JP2002248675A - Multilayer preform and its manufacturing method - Google Patents
Multilayer preform and its manufacturing methodInfo
- Publication number
- JP2002248675A JP2002248675A JP2001048092A JP2001048092A JP2002248675A JP 2002248675 A JP2002248675 A JP 2002248675A JP 2001048092 A JP2001048092 A JP 2001048092A JP 2001048092 A JP2001048092 A JP 2001048092A JP 2002248675 A JP2002248675 A JP 2002248675A
- Authority
- JP
- Japan
- Prior art keywords
- resin
- multilayer preform
- outer layer
- neck
- multilayer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 17
- 229920005989 resin Polymers 0.000 claims abstract description 157
- 239000011347 resin Substances 0.000 claims abstract description 157
- 238000005520 cutting process Methods 0.000 claims abstract description 8
- LLLVZDVNHNWSDS-UHFFFAOYSA-N 4-methylidene-3,5-dioxabicyclo[5.2.2]undeca-1(9),7,10-triene-2,6-dione Chemical compound C1(C2=CC=C(C(=O)OC(=C)O1)C=C2)=O LLLVZDVNHNWSDS-UHFFFAOYSA-N 0.000 claims description 11
- 229920001225 polyester resin Polymers 0.000 claims description 8
- 239000004645 polyester resin Substances 0.000 claims description 8
- 230000006835 compression Effects 0.000 claims 1
- 238000007906 compression Methods 0.000 claims 1
- 239000010410 layer Substances 0.000 abstract description 57
- 238000000748 compression moulding Methods 0.000 abstract description 11
- 238000000465 moulding Methods 0.000 abstract description 8
- 238000002425 crystallisation Methods 0.000 abstract description 7
- 230000008025 crystallization Effects 0.000 abstract description 7
- 238000000034 method Methods 0.000 abstract description 6
- 239000011229 interlayer Substances 0.000 abstract description 2
- 229920000139 polyethylene terephthalate Polymers 0.000 description 17
- 239000005020 polyethylene terephthalate Substances 0.000 description 17
- 238000001746 injection moulding Methods 0.000 description 16
- 230000002087 whitening effect Effects 0.000 description 11
- 238000002347 injection Methods 0.000 description 7
- 239000007924 injection Substances 0.000 description 7
- 230000032798 delamination Effects 0.000 description 4
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 3
- 238000000071 blow moulding Methods 0.000 description 3
- 238000007664 blowing Methods 0.000 description 3
- 239000003086 colorant Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 229920000728 polyester Polymers 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 239000011342 resin composition Substances 0.000 description 3
- 229920001169 thermoplastic Polymers 0.000 description 3
- 239000004416 thermosoftening plastic Substances 0.000 description 3
- MMINFSMURORWKH-UHFFFAOYSA-N 3,6-dioxabicyclo[6.2.2]dodeca-1(10),8,11-triene-2,7-dione Chemical group O=C1OCCOC(=O)C2=CC=C1C=C2 MMINFSMURORWKH-UHFFFAOYSA-N 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 230000009477 glass transition Effects 0.000 description 2
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229920001707 polybutylene terephthalate Polymers 0.000 description 2
- -1 polyethylene terephthalate Polymers 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 229920006230 thermoplastic polyester resin Polymers 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 235000016795 Cola Nutrition 0.000 description 1
- 235000011824 Cola pachycarpa Nutrition 0.000 description 1
- 229920001634 Copolyester Polymers 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 235000013405 beer Nutrition 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 235000014171 carbonated beverage Nutrition 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 235000019987 cider Nutrition 0.000 description 1
- 239000000805 composite resin Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 150000002009 diols Chemical class 0.000 description 1
- BXKDSDJJOVIHMX-UHFFFAOYSA-N edrophonium chloride Chemical compound [Cl-].CC[N+](C)(C)C1=CC=CC(O)=C1 BXKDSDJJOVIHMX-UHFFFAOYSA-N 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 235000011194 food seasoning agent Nutrition 0.000 description 1
- 235000015203 fruit juice Nutrition 0.000 description 1
- 238000009998 heat setting Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- KYTZHLUVELPASH-UHFFFAOYSA-N naphthalene-1,2-dicarboxylic acid Chemical compound C1=CC=CC2=C(C(O)=O)C(C(=O)O)=CC=C21 KYTZHLUVELPASH-UHFFFAOYSA-N 0.000 description 1
- 239000002667 nucleating agent Substances 0.000 description 1
- 239000011112 polyethylene naphthalate Substances 0.000 description 1
- 235000015067 sauces Nutrition 0.000 description 1
- 239000002453 shampoo Substances 0.000 description 1
- 235000013555 soy sauce Nutrition 0.000 description 1
- 229920005992 thermoplastic resin Polymers 0.000 description 1
- 239000006097 ultraviolet radiation absorber Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 230000037303 wrinkles Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B11/00—Making preforms
- B29B11/06—Making preforms by moulding the material
- B29B11/12—Compression moulding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/02—Combined blow-moulding and manufacture of the preform or the parison
- B29C49/0685—Compression blow-moulding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B11/00—Making preforms
- B29B11/14—Making preforms characterised by structure or composition
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C43/00—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
- B29C43/32—Component parts, details or accessories; Auxiliary operations
- B29C43/36—Moulds for making articles of definite length, i.e. discrete articles
- B29C43/42—Moulds for making articles of definite length, i.e. discrete articles for undercut articles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/071—Preforms or parisons characterised by their configuration, e.g. geometry, dimensions or physical properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/07—Preforms or parisons characterised by their configuration
- B29C2949/0715—Preforms or parisons characterised by their configuration the preform having one end closed
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/07—Preforms or parisons characterised by their configuration
- B29C2949/081—Specified dimensions, e.g. values or ranges
- B29C2949/082—Diameter
- B29C2949/0826—Diameter of the body
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/07—Preforms or parisons characterised by their configuration
- B29C2949/081—Specified dimensions, e.g. values or ranges
- B29C2949/082—Diameter
- B29C2949/0828—Diameter of a layer
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/07—Preforms or parisons characterised by their configuration
- B29C2949/0861—Other specified values, e.g. values or ranges
- B29C2949/0872—Weight
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/20—Preforms or parisons whereby a specific part is made of only one component, e.g. only one layer
- B29C2949/22—Preforms or parisons whereby a specific part is made of only one component, e.g. only one layer at neck portion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/20—Preforms or parisons whereby a specific part is made of only one component, e.g. only one layer
- B29C2949/24—Preforms or parisons whereby a specific part is made of only one component, e.g. only one layer at flange portion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/30—Preforms or parisons made of several components
- B29C2949/3016—Preforms or parisons made of several components at body portion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/30—Preforms or parisons made of several components
- B29C2949/302—Preforms or parisons made of several components at bottom portion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/30—Preforms or parisons made of several components
- B29C2949/3024—Preforms or parisons made of several components characterised by the number of components or by the manufacturing technique
- B29C2949/3026—Preforms or parisons made of several components characterised by the number of components or by the manufacturing technique having two or more components
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/02—Combined blow-moulding and manufacture of the preform or the parison
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/22—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor using multilayered preforms or parisons
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Physics & Mathematics (AREA)
- Geometry (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
Abstract
Description
【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION
【0001】[0001]
【発明の属する技術分野】本発明は、複数種の熱可塑性
樹脂を圧縮成形によって成形する多層プリフォーム及び
その製造方法に関するもので、より詳細には、バージン
樹脂の所定量と再生樹脂の所定量とを別個に押出して同
一の雌型内に供給し、雌型と雄型とによって圧縮成形す
る多層プリフォーム及びその製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a multilayer preform for molding a plurality of types of thermoplastic resins by compression molding and a method for producing the same. More specifically, the present invention relates to a predetermined amount of virgin resin and a predetermined amount of recycled resin. The present invention relates to a multilayer preform which is separately extruded and supplied into the same female mold, and compression-molded by a female mold and a male mold, and a method for producing the same.
