Apparatus and method for expanding thermally expandable thermoplastic microspheres to expanded thermoplastic microspheres

Abstract

An apparatus and a method for expanding a slurry of thermally expandable thermoplastic microsphere is disclosed. The apparatus and method expand the slurry of thermally expandable thermoplastic microsphere without any direct contact to a fluid heat transfer medium. The apparatus and method utilize a distribution pipe attached to an outlet pipe.

Claims

1. An apparatus for expanding thermally expandable thermoplastic microspheres, the apparatus comprising: a heating zone being capable of withstanding a pressure of at least 4 bars, the heating zone having an inlet pipe and an outlet pipe, a pump for feeding a slurry of thermally expandable thermoplastic microspheres into the heating zone and capable of generating a pressure of at least 4 bars in the heating zone; a means for heating the slurry of thermally expandable thermoplastic microspheres in the heating zone to a temperature of at least 60 C. without direct contact of the slurry to any fluid heat transfer medium; and a distribution pipe having an inlet and an outlet, wherein the outlet pipe is attached to the distribution pipe between the inlet and the outlet of the distribution pipe.

2. The apparatus according to claim 1, wherein the outlet pipe has a constant internal diameter.

3. The apparatus according to claim 1, wherein the outlet pipe increases in internal diameter such that an end section to an opening of the outlet pipe increases in an internal diameter to at least twice the internal diameter of the outlet pipe.

4. The apparatus according to claim 1, wherein the distribution pipe comprises at least one mixing/separating element within, or combinations thereof downstream from the attachment of the outlet pipe to the distribution pipe.

5. The apparatus according to claim 4, wherein the at least one mixing/separating element is selected from a rotating mixer, a static mixer, a rotating knife, a steam dividing unit or a sieve.

6. The apparatus according to claim 1, wherein the means for heating the slurry is at least one electric heating element, a heat exchanger or an electromagnetic radiation source.

7. The apparatus according to claim 1 further comprising a pulsation damper positioned between the pump and the heating zone.

8. A method for expanding thermally expandable thermoplastic microspheres comprising the steps: providing a slurry of thermally expandable thermoplastic microspheres into a heating zone, heating the slurry of thermally expandable thermoplastic microspheres in the heating zone to a temperature of at least 60 C. and generating a pressure of at least 4 bars, wherein the heating is achieved without any direct contact of the slurry with any fluid heat transfer medium, maintaining the pressure within the heating zone such that the thermally expandable thermoplastic microspheres do not fully expand; and withdrawing the slurry from the heating zone through an outlet pipe and then through a distribution pipe, wherein the outlet pipe is attached to the distribution pipe between an inlet and an outlet of the distribution pipe, and into a zone with a lower pressure to fully expand the thermally expandable thermoplastic microspheres.

9. The method according to claim 8, wherein the outlet pipe is used with a constant internal diameter.

10. The method according to claim 8, wherein the outlet pipe is used which increases in internal diameter such that an end section to an opening of the outlet pipe increases in an internal diameter to at least twice the internal diameter of the outlet pipe.

11. The method according to claim 8, wherein the distribution pipe comprises at least one mixing/separating element within, or combinations thereof downstream from the attachment of the of the outlet pipe with the distribution pipe.

12. The method according to claim 8 further comprising adding a cooling media via the inlet, wherein the cooling media is any one of a gas, a liquid or particulates or any combination thereof, selected from air, water, nitrogen gas, chalk particles, calcium carbonate particles, silica particles, clay particles and TiO.sub.2 particles.

13. The method according to claim 8, wherein the pressure in the heating zone is maintained from between 4 to 50 bars.

14. The method according claim 8, wherein the slurry of expandable microspheres is heated in the heating zone to a temperature from at least 60 to 250 C.

15. The method according to claim 8, wherein a content of thermally expandable thermoplastic microspheres in the slurry of thermally expandable thermoplastic microspheres is between 5 to 50 wt %.

