LAMINATED PIPE AND ITS USE

Abstract: A laminated pipe comprising a layer of siloxane-­ crosslinked polyolefin, a layer of a saponified product of ethylene-vinyl acetate copolymer, and a layer of siloxane-­ crosslinked polyolefin or polybutene is disclosed. This pipe is suitable for hot water circulation because of its superior durability and oxygen barrier properties. Heat exchangers, pumps, and other metal units connected to this pipe are protected from corrosion due to dissolved oxygen in hot water.

Description: LAMINATED PIPE AND ITS USE BACKGROUND OF THE INVENTION 1. Field of the Invention: The present invention relates to a pipe, and more particularly it relates to 2 hot water circulating pip for the central heating system, especially the floor heating system. The ? pe 15 superior in durability and permits very little permeation of oxygen, thereby keeping the amount of dissolved oxygen in hot water at an extremely low level and hence causing very little corrosion to metal units such as heat exchangers and pumps connected thereto. 2. Description of the Prior Art: Heretofore, the hot water pipe for floor heating has been mainly of iron or copper. It is usually embedded in the concrete flock laid under the floor, and in most cases its repair after installation is very difficult. Therefore, the pipe is required to have durability over a period as long as 50 years. To meet this requirement, plastic pipes appeared on the marKet because of their man advantages. That is, they are obtained in the continuous form (with no joints), they are completely immune against the leakage fro joints, they need no welding, and they do not corrode. Polyethylene pipes, polypropylene pipes, and polybutene pipes have been commonly used. However, an unexpected fact has recently been found , i.e. that severe corrosion takes place in heat exchangers, pumps, and other metal parts connected to the plastic pipes installed for the floor heating the system of/not water circulating type. It is interesting to note that this corrosion did not occur in conventional systems that employed iron or copper pipes. After this finding, the persons concerned took interest in composite plastic pipes. Unfortunately, those which have been developed so far are not completely suitable for preventing corrosion. A composite polyethylene pipe having an aluminum. interlayer has been one of tne recent developments. .ris pipe nas been developed based on the assumption that oxygen n tne atmosphere permeates through the pipe wall and dissolves in the hot water and the dissolved oxygen causes corrosion. This pipe, however, is not satisfactory because the aluzinum. layer often cracks. (The cause is not renown yet; but the temperature change seems to be a possible cause.) made Conventional pipes/of polyethylene, polypropylene, or other exhibit nave to polyolefins do not/satisfying heat resistance properties, and they usually/ a treatment undergo/radiation crosslinking/for the improvement of heat resistance. The radiation crosslinking is accomplished by irradiation (with electron rays) at a dose of as high as 12 to 2G Mrad so as to achieve a high degree of crosslinking and a high route of crosslinking for increased productivity. Such intense irradiation, which breaks the main chains and deteriorates the polymer, is not applicable to a multilayered pipe an having an interlayer of saponified product of/ethylene-vinyl acetate copolymer (abbreviated as EVOH) which has good properties as an oxygen barrier. a A film, sheet, or tank made of a laminate of/siloxane-crosslinked polyolefin and EVO is disclosed in Japanese Patent Laid-open Nos. 9611/1980 and 93542/1981. However, nothing is disclosedtherein about a laminate composed of outer layers of siloxane-crosslinked polyolefin and an interlayer of EVO and nothing is disclosed about the use of the laminate as a hot water circulating pipe. The two-layered laminate disclosed would not be suitable for such a use because it is poor ir. resistance to hot water and its oxygen barrier properties required to keep the amount of dissclved oxygen in hot