilmington Delaware 19801 UNITED STATES OF AMERICA Kou-Chang Liu, Lowell R Anderson, Eugene E Hardy, Yakir Reuven Spruson Ferauson. Patent Attornevs Level 33 St Martins Tower, 31 Market Street Sydney, New South Wales, 2000, Australia Process for Making Substantially Homogeneous Copolymers for Personal Care Applications The following statement is a full description of this invention, including the best method of performing it known to me/us:- 5845 PROCESS FOR MAKING SUBSTANTIALLY HOMOGENEOUS COPOLYMERS FOR PERSONAL CARE

APPLICATIONS

BACKGROUND OF THE INVENTION Field of the Invention This invention relates to a process for making substantially homogenous copolymers of at least two monomers having substantially differing reactivity rates, for use in hair styling and hair care applications.

Description of the Prior Art Several synthetic polymers containing vinyl lactams are presently being used in cosmetic formulations, particularly in hair care products, to contribute body, set retention and conditioning to such products.

Representative of the art in this field are the following U.S. patents: 3,914,403; 3,954,960; 4,057,533; 4,210,161; 4,586,518; 4,753,793; 4,764,363; 4,834,968; 4,842,850; is 4,902,499; 4,906,459; 4,923,694; 4,963,348; 4,983,377; 5,011,895 and 5,015,708; and WO 91/15186; WO 91/15185; EPO 0412704A2; EPO 0412707A1; and JP 57126409.

Generally these synthetic polymers were made by a "one-pot" polymerization process in which selected amounts of the several monomers were reacted together. The composition of these one-pot polymers was considered as being the same as the 20 composition of the charged monomers. However, in reality, such a polymerization process can provide only a mixture of polymers of various compositions, and, Sadditionally, an indeterminate amount of homopolymers and undesired copolymers.

Accordingly, it is an object of this invention to provide a process for making substantially homogeneous copolymers of at least two monomers having substantially 25 differing reactivity rates.

Summary of the Invention A process is described herein for making substantially homogeneous copolymers of 20-99% vinyl pyrrolidone and 1-80% N-3,3-dimethylaminopropyl methacrylamide, preferably about 50-95% VP and 5-50% DMAPMA, and most preferably about 80% VP 30 and 20% DMAPMA, by weight, having a weight average molecular weight of about I \DAYLIB\I.IBFF\0419 doc 2 200000 to 1500000, and a clear, low viscosity aqueous solution of the homogeneous copolymer at a 5-20% solids level, preferably about 10-15%, by weight of the solution, and having a viscosity of about 5,000 to 80,000cps, preferably about 10,000 to 70,000cps.

According to a broad form of the invention there is provided a process for making S substantially homogeneous polymers of at least two monomers having substantially differing reactivity rates, in a selected composition, by polymerisation of said monomers, comprising: precharging all of the slowest reacting monomer in an amount in accordance with the selected composition, optionally with part of one or more of said faster reacting I0 monomers, and introducing the faster reacting monomer or monomers independently and incrementally or continuously into the reactor at a specific feeding schedule for each monomer, as determined for each monomer before the polymerisation by the following equations: EQUATION 1 1 1 Aj(t) 1 1 exp alj t 1 exp a -a t 2 2 20 2(1 a where Aj(t) has four adjustable parameters, at, a2, a 3 and a4 for each monomer: 25 and a determines the center of the distribution; a2 affects the width of the distribution; a3 determines the ascending portion of the distribution; and "a4 determines the descending portion of the distribution; and t time in minutes during copolymerization; 31 and EQUATION 2 Aj(ti) of Monomer j charged at time t i x loo A (ti) i 0 where N the overall time of the polymerization reaction; wherein a set of determined values for a2, a 3 and a 4 provides said specific feeding schedule and assures that the curve of the rate of disappearance vs. time for the fastest reacting monomer substantially coincides with the rate of disappearance for each Sof the slower reacting monomer or monomers, as shown in Figure 2 herein.

The copolymer solution obtained herein is less viscous and has better clarity than solutions of non-homogenous copolymers of the same composition, or of related commercial products. When formulated into hair styling compositions, these homogeneous polymer solutions also provide improved curl retention (hold) during use.

io Brief Description of the Drawings FIGURE 1 is a graphical representation of a non-homogeneous (one-pot) process in which is plotted percent unreacted VP and DMAPMA vs. time for a reaction mixture of 80:20 by weight VP/DMAPMA copolymer at 15% solids.

