JP2018172600A - Foam pipe joint and method for producing same - Google Patents

Foam pipe joint and method for producing same Download PDF

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JP2018172600A
JP2018172600A JP2017072961A JP2017072961A JP2018172600A JP 2018172600 A JP2018172600 A JP 2018172600A JP 2017072961 A JP2017072961 A JP 2017072961A JP 2017072961 A JP2017072961 A JP 2017072961A JP 2018172600 A JP2018172600 A JP 2018172600A
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main body
center
pipe joint
thickness
opening
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JP6943597B2 (en
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大樹 久宿
Daiki Hisashuku
大樹 久宿
保 松永
Tamotsu Matsunaga
保 松永
久保 喜弘
Yoshihiro Kubo
喜弘 久保
豊正 松村
Toyomasa Matsumura
豊正 松村
由之介 野口
Yoshinosuke Noguchi
由之介 野口
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Sekisui Chemical Co Ltd
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Sekisui Chemical Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a foam pipe joint that is excellent in chemical resistance and impact resistance.SOLUTION: Provided is a foam pipe joint 1 formed by foaming and shaping a foamable resin composition containing a vinyl chloride resin and a foaming agent, and is characterized in: having a main body part 10 having a flow path inside and a socket part 12 formed integrally with the opening part 11 of the main body part 10, and in which (the thickness at the center of the socket part)/(the thickness at the center of the main body part) is 0.3 to 0.7, the expansion ratio at the center of the main body part is 1.2 to 2.5 folds, and the expansion ratio at the opening end part of the socket part 12 is 1.2 to 1.5 folds.SELECTED DRAWING: Figure 2

Description

本発明は発泡管継手およびその製造方法に関する。   The present invention relates to a foamed pipe joint and a method for manufacturing the same.

従来、鋼管や合成樹脂管からなる配管周りをグラスウール等の保温材で被覆することによって配管周りの結露等を防止するのが一般的である。
しかし、上記従来の方法では、配管の作業とは別に、保温材を巻いたり被せたりする作業が必要であるため作業効率が悪く、狭い作業スペースでは作業を行えない場合もある。
そこで、断熱層となる発泡層を有する樹脂製の配管や管継手が提案されている。断熱層を設けることにより、配管施工後に保温材で被覆しなくても結露の防止が可能となる。
一般的な管継手にあっては、流路となる本体部の開口部に、本体部の開口部よりも内径が大きい受口部が一体的に設けられており、この受口部に他の管部材が挿入されるようになっている。
Conventionally, it is common to prevent condensation around the pipe by covering the pipe made of a steel pipe or a synthetic resin pipe with a heat insulating material such as glass wool.
However, the above-described conventional method requires a work for winding or covering the heat insulating material separately from the work of the piping, so that the work efficiency is low and the work may not be performed in a narrow work space.
Therefore, resin-made piping and pipe joints having a foam layer serving as a heat insulating layer have been proposed. By providing the heat insulating layer, it is possible to prevent dew condensation without covering with a heat insulating material after pipe construction.
In general pipe joints, a receiving portion having an inner diameter larger than the opening of the main body is integrally provided at the opening of the main body serving as a flow path. A tube member is inserted.

特許文献1には、本体部の内部に発泡樹脂からなる断熱層を備える発泡管継手が提案されている。特許文献1には、管継手の製造に使用できる樹脂として、ポリ塩化ビニル、ABS樹脂、ポリエチレン、ポリプロピレン等が挙げられており、現行品では、耐衝撃性、耐熱性に優れるABS樹脂が使用されている。   Patent Document 1 proposes a foamed pipe joint including a heat insulating layer made of foamed resin inside a main body. Patent Document 1 lists polyvinyl chloride, ABS resin, polyethylene, polypropylene, and the like as resins that can be used in the manufacture of pipe joints. In the current product, ABS resin having excellent impact resistance and heat resistance is used. ing.

特許第3699579号公報Japanese Patent No. 3699579

近年、発泡管継手の用途も広がり、例えば、耐薬品性に優れる管継手のニーズがある。
塩化ビニル樹脂は耐薬品性に優れるが、現行のABS樹脂に比べると耐衝撃性が劣る。
本発明は、耐薬品性および耐衝撃性に優れる発泡管継手およびその製造方法の提供を目的とする。
In recent years, the use of foamed pipe joints has expanded, for example, there is a need for pipe joints having excellent chemical resistance.
Vinyl chloride resin is excellent in chemical resistance, but is inferior in impact resistance compared to the current ABS resin.
An object of this invention is to provide the foamed pipe joint excellent in chemical resistance and impact resistance, and its manufacturing method.

本発明は以下の態様を有する。
[1] 塩化ビニル樹脂と発泡剤とを含む発泡性樹脂組成物を、発泡・成形してなる発泡管継手であって、内部に流路を有する本体部と、該本体部の開口部に一体に形成された受口部とを有し、(受口部中央の厚さ)/(本体部中央の厚さ)の比が0.3〜0.7であり、本体部中央における発泡倍率が1.2〜2.5倍であり、かつ受口部の開口端部における発泡倍率が1.2〜1.5倍である、ことを特徴とする発泡管継手。
[2] 前記[1]の発泡管継手の製造方法であって、塩化ビニル樹脂と発泡剤とを含む発泡性樹脂組成物を射出成形する、発泡管継手の製造方法。
The present invention has the following aspects.
[1] A foamed pipe joint obtained by foaming and molding a foamable resin composition containing a vinyl chloride resin and a foaming agent, and a main body having a flow path therein and an opening of the main body The ratio of (thickness of the center of the mouthpiece) / (thickness of the center of the main body) is 0.3 to 0.7, and the expansion ratio at the center of the main body is A foamed pipe joint characterized by being 1.2 to 2.5 times and having a foaming ratio of 1.2 to 1.5 times at the open end of the receiving part.
[2] The method for producing a foamed pipe joint according to [1], wherein a foamable resin composition containing a vinyl chloride resin and a foaming agent is injection-molded.