16. The method according to claim 8, wherein a carrier liquid in the slurry of thermally expandable thermoplastic microspheres is a water based liquid or an oil based liquid.

17. The method according to claim 8, wherein heating the slurry of thermally expandable thermoplastic microspheres is carried out by at least one of an electric heating element, a heat exchanger or an electromagnetic radiation source.

Description

BRIEF DESCRIPTION OF FIGURES

(1) FIG. 1 shows an apparatus for expanding thermally expandable thermoplastic microspheres according to the present disclosure.

(2) FIG. 2 shows an expanded view of an end section of an outlet pipe and a distribution pipe according to the present disclosure.

DETAILED DESCRIPTION

(3) For a complete understanding of the present invention and the advantages thereof, reference is made to the following detailed description and the accompanying figures.

(4) It should be appreciated that the various aspects and embodiments of the detailed description and the accompanying figures as disclosed herein are illustrative of the specific ways to exercise the invention and do not limit the scope of invention when taken into consideration with the claims and the detailed description and the accompanying figures. It will also be appreciated that features from different aspects and embodiments of the invention may be combined with features from different aspects and embodiments of the invention.

(5) The apparatus and method according to present invention can be used for all kinds of thermally expandable thermoplastic microspheres.

(6) As used herein, thermally expandable thermoplastic microspheres refers to a thermoplastic polymer shell encapsulating a blowing agent. When expanded by heat the thermally expandable thermoplastic microspheres are referred to as expanded thermoplastic microspheres.

(7) In a first aspect the present invention relates to an apparatus for expanding thermally expandable thermoplastic microspheres. The apparatus is shown in FIG. 1. The apparatus comprises a heating zone 4 which is capable of withstanding a pressure of at least 4 bars. The heating zone 4 has an inlet pipe 10 and an outlet pipe 8. The apparatus comprises a pump 1 for feeding a slurry of thermally expandable thermoplastic microspheres into the heating zone 4. The pump 1 is capable of generating a pressure of at least 4 bars in the heating zone 4. The apparatus comprises a means for heating the slurry of thermally expandable thermoplastic microspheres in the heating zone 4 to a temperature of at least 60 C. without direct contact of the slurry to any fluid heat transfer medium. The outlet pipe 8 of the apparatus is attached to a distribution pipe 12 between an inlet 13 and an outlet 14 of the distribution pipe 12.

(8) The thermally expandable thermoplastic microspheres can be those marketed by AkzoNobel under the trademark Expancel. Thermally expandable thermoplastic microspheres and their manufacture are disclosed in, for example, U.S. Pat. No. 3,615,972, U.S. Pat. No. 3,945,956, U.S. Pat. No. 4,287,308, U.S. Pat. No. 5,536,756, U.S. Pat. No. 6,235,800, U.S. Pat. No. 6,235,394, U.S. Pat. No. 6,509,384, U.S. Pat. No. 6,617,363, U.S. Pat. No. 6,984,347, US 2004/0176486, EP 486080, EP 566367, EP 1067151, EP 1230975, EP 1288272, EP 1598405, EP 1811007, EP 1964903, WO 2002/096635, WO 2004/072160, WO 2007/091960, WO 2007/091961, WO 2007/142593, JP 1987-286534 and JP 2005-272633, which are hereby incorporated herein by reference.

(9) The thermoplastic polymer shell can be made from polymers or co-polymers by polymerising various ethylenically unsaturated monomers. The ethylenically unsaturated monomers can be nitrile containing monomers, such as acrylonitrile, methacrylonitrile, alpha-chloroacrylonitrile, alpha-ethoxyacrylonitrile, fumaronitrile and crotonitrile, acrylic esters, such as methylacrylate or ethyl acrylate, methacrylic esters, such as methyl methacrylate, isobornyl methacrylate and ethyl methacrylate, vinyl halides, such as vinyl chloride, vinylidene halides, such as vinylidene chloride, vinyl pyridine, vinyl esters, such as vinyl acetate, styrene, optionally substituted, such as styrene, halogenated styrenes and alpha-methyl styrene, dienes, such as butadiene, isoprene and chloroprene, and any mixtures thereof.