water at 2 low level are also poor. SUMMARY OF THE INVENTION 1. Problems tc be solved by the invention: It is an object of the present invention to provide a hot water circulating pipe for the central heating system, particularly of the a floor heating type. The pipe of this invention is of/three-layered structure that can be produced by coextrusion technique. The inner and outer layers are made of a resin that meets the above-menwioned requirements for heat resistance and durability, and the interlayer is made of EVO. The inner and outer layers can be crosslinked to a prescribec degree after molding without adverse effect on the interlayer of EVOH. The pipe of this invention is produced in a continuous form a with no joints. It has/good durability and causes no corrosion to metal units connected to it. 2. Means to solve the problems: The object of this invention is aschieved by a laminated pipe made up of a layer A.) of siloxane-crosslinked polyolefin (having a degree of crosslinklng higher than 55%), a layer (B) of EVOH containing 20 to 60 mol% of ethylene and having a degree of saponification higher than 95%, anc a layer (C) of siloxane-crosslinked polyolefin (having a degree of crctslinking higher than 55%) or polybutene. 3. Effect of the invention: The pipe of this invention permits tne amount of dissolved oxygen in hot water to increase very little wnen it is used for the circulation of hot water. Therefore, the corrosion of metal units such as heat exchangers and pumps connected tc the pipe is minimized. In addition, the pip of nis invention is superior in resistance to heat and hot water, and the EVOH layer effectively protects the siloxane-crosslinked polyethylene layer (inside the EVOH) from oxication degradation. This contributes to the long life time (durability) of the pipe. DESCRIPTION OF THE PREFERRED EMBODIMENTS optionally The siloxane-crosslinked polyolefin constituting the layer (A) or layer (C) of the pipe of this invention has a degree of crosslinking higher than 55%. It It is produce by grafting E silyl group-containing compound having hydrolyzable organic groups onto the polyolefin chain or copolymerizing the compound with an olefin, and then exposing the resulting grafted polymer or copolymer to water in the presence of sllanol condensation catalyst. Specifically speaking, the grafted preferably polymer is/a polyolefin modified with a vinyl silane represented by the formula of R-Si-(OR') {where R is H2C=CH- or EMI5.1 and R' is CH3-, C2H5-, or CH3-O-CH2-CH2-CH2-.) This modified polyolefin may be blended with an unmodified polyolefin resin so that the resulting blend has a degree of crosslinking higher than 55p. . With a degree of crosslinking lower than 55%, a polyolefin with (60 to 950C) a carbon atom number of 2 to 3 does not exhibit adequate heat resistance/ properties anc durability/. An excessively hig aegree of crosslinking decrease tne flexiollity of the polymer. Thus the degree of crosslinking snoulc be higner than 55% and lower than 90 , preferably lower than 85%. The degree of crosslinking as used in this Invention Is defined by he gel fraction in terms of t, which remains undissolved when the polymer is extracted with boiling xylene for 8 hours. The degree of crosslinking should preferably be higher than 65% from the standpoint of improved heat resistance and creep resistance of the polymer. The silyl group-containing compound having hydrolyzable organic groups includes, for example, vinyltrimethoxysilane, vinyltriethoxysilane, vinyltriacetoxysilane, and vinyl-tris (ss-methoxysilane). A process for producing siloxane-crosslinkable polyolefin by copolymerization is disclosed in Japanese Patent Laid-open No. 9611/1980. According to this process, ethylene and a vinylsilane are copolymerized simultaneously or stepwise in a tank reactor or tubular reactor (the former being preferate) in the presence of a radical polymerization initiator (and a chain transfer agent, if necessary), under a pressure of 500 to 4000 kg/cm2, preferably 1000 to 14000 kg/cm2, at a reaction temperature of 100 to 400 C, preferably 