【0002】[0002]
【従来技術】ポリエチレンテレフタレート(PET)樹
脂を射出成形してプリフォームを成形し、このプリフォ
ームを二軸延伸ブロー成形して得られたPETボトル
は、透明性、ガスバリヤー性、機械的強度等に優れ、液
体洗剤、シャンプー、化粧品、醤油、ソース等の調味
料、ビール、コーラ、サイダー等の炭酸飲料、果汁、ミ
ネラルウォーター等の飲料用容器として広く使用されて
いる。2. Description of the Related Art A PET bottle obtained by injection-molding a polyethylene terephthalate (PET) resin to form a preform, and biaxially stretch-blowing the preform, has a transparency, a gas barrier property, a mechanical strength and the like. It is widely used as a seasoning for liquid detergents, shampoos, cosmetics, soy sauce, sauces, etc., carbonated beverages such as beer, cola, cider, etc., fruit juices and beverage containers for mineral water.
【0003】また、PETボトルは最近需要が拡大して
ゴミ処理の問題が発生し、一度使用されたボトルを市場
から回収して再生したポストコンシューマーリサイクル
(PCR)樹脂を再利用することが求められる。PET
樹脂のリサイクルを目的として、使用済みのPETボト
ルを回収して再利用するため、回収したPETボトルを
粉砕、洗浄、乾燥してフレーク状の樹脂に加工し、この
フレーク状樹脂を外層或いは中間層とし、バージン樹脂
を内層とする多層プリフォームないし多層ボトルが特開
平10−337770号公報、特開平11−77744
号公報等で提案されている。[0003] In addition, the demand for PET bottles has recently increased and the problem of garbage disposal has arisen, and it is required to recycle post-consumer recycled (PCR) resins that have been used once and then recycled from the market. . PET
In order to collect and reuse used PET bottles for the purpose of resin recycling, the collected PET bottles are crushed, washed, dried and processed into flake-like resin, and this flake-like resin is placed in an outer layer or an intermediate layer. A multilayer preform or a multilayer bottle having a virgin resin as an inner layer is disclosed in JP-A-10-337770 and JP-A-11-77744.
It is proposed in Japanese Patent Publication No.
【0004】多層プリフォームは、一般に異なる樹脂を
金型内に共射出ないし多段射出して製造されるが、その
成形方法としては、大別して、逐次共射出成形法、同時
共射出成形法及び多段射出成形法が知られている。逐次
共射出成形法では、異なる樹脂を複数の射出機にそれぞ
れ供給し、金型内に最初に内外層を形成する樹脂を射出
し、続いて中間層となる樹脂を射出して多層プリフォー
ムを成形する。また、同時共射出成形法では、金型内に
最初に内層及び外層を形成する樹脂を射出し、若干時間
遅れて中間層を形成する樹脂を並行して射出して多層プ
リフォームを成形する。さらに、多段射出成形法では、
金型内に最初に内層を形成する樹脂を射出して一次成形
体を成形し、次いでこの一次成形体を別の金型に移して
外層を形成する樹脂を射出して多層プリフォームを成形
する。[0004] Multilayer preforms are generally manufactured by co-injection or multi-stage injection of different resins into a mold. The molding methods are roughly classified into a sequential co-injection molding method, a simultaneous co-injection molding method and a multi-stage injection molding method. Injection molding methods are known. In the sequential co-injection molding method, different resins are respectively supplied to a plurality of injection machines, a resin for forming inner and outer layers is first injected into a mold, and then a resin for an intermediate layer is injected to form a multilayer preform. Molding. In the simultaneous co-injection molding method, a resin for forming an inner layer and an outer layer is first injected into a mold, and a resin for forming an intermediate layer is injected in parallel with a slight delay to form a multilayer preform. Furthermore, in the multi-stage injection molding method,
First, a resin for forming an inner layer is injected into a mold to form a primary molded body, and then the primary molded body is transferred to another mold, and a resin for forming an outer layer is injected to form a multilayer preform. .
【0005】射出成形によって製造された多層プリフォ
ームの形状は、ボトルの口頸部に相当する口頸部と、延
伸ブロー成形されるべき有底筒状部とを備え、一般に試
験管形状している。通常、口頸部には密封用開口端や蓋
との係合手段である螺子部等が形成され、また、底部の
中心には射出成形時に樹脂が注入されるときのゲート部
ないしゲート部跡が必ず形成されている。[0005] The shape of a multilayer preform manufactured by injection molding has a mouth-neck portion corresponding to the mouth-neck portion of a bottle and a bottomed cylindrical portion to be stretch-blow-molded. I have. Normally, a screw opening or the like, which is a means for engaging with the lid, is formed in the mouth and neck, and a gate or a trace of the gate when the resin is injected during injection molding is formed in the center of the bottom. Is always formed.
【0006】[0006]
【発明が解決しようとする課題】従来の共射出成形法や
多段射出成形法では、PCR樹脂の含有割合を多くする
と多層プリフォーム、特に底部のゲート部近傍に白化や
樹脂流の乱れが生じるため、この多層プリフォームを二
軸延伸ブロー成形して得られたボトルは、底部の白化や
クレーズ等の外観特性が悪く、耐衝撃性が低下するとい
う問題があった。In the conventional co-injection molding method or multi-stage injection molding method, when the content ratio of the PCR resin is increased, whitening and turbulence of the resin flow occur in the multilayer preform, especially near the bottom gate. However, bottles obtained by biaxially stretch-blowing the multilayer preform have poor appearance properties such as whitening of the bottom and craze, and have a problem of reduced impact resistance.