(10) The ethylenically unsaturated monomers may also comprise crosslinking multifunctional monomers. The crosslinking multifunctional monomers include any one of divinyl benzene, ethylene glycol di(meth)acrylate, diethylene glycol di(meth)acrylate, triethylene glycol di(meth)acrylate, propylene glycol di(meth)acrylate, 1,4-butanediol di(meth)acrylate, 1,6-hexanediol di(meth)acrylate, glycerol di(meth)acrylate, 1,3-butanediol di(meth)acrylate, neopentyl glycol di(meth)acrylate, 1,10-decanediol di(meth)acrylate, pentaerythritol tri(meth)acrylate, pentaerythritol tetra(meth)acrylate, pentaerythritol hexa(meth)acrylate, dimethylol tricyclodecane di(meth)acrylate, triallylformal tri(meth)acrylate, allyl methacrylate, trimethylol propane tri(meth)acrylate, trimethylol propane triacrylate, tributanediol di(meth)acrylate, PEG #200 di(meth)acrylate, PEG #400 di(meth)acrylate, PEG #600 di(meth)acrylate, 3-acryloyloxyglycol monoacrylate, triacryl formal or triallyl isocyanate, triallyl isocyanurate or any mixtures thereof. The crosslinking multifunctional monomers make up from 0.1 to 1 wt %, most preferably from 0.2 to 0.5 wt % of the total amounts of ethylenically unsaturated monomers of the thermoplastic polymer shell.

(11) It is preferable that the thermoplastic polymer shell constitutes from 60 to 95 wt % of the thermally expandable thermoplastic microsphere and more preferably from 75 to 85 wt %.

(12) A softening temperature of the thermoplastic polymer shell corresponds to its glass transition temperature (T.sub.g). T.sub.g is within the range of 50 to 250 C., and more preferably in the range of 70 to 200 C.

(13) The blowing agent in the thermally expandable thermoplastic microspheres can be a liquid which has a boiling temperature (at room temperature and pressure) not higher than the T.sub.g. The blowing agent can be at least one hydrocarbon or any mixtures thereof. The hydrocarbons can be selected from n-pentane, isopentane, neopentane, butane, isobutane, hexane, isohexane, neohexane, heptane, isoheptane, octane and isooctane. The hydrocarbons can also be petroleum ether, chlorinated or fluorinated hydrocarbons, such as methyl chloride, methylene chloride, dichloro ethane, dichloro ethylene, trichloro ethane, trichloro ethylene and trichlorofluoro methane. The blowing agent is preferably at least one of isobutane, isopentane, isohexane, cyclohexane, isooctane, isododecane, and any mixtures thereof. The blowing agent is more preferably isobutane and isopentane.

(14) The blowing agent is present in an amount of from 5 to 40 wt % of the thermally expandable thermoplastic microspheres.

(15) The boiling temperature (at room temperature and pressure) of the blowing agent is preferably between 20 to 200 C., more preferably between 20 to 150 C. and even more preferably between 20 to 100 C.

(16) A temperature at which the thermally expandable thermoplastic microspheres begin expanding at atmospheric pressure is referred to as T.sub.start. T.sub.start depends on the type and combination of the thermoplastic polymer shell and the blowing agent. The thermally expandable thermoplastic microspheres used in the present invention preferably have a T.sub.start from between 40 to 230 C. and more preferably between 60 to 180 C.

(17) The apparatus comprises the heating zone 4 into which a slurry of thermally expandable thermoplastic microspheres flows through. The heating zone 4 can be in the form of a vessel, pipe or tube. The heating zone 4 is provided with the inlet pipe 10 and the outlet pipe 8.