150 to 250 C. The reaction system may contain a third monomer such as vinyl acetate, acrylic acid, methacrylic acid, and esters thereof in such an amount that does not impair the heat resistance, creep resistance, and Jurability. a A process for producing/siloxane-crosslinkable polyolefin by grating is disclosed in Japanese Patent Publication Nc. 171/197 According to this process, a polyolefln, a free radical generator, and a -in-silane are fed tc an extrude and extrusion is performed at E cylinder temperature of 180 to 2400C, preferably 200 to 220 C. Preferred examples of the free radical generator include organic peroxides such as dicumyl peroxide and benzoyl peroxide. The copolymerized or grafted polyolefin prepared as mentioned above should contain 0.001 to 15 wt%, preferably 0.01 to 5 wt%, and more preferably 0.1 to 2 wtS of the silane compound. The crosslinking stage is facilitated by the use of a si;anol condensation catalyst which is an organotin compound (such as dibutyltin dilaurate, dibutyltin acetate, dioctyltin diacetate, and dioctyltin dilaurate), cuprous acetate, an acid (such as inorganic acid and fatty acid), and a base (such as ethylamine and dibutylamine). This silanol condensation catalyst should previously be Incorporated into the siloxane-crosslinkable polyolefin In the forti: of E maser batch wit an unmodified polyolefin. The polyolefin to be rendered siloxane-crosslinkable by grafting is an a homopolymer of/a-olefin with 2 to 12 carbon atoms, a random or block an copolymer of &alpha;-olefins, or a copolymer of / &alpha;-olefin and a comonomer such as vinyl acetate and acrylic acid or esters thereof in an amount that is not injurious to the requirements for the floor heating pipe. A high-density polyethylene having a high degree of polymerization is preferred. Another preferred example of the polyolefin is a modified polyolefin formed by grafting z small amount (say, 0.005 to 5 wt%, preferably 0.01 to 2 wt%) of maleic anhydride onto an olefin homopolymer or copolymer. This modified polyolefin, when rendered siloxane-crosslinkable as mentioned abobe, is preferred because of it good adhesion to EVOH which is achieved wtnout loss of creep resistance and heat resistance. preferred is maleic anhyoride-modified high- density polyethylene which is rendered siloxane-crosslinkable. This modified siloxane-crosslinkable polyolefine may be blended with an unmodisied, siloxane-crosslinkable polyolefine. The EVOH used for the layer (B) contains 2C to 60 mol% of ethylene and has a degree of saponification higher than 95%. EVOH containing less than 20 mol% of ethylene shows coo oxygen barrier has properties but /a poor ir. moldability, while EVOH containing more than 60 mcl e of ethylene exhibits a good moldability but shows poor oxygen barrier properties. Thus the ethylene content should preferably be 25 to 55 mol%. An EVOH having a degree of saponification lower than 95% shows poor oxygen barrier properties and is not suitable for this invention. More than two kinds of EVOH, each containing a different amounts of ethylene in the range of 20 to 60 mol , can be used in the blend form. The pipe of this invention is used for circulating hot water at 60 tc 95 C, preferably 60 to 90 C, as mentioned above. This object is best acnievec by a multi-layered pipe including two PVOH layers, the inner layer being made of EVOH containing 40 to 60 mol%, preferably 40 to 55 mol% of ethylene, and the outer layer being made of EVOH containing 20 to 35 mol, preferably 25 to 35 mol% of ethylene. The pipe of this structure is suitable for hot water of higher temperatures. The EVOH constituting each Layer may be a blend of two or more than two kinds of EVOH each containing a different amounts of ethylene. The EVOH used in this invention includes EVOH containing a comonomer suor as propylene (anz other olefins having more ther 3 carbon atoms) and (meth) acrylic acid in such an amount that is not injurious to the oxygen barrier properties, and also silane-modified EVOH which is obtained by copolymerizing ethylene, vinyl acetate, and a vinyl