本発明によれば、耐薬品性および耐衝撃性に優れる発泡管継手が得られる。   According to the present invention, a foamed pipe joint having excellent chemical resistance and impact resistance can be obtained.

本発明の一実施形態に係る発泡管継手を示す側面図である。It is a side view which shows the foaming pipe joint which concerns on one Embodiment of this invention. 図1に示す発泡管継手の縦断面図である。It is a longitudinal cross-sectional view of the foamed pipe joint shown in FIG. 図1に示すA−A線断面図である。It is the sectional view on the AA line shown in FIG.

以下、本発明の実施の形態による発泡管継手について、図面に基づいて説明する。
図1に示すように、本実施形態の発泡管継手1は、例えばドレンパイプの接続に使用されるチーズ型(ティー型)管継手である。
発泡管継手1は、第1の管軸O1と、第2の管軸O2を有する。二つの管軸O1及びO2は直線状であり互いに直交する。
発泡管継手1は、内部に流路(例えばドレンの流路)を有する管状の本体部10と、この本体部10の三つの開口部11にそれぞれ一体に形成された受口部12を有する。発泡管継手1は、本体部10と受口部12とが一体的に形成された発泡樹脂層からなる。
受口部12には、本体部10の開口部11の内径とほぼ同内径の管部材(例えばドレンパイプ)が挿入される。受口部12の開口部の内径D2は、本体部10の開口部11の内径D1より大きい。
Hereinafter, a foamed pipe joint according to an embodiment of the present invention will be described with reference to the drawings.
As shown in FIG. 1, the foamed pipe joint 1 of this embodiment is a cheese type (tee type) pipe joint used for connection of a drain pipe, for example.
The foamed pipe joint 1 has a first pipe axis O1 and a second pipe axis O2. The two tube axes O1 and O2 are linear and orthogonal to each other.
The foamed pipe joint 1 includes a tubular main body portion 10 having a flow path (for example, a drain flow path) therein, and a receiving portion 12 formed integrally with each of the three openings 11 of the main body portion 10. The foamed pipe joint 1 is composed of a foamed resin layer in which a main body 10 and a receiving port 12 are integrally formed.
A tube member (for example, a drain pipe) having substantially the same inner diameter as the inner diameter of the opening portion 11 of the main body portion 10 is inserted into the receiving portion 12. The inner diameter D <b> 2 of the opening of the receiving portion 12 is larger than the inner diameter D <b> 1 of the opening 11 of the main body 10.

以下、本体部10の三つの開口部11のうち、二つは第1の管軸O1と同軸の円形である。第1の管軸O1の一端側の開口部を第1の本体開口部11a、他端側の開口部を第2の本体開口部11bということもある。残りの一つは第2の管軸O2と同軸の円形であり、第3の本体開口部11cということもある。
また、三つの受口部12のうち、二つは第1の管軸O1と同軸の管状である。第1の管軸O1の一端側の受口部を第1の受口部12A、他端側の受口部を第2の受口部12Bということもある。残りの一つは第2の管軸O2と同軸の管状であり、第3の受口部12Cということもある。
本体部10の表面上であって、第1〜3の受口部12A〜12Cの、各開口部12bからの距離が最も遠い位置に、成形時に射出される位置となる射出ゲート部14が設けられている。
Hereinafter, two of the three openings 11 of the main body 10 have a circular shape coaxial with the first tube axis O1. The opening on one end side of the first tube axis O1 may be referred to as a first main body opening 11a, and the opening on the other end may be referred to as a second main body opening 11b. The remaining one has a circular shape coaxial with the second tube axis O2, and may be referred to as a third main body opening 11c.
Of the three receiving ports 12, two are tubular and coaxial with the first tube axis O1. The receiving portion on one end side of the first tube axis O1 may be referred to as a first receiving portion 12A, and the receiving portion on the other end side may be referred to as a second receiving portion 12B. The remaining one has a tubular shape coaxial with the second tube axis O2, and may be referred to as a third receiving portion 12C.
On the surface of the main body 10, an injection gate portion 14 is provided at a position where the distance from each opening 12 b of the first to third receiving portions 12 </ b> A to 12 </ b> C is farthest from that at the time of molding. It has been.

図2に示すように、受口部12の内面は、開口部12bから内方に向かって漸次縮径するテーパ部12aと、テーパ部12aの本体部10側の端部から、本体部10の開口部11に達するまで、さらに漸次縮径する段部13を有する。段部13は、受口部12に挿入された管部材の先端面が突き当たるストッパーとしての役割を果たす。   As shown in FIG. 2, the inner surface of the receiving portion 12 has a tapered portion 12 a that gradually decreases inward from the opening portion 12 b and an end portion of the tapered portion 12 a on the main body portion 10 side from the end portion of the main body portion 10. Until the opening 11 is reached, the stepped portion 13 is further gradually reduced in diameter. The step portion 13 serves as a stopper against which the distal end surface of the pipe member inserted into the receiving portion 12 abuts.