(18) The heating zone 4 heats the slurry of thermally expandable thermoplastic microspheres therein without any direct contact of the slurry with any fluid heat transfer medium i.e. steam, or heated gas.

(19) The heating zone 4 may be a heat exchanger. The heating zone 4 when in the form of the heat exchanger then comprises at least one pipe or tube surrounded by a heat transfer medium not being in direct contact with the slurry of thermally expandable thermoplastic microspheres. The heat exchanger may, for example, comprise several preferably parallel pipes or tubes, for example from 2 to 10 or from 3 to 7 pipes or tubes, preferably connected to a common inlet and a common outlet. The pipes or tubes, may each have an inner diameter from 2 to 25 mm, or preferably from 4 to 15 mm or even more preferably from 6 to 12 mm. It is also possible to have only one pipe or tube. Using a single pipe or tube has the advantage of decreasing the risk for uneven flow distribution caused by partial clogging in one of several parallel pipes or tubes. Such a single pipe or tube is preferably surrounded by a heat transfer media, positioned in a vessel or tank containing the heat transfer media. The heat transfer media may be any suitable fluid medium such as hot water, steam or oil.

(20) The heating zone 4 may be provided with at least one electric heating element. The at least one electric heating element may be positioned inside or outside the heating zone 4, or any combination thereof. The electric heating element may be provided in the centre of the heating zone 4, such that the slurry of thermally expandable thermoplastic microspheres flows in the gap around that electric heating element within the heating zone 4. It is preferable that the electric heating elements are provided both inside and outside the at least one pipe or tube.

(21) The heating zone 4 may be provided with an electromagnetic radiation microwave source, such as microwaves.

(22) The heating zone 4 is preferably made from a thermally conductive metal such as steel or copper. The thermally conductive metal is advantageous where heating of the slurry is provided by means of a fluid heat transfer medium or by electric heating elements.

(23) If the heating is provided by the electromagnetic radiation source, the heating zone 4 is made of a material permeable for such radiation emanating from the electromagnetic radiation source, such as a polymeric material.

(24) The heating zone 4 heats the slurry of thermally expandable thermoplastic microspheres to a temperature of at least 60 C. The temperature at the heating zone 4 is measured by a thermometer 7. However with the heating zone 4 of the present invention it is possible to expand the thermally expandable thermoplastic microspheres requiring higher temperatures than practically achievable by steam, for e.g. by using electric heating elements or hot oil as a heat transfer medium. The temperature to which the slurry of thermally expandable thermoplastic microspheres is heated in the heating zone 4 depends on the type of thermally expandable thermoplastic microspheres. The temperature is at least 60 C. and preferably within the range of 60 to 250 C., more preferably 80 to 230 C. and even more preferably 80 to 200 C.

(25) According to the present invention, the slurry of thermally expandable thermoplastic microspheres is used. By using the slurry of thermally expandable thermoplastic microspheres dusting is avoided. By using the slurry of thermally expandable thermoplastic microspheres, blockage of the apparatus by dry expanded thermoplastic microspheres is avoided.

(26) The slurry of thermally expandable thermoplastic microspheres is obtained by providing to the thermally expandable thermoplastic microspheres a carrier liquid. The carrier liquid is inert to the thermally expandable thermoplastic microspheres. The carrier liquid can withstand temperatures to which the slurry is heated. The carrier liquid can be water, or a water based liquid to form an aqueous slurry of thermally expandable thermoplastic microspheres. The carrier liquid can be an organic liquid, such as vegetable oil, mineral oil and glycerol or any mixtures thereof. Since the organic liquids are free of water and since no steam or water needs to be added to the slurry, it is possible to prepare a water-free slurry of thermally expandable thermoplastic microspheres, this is advantageous where the resulting expanded thermoplastic microspheres are needed in applications that need to be water-free.

