Low density porous elastic crosslinked polymeric materials and their preparation

Abstract: This invention discloses a novel elastic cross-linked porous polymer having a porosity in the range 75 to 98% internal phase volume and having interconnected pores, said pores having a mean pore diameter in the range 15µm to 80µm, said polymer having an elastic return from 50% compression to 90% of initial thickness of less than 120 seconds, and a process for its production.

Description: This invention relates to low density polymeric materials, more particularly to low density porous elastic cross-linked polymeric materials and methods for their preparation. The porous materials comprise pores interconnected by holes in their side walls so forming a permeable structure. Prior Art In US-A-4522953 (and equivalent EP-A-60138) there have been disclosed novel vinyl polymeric materials prepared from high internal phase emulsions and these materials have outstanding porosity with respect to hydrophobic liquids such as oils. These known materials are prepared by polymerising water-in-oil high internal phase emulsions comprising various vinyl monomers and using certain selected surfactants. In EP-A-68830 a similar polymer made of a mixture of an acrylate monomer and styrene is disclosed, in which the acrylate component is less than 50%. EP-A-156241 discloses similar polymers which are subsequently functionalized. Styrene or alkyl acrylate monomers are used. Other specifications referred to in the above-mentioned United States patent have disclosed the preparation of porous polymeric beads and also the use of various pre-formed polymers together with monomers to prepare water-filled porous objects. The Present Invention It has now been found that by careful selection of monomers and by control of processing conditions low density porous cross-linked polymeric materials having a useful degree of elasticity can be obtained. Accordingly, the present invention provides an elastic cross-linked porous polymer as set out in claim 1. Preferably the elastic porous polymer has an elastic return from 50% compression to 90% of initial thickness of less than 40 seconds. Any elastic material will have a glass transition temperature below ambient temperature i.e. its surrounding temperature. Thus the present porous polymers should have a glass transition temperature (Tg) below ambient temperature, which is usually room temperature, but can be above or below room temperature depending on the conditions of the intended use of the polymer. In this invention, the polymer comprises up to 50% by weight of styrene and at least 50% by weight of an alkyl acrylate or methacrylate or mixture thereof. In a preferred form of the invention, the alkyl acrylate comprises 2-ethyl hexyl acrylate, n-butyl acrylate or a mixture thereof. A surprising feature of the present invention is that the desired elastic properties of the porous polymer are only achieved when the mean pore diameter is in the specified range. It has been found that additional or excessive mixing of the emulsion, which reduces both the breadth and mean value of the distribution of pore diameters, produces a material which collapses irreversibly on drying. Preferably the elastic cross-linked polymer has pores having a mean pore diameter in the range 25µm to 80µm. Accordingly, in a further aspect of the present invention there is provided a process for the preparation of the elastic porous polymer in which the monomers and an oil-soluble surfactant are mixed together and an aqueous phase is added in sufficient quantity to generate a high internal phase volume emulsion in the range 75 to 98% internal phase volume, the emulsion being given further sufficient stirring to generate droplets having a mean droplet diameter in the range 15 to 80µm, said emulsion in the presence of a polymerisation initiator then being subjected to heating to polymerise the monomers. Suitably a water-soluble polymerisation initiator is employed and is added to the monomer mixture in the aqueous phase. Alternatively, however, or as well as an oil-soluble polymerisation initiator can be employed, suitably being admired with the monomer mixture prior to addition of the aqueous phase. The porous polymer produced by the above process will have the desired structure for the production of an elastic porous polymer. However, the porous polymer will contain residual surfactant and for some applications this should be removed. Accordingly, in a further preferred form of the present invention, the polymer is washed substantially free of surfactant and dried to produce the novel elastic cross-linked porous polymer provided according to the present invention. The oil-soluble surfactant to be used in the preparation of the high internal phase emulsion preferably has an HLB value in the range of about 2 to about 6 and a preferred surfactant is sorbitan monooleate sold under the trade name Span 80. To determine the distribution of pore sizes and the mean pore diameter of the porous polymer an image analysis technique was used to compile a histogram representing the distribution of void sizes in the sample. The image analysis was carried out on a fracture surface of the dried porous elastic polymer. The mean void diameter d was then calculated as the number-average d = Σn i d i /Σn i where n i is the number of voids of diameter d i in bin i of the histogram. The term "elastic return" employed in the present specification and claims is described by the following experiment. Dry samples of the washed porous polymeric material, in the form of cylinders 5.5cm in diameter and 2 cm thick were compressed to approximately 50% of their initial thickness using an Instron Tensometer (model 4202) at a strain rate of 2.5mm min⁻¹. The samples were kept in a compressed state for 30 seconds and the load was then released. The time for recovery from 50% to 90% of the initial sample thickness was determined using a high speed video camera and a graduated scale mounted behind the sample. The polymer may be a cross-linked homopolymer or a copolymer with a Tg below ambient and the preferred monomers for use according to the present invention include styrene, 2-ethyl hexyl acrylate, n-butyl and isobutyl acrylate, hexyl acrylate, lauryl methacrylate and isodecyl methacrylate and mixtures thereof. Other monomers can also be used providing the glass transition temperature (Tg) of the final polymer is below ambient temperature. Suitable cross-linking agents for use in this invention include divinyl benzene, diethylene glycol dimethacrylate and 3-butylene dimethacrylate. The degree of cross-linking ranges from 2% to about 20% and is preferably about 5%. A factor concerned with stability of the emulsion is the presence in the aqueous phase of a water-soluble salt. Suitable salts include soluble sodium, calcium and aluminium salts. The amount present depends on the monomer and surfactant combination and is related to the valences of the metal component of the salt and it is preferred to use a polyvalent salt. The following examples illustrate the preparation of the porous elastic polymeric materials provided by this invention. Example 1 2 g of SPAN 80 were dissolved in a mixture of 6ml of 2-ethyl hexyl acrylate, 4ml of styrene and 1ml of commercial divinyl benzene (DUB) containing ≃0.5ml of ethyl vinyl benzene. The aqueous phase (100ml of water containing 2.5gl⁻¹ of potassium persulphate and 0.1 moles 1⁻¹ of calcium chloride) was dispersed in the monomer mixture using a three bladed paddle stirrer in a polypropylene beaker. Once all the aqueous phase was added the high internal phase emulsion was stirred for a further 120 seconds and then poured into a polypropylene bottle and sealed. The emulsion was then left to polymerise at 60°C for approximately 8 hours. The sample was removed from its container and squeezed to remove the aqueous phase. The porous polymer was then washed in water and isopropanol by repeatedly squeezing and re-expanding the sample. Finally the sample was squeezed to remove the last isopropanol wash liquor and allowed to dry in air. A sample of the dried, cleaned surfactant-free polymer was subjected to the elastic return test as described above. Further porous polymer samples were made using the procedure outlined above with different styrene/ethyl hexyl acrylate compositions and the results are set out below in Table I. Mixing time for example - 2 minutes. From the above table it will be appreciated that the content of ethyl hexyl acrylate in the total composition has a significant effect upon the elastic return time. Each of the above samples had an internal phase volume of 90%. Example 2 2g of SPAN 80 were dissolved in a mixture of 7ml of n-butyl acrylate, 3ml of styrene and 1ml of commercial divinyl benzene (DVB) containing ≃0.5ml of ethyl vinyl benzene. 100ml of an aqueous phase containing 2.5gl⁻¹ of potassium persulphate and 0.1 moles 1⁻¹ of calcium chloride were dispersed in the monomer mixture using a three bladed paddle stirrer in a polypropylene beaker. Once all the aqueous phase was added the high internal phase emulsion was stirred for a further 120 seconds and then poured into a polypropylene mould and sealed. The emulsion was then left to polymerise at 60°C for approximately 8 hours. The sample was then washed and dried as set out in Example 1. The present procedure was repeated employing 2g of Span 80, 8ml of n-butyl acrylate, 2ml of styrene, 1ml of DVB and 100ml of the aqueous phase containing 2.5gl⁻¹ potassium persulphate and 0.1 moles ⁻¹ calcium chloride. Each of the resulting washed and dried polymers was subjected to the elastic return test described above. The results are given in Table II. As in Example 1 the sample with the greater amount of acrylate had the shorter elastic return time. Each of the above samples had an internal phase of approximately 91%. The sample having an infinite time to return from 50% to 90% initial thickness had a glass transition temperature (Tg) above ambient temperature whilst those samples embodying the present invention had a glass transition temperature (Tg) below ambient temperature, which in the present case was a room temperature of 23°C.