silane (such as vinylmethoxysilane and vinylethoxysilane) and subsequently saponifying the resulting copolymer. in tne preferred embodiments of this invention, the layers (A) and (C) are made of siloxane-crosslin}cable polyolefin and the layer (B) is made of EVO. owever, the layer (C) may be made of polybutene. Polybutene is superior in heat resistance and is also superior in coextrudability with EVOH. The layer of polybutene may be arranged either inside or outside; but the one arranged inside is preferred. Polybutene is a homopolymer of butene-1 or a copolymer or graft copolymer composed of butene-1 as a principal component and a small a a amount of/vinyl monomer (such as ethylene and propylene) or/diolefin or carboxylic acid anhydride as a comonomer. Into the polybutene there may be incorporated a proper thermoplastic polymer (such as polyethylene, a polypropylene, and ethylene-vinyl acetate copolymer) and/thermoplastic elastomer (such as ethylene-propylene rubber and polyisobutylene rubber) in an amount which is not injurious to the performance of the pipe. In addition, into the polybutene there may be incorporated further one or more of the following compounds: a slip agent, antistatic agent, ultraviolet light absorber, antioxidant, crosslinking agent, crosslinking auxiliary agent, metal chelating agent, inorganic powder, and coloring agent. A maleic anhydride rflOcLl ied polybutene is preferred. As explained for the polybutene, both into the siloxane-crosslinlable polyolefin and the EVOH there may be incorporated thermoplastic resins and additives in proper amounts which are not injurious to the performance of the pipe. The pipe of this invention has an outside diameter of 10 to 30 mm and a wall thickness of 1 to 5 mm. It is useful for hot water at 60 to 95 C, preferably 60 to 900C. The thickness of the EVOH layer is in the the range of 15 to 150 vm, depending on the temperature of/hot water. It is preferably the /7C to 120 m when the temperature of/hot water is 60 to 95 C. The oxygen barrier properties of EVOH depend on the water content the in/EVOH, and tney become poor as the water content increases. This holds particularly true for high temperatures. According to this Invention, the EVOTh: layer is an interlayer but its position Is not specifically limited. In preferred embodiments, however, the vVOB layer should be positioned near the external surface rather than at the center within the thickness of the pipe well. This arrangement lowers the steady state water content in the EVOH layer. In other words, the EVOH should be such a way positioned in/that the inequality al/a2 < 1 s Is satisfied, where a, is the thickness of the layer (A) or (C) outside the EVOH layer and a2 is the thickness of the layer (A) or (C) inside the EVOH layer. The ratio of a1 to a2 should preferably be smaller than 0.9, more preferably smaller than 0.8. Because of its oxygen barrier properties, the EVOH layer protects the inside layer from degradation by oxygen. The effect is remarkable the when the temperature of / hot water is high, in which cases degradation is accelerated. If the EVOH layer is too close to the outer surface of the pipe, any damage of the surface that might occur curing installation wold reach the EVOH layer. Therefore, the lower limit of a/a2 should be 0.01. The thickness a1 of the outside layer (A) or (C) should be 0.02 to 1.l mm, preferably 0.03 to 1.3 mm; and the thickness a2 of the inside layer (A) or (C) should be 1.0 to 3.0 mm, preferably 1.2 to 2.9 mm. Into the layers(A), (B), or (C) there may De incorporated an antioxidant (e.g., 3,5-t-butyl-4-hydroxytoluene, Irganox # 1010, and Irganox 1076X. However, the resin layer inside the EVOH needs none an or only a small amount of /antioxidant. where the inside and outside layers are made of the same kind of resin, they should preferably contain the same amount of the antioxidant in order to achieve a convenient coextrusion. (Otherwise, two extruders would be necessary for the individual layers.) Where the pipe composed of three layers (A), (B), and (C) is produced by