【0007】特に、PCR樹脂等の再生樹脂は、バージ
ン樹脂に比べて熱履歴を多く受け、かつ不純物が多少混
入されているため結晶化し易くなっており、PCR樹脂
等の割合を多くすれば、共射出成形では冷却効率の関係
で結晶化による白化が生じ、多段射出成形では各層間の
接着強度不足が生じる。それ故、この多層プリフォーム
を二軸延伸ブロー成形して得られた多層ボトルは、結晶
化による白化が生じて外観特性が悪く、また層間剥離を
生じ易くて耐衝撃性も低下する。[0007] In particular, a regenerated resin such as a PCR resin has a higher thermal history than a virgin resin, and is easily crystallized due to the inclusion of some impurities. In co-injection molding, whitening occurs due to crystallization due to cooling efficiency, and in multi-stage injection molding, insufficient bonding strength occurs between layers. Therefore, the multilayer bottle obtained by biaxially stretch-blow-molding this multilayer preform has whitening due to crystallization, has poor appearance characteristics, and is liable to cause delamination and has a reduced impact resistance.
【0008】本発明者らは、上記問題点を解決するため
に、最初にPCR樹脂を押出機に供給してこの押出機か
ら押し出される溶融PCR樹脂の一定量を切断して雌金
型内に投入し、次いでバージン樹脂を別の押出機に供給
してこの押出機から押し出される溶融バージン樹脂の一
定量を切断して溶融PCR樹脂の上に投入した後、雄型
を雌型内に挿入し圧縮成形して多層プリフォーム成形す
ることによって、結晶化による白化の発生がなく、底部
に樹脂流の乱れもなく、さらに各層間の接着も良好であ
ることを見出した。さらに、得られた多層プリフォーム
を二軸延伸ブロー成形した多層ボトルも、結晶化による
白化もなく、底部にクレーズが発生することもなく、耐
衝撃性も良好であった。[0008] In order to solve the above problems, the present inventors first supply a PCR resin to an extruder, cut a fixed amount of the molten PCR resin extruded from the extruder, and place the cut resin in a female mold. And then supply the virgin resin to another extruder, cut a certain amount of the molten virgin resin extruded from this extruder and throw it on the molten PCR resin, then insert the male mold into the female mold. It has been found that by performing compression molding to form a multilayer preform, there is no occurrence of whitening due to crystallization, no disturbance of resin flow at the bottom, and good adhesion between layers. Furthermore, the multilayer bottle obtained by biaxially stretch-blowing the obtained multilayer preform also had no whitening due to crystallization, no craze occurred at the bottom, and good impact resistance.
【0009】即ち、本発明者らは、PCR樹脂等の再生
樹脂からなる溶融樹脂塊Aの所定量を雌型内の下方に供
給し、その上方にバージン樹脂からなる溶融樹脂塊Bの
所定量を供給して、雌型内に供給された溶融樹脂塊A及
び溶融樹脂塊Bを雄型及びネック型を用いて圧縮成形す
ることによって、前記再生樹脂の割合を多くしても透明
性を低下させることがなく、ゲート部ないしゲート部跡
もなく、かつ口頸部及びネックリング部がバージン樹脂
のみからなる多層プリフォームを得ることに成功した。That is, the present inventors supply a predetermined amount of a molten resin mass A made of a regenerated resin such as a PCR resin below the inside of a female mold, and a predetermined amount of a molten resin mass B made of a virgin resin thereabove. And the molten resin mass A and the molten resin mass B supplied into the female mold are compression-molded using the male mold and the neck mold, so that the transparency is reduced even if the ratio of the recycled resin is increased. No multilayer gate preform having no gate portion, no gate portion mark, and a mouth-neck portion and a neck ring portion made of only virgin resin was successfully obtained.
【0010】従って、本発明の目的は、PCR樹脂等の
前に熱履歴を受けた再生樹脂を使用しても結晶化による
白化が生じることなく、かつ底部にゲート部ないしゲー
ト部跡もなく、層間剥離も起こりにくく、耐衝撃性も良
好であるボトル成形用多層プリフォームを提供する。さ
らに、PCR樹脂等の再生樹脂をより多く再利用するこ
と、即ち多層プリフォームの全重量に対して25重量%
以上、好ましくは30重量%以上を再利用し得る多層プ
リフォームの製造方法を提供する。[0010] Accordingly, an object of the present invention is to provide a regenerated resin which has undergone a thermal history before a PCR resin or the like, without causing whitening due to crystallization and without a gate portion or a gate mark on the bottom. Provided is a multilayer preform for bottle molding, in which delamination hardly occurs and impact resistance is good. Furthermore, the recycling resin such as a PCR resin is reused more, that is, 25% by weight based on the total weight of the multilayer preform.
As described above, the present invention provides a method for producing a multilayer preform capable of recycling at least 30% by weight.
【0011】[0011]
【課題を解決するための手段】本発明によれば、再生樹
脂からなる外層とバージン樹脂からなる内層を有する多
層プリフォームにおいて、多層プリフォームの全体の重
量をW、ネックリングを含む口頸部の重量をX、多層プ
リフォームの外層の厚さをTo及び内層の厚さをTi、
外層の重量比率をYとするとき、下記式、 Y=〔(W−X)/W〕×〔To/(To+Ti)〕×
100(%) で表される外層の重量比率(Y)が、25〜65%であ
る多層プリフォームが提供される。ここで、外層の重量
比率(Y)は、多層プリフォームを形成する樹脂の全重
量に対する外層樹脂の重量の比率を意味する。According to the present invention, in a multilayer preform having an outer layer made of recycled resin and an inner layer made of virgin resin, the total weight of the multilayer preform is W, the mouth and neck including the neck ring, and the like. X, the thickness of the outer layer of the multilayer preform is To, and the thickness of the inner layer is Ti,
When the weight ratio of the outer layer is Y, the following formula is used: Y = [(W−X) / W] × [To / (To + Ti)] ×
A multilayer preform is provided, wherein the weight ratio (Y) of the outer layer represented by 100 (%) is 25 to 65%. Here, the weight ratio (Y) of the outer layer means the ratio of the weight of the outer layer resin to the total weight of the resin forming the multilayer preform.