(27) Furthermore, as no other fluid media needs to be added to the slurry, it is possible to prepare a slurry of expanded microspheres having a high and controlled solids content of the expanded thermoplastic microspheres.

(28) A content of thermally expandable thermoplastic microspheres in the slurry of thermally expandable thermoplastic microspheres is between 5 to 50 wt %, preferably between 5 to 30 wt % and more preferably between 10 to 20 wt %. When the content is within these ranges a pump-ability of the slurry and/or a transportation of the slurry of thermally expandable thermoplastic microspheres in the apparatus is optimal.

(29) The slurry of thermally expandable thermoplastic microspheres is fed into the heating zone 4 through the inlet pipe 10 by a pump 1. The pump 1 provides sufficiently high pressure (at least 4 bars) in the heating zone 4 so that the thermally expandable thermoplastic microspheres do not fully expand in the heating zone 4 when heated. The thermally expandable thermoplastic microspheres may expand partially within the heating zone 4, e.g. to a volume of from 10 to 80% or from 20 to 70% of the volume after the completed expansion outside the heating zone 4, but may also be prevented from expanding at all within the heating zone 4 by manipulating the pressure provided by the pump 1. The pump 1 can be any one of a hydraulic diaphragm pump, a piston pump, a screw pumps (e.g. eccentric screw pumps), a gear pumps, a rotary lobe pump and a centrifugal pumps. Hydraulic diaphragm pumps are particularly preferred. The pump 1 provides a force required for transporting the slurry of thermally expandable thermoplastic microspheres through apparatus.

(30) The pressure within the apparatus is measured by a pressure gauge 3.

(31) The apparatus may further be provided with a conduit (not shown) for transporting the slurry of thermally expandable thermoplastic microspheres to the pump 1, for example from a tank (not shown) holding the slurry of thermally expandable thermoplastic microspheres. The conduit (not shown) would be connected to a three way valve 9, which directs the slurry of thermally expandable thermoplastic microspheres through the apparatus.

(32) The pressure provided by the pump 1 and required in the heating zone 4 depends on the specific thermally expandable thermoplastic microspheres. Preferably the pressure is at least 10 bars. The upper pressure limit is determined by practical considerations and may, for example, be up to 40 bars or up to 50 bars.

(33) As noted above, the thermally expandable thermoplastic microspheres do not fully expand in the heating zone 4 when heated. As the thermally expandable thermoplastic microspheres are transported to an outlet 14 of a distribution pipe 12 the thermally expandable thermoplastic microspheres finally and fully expand when the pressure drops at the outlet 14 since the thermally expandable thermoplastic microspheres reach an area of sufficiently low pressure (such as atmospheric pressure) to facilitate the final expansion.

(34) As shown in FIG. 2 the distribution pipe 12 is attached to the outlet pipe 8. The outlet pipe 8 is attached to the distribution pipe 12 between the inlet 13 and the outlet 14 of the distribution pipe 12. FIG. 2 (panel b) shows a cross-sectional view of FIG. 2 (panel a).

(35) With the set up as shows in FIG. 2, as the expanded thermoplastic microspheres enter the distribution pipe 12, they bounce around in the inner walls of the distribution pipe 12 before leaving the distribution pipe 12 via the outlet 14. It has been found that this leads to less agglomeration of the expanded thermoplastic microspheres. It is thought that this is a result of the expanded thermoplastic microspheres hitting the inner walls of the distribution pipe 12 and by a type of vortex effect that is caused in the distribution pipe 12 by having the inlet 13, which facilitates air flow entering the distribution pipe 12. The air flow entering the distribution pipe 12 facilitates the cooling of the expanded thermoplastic microspheres as they enter the distribution pipe 12.

(36) The outlet pipe 8 may have a constant internal diameter.