発泡管継手1は、塩化ビニル樹脂と発泡剤とを含む発泡性樹脂組成物を、発泡・成形して形成される。本発明の発泡管継手の製造方法は発泡性樹脂組成物を射出成形する方法である。
具体的には、発泡性樹脂組成物を射出成形機に供給し、加熱して塩化ビニル樹脂を溶融し、金型内に射出し、冷却して所望の形状に成形する。発泡性樹脂組成物中の発泡剤は、加熱によって分解されガスを発生し、溶融した塩化ビニル樹脂中に独立気泡が形成される。こうして得られる発泡管継手は、全体が発泡樹脂層からなる。
成形時に射出される位置となる射出ゲート部14は、金型全体に発泡性樹脂組成物を充填できる位置であればよく、特に限定されない。本実施形態では、本体部10の表面上において、第1〜3の受口部12A〜12Cの各開口部12bからの距離が最も遠い位置に射出ゲート部14が設けられている。
金型の温度は、射出直前の発泡性樹脂組成物の温度よりも低く、射出された発泡性樹脂組成物は金型内を流動する間に温度が低下する。例えば、射出される直前の発泡性樹脂組成物の温度(成形温度)は150〜190℃が好ましく、160〜180℃がより好ましい。また発泡性樹脂組成物が射出される直前の金型の温度は20〜100℃が好ましく、30〜80℃がより好ましい。
発泡性樹脂組成物については後述する。
The foamed pipe joint 1 is formed by foaming and molding a foamable resin composition containing a vinyl chloride resin and a foaming agent. The method for producing a foamed pipe joint of the present invention is a method for injection molding a foamable resin composition.
Specifically, the foamable resin composition is supplied to an injection molding machine, heated to melt the vinyl chloride resin, injected into a mold, and cooled to be molded into a desired shape. The foaming agent in the foamable resin composition is decomposed by heating to generate gas, and closed cells are formed in the melted vinyl chloride resin. The foamed pipe joint obtained in this way consists entirely of a foamed resin layer.
The injection gate portion 14 that is a position to be injected at the time of molding is not particularly limited as long as it is a position where the entire mold can be filled with the foamable resin composition. In the present embodiment, the injection gate portion 14 is provided on the surface of the main body portion 10 at a position where the distances from the opening portions 12b of the first to third receiving port portions 12A to 12C are farthest.
The temperature of the mold is lower than the temperature of the expandable resin composition immediately before injection, and the temperature of the injected expandable resin composition decreases while flowing in the mold. For example, the temperature (molding temperature) of the foamable resin composition immediately before being injected is preferably 150 to 190 ° C, and more preferably 160 to 180 ° C. Moreover, 20-100 degreeC is preferable and, as for the temperature of the metal mold | die just before a foamable resin composition is inject | emitted, 30-80 degreeC is more preferable.
The foamable resin composition will be described later.

発泡管継手1は、(受口部中央の厚さ)/(本体部中央の厚さ)の比が0.3〜0.7である。
本発明において、最も長い管軸(本実施形態では第1の管軸O1)上の点であって、該管軸の一端側の開口部(第1の本体開口部11a)および他端側の開口部(第2の本体開口部11b)から等距離にある点P1を通り、該管軸に垂直な面で、本体部10を切断して得られる断面を本体部中央の断面とする。本実施形態では、図3に示す断面のうち、符号Rで示す部分が本体部中央の断面である。
本体部中央の断面における本体部10(射出ゲート部は除く)の厚さT1を本体部中央の厚さとする。本体部中央の断面において、本体部10の厚さT1が均一でない場合は、最も厚い箇所における厚さを本体部中央の厚さとする。
本発明において、受口部12の管軸上の点であって、受口部12の開口部12bおよび本体部10の開口部11から等距離にある点P2を通り、該管軸に垂直な面で、受口部12を切断して得られる断面を受口部中央の断面とする。受口部中央の断面における受口部12の厚さT2を受口部中央の厚さとする。受口部中央の断面において、受口部12の厚さT2が均一でない場合は、最も厚い箇所における厚さを受口部中央の厚さとする。
発泡管継手1を構成する複数の受口部12の全部において、それぞれの(受口部中央の厚さ)/(本体部中央の厚さ)の比が上記の範囲内であればよい。
In the foamed pipe joint 1, the ratio of (thickness at the center of the receiving port) / (thickness at the center of the main body) is 0.3 to 0.7.
In the present invention, it is a point on the longest tube axis (first tube axis O1 in the present embodiment), which is an opening on the one end side of the tube axis (first main body opening 11a) and the other end side. A cross section obtained by cutting the main body portion 10 along a plane perpendicular to the tube axis passing through the point P1 that is equidistant from the opening portion (second main body opening portion 11b) is a cross section at the center of the main body portion. In the present embodiment, of the cross section shown in FIG. 3, the portion indicated by the symbol R is a cross section at the center of the main body.
The thickness T1 of the main body 10 (excluding the injection gate) in the cross section at the center of the main body is defined as the thickness of the main body. In the cross section at the center of the main body, when the thickness T1 of the main body 10 is not uniform, the thickness at the thickest portion is the thickness at the center of the main body.
In the present invention, a point on the tube axis of the receiving port 12, which passes through a point P 2 that is equidistant from the opening 12 b of the receiving port 12 and the opening 11 of the main body 10, is perpendicular to the tube axis. The cross section obtained by cutting the receiving part 12 on the surface is taken as the cross section at the center of the receiving part. The thickness T2 of the receiving portion 12 in the cross section at the center of the receiving portion is defined as the thickness at the center of the receiving portion. When the thickness T2 of the receiving port 12 is not uniform in the cross-section at the center of the receiving port, the thickness at the thickest portion is set as the thickness of the receiving port.
The ratio of (thickness at the center of the receiving port) / (thickness at the center of the main body) may be within the above range in all of the plurality of receiving ports 12 constituting the foamed pipe joint 1.