FIGURE 2 is a graphical representation of the homogeneous process of the invention in which is plotted percent unreacted VP and DMAPMA vs. time during the preparation of an aqueous solution of 80:20 by weight VP/DMAPMA copolymer at solids.

Detailed Description of the Invention Disclosed herein is a process provided for making substantially homogeneous 20 copolymers of vinyl pyrrolidone and N-3,3-dimethylamino-propyl methacrylamide of nredetermined composition.

In this process, the less reactive monomer of the copolymer (VP) is precharged into a reactor at a suitable reaction temperature, generally about 50-80°C., preferably 55-75°C.

Then the more reactive monomer (DMAPMA) is introduced incrementally into the VP- 25 charged reactor at a rate which corresponds to the observed rate of disappearance of VP.

I:\Dayli.h\.IBI:\0419 doc 4 The entire predetermined amount of the DMAPMA monomer is added before substantially all the VP monomer has been consumed so that both monomers can react to form a substantially homogeneous copolymer in a desired compositional ratio of VP:DMAPMA. Consequently, a copolymer is obtained whose composition approaches the nominal monomer ratio of the desired copolymer composition and whose structure has the two individual monomeric units of the copolymer distributed substantially uniformly in a homogeneous chain along the backbone of the polymer. For example, for an 80:20 weight ratio of VP/DMAPMA copolymer, which is approximately equivalent to a 6:1 mole ratio of VP/DMAPMA, the homogeneous copolymer of the invention has a monomer distribution corresponding substantially close to VP[-VP-VP-VP-VP-VP-DMAPMA-VP-VP-VP-Vp-Vp-VPDMAPA The precharge in the process of the invention may include some DMAPMA therein, generally in an amount which is less than 10% of the total amount of DMAPMA required for the predetermined copolymer composition without affecting the homogeneous polymerization process.

However, it is still neceasry that the rate of V DMAPMA after any precharge is carried out at *pop substantially the rate of disappearance of VP during 25 copolymerization.

The schedule of addition of DMAPMA to accomplish the desired matched rate of reaction of VP is determined Sin t in the following manner.

o V V...ap DETERMINATION OF ADDITION SCHEDULE FOR DMAPM TO FORM A HOMOGENEOUS COPOLYMER OF VP AND DpMA A. First, a one-pot copolymerization of VP and DMAPMA was carried out as follows: EXAMPLE 1 VP (215 DMAPMA (54 and deionized water (1530 g) were charged into a 2-liter resin pot equipped with a gas inlet, a liquid inlet, a thermometer and a condenser. A stream of nitrogen then was bubbled through the solution and maintained during the reaction. The solution was gradually heated to 689C.; then 0.25 ml of Lupersol 11 (t-butylperoxy pivalate) as catalyst was added; then another 0.25 ml of the catalyst was added after 10 minutes; and another 6 units of 0.25 ml was added each 30 minutes. The total addition was carried out over a 4-hour period.

The relative percentage amounts of residual monomers present during the course of the one-pot reaution was determined by gas chromatographic analysis 20 after sampling the reaction mixture periodically. The analytical data obtained then was plotted as the graph of FIGURE 1 As shown in FIGURE 1, DMAPMA reacts much more rapidly than VP. Accordingly, after 240 minutes, all the 25 DMAPMA is consumed while residual VP monomer still is available for homopolymerization. Thus the copolymer formed is of a composition different from the desired monomer ratio selected by the precharged amounts of the two monomers. Under these experimental conditions, the polymer product obtained is a complex mixture of a homopolymer which is polyvinylpyrrolidone, and a copolymer of VP and DMAPMA of uncertain composition.

6 B. To form a homogeneous copolymer, it is necessary that the curve of rate of reaction vs. time for DMAPMA substantially coincide or match the rate of reaction curve for VP. To accomplish this, the VP is precharged and substantially all the DMAPMA is fed after to the precharge at a feeding schedule determined by analysis of the data of FIGURE 1. The DMAPMA monomer to be fed at time t of the polymerization is determined from the Asymmetric Double Sigmoidal Distribution formula, At, below, which has four adjustable parameters, a 2 a 3 and a 4 1 1 At 1 1 exp a. t 1 exp a, t a2 l -exp a 1 a3 a4 where t time in minutes during copolymerization; a, is a parameter which determines the center of the distribution; 15 a 2 is a parameter which affects the width of the distribution; a 3 is a parameter which determines the ascending portion of the distribution; and a 4 is a parameter which determines the descending portion of the distribution.