【0012】さらに、本発明によれば、外層先端が口頸
部の下方にあるネックリングの下で終わっている多層プ
リフォームが提供され、バージン樹脂がエチレンテレフ
タレートを主体とするポリエステル樹脂で、再生樹脂が
エチレンテレフタレートを主体とするポリエステル樹脂
からなるPCR樹脂である多層プリフォームが提供さ
れ、底部にゲート部又はゲート部跡が存在しない多層プ
リフォームが提供される。Further, according to the present invention, there is provided a multilayer preform in which the outer layer tip ends under a neck ring below the mouth and neck, and the virgin resin is a polyester resin mainly composed of ethylene terephthalate, which is recycled. Provided is a multilayer preform in which a resin is a PCR resin composed of a polyester resin mainly composed of ethylene terephthalate, and a multilayer preform in which a gate portion or a trace of a gate portion does not exist at the bottom is provided.
【0013】また、本発明によれば、再生樹脂を溶融押
出して所定量を切断してなる溶融樹脂塊Aを雌型内に供
給し、次いでバージン樹脂を溶融押出して所定量を切断
してなる溶融樹脂塊Bを前記雌型内の溶融樹脂塊Aの上
に供給した後、雌型内に雄型を圧入して溶融樹脂塊Aが
外層を形成し、溶融樹脂塊Bが内層を形成するように圧
縮成形してなる多層プリフォームの製造方法が提供され
る。Further, according to the present invention, a molten resin mass A obtained by melt-extruding a regenerated resin and cutting a predetermined amount is supplied into a female mold, and then a virgin resin is melt-extruded and cut to a predetermined amount. After supplying the molten resin mass B onto the molten resin mass A in the female mold, the male mold is pressed into the female mold to form the outer layer, and the molten resin mass B forms the inner layer. Thus, a method for producing a multilayer preform formed by compression molding is provided.
【0014】さらに、本発明によれば、バージン樹脂が
エチレンテレフタレートを主体とするポリエステル樹脂
で、再生樹脂がエチレンテレフタレートを主体とするポ
リエステル樹脂からなるPCR樹脂である多層プリフォ
ームの製造方法が提供され、多層プリフォームの全体の
重量をW、ネックリングを含む口頸部の重量をX、多層
プリフォームの外層の厚さをTo及び内層の厚さをT
i、外層の重量比率をYとするとき、下記式、 Y=〔(W−X)/W〕×〔To/(To+Ti)〕×
100(%) で表される外層の重量比率(Y)が25〜65%である
多層プリフォームの製造方法が提供され、外層先端が口
頸部の下方にあるネックリングの下で終わっている多層
プリフォームの製造方法が提供され、底部にゲート部又
はゲート部跡が存在しない多層プリフォームの製造方法
が提供される。Further, according to the present invention, there is provided a method for producing a multilayer preform wherein the virgin resin is a polyester resin mainly composed of ethylene terephthalate and the regenerated resin is a PCR resin composed of a polyester resin mainly composed of ethylene terephthalate. , The total weight of the multilayer preform is W, the weight of the neck and neck including the neck ring is X, the thickness of the outer layer of the multilayer preform is To, and the thickness of the inner layer is T.
i, when the weight ratio of the outer layer is Y, the following formula: Y = [(W−X) / W] × [To / (To + Ti)] ×
A method is provided for producing a multilayer preform wherein the weight ratio (Y) of the outer layer, expressed as 100 (%), is 25-65%, the outer layer tip ending under the neck ring below the mouth and neck. A method for manufacturing a multilayer preform is provided, and a method for manufacturing a multilayer preform without a gate portion or a gate mark at the bottom is provided.
【0015】[0015]
【発明の実施の形態】本発明を図1ないし図5に基づい
て説明する。図1は本発明によって製造された多層プリ
フォームを示す。図1において、バージン樹脂とPCR
樹脂とを圧縮成形して製造した多層プリフォーム1は、
口頸部2、ネックリング3、胴部4及び底部5から構成
されている。さらに、多層プリフォーム1の口頸部2及
びネックリング3はバージン樹脂のみからなり、その他
の部分はバージン樹脂の内層6及び再生樹脂の外層7か
らなっている。この具体例において、底部5は略半球形
状になっているが、この形状に限定されず、楕円形状や
底部先端を平坦にすることもできる。多層プリフォーム
1の底部5には、底部にゲート部ないしゲート部跡がな
く、射出時に生じる流動配向による残留歪みも緩和さ
れ、かつ着色剤を添加しない状態では実質上透明になっ
ている。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described with reference to FIGS. FIG. 1 shows a multilayer preform made according to the present invention. In FIG. 1, virgin resin and PCR
The multilayer preform 1 manufactured by compression molding of resin is
It is composed of a mouth and neck 2, a neck ring 3, a trunk 4 and a bottom 5. Further, the mouth and neck portion 2 and the neck ring 3 of the multilayer preform 1 are made of only virgin resin, and the other portions are made of an inner layer 6 of virgin resin and an outer layer 7 of recycled resin. In this specific example, the bottom 5 has a substantially hemispherical shape, but is not limited to this shape, and may have an elliptical shape or a flat bottom end. The bottom portion 5 of the multilayer preform 1 has no gate portion or gate mark on the bottom portion, the residual strain due to the flow orientation generated at the time of injection is reduced, and the multilayer preform 1 is substantially transparent when no coloring agent is added.
【0016】次に、図2及び図3は溶融樹脂を雌型に供
給する工程を示す。図2に示すように、最初に再生樹脂
のみ又はバージン樹脂に再生樹脂を配合した再生樹脂組
成物を押出機に供給してダイヘッド11aから溶融押出
された再生樹脂を切断手段12aによって切断してなる
溶融樹脂塊Aを雌型13内に供給する。次いで、図3に
示すように、別の押出機にバージン樹脂を供給してダイ
ヘッド11bから溶融押出されたバージン樹脂を切断手
段12bによって切断してなる溶融樹脂塊Bを雌型13
内の溶融樹脂塊Aの上部に供給する。Next, FIGS. 2 and 3 show a process of supplying the molten resin to the female mold. As shown in FIG. 2, first, a recycled resin composition obtained by mixing a recycled resin alone or a virgin resin with a recycled resin is supplied to an extruder, and the recycled resin melt-extruded from a die head 11a is cut by a cutting unit 12a. The molten resin mass A is supplied into the female mold 13. Next, as shown in FIG. 3, a virgin resin is supplied to another extruder, and the virgin resin melt-extruded from the die head 11b is cut by a cutting means 12b to form a molten resin block B into a female mold 13.
Is supplied to the upper part of the molten resin mass A in the inside.
【0017】尚、溶融樹脂塊A及び溶融樹脂塊Bの雌型
13内への供給は、切断された溶融樹脂塊A及び溶融樹
脂塊Bをそれぞれ受具手段で保持して雌型13内に供給
することもでき、また、雌型13をダイヘッド11a及
び11bの下に順次移動して雌型13内に供給すること
もできる。The molten resin lump A and the molten resin lump B are supplied into the female mold 13 by holding the cut molten resin lump A and the molten resin lump B by receiving means. The female mold 13 can be supplied into the female mold 13 by sequentially moving the female mold 13 below the die heads 11a and 11b.