coextrusion, it is desirable that an adhesive resin layer should be placed between layer (A) and layer (B), or between layer (B) and layer (C). This is not applicable to the case where layer (A) or (C) is made of maleic anhydride-modified polyolefin so that the adhesion between layer (A) or (C) and layer (B) is improved. The adhesive resin is a polyolefin modified with an unsaturated a carboxylic acic or/derivative thereof. Examples of the unsaturated carboxylic acid or derivatives thereof include monobasic acicsanc esters trof (such as acrylic acid, methacrylic acid, and methyl methacrylate) and dibasic acidsor anhydridesthereof (such as maleic acid, fumaric acid, itaconic acid, citraconlc acid, and himic acid). They may be used individually or in combination with one another. Maleic anhydride is preferred. The polyolefin used for the adhesive resin includes polymers of having a of a-olefins / carbon number/2 to 12 (e.g., polyethylene, polypropylene, and polybutene), linear low-density polyethylene (which is a copclymer with a of cf ethylene and a-olefin / carbon number/2 to 12), copolymers of atoms, c-oletin with 2 to 12 carbon / and a copolymerizable vinyl monomer (e.g., vinvl acetate and ethyl acrylate), and siloxane-crosslinked polyolefins(having a degree cf crosslinking higher than 55%). an The above-mentioned polyolefins should be modified with/unsaturated an carboxylic acid or/anhydride thereof so that the amount of chemically bonded modifier in the modified polyolefin is C.005 to 5 wt, preferably 0.01 to 2 wt. A blend of the modified polyolefin and an unmodified polyolefin may be used as the adhesive resin. In this case, the amount of maleic anhyoride in the modified polyolefin should be selected such that the content of chemically bonded maleic anhydride in the blend is 0.005 to 5 wt%, preferably C.01 to 2 w . The thickness of the adhesive resin layer should be 2 to 100 p., and preferably 4 to 60 ijm. Any of the resin layers constituting the pipe may be incorporated with an antioxidant such as 3,5-t-butyl-4-hydroxytoluene (BHT), Irganox 101C, and Irganox # 1076. The Incorporation of an antioxidant into the outside layer is necessary tc extend the life of the pipe. The multi-layerec pipe cf this InventIon can be efficient produced in the continous form by coextrusion from a circular die connected to two or three extruders. At the stage cf coextrusion, the silane-modified polyolefin is not yet crosslinked and it can be easily formed into a pipe. After extrusion, the layer of the silane-modified polyolefin is exposed to water to effect crosslinking. The crosslinking may be accomplished by permitting the green pipe to stand in the atmosphere for a long time so that the silane grafted onto polyolefin reacts wit water vapor in the atmosphere; by immersing the green pipe in hot water or cold water; or by exposing the green pipe to steam. These are all know. metnods. The siloxane-crosslinked polyolefin thus obtained should have a degree of crosslinking higher than 55, preferably higher than 60%. The pipe of this invention is most suitable to be used as a hot water circulating pipe for floor heatings. It may also be used as a pipe for handling various kinds of liquids and gases. Another use is as a parison the fcr/blow molding of bottles. The invention is now described with reference to the following examples, which should not be construed to limit the scope of the invention. EXAMPLE 1 100 parts by weight of high-density polyethylene having a density # of 0.952 g/ml and a melt index of 0.5 g/10 min ("Yukalon / Hard BX-50", a product of Mitsubishi Petrochemical Co., Ltd) was mixed with 2 parts by weg:- of vinyltrimethoxysilane dissolved in acetone and 0.2 parts of dieumy peroxide. The resulting mixture was extruded by 65-mm extruder (L/D : 24) at 23000 into strands, which were subsequently cut Into pellets. Thus there was obtained modified polyethylene onto which is grafted 1.5 t of vinylsilane. The gel fraction of this modified polyethylene is O . Coextrusion for pipe molding was accomplished by the use of three extruders. To the first