At DMAPMA to be fed at time t x 00

N

t 0 where N time when the polymerization is completed.

7 To match the DMAPMA curve to the VP curve of FIGURE 1, an "initial guess" is made for the values of a 2 a 3 and a 4 These values are inserted into the A t formula and the DMAPMA to be fed at time t is calculated. Then a polymerization reaction is carried out using this schedule. The resulting unreacted DMAPMA during this polymerization will probably not match the unreacted VP at the same time t. If the unreacted DMAPMA at time t is too large, then the value of a 3 (ascendency) in the At formula is increased, a 4 (descendency) is decreased, a 1 (center) is decreased, and a 2 (width) is decreased. Conversely, if the initial guess values of a, through a 4 give a reaction rate for DMAPMA which is too fast, then changes in the values of aI through a 4 are made in a direction opposite to those discussed above.

These new values of the parameters are then used to determine a new feeding schedule. Using this feeding schedule, another polymerization is carried out, and the 20 process of adjustment of the parameters described above is repeated.

This process is known as "interative fitting" of data to a curve. After 4 or 5 such iterative fittings, the experimental VP and DMAPMA curves will be matched to a satisfactory degree, as shown in FIGURE 2 herein.

The matching curve of DMAPMA in FIGURE 2 can originate from at least one set of values for al, a 2 a 3 and a 4 (the last set of the iterative fitting process) used to calculate a suitable feeding schedule of DMAPMA over the entire period of the polymerization. One such set is: alI 17 a 2 28 a 3 2 a 4 8 9. With such a suitable DMAPMA feeding schedule available, a homogeneous copolymer of VP and DMAPMA was prepared as described in Example 2 below.

EXAMPLE 2 Preparation of a Homogeneous Copolvmer of VP and DMAPMA In this process, 216 grams of vinylpyrrolidone (recrystallized material) and 580 grams of deionized water were charged to a 2-liter water jacketed resin flask.

The flask was equipped with an overhead stirrer connected to an anchor stirrer, a nitrogen inlet for sparging to remove dissolved air and a thermocouple which is connected to a temperature controller. The temperature was raised to 68°C., by passing heated water from a temperature controlled bath into the jacket of the resin flask. A mechanical syringe pump which could be set to deliver DMAPMA at a set rate was connected to the reactor through polyethylene tubing.

20 The DMAPMA reactant was added from the syringe pump as a 1 liter solution of 54 grams of DMAPMA in water, according to the following feeding schedule: Time Amount of DMAPMA (min.) Solution Added (ml) 0-30 418.58 30-60 269.80 60-90 153.90 90-120 80.56 120-150 40.10 150-180 19.38 180-210 9.32 210-240 4.38 9 The totals added during the entire reaction were VP (216 grams), DMAPMA (54 grams) and water (1530 grams).

Additions of Lupersol 11 (t-butyl peroxypivalate, Atochem, NA) initiator were made at various intervals throughout the initial part of the reaction. Additions of 0.25 ml of the initiator were made at 0, 10, 40, 70, 100, 140 and 180 minutes. At 210 and 240 minutes, 0.25 ml of either VAZO 501 4 ,4'-azobis(4-cyanovaleric) acid, Wako Pure Chemical Industries, Ltd, Japan) was added to complete the reaction of any residual vinylpyrrolidone monomer. For this purpose, the reaction was allowed to proceed for a total of 10 hours. During this final period the temperature was raised to 750C. where it was maintained until the reaction was completed.

The product was discharged as a clear, moderately viscous, aqueous solution of a substantially homogeneous copolymer of VP and DMAPMA in an 80:20 weight Sratio at a 15% solids level. The residual vinylpyrrolidone content was The procedure described above can be repeated to provide optimized DMAPMA feeding schedules for any selected copolymer composition, and at any particular solids content, at a prescribed polymerization 25 temperature, solvent level, and amount of initiator.

Table 1 below shows the advantageous physical properties of low viscosity and enhanced clarity for the homogeneous copolymer solution of the invention, as compared to non-homogeneous copolymer solutions of the 30 same composition.

10 TABLE 1 Viscosity*** Clarity (cps) (NTU) Mol. Wt.

Homogeneous 61,500 1.80* 610,000 copolymer solution Non-homogeneous 150,000 14.15** 620,000 copolymer solution Hach; on 0.4% aqueous solution pH 7.98 pH 7.44 Brookfield viscosity, on aqueous solution; Model RTV, rpm, Spindle 17, 25 0

C.