【0018】さらに、図4及び図5は雌型に供給された
溶融樹脂塊を雌型、雄型及びネック型を用いて圧縮成形
する工程を示す。雌型13に充填された溶融樹脂塊A及
び溶融樹脂塊Bは、雌型13、雄型14及びネック型1
5を用いて圧縮成形することによって、最初に溶融樹脂
塊Bが雌型13と雄型14との間の間隙に沿って流動
し、引き続いて溶融樹脂塊Aと溶融樹脂塊Bとが最初に
流動された溶融樹脂塊Bを上方へ押しやりながら流動し
て多層プリフォーム1を形成する。ここでは、雌型とネ
ック型を別体のものとして説明したが、これらを一体成
形のものとしても適用することができる。FIGS. 4 and 5 show a step of compression-molding the molten resin mass supplied to the female mold using a female mold, a male mold and a neck mold. The molten resin mass A and the molten resin mass B filled in the female mold 13 are the female mold 13, the male mold 14 and the neck mold 1
5, the molten resin mass B first flows along the gap between the female mold 13 and the male mold 14, and subsequently, the molten resin mass A and the molten resin mass B The multilayered preform 1 is formed by flowing while flowing the molten resin mass B upward. Here, the female mold and the neck mold have been described as being separate bodies, but these can also be applied as an integrally molded body.
【0019】上記圧縮成形によって得られた多層プリフ
ォーム1は、口頸部2及びネックリング3がバージン樹
脂のみからなり、胴部4及び底部5がバージン樹脂から
なる内層6及び再生樹脂からなる外層7からなってお
り、バージン樹脂がPET樹脂ないしPET樹脂を主体
とする樹脂からなり、再生樹脂がPET樹脂ないしPE
T樹脂を主体とするPCR樹脂又はその樹脂組成物であ
ることが好ましい。The multilayer preform 1 obtained by the compression molding has an inner layer 6 made of a virgin resin in the mouth and neck portion 2 and the neck ring 3 and an outer layer made of the virgin resin in the body portion 4 and the bottom portion 5. 7, the virgin resin is made of PET resin or a resin mainly composed of PET resin, and the recycled resin is made of PET resin or PE.
It is preferably a PCR resin mainly composed of a T resin or a resin composition thereof.
【0020】従来の射出成形で製造された多層プリフォ
ームに存在するゲート部が、生産性や製造コスト、最終
的なブロー成形品の特性の点で、種々の問題を抱えてい
る。一方、本発明によって製造された多層プリフォーム
は、最終成形品である多層ボトルの口部と対応する形状
及び寸法を有する口部と、延伸ブロー成形されるべき胴
部及び底部を備えているが、底部にはゲート部が一切存
在しないため、ゲート部の切断工程が不要であり、底部
中心も滑らかで均質であり、しかも透明性が低下するこ
とがなく、結晶化による白化もなく、底部には樹脂の流
動配向による残留歪みやしわが生じることもないという
特徴を備えている。The gate portion existing in the multilayer preform manufactured by the conventional injection molding has various problems in terms of productivity, manufacturing cost, and characteristics of a final blow molded product. On the other hand, the multilayer preform manufactured according to the present invention has a mouth having a shape and dimensions corresponding to the mouth of a multilayer bottle as a final molded product, and a body and a bottom to be stretch blow-molded. Since there is no gate at the bottom, there is no need to cut the gate, and the center of the bottom is also smooth and uniform, and there is no decrease in transparency, no whitening due to crystallization, Is characterized in that no residual strain or wrinkles are caused by the flow orientation of the resin.
【0021】この多層プリフォームを延伸温度である8
5〜120℃の温度範囲で、それ自体公知の延伸ブロー
成形法によって、延伸ロッドにより縦方向に延伸すると
共にブローエアによって横方向に延伸して多層ボトルを
製造する。得られた多層ボトルの延伸倍率は、縦方向で
1.2〜6倍、横方向で1.2〜4.5倍の範囲にある
ことが好ましい。また、耐熱性を必要とする用途には、
それ自体公知の手段でヒートセットを行うこともでき
る。The multilayer preform is stretched at a temperature of 8
In a temperature range of 5 to 120 ° C., a multilayer bottle is manufactured by stretching in the longitudinal direction by a stretching rod and in the transverse direction by blow air by a stretch blow molding method known per se. The stretching ratio of the obtained multilayer bottle is preferably in the range of 1.2 to 6 times in the vertical direction and 1.2 to 4.5 times in the horizontal direction. For applications requiring heat resistance,
The heat setting can be performed by a means known per se.
【0022】本発明によって製造された多層ボトルは、
透明性が低下することもなく、耐層間剥離性や耐衝撃性
に優れ、かつ再生樹脂の割合を多くすることができる。
さらに、底部にはゲート部ないしゲート跡が一切存在せ
ず、かつ底部中心付近も滑らかで均質に延伸され、クレ
ーズの発生もない。The multilayer bottle manufactured according to the present invention is:
The transparency is not reduced, the delamination resistance and the impact resistance are excellent, and the ratio of the recycled resin can be increased.
Further, there is no gate portion or gate mark at the bottom, and the vicinity of the center of the bottom is stretched smoothly and uniformly, and no craze occurs.
【0023】本発明に用いるバージン樹脂としては、P
ET、ポリブチレンテレフタレート(PBT)、ポリエ
チレンナフタレート(PEN)、またはそれらの共重合
体等の熱可塑性ポリエステル樹脂、これらの樹脂あるい
は他の樹脂とのブレンド物が好適に使用される。さら
に、これらの樹脂に成形品の品質を損なわない範囲内で
種々の添加剤、例えば、着色剤、紫外線吸収剤、離型
剤、滑剤、核剤、酸化防止剤、帯電防止剤等を配合する
こともできる。The virgin resin used in the present invention includes P
A thermoplastic polyester resin such as ET, polybutylene terephthalate (PBT), polyethylene naphthalate (PEN), or a copolymer thereof, or a blend of these resins or other resins is preferably used. Further, various additives such as a colorant, an ultraviolet absorber, a release agent, a lubricant, a nucleating agent, an antioxidant, and an antistatic agent are added to these resins within a range that does not impair the quality of the molded product. You can also.