(37) The outlet pipe 8 may increases in internal diameter such that an end section to an opening of the outlet pipe 8 has an internal diameter at least twice the internal diameter of the outlet pipe 8. The end section to the opening of the outlet pipe 8 may have an inner diameter up-to six times the internal diameter of the outlet pipe 8.

(38) When the end section to an opening of the outlet pipe 8 has an internal diameter at least twice the internal diameter of the outlet pipe 8, this facilitates a more efficient expansion of the thermally expandable thermoplastic microspheres thermoplastic microspheres. When the end section to an opening of the outlet pipe 8 has an internal diameter at least twice the internal diameter of the outlet pipe 8 this creates a flow restriction of the manufactured expanded thermoplastic microspheres in the outlet pipe 8 to maintain pressure within the heating zone 4. It is observed that when the end section to an opening of the outlet pipe 8 has an internal diameter at least twice the internal diameter of the outlet pipe 8 this allows the thermally expandable thermoplastic microspheres to expand more freely in three dimensions leading to uniformly expanded thermoplastic microspheres of lower density and prevents agglomeration of the expanded thermoplastic microspheres, providing a more uniform (and less dense) density distribution of the expanded thermoplastic microspheres.

(39) Furthermore it has been observed that having the end section to an opening of the outlet pipe 8 with an internal diameter at least twice the internal diameter of the outlet pipe 8, this prevents blockage of the opening of the outlet pipe 8 when the thermally expandable thermoplastic microspheres expand as they come to atmospheric pressure when leaving the outlet pipe 8 and into the distribution pipe 12.

(40) As the expanded thermoplastic microspheres are good heat insulators a risk that the expanded thermoplastic microspheres and in particular the thermoplastic polymer shells stick to each other and form agglomerates is eliminated.

(41) With the set up as shows in FIG. 2, as the expanded thermoplastic microspheres enter the distribution pipe 12, they traverse a direction of flow provided by a cooling media which can be applied via the inlet 13. In this embodiment the distribution pipe 12 allows instantaneous cooling of the expanded thermoplastic microspheres and immediately prevents further expansion and agglomeration of the expanded thermoplastic microspheres. The cooling media is passed from the inlet 13 of the distribution pipe 12 in a flow direction as shown in FIG. 2.

(42) The cooling media can be air, water, nitrogen gas, or any other gasses or liquids, provided they are inert to the expanded thermoplastic microspheres. The cooling media can also be a flow of particles such as chalk particles, calcium carbonate particles, silica particles, clay particles and TiO.sub.2 particles or any combination thereof. The addition of such particles through the inlet 13 of the distribution pipe 12 ensure a homogenous mixture of expanded thermoplastic microspheres and the particles exists as the expanded thermoplastic microspheres traverse a direction of flow provided by inlet 13. This is important when modified expanded thermoplastic microspheres are required in the end application.

(43) The distribution pipe 12 may comprise at least one mixing/separating element 15 or combinations thereof. The at least one mixing/separating element(s) 15 are located within the mixing/separation device 12 downstream from the attachment of the outlet pipe 8 to the distribution pipe 12 as shown in FIG. 2b.

(44) The at least one mixing/separating elements 15 can be selected from static mixers, rotating mixer, rotating knife or sieve or a stream dividing unit.

(45) By having a combination of cooling media and mixing/separating elements 15 it is possible to instantly cool the expanded thermoplastic microspheres and simultaneously provide high energy mixing of the material. The mixing/separation device 12 provides efficient mixing of the cooling media with the expanded thermoplastic microspheres. The flow of the cooling media carries the expanded thermoplastic microspheres through the distribution pipe 12. Enough mechanical energy is thus provided for the distribution pipe 12 to separate the individual expanded thermoplastic microspheres from each other.

(46) In order to further ensure a uniform output and heating of thermally expandable thermoplastic microspheres in the heating zone 4, a pulsation damper 2 may be present. The pulsation damper 2 stabilises a flow of the slurry of thermally expandable thermoplastic microspheres in the apparatus.