Claims: An elastic cross-linked porous polymer derived from vinyl polymerisation of a mixture of monomers comprising up to 50% by weight of styrene and at least 50% by weight of an alkyl acrylate or methacrylate or mixture thereof and an amount of cross-linking agent providing a degree of cross-linking in the range 2 to 20%, the polymer having a porosity in the range 75 to 98% internal phase volume and having interconnected pores, said pores having a mean pore diameter in the range 15µm to 80µm, said polymer having an elastic return from 50% compression to 90% of initial thickness of less than 120 seconds. An elastic porous polymer as claimed in claim 1 having an elastic return from 50% compression to 90% of initial thickness of less than 40 seconds. An elastic porous polymer as claimed in claim 1 or claim 2, in which the alkyl acrylate comprises 2-ethylhexyl-acrylate. An elastic porous polymer as claimed in any one of the preceding claims in which the said pores have a mean pore diameter in the range 25µm to 80µm. An elastic porous polymer as claimed in any one of the preceding claims, in which the void volume is between 85 and 93%. A process for the preparation of an elastic porous polymer as claimed in any one of the preceding claims, in which the monomers and an oil soluble surfactant are mixed together and an aqueous phase is added in a sufficient quantity to generate a high internal phase volume emulsion in the range 75 to 98% internal phase volume, the emulsion being given sufficient stirring to generate droplets having a mean droplet diameter in the range 15µm to 80µm, said emulsion in the presence of a polymerisation initiator then being subjected to heating to polymerise the monomers. A process as claimed in claim 6 in which a water-soluble polymerisation initiator is added in the aqueous phase. A process as claimed in claim 6 or claim 7 in which the polymer is washed substantially free of surfactant and dried. A process as claimed in any one of claims 6 to 8 in which a water-soluble salt is added to the aqueous phase to enhance the stability of the emulsion prior to polymerisation.

Inventors: EDWARDS CHRISTOPHER JOHN CARRU, GREGORY DONALD PETER, SHARPLES MARTIN, EDWARDS, CHRISTOPHER JOHN CARRUTHERS, GREGORY, DONALD PETER, SHARPLES, MARTIN
Applicants: UNILEVER NV, UNILEVER PLC, UNILEVER N.V.
Application year: 1987
Main classification: C08J9
IPC codes: C08F212, C08F2, C08F220, C08J9