extruder was fed a blend composed of 100 parts by weight of the above-mentioned modified polyethylene pellets and 5 parts 5 weight of a master batch composed of 100 parts by weight of BX-50 and L parts b we of dibutyltin dilaurate. To the second extruder was fed EVOH containing 31 mol% of ethylene and having 2 degree of saponIfication of 99.3% and a melt index of 1.2 g/10 min (at 190 C a under a load of 216G g). To the third extruder was fed/modified polyethylene ("Admer NF-500", a product of Mitsui Petrochemical Industries, Ltd.) modified with 0.02 wt of maleic anhydride, having a melt index of 1.3 g/10 min (at 1900C under a load of 2160 g). Coextrusion was performed through a five-layer circular die for three extrudates. The die temperature was 230 C. The extruded pipe was cooled with water under reduced pressure. The extrusion rate was 1 m/min. Thus there was obtained a five-layered pipe, 20 mm in outside diameter, which is composed of (A)/(Ad)/(B)/(AD)/(C), wherein (A) is the silane-modified polyethylene layer, (Ad) is the maleic anhydride- modified polyethylene layer, (B) is the EVOH layer, and (C) is the silane-modified polyethylene layer. Steam at 1200C was introduced into the pipe and at the same time the outside of the pipe was exposed to steam at 12000 in order to effect crosslinking. The degree of crosslinking in the layer (A) was 76 . The outside layer (A) was 50 um thick, the inside layer (C) was 1950 m thick, the layer (B) was 98 um, and each of the layers (Ad) was 50 m. Incidentally, the resin for layers (A) and (C) was incorporated with 0.5 t of Irganox 1010. The pipe thus produced was examined for the ability to prevent the increase of dissolved oxygen, by circulating water at 70 C through the pipe which had been depleted of dissolved oxygen b the use of a column filled with metallic ti. The rate of increase of dissolved oxygen in water was measured in tne atmosphere of a relative humidity (RH) of 65E (20 C). The measured value was 3.5 ssg/liter/hour. For comparison, a 2000- m thick pipe made up of the layer (A.) alone was prepared and crosslinking was achieved with steam as mentioned above. The degree of crosslinking was 75%. The rate of increase of dissolved oxygen in water measured for this pipe was 280 g/liter/hour. The rate of increase of dissolved oxygen in water expressed by g/liter/hour is applied to the water in the pipe only, and it is calculated from the equation A = E x (V/v), where A is the rate of increase of dissolved oxygen in water in the pipe, B is the rate of increase cf dissolved oxygen in water in the entire syste. including the pipe, V is the vclume (ml) of water in the entire system including the pipe, and v is the volume (ml) of water in the pipe. EXAMPLE 2 A multi-layered pipe was produced in the same manner as in Example 1 except that high-density polyethylene was replaced by the one having a # melt index of 0.1 g/10min and a density of 0.955 ("Yukalon / Hard BX-70", a product of Mitsubishi Petrochemical Co., Ltd.) and EVOH was replaced by the one containing 40 molZ of ethylene and having a degree of saponification of 99.2% and a melt index of 3.5 g/1C min. The inside and outside layers of the pipe had a degree of crosslinking of 74%. The rate of increase of dissolved oxygen was 5.7 m/liter/hour. For comparison, a 200- m thick pipe made up of crosslinked polyethylene alone was prepared. The rate of increase of dissolved oxygen was 29C g/liter/hour. EXAMPLE 3 A multi-layered pipe was produced in the same manner as in an Example 1 except that EVOH was replaced by a 50:50 blend of/EVOH (X) containing 29 mol% of ethylene and having a degree of saponification of an 99.4% and a melt index of 0.8 g/10 min and/EVOH (Y) containing 45 mol% of ethylene and having degree of saponification of 99.2% and melt index of 4.1 g/10 min. The rate of increase of dissolved oxygen was 6.0 g/liter/hour. EXAMPLE 4 A multi-layered pipe was produced in the same manner as in Example 3 except that tne EVOF was formed in double layers by using two extruders, EVOH (X) being outside and EVOH :; being inside. The inside