【0024】熱可塑性ポリエステル樹脂の中でも、特に
PET等のエチレンテレフタレート系熱可塑性ポリエス
テルが好適に使用される。エチレンテレフタレート系熱
可塑性ポリエステルは、エステル反復単位の大部分、一
般に70モル%以上をエチレンテレフタレート単位を占
めるものであり、ガラス転移点(Tg)が50〜90
℃、融点(Tm)が200〜275℃の範囲にあるもの
が好適である。エチレンテレフタレート系熱可塑性ポリ
エステルとしてPETが耐圧性、耐熱性、耐熱圧性等の
点で特に優れているが、エチレンテレフタレート単位以
外にイソフタル酸やナフタレンジカルボン酸等の二塩基
酸とプロピレングリコール等のジオールからなるエステ
ル単位の少量を含む共重合ポリエステルも使用できる。Among the thermoplastic polyester resins, an ethylene terephthalate thermoplastic polyester such as PET is particularly preferably used. Ethylene terephthalate-based thermoplastic polyesters occupy most of the ester repeating units, generally 70 mol% or more, of ethylene terephthalate units, and have a glass transition point (Tg) of 50 to 90.
C. and those having a melting point (Tm) in the range of 200 to 275C are preferred. PET is particularly excellent in terms of pressure resistance, heat resistance, heat pressure resistance, etc. as an ethylene terephthalate-based thermoplastic polyester, but in addition to ethylene terephthalate units, dibasic acids such as isophthalic acid and naphthalenedicarboxylic acid and diols such as propylene glycol. Copolyesters containing small amounts of the following ester units can also be used.
【0025】一方、本発明に用いる再生樹脂としては、
市場から回収したボトルを洗浄・粉砕・分別して再生処
理したPCR樹脂、ボトルの生産工場内で発生する不良
ボトルを粉砕したスクラップ(SCR)樹脂等を用いる
ことができる。再生樹脂は、バージン樹脂と同種のもの
を適用することが好ましい。また、再生樹脂としては、
PCR樹脂やSCR樹脂を単独で使用することもでき、
バージン樹脂に同種のPCR樹脂やSCR樹脂を配合し
た樹脂組成物として使用することもできる。さらに、固
有粘度(IV)を上げる場合にはIV値の高い同種の樹
脂を混合し、また、着色して使用する場合には再生樹脂
に着色剤を添加して用いることもできる。On the other hand, the recycled resin used in the present invention includes:
A PCR resin obtained by washing, pulverizing, sorting, and regenerating a bottle collected from the market, a scrap (SCR) resin obtained by pulverizing a defective bottle generated in a bottle production plant, and the like can be used. It is preferable to apply the same type of recycled resin as the virgin resin. Also, as recycled resin,
PCR resin or SCR resin can be used alone,
It can also be used as a resin composition in which the same kind of PCR resin or SCR resin is blended with virgin resin. Further, when the intrinsic viscosity (IV) is increased, the same kind of resin having a high IV value may be mixed, and when the resin is colored and used, a colorant may be added to the regenerated resin.
【0026】[0026]
【実施例】本発明を次の実施例により、具体的に説明す
る。 [外観評価試験]多層ボトルをそれぞれ10本ずつ抽出
して、30℃、90%RHの条件下で3週間保存し、多
層ボトルの底部中心部分における白化及びクレーズの有
無を目視により観察し、発生本数を調べた。 [剥離試験]多層ボトルの胴部を幅15mm、長さ50
mmの短冊状片に切り取り、この短冊状片の一端を一部
剥離して、Tピール強度測定機「テンシロン」にて剥離
強度を測定した。 [耐衝撃性試験]500ccの水を入れて密封した多層
ボトルを、高さ120cmからコンクリート床上に垂直
落下させて、破損したボトルの本数を調べた。EXAMPLES The present invention will be specifically described with reference to the following examples. [Appearance Evaluation Test] Ten multi-layer bottles were extracted and stored at 30 ° C. and 90% RH for 3 weeks, and the center of the bottom of the multi-layer bottle was visually inspected for whitening and craze for occurrence. The number was checked. [Peeling test] The body of the multilayer bottle was 15 mm in width and 50 in length.
mm, and one end of the strip was partially peeled off, and the peel strength was measured with a T-peel strength measuring machine “Tensilon”. [Impact resistance test] A multilayer bottle sealed by adding 500 cc of water was vertically dropped on a concrete floor from a height of 120 cm, and the number of damaged bottles was examined.
【0027】(実施例1)市場から回収したPET容器
を再生処理してなる固有粘度0.72dl/gのPCR
樹脂を、ダイ温度270℃、樹脂圧力が70kgf/c
m2の条件で押出機より溶融押出し、9gのPCR樹脂
塊Aを雌型内に供給する。次いで、別の押出機より固有
粘度0.82dl/gのバージンのPET樹脂を同様の
条件で溶融押出し、前記雌型内にあるPCR樹脂塊Aの
上に16gのPET樹脂塊Bを供給する。この雌型内に
ある複合樹脂塊を雄型と共同作用によって型締め圧力1
00kgf/cm2の条件で多層圧縮成形を行い、胴部
における外層の平均厚さが1.38mmのPCR樹脂、
胴部における内層の胴部平均厚さが1.62mmのバー
ジンのPET樹脂で、プリフォーム全体の重量が25.
0g、ネックリングを含む口頸部の重量が5.5gであ
る2層プリフォームを製造した。このプリフォームの目
付量は25gであり、PCR樹脂の割合は約36重量%
であった。(Example 1) PCR having an intrinsic viscosity of 0.72 dl / g obtained by regenerating a PET container recovered from the market
Die temperature 270 ° C, resin pressure 70kgf / c
Conditions melt from an extruder at an extrusion of m 2, and supplies the PCR resin mass A of 9g into the female mold. Next, a virgin PET resin having an intrinsic viscosity of 0.82 dl / g is melt-extruded from another extruder under the same conditions, and 16 g of the PET resin block B is supplied onto the PCR resin block A in the female mold. The composite resin mass in the female mold is cooperated with the male mold to form a mold clamping pressure of 1
A multilayer compression molding is performed under the condition of 00 kgf / cm 2 , and the average thickness of the outer layer in the body is 1.38 mm,
Virgin PET resin having an average body thickness of 1.62 mm in the inner layer of the body, and the weight of the entire preform is 25.
A two-layer preform having a weight of 5.5 g at the mouth and neck including the neck ring was produced. The basis weight of this preform is 25 g, and the proportion of the PCR resin is about 36% by weight.
Met.
【0028】(比較例1)射出機よりPET樹脂を射出
ノズルの温度を280℃、樹脂圧力250kgf/cm
2の条件で金型内に射出成形して、胴部における平均厚
さが1.62mmのバージンのPET樹脂からなる内層
用中間体を成形する。次いで、PCR樹脂を別の射出機
より前記内層用中間体の外面に射出成形して、胴部にお
ける外層の平均厚さが1.38mmである2層プリフォ
ームを製造した。このプリフォームの目付量は25gで
あり、PCR樹脂の割合は約36重量%であった。尚、
ゲート部は1mm以内に切断した。Comparative Example 1 PET resin was injected from an injection machine at an injection nozzle temperature of 280 ° C. and a resin pressure of 250 kgf / cm.