本発明では、(受口部中央の厚さ)/(本体部中央の厚さ)の比を上記範囲の下限値より大きくすることによって、本体部の発泡倍率を高くすることができる。その結果、発泡管継手1全体が軽量化され、耐衝撃性が向上する。
本体部の発泡倍率が高くなる理由は以下のように考えられる。発泡管継手1を射出成形により製造する際、射出ゲート部14から射出された発泡性樹脂組成物は金型内を流動し、金型内の空間に充填されながら、ガスを発生して発泡する。射出ゲート部14の位置にかかわらず、発泡性樹脂組成物の一部は、本体部10に対応する空間を通って、受口部12に対応する空間に流入する。このとき、本体部10よりも受口部12の方が管壁の厚さが小さいため、発泡性樹脂組成物の流路が狭くなり、本体部10に対応する空間内の発泡性樹脂組成物に圧力が加わり、該圧力が大きいと、本体部の発泡倍率が低下する。
本発明において(受口部中央の厚さ)/(本体部中央の厚さ)が1に近いほど、本体部10から受口部12にかけて発泡性樹脂組成物の流路の大きさの変化が小さくなるため、本体部10に対応する空間内の発泡性樹脂組成物にかかる圧力が緩和され、発泡倍率が高くなると考えられる。
一方、(受口部中央の厚さ)/(本体部中央の厚さ)の比が上記範囲の上限値を超えると、受口部12に対応する空間の隅々にまで発泡性樹脂組成物を充填するための圧力が不足して、受口部12の成形不良が生じやすい。
(受口部中央の厚さ)/(本体部中央の厚さ)の比は0.3〜0.7が好ましく、0.4〜0.6がより好ましい。
本体部中央の厚さT1は、例えば6〜12mmが好ましく、8〜10mmがより好ましい。
受口部中央の厚さT2は、例えば2〜8mmが好ましく、4〜5mmがより好ましい。
In the present invention, the foaming ratio of the main body can be increased by increasing the ratio of (thickness at the center of the receiving port) / (thickness at the center of the main body) above the lower limit of the above range. As a result, the entire foamed pipe joint 1 is reduced in weight and the impact resistance is improved.
The reason why the expansion ratio of the main body is high is considered as follows. When the foamed pipe joint 1 is manufactured by injection molding, the foamable resin composition injected from the injection gate portion 14 flows in the mold and generates gas and foams while filling the space in the mold. . Regardless of the position of the injection gate part 14, a part of the foamable resin composition flows into the space corresponding to the receiving part 12 through the space corresponding to the main body part 10. At this time, since the thickness of the tube wall of the receiving portion 12 is smaller than that of the main body portion 10, the flow path of the foamable resin composition becomes narrow, and the foamable resin composition in the space corresponding to the main body portion 10. When pressure is applied to the main body, and the pressure is large, the expansion ratio of the main body portion is reduced.
In the present invention, the closer the (thickness at the center of the receiving port) / (thickness at the center of the main body) is to 1, the more the change in the size of the flow path of the foamable resin composition from the main body 10 to the receiving port 12 occurs. Since it becomes small, the pressure concerning the foamable resin composition in the space corresponding to the main-body part 10 is relieved, and it is thought that a foaming ratio becomes high.
On the other hand, if the ratio of (thickness at the center of the receiving port) / (thickness at the center of the main body) exceeds the upper limit of the above range, the foamable resin composition extends to every corner of the space corresponding to the receiving port 12. Insufficient pressure to fill the inlet portion 12 tends to cause molding failure of the receiving portion 12.
The ratio of (thickness at the center of the opening) / (thickness at the center of the main body) is preferably 0.3 to 0.7, and more preferably 0.4 to 0.6.
For example, the thickness T1 at the center of the main body is preferably 6 to 12 mm, and more preferably 8 to 10 mm.
The thickness T2 at the center of the opening is preferably 2 to 8 mm, for example, and more preferably 4 to 5 mm.

発泡管継手1は、受口部の開口端部における発泡倍率が1.2〜1.5倍である。
受口部の開口端部における発泡倍率は、受口部の開口部12bの端面を含む厚さ1〜2mmの円環状のサンプルを切り出し、その比重(x)を測定し、発泡させなかった時の樹脂の比重を、サンプルの比重(x)で除して求められる値である。
具体的には、「発泡倍率=発泡させなかった時の樹脂の比重/x」を開口端部における発泡倍率の値とする。発泡させなかった時の樹脂の比重は、上記サンプルを溶融したものから測定できる。
比重は、JIS 7122に従い、23℃±2℃で水置換式比重測定器を用いて測定する。
受口部の開口端部における発泡倍率が1.0倍に近いほど、開口部の強度は高くなり、耐衝撃性が向上する。
受口部の開口端部における発泡倍率が上記範囲の下限値以上であると断熱性能に優れ、上限値以下であると耐衝撃性に優れる。
複数の受口部において、開口端部における発泡倍率が互いに異なる場合は、最も大きい値が上記の範囲内であればよい。
The foaming pipe joint 1 has a foaming ratio of 1.2 to 1.5 times at the opening end of the receiving part.
The foaming magnification at the opening end of the receiving portion is determined by cutting an annular sample having a thickness of 1 to 2 mm including the end face of the opening 12b of the receiving portion, measuring its specific gravity (x), and not foaming. This is a value obtained by dividing the specific gravity of the resin by the specific gravity (x) of the sample.
Specifically, “foaming ratio = specific gravity of resin when not foamed / x” is set as the value of the foaming ratio at the opening end. The specific gravity of the resin when not foamed can be measured from the melted sample.
The specific gravity is measured according to JIS 7122 at 23 ° C. ± 2 ° C. using a water displacement specific gravity measuring instrument.
The closer the foaming magnification at the opening end of the receiving portion is to 1.0 times, the higher the strength of the opening and the better the impact resistance.
When the expansion ratio at the opening end of the receiving portion is not less than the lower limit of the above range, the heat insulating performance is excellent, and when it is not more than the upper limit, the impact resistance is excellent.
In the plurality of receiving portions, when the expansion ratios at the opening end portions are different from each other, the largest value may be within the above range.