(47) The outlet pipe 8 of heating zone 4 is preferably insulated to facilitate maximum expansion of the thermally expandable thermoplastic microspheres.

(48) The outlet pipe 8 of heating zone 4 may be a rigid pipe or a flexible pipe. When in the form of the flexible pipe, this facilitates directing the expanded thermoplastic microspheres to their end use application without moving the entire apparatus.

(49) The apparatus and method as disclosed herein are particularly useful for on-site expansion of the thermally expandable thermoplastic microspheres for water based applications e.g. emulsion explosives, paint, water based coatings, coatings for thermal printing paper and other, porous ceramics, gypsum board, modelling clay, crack fillers, and cementitious compositions. The apparatus and method as disclosed herein are particularly useful for on-site expansion of the thermally expandable thermoplastic microspheres for non-water based applications e.g. polyester putty, artificial wood formulations based on polyester, polyurethane or epoxy, cultured marble based on polyester, underbody coatings, elastomers, sealants, adhesives, phenolic resins, stucco, cable filling compound, and microcellular polyurethane foams. The expanded thermoplastic microspheres exiting the apparatus can be added directly into the production lines of such products. For example, the flow of expanded thermoplastic microspheres can be added, in-line, directly into the emulsion flow during the production of emulsion explosives or directly into the emulsion flow during the filling of a bore hole with emulsion explosives from a truck. In the latter case the explosives can be sensitized at the mining site and be transported unsensitized to the mine.

(50) A control valve 6 within the apparatus can be used to direct flow within the apparatus and to maintain the pressure within the apparatus.

(51) A safety valve 5 can be used in the apparatus prior to the heating zone 4 in order to shut off a flow of the slurry of thermally expandable thermoplastic microspheres to the heating zone 4 and/or to maintain a pressure within the heating zone 4.

(52) The apparatus can be cleaned by replacing the slurry of thermally expandable thermoplastic microspheres with for e.g. water and running the apparatus by manipulating the positions of the safety valve 5, the control valve 6 and the three way valve 9.

(53) The teachings of the present invention enable the expansion of thermally expandable thermoplastic microspheres directly in the apparatus such that the thermally expandable thermoplastic microspheres have a uniform density distribution and are well disperse (i.e. non-agglomerated).

(54) The following non-limiting examples demonstrate the effects of the present invention.

Example 1Expansion with Distribution Pipe

(55) As a control experiment, a slurry of thermally expandable thermoplastic microspheres (Expancel 461WU40) were expanded on an apparatus by a method where an outlet pipe of constant diameter was used without a distribution pipe. The thermally expandable thermoplastic microspheres were expanded by using an apparatus with a single 15 m long copper pipe (heating zone) positioned in a tank filled with hot water maintained at a temperature of 100 C. The copper pipe had a constant inner diameter of 7.8 mm. An aqueous slurry of 20 wt % microspheres was pumped with a diaphragm pump at a rate of 80 liter/hr through the copper pipe. The diaphragm pump generated a pressure of 6 bars. The expanded thermoplastic microspheres exited the copper pipe through the outlet pipe.

(56) As an experiment according to the present invention, thermally expandable thermoplastic microspheres (Expancel 461WU40) were expanded on an apparatus by a method as described above but where a distribution pipe was used attached to the outlet pipe.

(57) With the experiment according to the present invention, it was found that the level of agglomeration was improved by a visual inspection of the expanded material. Furthermore it was found that the temperature of the expanded thermoplastic microspheres was much cooler (65 C.) in a storage bag after 10 mins of expansion compared to the control experiment (90 C.). This is indicative that no further expansion would occur and reduces the risk of agglomeration in bagging, compared to control experiment where a same volume of expanded thermoplastic microspheres was bagged in a same sized storage bag.