and outside layers of crosslinked polyethylene were formed so that the thickness ratio a1/a2 was 0.05. The rate of increase of dissolved oxygen was 5.9 g/liter/hour. EXAMPLE 5 A three-layered pipe was produced by coextrusion In the same manner as in Example 1. The adhesive resin (modified polyethylene "Admer NF-500") was not used, and the inside and outside layers were made of high-density polyethylene ("Yukalon # Hard BX-50") onto which is grafted 0.015 wt of maleic anhydride. The adhesion of the EVOH layer to the Inside and outside layers was satisfactory. The degree of crosslinking of the modified high-densfty polyethylene was 78p. The rate of increase of dissolved oxygen was 3.8 g/liter/hour. tcr comparison, a pipe having no EVOH layer was made of said modified high-density polyethylene alone, followed by crosslinking. The rate of increase of dissolved oxygen was 26C g/liter/hour. EXAMPLE 6 Example 1 was repeated except that the matrix of the master batch containing dibutyltln diiaurate was replaced by modified high-density polyethylene onte which 0.3 wt of maleic anhydride is grafted and the amount of the master batch was changed to 10 parts by weight. The adhesion of the EVOH layer to the inside and outside layers was satisfactory for practical use. The rate of increase of dissolved oxygen was 3.0 g/liter/hour. EXAMPLE 7 An ethylene-vinyltrimethoxysilane copolymer was produced by feeding ethylene, vinyltrimethoxysilane, propylene(as a chain transfer agent), and t-butyl-peroxyisobutyrate (as a polymerization initiator at a rate of 43 kg/h, 95 g/h, 450 g/h, and 2 g/h, respectively, to a 1,5-liter stirred autoclave. The polymerization pressure was 2400 kg/cm2 and the polymerization temperature was 220 C. The conversion of ethylene was 15. The resulting copolymer was found to have a melt index of 1.0 g/10 min (measured according to JIS K6760) and to contain C.7 wt% of vinylsilane. a This copolymer was blended with 5 wt% of/master batch containing 1 wt% of dibutyltin dilaurate. The resulting blend was used as the crosslinkable polyethylene for producIng a pipe in the same manner as in Example 1. After crosslinking, the polyethylene of the inside and outside layers had a degree of crosslinking of 72%. The rate of increase of dissolved oxygen was 3.9 g/liter/hour. EXAMPLE 8 Copolymerization was performed in the same manner as in Example 7 except that the feed rate of vinyltrimethoxysilane changed to 190 g/h. The conversion of ethylene was 15%. The resulting copolymer was found to have a melt inoex of 1.0 g/10 min and to contain 1.8 wt of vinylsilane. A pipe composed of inside and outside layers of crosslinkable polyethylene and an interlayer of EVOH was produced in the same manner as in Example 1. The degree of crosslinking of the inside and outside avers was 80%. The rate of increase of dissclvea oxygen was 3.7 /liter/hour. COMPARATIVE EXAMPLE 1 A three-layered pipe, 20 an in outside diameter, was produced by coextrusion from a three-layer circular die for three extrudates. The outside layer (A) was mad of vinylsilane-modified polyethylene containing dibutyltin dilaurate. The interlayer (Ad) was made of maleic anhydride-modified polyethylene. The inside layer (B) was made of EVOH. These raw materials are the same as those used in Example i. The thus produced pipe was exposed to steam at 1200C to effect crosslinking. The degree of crosslinking in the layer (A) was 66%. The thicknesses of the layers (A), (Ad), and (B) 2000 m, 50 m, and 105 m, respectively. Each of the resins used was incorporated wit 0.5 wt% of Irganox 1010. outer circulation of hot water (85 C) for several days, the surface of the EVOH layer lost luster and became irregular and the FVOr, layer partly peelec off. The rate of increase of dissolved oxygen was 250 g/liter/hour. EXAMPLE 9 The coposite pipe produced in Example 1 was embedded in the floor for floor heating of six rooms. The length of the pipe per room was 80 meters. The heating system was run for six months, with an iron test piece (10 cm square and 0.1 mm thick) placed in the hot water circulating