本実施形態では、第1〜3の受口部12A〜12Cの各開口部12bからの距離が最も遠い位置に、射出ゲート部14が設けられているため、射出された発泡性樹脂組成物が、金型内の空間を流動して開口部12bに到達したときの、発泡性樹脂組成物の温度がより低くなりやすい。開口端部に充填された発泡性樹脂組成物の温度が低いほど、開口端部の発泡倍率が低くなりやすい。
また、本実施形態では、受口部12の内面がテーパ部12aを有し、受口部12の管壁の厚さが開口部12bに向かって小さくなっている。すなわち、金型内の受口部12に対応する空間が開口部12bに向かって狭くなっている。開口端部に対応する空間が狭いほど、開口端部の発泡倍率が低くなりやすい。
受口部12のテーパ部12aと、受口部12の外面とのなす角度θ(以下、テーパ角度θともいう)は、例えば0.05〜1.5°が好ましく、0.07〜1.2°がより好ましく、0.09〜1.18°が最も好ましい。
開口部12bにおける受口部12の厚さT3は、薄すぎると受口部12の開口部12bが衝撃を受けたときに欠けが生じすい。該厚さT3は、例えば2〜8mmが好ましく、4〜5mmがより好ましい。
In this embodiment, since the injection gate part 14 is provided in the position where the distance from each opening part 12b of the 1st-3rd receiving part 12A-12C is the furthest, the injected foamed resin composition is The temperature of the foamable resin composition tends to be lower when it flows through the space in the mold and reaches the opening 12b. The lower the temperature of the foamable resin composition filled in the opening end, the lower the expansion ratio of the opening end.
In the present embodiment, the inner surface of the receiving portion 12 has a tapered portion 12a, and the thickness of the tube wall of the receiving portion 12 decreases toward the opening portion 12b. That is, the space corresponding to the receiving port 12 in the mold is narrowed toward the opening 12b. The narrower the space corresponding to the opening end, the lower the expansion ratio of the opening end.
The angle θ (hereinafter also referred to as taper angle θ) formed by the tapered portion 12a of the receiving portion 12 and the outer surface of the receiving portion 12 is preferably 0.05 to 1.5 °, for example, 0.07 to 1. 2 ° is more preferable, and 0.09 to 1.18 ° is most preferable.
If the thickness T3 of the receiving portion 12 in the opening 12b is too thin, the opening 12b of the receiving portion 12 is hardly chipped when subjected to an impact. The thickness T3 is preferably 2 to 8 mm, for example, and more preferably 4 to 5 mm.

発泡管継手1は、本体部中央における発泡倍率が1.2〜2.5倍であることが好ましく、1.3〜2.5倍がより好ましく、1.5〜2.2倍が最も好ましい。
本体部中央における発泡倍率は、本体部中央の断面を含む厚さ1〜2mmのサンプルを切り出し、その比重値(y)を測定し、発泡させなかった時の樹脂の比重を、サンプルの比重(y)で除して求められる値である。
具体的には、「発泡倍率=発泡させなかった時の樹脂の比重/y」を本体部中央における発泡倍率の値とする。
比重は、JIS 7122に従い、23℃±2℃で水置換式比重測定器を用いて測定する。
本体部中央における発泡倍率が上記範囲の下限値以上であると断熱性能に優れ、上限値以下であると耐衝撃性に優れる。
本体部中央における発泡倍率は、例えば成形温度、製品肉厚、配合組成によって調整することができる。
The expansion ratio of the foamed pipe joint 1 at the center of the main body is preferably 1.2 to 2.5 times, more preferably 1.3 to 2.5 times, and most preferably 1.5 to 2.2 times. .
The foaming magnification at the center of the main body is obtained by cutting out a sample having a thickness of 1 to 2 mm including the cross section at the center of the main body, measuring the specific gravity value (y), and determining the specific gravity of the resin when not foamed by the specific gravity of the sample ( The value obtained by dividing by y).
Specifically, “foaming ratio = specific gravity of resin when not foamed / y” is set as the value of the foaming ratio at the center of the main body.
The specific gravity is measured according to JIS 7122 at 23 ° C. ± 2 ° C. using a water displacement specific gravity measuring instrument.
When the expansion ratio at the center of the main body is not less than the lower limit of the above range, the heat insulating performance is excellent, and when it is not more than the upper limit, the impact resistance is excellent.
The expansion ratio at the center of the main body can be adjusted by, for example, molding temperature, product thickness, and composition.

<発泡性樹脂組成物>
発泡性樹脂組成物は、塩化ビニル樹脂と発泡剤とを含む。
塩化ビニル樹脂は、管継手の材料として公知の硬質塩化ビニル樹脂を用いることができる。硬質塩化ビニル樹脂とは、可塑剤を実質的に含まない塩化ビニル樹脂である。
塩化ビニル樹脂は、塩化ビニル単量体の単独重合体でもよいし、塩化ビニル単量体と、該塩化ビニル単量体と共重合可能な他の単量体との共重合体であってもよい。
上記塩化ビニル単量体と共重合可能な他の単量体としては、例えば、エチレン、プロピレン、塩化アリル、アクリル酸、メタクリル酸、アクリル酸エステル、メタクリル酸エステル、酢酸ビニル、無水マレイン酸、アクリロニトリル等の単量体が挙げられる。これらは単独で用いられてもよく、2種類以上が併用されてもよい。
塩化ビニル樹脂は単独で用いられてもよく、2種類以上が併用されてもよい。
塩化ビニル樹脂の平均重合度は450〜800が好ましく、600〜700がより好ましい。
<Foaming resin composition>
The foamable resin composition contains a vinyl chloride resin and a foaming agent.
As the vinyl chloride resin, a known hard vinyl chloride resin can be used as a material for the pipe joint. The hard vinyl chloride resin is a vinyl chloride resin substantially free of a plasticizer.
The vinyl chloride resin may be a homopolymer of a vinyl chloride monomer or a copolymer of a vinyl chloride monomer and another monomer copolymerizable with the vinyl chloride monomer. Good.
Examples of other monomers copolymerizable with the vinyl chloride monomer include, for example, ethylene, propylene, allyl chloride, acrylic acid, methacrylic acid, acrylic acid ester, methacrylic acid ester, vinyl acetate, maleic anhydride, and acrylonitrile. And the like. These may be used alone or in combination of two or more.
A vinyl chloride resin may be used independently and 2 or more types may be used together.
The average degree of polymerization of the vinyl chloride resin is preferably 450 to 800, more preferably 600 to 700.