Example 2Expansion with Distribution Pipe

(58) A degree of agglomeration (dispersability) can be ranked on a 5 point scale, where 1 is highly agglomerated and 5 is completely free from agglomerates.

(59) A degree of agglomeration was detected by using the following method. The expanded thermoplastic microspheres product is dispersed in Mowilith LDM 1871S binder of viscosity 0.95-1.50 Pas (as measured with a Brookfield sp. 3, 10 rpm) to provide a 5 wt % dispersion. The resulting dispersion is homogenized using a planet mixer (57.5 mm) at 100 rpm for 5 minutes. The homogenized dispersion of the expanded thermoplastic microspheres is applied to a plastic sheet to a 180 m film thickness. The film is dried for 10 minutes. The number of agglomerates was analysed on a 1010 cm area of the film.

(60) As a control experiment, various slurries of Expancel 461WU40 were expanded on an apparatus by a method similar to Example 1 in a heating zone heated by oil at a temperature of 100.5 C. at flow rate of 120 kg slurry per hour. Four slurry concentrations were evaluated with a different dry content of thermally expandable thermoplastic microspheres. The expanded thermoplastic microspheres were produced into a 50 L plastic bag. An outlet pipe of constant diameter was used and no distribution pipe was attached to the outlet pipe.

(61) The resulting agglomerates were analysed on a 1010 cm area of film and results shown in Table 1.

(62) TABLE-US-00001 TABLE 1 Dry content % Dry density (g/L) Dispersability 20 30.8 1 15 27.3 1 10 24.6 1 7.5 23.2 1

(63) As an experiment according to the present invention, various slurries of Expancel 461WU40 were expanded on an apparatus by a method similar to the control experiment in a heating zone heated by oil at a temperature of 100.5 C. at flow rate of 120 kg slurry per hour. Four slurry concentrations were evaluated with a different dry content of thermally expandable thermoplastic microspheres. The expanded thermoplastic microspheres were produced into a 50 L plastic bag. The inlet of the distribution pipe was subjected to a cooling media of pressurised air (5.3 bar).

(64) The resulting agglomerates were analysed on a 1010 cm area of film and results shown in Table 2.

(65) TABLE-US-00002 TABLE 2 Dry content % Dry density (g/L) Dispersability 20 48.5 3 15 43.1 3.5 10 38.0 4 7.5 37.0 5

(66) As can be seen the dispersability is remarkably improved even when the density is higher. What is apparent from the example according to the present invention is that by having a lower dry-contentthe dispersability is improved and the expansion is better (lower density). By cooling the expanding microspheres immediately at the exit from the outlet pipe by air, expansion is prevented. A higher density is achieved compared to when no cooling media is applied.

(67) When combining the distribution pipe and device and cooling media of air expanded thermoplastic microspheres are produced with a much lower degree of agglomeration.

Example 3Outlet Pipe with Increasing Diameter, with Distribution Pipe

(68) An experiment was performed analogously to experiment 2, with slurry having a dry content of thermally expandable thermoplastic microspheres of 10%.

(69) As a control experiment the outlet pipe had a constant inner diameter of 7.8 mm was used with a distribution pipe and a cooling media of pressurized air of 5.3 bar was applied via the inlet.

(70) In a further experiment the outlet pipe was replaced with which widens with an inner diameter from 7.8 mm to 16.0. A distribution pipe and a cooling media of pressurized air of 5.3 bar was applied via the inlet.

(71) The resulting agglomerates were analysed on a 1010 cm area of film and results shown in Table 3.

(72) TABLE-US-00003 TABLE 3 Dry content % Dry density (g/L) Dispersability 10 38.0 4 10 30.1 5

(73) Table 3 shows in the top row; constant pipe diameter before cooling with air and in the bottom row; increasing pipe diameter before cooling with air.

(74) The results clearly demonstrate with the wider outlet pipe thermoplastic microspheres are produced with a much lower density and with a lower degree of agglomeration.