HAIR STYLING COMPOSITIONS The substantially homogeneous copolymer of the Sinvention finds particular utility in multifunctional hair care products such as water-based, rinse-off hair styling and conditioning products, and in mousse hair care products. It may be included in such compositions as a concentrate, or as a gel, and applied as a selfactuated pump hair spray, or in an aerosol product with a propellant. Various actuator and packaging devices known in the art may be used therewith.

Such hair styling products have significantly improved hair holding (curl retention) and hair stiffness properties, while maintaining enhanced hair conditioning (detangling, flyaway and combability) properties, compared to non-homogeneously prepared copolymers of the same monomers, when formulated into hair styling compositions.

11 HAIR STYLING COMPOSITIONS OF IIUENT.ION Hair Styling Gel Lq) Homogeneous copolymer of VP/DMAPMA (80:20) (as 15% aqueous Solution) Hydroxyethyl cellulose (Natrosole 250 HHR-Aqulon) Triethanolamine

(TEA)

Deionized water 5.00 0.50 0.20 qs Preparation: Heat to 850C.

Add while mixing well.

Add with rapid mixing.

Neutralize with a. a Hair Styling~ Mousse Homogeneous copolymer of VP/DMAPMA (80:20) (as 15% aqueous solution) Sodium cocoyl isothionate (IgeponO AC-78 Rhone-Poulenc) Emulsifying wax (PolowaxO A-31 Croda) Propylene glycol, diazolidinyl urea, methyl paraben and propyl paraben (GermabenO II Sutton (ISP) DymelO 152A 1-dif luoroethane) Hydrocarbon A-17 (n-butane) Water wt (g) 0.75 0.15 0.25 4 .00 4 .00 qs 12 Preparation: 1. Add to while agitating and heating to 55-600C.

2. Add while mixing at 55 0 C. Begin cooling.

3. Add and mix rapidly.

4. Cool to 25oC. and add Charge into pressurized container and add and Table 2 below demonstrates the advantageous curl retention property for a hair styling composition (gel) containing the homogeneous copolymer of the invention as compared to a non-homogeneous copolymer.

TABLE 2 CURL RETENTION PROPERTY Copolymer in Hair Relative Curl Retention Styling Composition of Composition* Homogeneous Copolymer 116.9 *Non-homogeneous Copolymer 95.3 v s. standard at 90% RH and 90 min. duration While the invention has been described with particular reference to certain embodiments thereof, it will be understood that changes and modifications may be made which are within the skill of the art. Accordingly, it is intended to be bound only by the following claims, in which:

Claims (4)

1. A process for making substantially homogeneous polymers of at least two monomers having substantially differing reactivity rates, in a selected composition, by polymerization of said monomers, comprising: precharging all of the slowest reacting monomer in an amount in accordance with the selected composition, optionally with part of one or more of said faster reacting monomers, and introducing the faster reacting monomer or monomers independently and incrementally or continuously into the reactor at a specific feeding schedule for each 1I monomer, as determined for each monomer before the polymerization by the following equations: EQUATION 1 1 1 Aj(t) 1 Sa 2 j La 2 J 1+ exp a t 1 exp a a 3 j &4j where Ai(t) has four adjustable parameters, a 2 a3 and a4 for each monomer: 20 and a, determines the center of the distribution; a* a2 L ,J3 I L %,rl a 3 determines the ascending portion of the distribution; and a4 determines the descending portion of the distribution; and *t time in minutes during copolymerization; and EQUATION 2 Aj of Monomer j charged at time t i x 100 A (ti) i=0 I \tI )yLib\lIFF\041 '.doc 14 where N time the overall time of the polymerization reaction; wherein a set of determined values for a 2 a 3 and a 4 provides said specific feeding schedule and assures that the curve of the rate of disappearance vs. time for the fastest reacting monomer substantially coincides with the rate of disappearance for each of S the slower reacting monomer or monomers, as shown in Figure 2 herein.

2. A process according to claim 1 where said monomers are VP and DMAPMA.

3. A process for making a substantially homogeneous polymer of at least two monomers having substantially differing reactivity rates, substantially as hereinbefore described with reference to Example 1 and Example 2. Ji

4. A substantially homogenous polymer prepared by the process of any one of claims 1 to 3. Dated 19 May, 2000 ISP Investments Inc. Patent Attorneys for the Applicant/Nominated Person SPRUSON FERGUSON i* f* 99 9 :\DayLib\LBA]031 58.doc:tlt