発泡剤としては、揮発性発泡剤、分解型発泡剤のいずれを使用してもよい。
揮発性発泡剤としては、例えば脂肪族炭化水素、脂環族炭化水素、ハロゲン化炭化水素、エーテル、ケトン等が挙げられる。このうち脂肪族炭化水素としては、例えばプロパン、ブタン(ノルマルブタン、イソブタン)、ペンタン(ノルマルペンタン、イソペンタンなど)等が挙げられ、脂環族炭化水素としては、例えばシクロペンタン、シクロへキサン等が挙げられる。ハロゲン化炭化水素としては、例えばトリクロロフルオロメタン、トリクロロトリフルオロエタン、テトラフルオロエタン、クロロジフルオロエタン、ジフルオロエタン等のハロゲン化炭化水素などの1種または2種以上が挙げられる。さらにエーテルとしては、例えばジメチルエーテル、ジエチルエーテル等が挙げられ、ケトンとしては、例えばアセトン、メチルエチルケトン等が挙げられる。
また分解型発泡剤としては、例えば重炭酸ナトリウム(炭酸水素ナトリウム)、炭酸ナトリウム、重炭酸アンモニウム、亜硝酸アンモニウム、アジド化合物、ホウ水素化ナトリウムなどの無機系発泡剤、アゾジカルボンアミド、アゾジカルボン酸バリウム、ジニトロソペンタメチレンテトラミンなどの有機系発泡剤が挙げられる。
その他、炭酸ガス、窒素、空気等のガスを発泡剤として用いてもよい。
発泡性能に優れる観点から、分解型発泡剤が好ましく、中でも重曹、アゾジカルボンアミドがより好ましい。
これらは単独で用いられても良く、2種以上が併用されてもよい。
発泡剤の使用量は、塩化ビニル樹脂100質量部に対して、0.1〜8質量部が好ましく、2〜5質量部がより好ましく、1〜3質量部が最も好ましい。
As the foaming agent, either a volatile foaming agent or a decomposable foaming agent may be used.
Examples of the volatile foaming agent include aliphatic hydrocarbons, alicyclic hydrocarbons, halogenated hydrocarbons, ethers, and ketones. Among these, examples of the aliphatic hydrocarbon include propane, butane (normal butane, isobutane), pentane (normal pentane, isopentane, etc.), and examples of the alicyclic hydrocarbon include cyclopentane, cyclohexane, and the like. Can be mentioned. Examples of the halogenated hydrocarbon include one or more of halogenated hydrocarbons such as trichlorofluoromethane, trichlorotrifluoroethane, tetrafluoroethane, chlorodifluoroethane, difluoroethane, and the like. Furthermore, examples of the ether include dimethyl ether and diethyl ether, and examples of the ketone include acetone and methyl ethyl ketone.
Examples of the decomposable foaming agent include sodium bicarbonate (sodium bicarbonate), sodium carbonate, ammonium bicarbonate, ammonium nitrite, azide compound, sodium borohydride and other inorganic foaming agents, azodicarbonamide, barium azodicarboxylate And organic foaming agents such as dinitrosopentamethylenetetramine.
In addition, a gas such as carbon dioxide, nitrogen, or air may be used as the foaming agent.
From the viewpoint of excellent foaming performance, a decomposable foaming agent is preferable, and sodium bicarbonate and azodicarbonamide are more preferable.
These may be used alone or in combination of two or more.
0.1-8 mass parts is preferable with respect to 100 mass parts of vinyl chloride resin, the usage-amount of a foaming agent has more preferable 2-5 mass parts, and its 1-3 mass parts are the most preferable.

発泡性樹脂組成物は、塩化ビニル樹脂および発泡剤以外の他の成分(任意成分)を含んでもよい。任意成分としては、例えば、安定剤、滑剤、加工助剤、顔料等の公知の添加剤が挙げられる。
安定剤としては、塩化ビニル樹脂の安定剤として公知の化合物を用いることができる。例えば、鉛系安定剤、CaZn系安定剤、錫系安定剤等が挙げられるが、発泡性樹脂組成物中には、鉛系安定剤が含まれないことが好ましい。
発泡性樹脂組成物中に鉛系安定剤が含まれると、アゾジカルボンアミド等の有機系発泡剤の分解が活性化され、発泡開始温度が低下する。その結果、発泡残渣が発生し、ヤケ(変色した異物)と呼ばれる製品不良が生じやすくなり、好ましくない。
The foamable resin composition may contain other components (optional components) other than the vinyl chloride resin and the foaming agent. Examples of optional components include known additives such as stabilizers, lubricants, processing aids, and pigments.
As the stabilizer, a known compound can be used as a stabilizer for the vinyl chloride resin. For example, lead-based stabilizers, CaZn-based stabilizers, tin-based stabilizers and the like can be mentioned, but it is preferable that the foamable resin composition does not contain lead-based stabilizers.
When the lead-based stabilizer is contained in the foamable resin composition, the decomposition of the organic foaming agent such as azodicarbonamide is activated, and the foaming start temperature is lowered. As a result, a foaming residue is generated, and a product defect called burn (discolored foreign matter) tends to occur, which is not preferable.

発泡性樹脂組成物中の安定剤は、錫系安定剤であることが好ましい。錫系安定剤を用いることにより、塩化ビニル樹脂の熱安定性を高めやすくなり、ヤケの発生を抑えることができる。錫系安定剤としては、ジアルキル錫の有機酸塩を用いることができる。アルキル基としては、メチル、ブチル、オクチルの3種類が挙げられる。有機酸としては、チオグリコール酸のエステル、メルカプトエタノールのエステル等のメルカプト系化合物;マレイン酸エステル、マレイン酸のハーフエステルの有機錫塩等のマレート系化合物;ラウリン酸の塩等のラウレート系化合物等が挙げられる。非発泡層の透明性を担保する観点から、錫系安定剤としては、メルカプト系化合物が好ましい。例えば、ジブチル錫メルカプタン、ジオクチル錫メルカプタン等が挙げられる。
これらの錫系安定剤は、1種でもよく、2種以上を併用してもよい。塩化ビニル樹脂の熱安定性をより高め、加工性を向上させる観点から、錫系安定剤を2種以上併用することが好ましい。
錫系安定剤は、1種でもよく、2種以上を併用してもよい。
The stabilizer in the foamable resin composition is preferably a tin-based stabilizer. By using a tin-based stabilizer, it becomes easy to increase the thermal stability of the vinyl chloride resin, and the occurrence of burns can be suppressed. As the tin stabilizer, an organic acid salt of dialkyl tin can be used. Examples of the alkyl group include methyl, butyl, and octyl. Examples of organic acids include mercapto compounds such as esters of thioglycolic acid and esters of mercaptoethanol; malate compounds such as maleic acid esters and organic tin salts of maleic acid half esters; laurate compounds such as salts of lauric acid, etc. Is mentioned. From the viewpoint of ensuring the transparency of the non-foamed layer, a mercapto compound is preferred as the tin stabilizer. For example, dibutyltin mercaptan, dioctyltin mercaptan, etc. are mentioned.
These tin stabilizers may be used alone or in combination of two or more. From the viewpoint of further improving the thermal stability of the vinyl chloride resin and improving the workability, it is preferable to use two or more tin stabilizers in combination.
The tin stabilizer may be used alone or in combination of two or more.