Injection molding is performed in a mold under the conditions of 2 , to form an intermediate for an inner layer made of virgin PET resin having an average thickness of 1.62 mm in the body. Next, the PCR resin was injection-molded on the outer surface of the intermediate for an inner layer by another injection machine to produce a two-layer preform in which the average thickness of the outer layer in the body was 1.38 mm. The basis weight of this preform was 25 g, and the proportion of the PCR resin was about 36% by weight. still,
The gate was cut within 1 mm.
【0029】実施例1及び比較例1の2層プリフォーム
用いて、PET樹脂のガラス転移点以上融点以下である
110℃の延伸適温に加熱し、このプリフォームを60
℃に加熱された成形金型内にセットして二軸延伸ブロー
成形を行い、内容量が500ccの2層ボトルを得た。The two-layer preforms of Example 1 and Comparative Example 1 were heated to an appropriate stretching temperature of 110 ° C., which was equal to or higher than the glass transition point of the PET resin and lower than the melting point.
The mixture was set in a molding die heated to 0 ° C. and subjected to biaxial stretch blow molding to obtain a two-layer bottle having a content of 500 cc.
【0030】これらの多層プリフォーム及び多層ボトル
の評価結果を表1に示す。Table 1 shows the evaluation results of these multilayer preforms and multilayer bottles.
【表1】 [Table 1]
【0031】実施例1の多層プリフォームを用いて製造
した多層ボトルでは、底部中央部分における白化やクレ
ーズの発生がなく、内層と外層との間の層間剥離も発生
せず、また、ゲート部も存在しないため、良好な外観特
性を有した。一方、比較例1の多層プリフォームを用い
て製造した多層ボトルでは、底部中央部分、特にゲート
部付近においてクレーズは発生して乳白色に白化し、層
間強度も低下し、ゲート部が中心からずれている容器も
存在した。In the multi-layer bottle manufactured using the multi-layer preform of Example 1, no whitening or craze occurs at the center of the bottom, no delamination between the inner layer and the outer layer occurs, and the gate portion is not formed. Since it did not exist, it had good appearance characteristics. On the other hand, in the multi-layer bottle manufactured using the multi-layer preform of Comparative Example 1, craze occurs at the bottom center part, particularly near the gate part, whitens to milky white, the interlayer strength decreases, and the gate part shifts from the center. Some containers were present.
【0032】[0032]
【発明の効果】本発明によれば、再生樹脂からなる溶融
樹脂塊の所定量を雌型内の下方に供給し、その上方にバ
ージン樹脂からなる溶融樹脂塊の所定量を供給して、雄
型及びネック型を用いて圧縮成形することによって、再
生樹脂の割合が多くても透明性が良好で、底部の白化も
なく、ゲート部ないしゲート部跡が存在せず、ゲート部
の切断工程が不要であり、底部中心も滑らかで均質であ
り、かつ口頸部及びネックリング部がバージン樹脂のみ
からなる多層プリフォームを得ることできる。According to the present invention, a predetermined amount of a molten resin mass made of a recycled resin is supplied to the lower part of a female mold, and a predetermined amount of a molten resin mass made of a virgin resin is supplied above the same. By compression molding using a mold and a neck mold, even if the ratio of the recycled resin is large, the transparency is good, there is no whitening of the bottom, there is no gate or gate trace, and the gate cutting process is not performed. A multi-layer preform is unnecessary, the center of the bottom is smooth and uniform, and the neck and neck and the neck ring are made of only virgin resin.
【図1】本発明によって製造された多層プリフォームの
断面図である。FIG. 1 is a cross-sectional view of a multilayer preform manufactured according to the present invention.
【図2】本発明の溶融樹脂塊Aを供給する工程を示す一
部断面図である。FIG. 2 is a partial cross-sectional view showing a step of supplying a molten resin mass A of the present invention.
【図3】本発明の溶融樹脂塊Bを供給する工程を示す一
部断面図である。FIG. 3 is a partial cross-sectional view showing a step of supplying a molten resin block B of the present invention.
【図4】本発明の圧縮成形工程における成形前の工程を
示す一部断面図である。FIG. 4 is a partial cross-sectional view showing a step before molding in a compression molding step of the present invention.
【図5】本発明の圧縮成形工程における成形後の工程を
示す一部断面図である。FIG. 5 is a partial cross-sectional view showing a step after molding in the compression molding step of the present invention.
1 多層プリフォーム 6 内層 7 外層 11a、11b ダイヘッド 13 雌型 14 雄型 15 ネック型 DESCRIPTION OF SYMBOLS 1 Multilayer preform 6 Inner layer 7 Outer layer 11a, 11b Die head 13 Female type 14 Male type 15 Neck type
フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B29L 9:00 B29L 9:00 Fターム(参考) 4F201 AA24 AA50 AG03 AG07 BA03 BC01 BC02 BC12 BC21 BC25 BM07 BM13 4F208 AA24 AA50 AG03 AG07 LA08 LB01 LG03 LG06 LG13 LG32Continued on the front page (51) Int.Cl. 7 Identification code FI Theme coat II (reference) B29L 9:00 B29L 9:00 F term (reference) 4F201 AA24 AA50 AG03 AG07 BA03 BC01 BC02 BC12 BC21 BC25 BM07 BM13 4F208 AA24 AA50 AG03 AG07 LA08 LB01 LG03 LG06 LG13 LG32
Claims (9)
なる内層を有する多層プリフォームにおいて、多層プリ
フォームの全体の重量をW、ネックリングを含む口頸部
の重量をX、多層プリフォームの外層の厚さをTo及び
内層の厚さをTi、外層の重量比率をYとするとき、下
記式、 Y=〔(W−X)/W〕×〔To/(To+Ti)〕×
100(%) で表される外層の重量比率(Y)が25〜65%である
ことを特徴とする多層プリフォーム。1. A multilayer preform having an outer layer made of a recycled resin and an inner layer made of a virgin resin, wherein the total weight of the multilayer preform is W, the weight of the mouth and neck including the neck ring is X, and the outer layer of the multilayer preform is Where To is the thickness of the inner layer, Ti is the thickness of the inner layer, and Y is the weight ratio of the outer layer, Y = [(W−X) / W] × [To / (To + Ti)] ×
A multilayer preform, wherein a weight ratio (Y) of the outer layer represented by 100 (%) is 25 to 65%.
グの下で終わっている請求項1に記載の多層プリフォー
ム。2. The multilayer preform according to claim 1, wherein the outer layer tip terminates under a neck ring below the mouth and neck.