tank. At the end of the period, the test piece was examined. The surface or the test piece was smooth although covered with brown rust. The rust was easily removed by a ie brush and the metal surface appeared again. The weight loss of the test piece was 0.2%. For comparison, a pipe composed of layer (A) alone (200C m thick) was installed and tested in the same manner as mentioned above. The test piece at the end of the perioc had an irregular surface with 1 to 1.5 mm thick rust. The rust, which partly penetrated the test piece, was not easily removed by a wire brush. The weight loss measured after the removal of rust was 35%. EXAMPLE 10 A five-layered pipe of the following construction, 20 mm in outside dlameter, was produced by coextrusion from a five-layer circular die for four extrudates. Outside layer (A) of vinylsilane-modified high-density polyethylene containing dibutyltin dilaurate / layer (Ad) of maleic anhydride-modified polyethylene / layer (E) cf EVO ' aver (Ad) of maleic anhydride-modified polyethylene / inside layer (C) of polybutene-1 ("WITRON" R made by Adeka-Argus Co., Ltd.). The raw materials other than polybutene-1 are the same as those used in Example 1. The thus produced pipe was exposed to steam at 120 C to effect crosslinking. The degree of crosslinking in the layer (A) was 75%. The thicknesses of the layers (A), (Ad), (B0, (Ad), and (C) was 50 vm, 50 pm, 98 m, 50 m, and 1950 m, respectively. The rate of increase of dissolved oxygen was 3.8 g/liter/hour. EXAMPLE 11 A three-layered pipe of tne following construction, 2C mm in outside diameter, was produced by coextrusion. Outside layer (A) of vinylsilane-modified, maleic anhydride-grafted (0.015 wt%) hign-density polyethylene containing dibutyltin dilaurate / layer (B) of EVOH / inside layer (C) of maleic anhydride-grafted (0.018 wt%) polybutene-1. The adhesion of the outside and inside layers to the EVOH layer was satisfactory for practical use. The degree of crosslinking in the layer (A) was 76%. The thicknesses of the layers (A), (B), and (C)was 50 vm, 98 m, and 1950 m, respectively. The rate of increase of dissolved oxygen was 3.9 g/liter/hour.

Claims: WHAT IS CLAIMED IS: 1. A laminated pipe comprising a layer (A) of siloxane-crosslinked polyolefin (having a degree of crosslinking higher than 55), a layer an (B) of z saponified product of/ethylene-vinyl acetate copolymer containing 2C to 60 molA of ethylene and having a degree of saponifica a tion higher than 95%, and a layer (C) of/siloxane-crosslinked polyolefin of a (having a degree of crosslinking higner than 55%) or/polybutene. 2. A laminated pipe as claimed in Claim 1, wherein the layer (C) is made of siloxane-crosslinked polyolefin (having a degree of grosslinking higner than 55%). 3. A laminated pipe as claimed in Claim 1, wherein the layer (A) is the outside layer ant the layer (C) is the inside layer. A laminated pipe as claimed in Claim 1, wherein the layer (C) is the outside layer and the layer (A.) is the inside layer. 5. A laminated pipe as caimec in Claim 1, wherein the ratio of the thickness of the outsice layer to the thickness of the inside layer is smaller than 1 and not smaller than 0.01. 6. A laminated pipe as claimed in Claim 1, wherein the siloxanecrosslinked polyolefin has a degree of crosslinking higner than 65%. 7. A laminated pipe as claimed in Claim 1, wherein the siloxanecrosslinked polyolefin is siloxane-crosslinked polyethylene. 8. A laminated pipe as claimed in Claim 1, wherein the siloxanecrosslinked polyolefin is siloxane-crosslinked, maleic anhydridemodified polyolefin. 9. h laminated pipe as claimed In Claim 1, wherein the polybutene is a maleic anhydride-modified polybutene. 10. Use of a laminated pipe as claimed in any of Claims 1 to 9 for hot water circulation in heating systems. 11. Use of a laminated pipe as claimed in any of Claims 1 to 9 for floor heating by hot water circulation.

Inventors: IKARI, KYOICHIRO, NEGI, TAICHI, OKAYA, TAKUJI, SATOH, KENJI
Applicants: KURARAY CO., LTD.
Application year: 1985
Main classification: B32B27
IPC codes: F16L9, B32B1, B32B27