錫系安定剤の含有量は、安定剤の総質量に対して95質量%以上が好ましく、100質量%が特に好ましい。
また、錫系安定剤の含有量は、塩化ビニル樹脂100質量部に対して、0.1質量部以上10質量部以下が好ましく、0.5質量部以上5質量部以下がより好ましく、1質量部以上5質量部以下がさらに好ましい。錫系安定剤の含有量が、前記下限値以上であると、塩化ビニル樹脂の熱安定性をより高めやすい。前記上限値以下であると、発泡性樹脂組成物の耐熱性、加工性をより高めやすい。
The content of the tin-based stabilizer is preferably 95% by mass or more, particularly preferably 100% by mass with respect to the total mass of the stabilizer.
The content of the tin-based stabilizer is preferably 0.1 parts by mass or more and 10 parts by mass or less, more preferably 0.5 parts by mass or more and 5 parts by mass or less, with respect to 100 parts by mass of the vinyl chloride resin. More preferred is 5 parts by mass or more. When the content of the tin stabilizer is equal to or more than the lower limit, the thermal stability of the vinyl chloride resin can be easily increased. It is easy to improve the heat resistance of a foamable resin composition and workability as it is below the said upper limit.

任意成分の含有量は、塩化ビニル樹脂100質量部に対して、30質量部以下が好ましく、20質量部以下がより好ましく、10質量部以下がさらに好ましい。   The content of the optional component is preferably 30 parts by mass or less, more preferably 20 parts by mass or less, and still more preferably 10 parts by mass or less with respect to 100 parts by mass of the vinyl chloride resin.

本発明の発泡管継手は、塩化ビニル樹脂と発泡剤とを含む発泡性樹脂組成物を、発泡・成形したものであり、耐薬品性および断熱性に優れる。また、全体が塩化ビニル樹脂の発泡層からなる成形品であるにもかかわらず、耐衝撃性に優れる。
管継手の形状は、本実施形態のチーズ型(ティー型)に限らず、エルボ、レジューサ、バルブソケット、ニップル等の各種形状を適用することができる。
The foamed pipe joint of the present invention is obtained by foaming and molding a foamable resin composition containing a vinyl chloride resin and a foaming agent, and is excellent in chemical resistance and heat insulation. Moreover, it is excellent in impact resistance, although the whole is a molded article made of a foamed layer of vinyl chloride resin.
The shape of the pipe joint is not limited to the cheese type (tea type) of the present embodiment, and various shapes such as an elbow, a reducer, a valve socket, and a nipple can be applied.

以下に実施例を用いて本発明をさらに詳しく説明するが、本発明はこれら実施例に限定されるものではない。
各実施例及び比較例で使用した原料、評価方法は、以下の通りである。
Hereinafter, the present invention will be described in more detail using examples, but the present invention is not limited to these examples.
The raw materials and evaluation methods used in each example and comparative example are as follows.

[使用原料]
塩化ビニル樹脂:重合度640、徳山積水工業社製、商品名「TS−640M」。
発泡剤:アゾジカルボンアミド、永和化成社製、商品名「AC3」。
安定剤:メチル錫、勝田化工社製、商品名「KM−19D−2」。
[Raw materials]
Vinyl chloride resin: Degree of polymerization 640, manufactured by Tokuyama Sekisui Industry Co., Ltd., trade name “TS-640M”.
Foaming agent: Azodicarbonamide, manufactured by Eiwa Kasei Co., Ltd., trade name “AC3”.
Stabilizer: Methyl tin, manufactured by Katsuta Chemical Co., Ltd., trade name “KM-19D-2”.

[耐衝撃性試験]
雰囲気温度0℃で、1mの高さから床(材質:コンクリート)に落とす落下試験を行い、下記の基準で判定した。落下試験は、1個の発泡管継手の複数の受口部の全部について行う。したがって、チーズ型管継手は、3つの受口部がそれぞれ床に衝突するように3回の落下試験を行った。
×:1つ以上の受口部で割れが発生した。
〇:全部の受口部で割れが発生しなかった。
[Impact resistance test]
A drop test was carried out by dropping from a height of 1 m onto a floor (material: concrete) at an atmospheric temperature of 0 ° C. and judged according to the following criteria. The drop test is performed on all of the plurality of receiving portions of one foamed pipe joint. Therefore, the cheese type pipe joint was subjected to a drop test three times so that the three receiving portions collide with the floor.
X: Cracks occurred at one or more receiving portions.
○: No cracks occurred in all the receiving parts.