主体とするポリエステル樹脂で、再生樹脂がエチレンテ
レフタレートを主体とするポリエステル樹脂からなるポ
ストコンシューマーリサイクル樹脂である請求項1また
は2に記載の多層プリフォーム。3. The multilayer preform according to claim 1, wherein the virgin resin is a polyester resin mainly composed of ethylene terephthalate, and the regenerated resin is a post-consumer recycled resin composed of a polyester resin mainly composed of ethylene terephthalate.
い請求項1ないし3の何れかに記載の多層プリフォーム
の製造方法。4. The method for producing a multilayer preform according to claim 1, wherein no gate portion or gate mark is present at the bottom.
なる溶融樹脂塊Aを雌型内に供給し、次いでバージン樹
脂を溶融押出して所定量を切断してなる溶融樹脂塊Bを
前記雌型内の溶融樹脂塊Aの上に供給した後、雌型内に
雄型を圧入して溶融樹脂塊Aが外層を形成し、溶融樹脂
塊Bが内層を形成するように圧縮成形することを特徴と
する多層プリフォームの製造方法。5. A molten resin mass A obtained by melt-extruding a regenerated resin and cutting a predetermined amount is supplied into a female mold, and then a molten resin mass B obtained by melt-extruding a virgin resin and cutting a predetermined amount is formed. After feeding onto the molten resin mass A in the female mold, the male mold is pressed into the female mold and compression molded so that the molten resin mass A forms the outer layer and the molten resin mass B forms the inner layer. A method for producing a multilayer preform, characterized in that:
主体とするポリエステル樹脂で、再生樹脂がエチレンテ
レフタレートを主体とするポリエステル樹脂からなるポ
ストコンシューマーリサイクル樹脂である請求項5に記
載の多層プリフォームの製造方法。6. The method for producing a multilayer preform according to claim 5, wherein the virgin resin is a polyester resin mainly composed of ethylene terephthalate, and the regenerated resin is a post-consumer recycled resin composed of a polyester resin mainly composed of ethylene terephthalate.
クリングを含む口頸部の重量をX、多層プリフォームの
外層の厚さをTo及び内層の厚さをTi、外層の重量比
率をYとするとき、下記式、 Y=〔(W−X)/W〕×〔To/(To+Ti)〕×
100(%) で表される外層の重量比率(Y)が25〜65%である
請求項5または6に記載の多層プリフォームの製造方
法。7. The overall weight of the multilayer preform is W, the weight of the neck and neck including the neck ring is X, the thickness of the outer layer of the multilayer preform is To, the thickness of the inner layer is Ti, and the weight ratio of the outer layer is Ti. When Y is used, the following equation is used: Y = [(W−X) / W] × [To / (To + Ti)] ×
The method for producing a multilayer preform according to claim 5 or 6, wherein the weight ratio (Y) of the outer layer represented by 100 (%) is 25 to 65%.
グの下で終わっている請求項5ないし7の何れか1項に
記載の多層プリフォームの製造方法。8. The method for producing a multilayer preform according to claim 5, wherein the outer layer tip ends under a neck ring below the mouth and neck.
い請求項5ないし8の何れかに記載の多層プリフォーム
の製造方法。9. The method for producing a multilayer preform according to claim 5, wherein a gate portion or a trace of the gate portion does not exist at the bottom.
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Cited By (10)
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EP1579979A1 (en) * | 2002-10-30 | 2005-09-28 | Toyo Seikan Kaisya, Ltd. | Preform, process for producing the same, and biaxially stretched container obtained from the preform |
WO2006075366A1 (en) * | 2005-01-12 | 2006-07-20 | Toyo Seikan Kaisha, Ltd | Extrusion feed device for composite resin and composite resin lump |
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Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5527201A (en) * | 1978-04-21 | 1980-02-27 | Toppan Printing Co Ltd | Producing process of multi-wall hollow container |
JPH01153453A (en) * | 1987-12-10 | 1989-06-15 | Toyo Seikan Kaisha Ltd | Pressure-and heat-resisting container and production thereof |
JPH03234604A (en) * | 1990-02-13 | 1991-10-18 | Kuwabara Yasunaga | Compression molding |
JPH10337770A (en) * | 1997-06-05 | 1998-12-22 | Toyo Seikan Kaisha Ltd | Multilayer preform with recovery polyester resin layer, its manufacture, and multilayer container molded from the preform |
JPH1177744A (en) * | 1997-09-11 | 1999-03-23 | Toyo Seikan Kaisha Ltd | Preparation of multilayer preform having recovered polyester resin layer and multilayer preform |
JP2000238734A (en) * | 1998-12-25 | 2000-09-05 | Tsutsumi Yotaro | Bottle |
-
2001
- 2001-02-23 JP JP2001048092A patent/JP2002248675A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5527201A (en) * | 1978-04-21 | 1980-02-27 | Toppan Printing Co Ltd | Producing process of multi-wall hollow container |
JPH01153453A (en) * | 1987-12-10 | 1989-06-15 | Toyo Seikan Kaisha Ltd | Pressure-and heat-resisting container and production thereof |
JPH03234604A (en) * | 1990-02-13 | 1991-10-18 | Kuwabara Yasunaga | Compression molding |
JPH10337770A (en) * | 1997-06-05 | 1998-12-22 | Toyo Seikan Kaisha Ltd | Multilayer preform with recovery polyester resin layer, its manufacture, and multilayer container molded from the preform |
JPH1177744A (en) * | 1997-09-11 | 1999-03-23 | Toyo Seikan Kaisha Ltd | Preparation of multilayer preform having recovered polyester resin layer and multilayer preform |
JP2000238734A (en) * | 1998-12-25 | 2000-09-05 | Tsutsumi Yotaro | Bottle |
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KR101041416B1 (en) | 2003-10-22 | 2011-06-15 | 도요 세이칸 가부시키가이샤 | Multilayered molten resin mass, multilayered preform for blow molding formed from the multilayered molten resin mass by compression molding, and multilayered container |
US8157555B2 (en) | 2005-01-12 | 2012-04-17 | Toyo Seikan Kaisha, Ltd. | Extrusion feed device for composite resin and composite resin mass |
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US12017816B2 (en) | 2006-03-06 | 2024-06-25 | Plastipak Packaging, Inc. | Lightweight plastic container and preform |
JP2009539654A (en) * | 2006-06-14 | 2009-11-19 | サクミ コーペラティバ メッカニチ イモラ ソチエタ コーペラティバ | Molded product compression molding equipment |
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KR100868915B1 (en) * | 2007-06-21 | 2008-11-17 | 도요 세이칸 가부시키가이샤 | Extrusion feed device for composite resin and composite resin lump |
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