(例1〜6)
例2〜4は実施例、例1、5、6は比較例である。
塩化ビニル樹脂100質量部と、発泡剤1質量部と、安定剤2質量部を混合した発泡性樹脂組成物を射出成形して、図1〜3に示す形状の発泡管継手を製造した。成形温度は170℃、金型温度は40℃、射出開始から脱型までの成形時間は120秒とした。
発泡管継手における各寸法が表1に示す通りとなるように、金型の寸法を変更した。
例5は、例3において射出ゲートの位置を受口部の開口部近傍に変更したほかは、例3と同様とした。
得られた発泡管継手について、表1に示す各項目について測定または評価を行った。発泡させなかった時の樹脂の比重は1.4であった。結果を表1に示す。
なお、例6は発泡性樹脂組成物の充填不足による開口部12bの成形不良が生じたため、開口端部における発泡倍率の測定および耐衝撃性試験は行わなかった。
(Examples 1-6)
Examples 2 to 4 are examples, and examples 1, 5, and 6 are comparative examples.
A foamable pipe joint having a shape shown in FIGS. 1 to 3 was produced by injection molding a foamable resin composition in which 100 parts by mass of a vinyl chloride resin, 1 part by mass of a foaming agent, and 2 parts by mass of a stabilizer were mixed. The molding temperature was 170 ° C., the mold temperature was 40 ° C., and the molding time from the start of injection to demolding was 120 seconds.
The dimensions of the mold were changed so that the dimensions of the foamed pipe joint were as shown in Table 1.
Example 5 was the same as Example 3 except that the position of the injection gate in Example 3 was changed to the vicinity of the opening of the receiving port.
About the obtained foamed pipe joint, each item shown in Table 1 was measured or evaluated. The specific gravity of the resin when not foamed was 1.4. The results are shown in Table 1.
In Example 6, since the molding of the opening 12b was poor due to insufficient filling of the foamable resin composition, the measurement of the expansion ratio and the impact resistance test at the opening end were not performed.

Figure 2018172600
Figure 2018172600

表1の結果に示されるように、(受口部中央の厚さ)/(本体部中央の厚さ)の比が0.3〜0.7であり、本体部中央における発泡倍率が1.2〜2.5倍であり、かつ受口部の開口端部における発泡倍率が1.2〜1.5倍である例2〜4の発泡管継手は、耐衝撃性に優れる。
これに対して、受口部の開口端部における発泡倍率は1.0であるものの、(受口部中央の厚さ)/(本体部中央の厚さ)の比が小さい例1は、本体部中央における発泡倍率が低く、耐衝撃性が劣る。
例5は、射出ゲート部14の位置を変更したため、受口部の開口端部における発泡倍率が高くなり、耐衝撃性に劣る。
例6は、受口部中央の厚さ(T2)が大きすぎるため、受口部に発泡性樹脂組成物の充填不足が生じたと考えられる。
As shown in the results of Table 1, the ratio of (thickness at the center of the receiving port) / (thickness at the center of the main body) is 0.3 to 0.7, and the expansion ratio at the center of the main body is 1. The foamed pipe joints of Examples 2 to 4 that are 2 to 2.5 times and the foaming magnification at the opening end of the receiving portion is 1.2 to 1.5 times are excellent in impact resistance.
On the other hand, although the expansion ratio at the opening end of the receiving port is 1.0, the ratio of (thickness at the center of the receiving port) / (thickness at the center of the main body) is small. The expansion ratio at the center of the part is low and the impact resistance is poor.
In Example 5, since the position of the injection gate portion 14 is changed, the expansion ratio at the opening end portion of the receiving portion is increased, and the impact resistance is inferior.
In Example 6, since the thickness (T2) at the center of the receiving part is too large, it is considered that insufficient filling of the foamable resin composition occurred in the receiving part.

1 発泡管継手
10 本体部
11 開口部
11a 第1の本体開口部
11b 第2の本体開口部
11c 第3の本体開口部
12 受口部
12A 第1の受口部
12B 第2の受口部
12C 第3の受口部
12a テーパ部
12b 開口部
13 段部
14 射出ゲート部
O1 第1の管軸
O2 第2の管軸
DESCRIPTION OF SYMBOLS 1 Foam pipe joint 10 Main-body part 11 Opening part 11a 1st main-body opening part 11b 2nd main-body opening part 11c 3rd main-body opening part 12 Receiving part 12A 1st receiving part 12B 2nd receiving part 12C Third receiving portion 12a Taper portion 12b Opening portion 13 Step portion 14 Injection gate portion O1 First tube axis O2 Second tube shaft

Claims (2)

塩化ビニル樹脂と発泡剤とを含む発泡性樹脂組成物を、発泡・成形してなる発泡管継手であって、
内部に流路を有する本体部と、該本体部の開口部に一体に形成された受口部とを有し、
(受口部中央の厚さ)/(本体部中央の厚さ)の比が0.3〜0.7であり、
本体部中央における発泡倍率が1.2〜2.5倍であり、かつ
受口部の開口端部における発泡倍率が1.2〜1.5倍である、ことを特徴とする発泡管継手。
A foam pipe joint formed by foaming and molding a foamable resin composition containing a vinyl chloride resin and a foaming agent,
A main body having a flow path inside, and a receiving portion formed integrally with the opening of the main body,
The ratio of (thickness at the center of the receiving port) / (thickness at the center of the main body) is 0.3 to 0.7,
A foamed pipe joint having a foaming ratio of 1.2 to 2.5 times at the center of the main body and a foaming ratio of 1.2 to 1.5 times at the opening end of the receiving part.
請求項1に記載の発泡管継手の製造方法であって、塩化ビニル樹脂と発泡剤とを含む発泡性樹脂組成物を射出成形する、発泡管継手の製造方法。   The method for producing a foamed pipe joint according to claim 1, wherein a foamable resin composition containing a vinyl chloride resin and a foaming agent is injection-molded.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7474163B2 (en) 2020-09-23 2024-04-24 積水化学工業株式会社 Transparent fireproof joint

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0687496U (en) * 1993-05-31 1994-12-22 積水化学工業株式会社 Drain
JPH11201382A (en) * 1998-01-13 1999-07-30 Sekisui Chem Co Ltd Pipe joint having heat insulation layer, and its manufacture

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0687496U (en) * 1993-05-31 1994-12-22 積水化学工業株式会社 Drain
JPH11201382A (en) * 1998-01-13 1999-07-30 Sekisui Chem Co Ltd Pipe joint having heat insulation layer, and its manufacture

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7474163B2 (en) 2020-09-23 2024-04-24 積水化学工業株式会社 Transparent fireproof joint

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