JPH0788864A - Powder slush molding method - Google Patents

Powder slush molding method

Info

Publication number
JPH0788864A
JPH0788864A JP25902693A JP25902693A JPH0788864A JP H0788864 A JPH0788864 A JP H0788864A JP 25902693 A JP25902693 A JP 25902693A JP 25902693 A JP25902693 A JP 25902693A JP H0788864 A JPH0788864 A JP H0788864A
Authority
JP
Japan
Prior art keywords
temperature
mold
heat medium
temp
refrigerant
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.)
Granted
Application number
JP25902693A
Other languages
Japanese (ja)
Other versions
JP2622075B2 (en
Inventor
Koji Hayashi
公二 林
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsuboshi Belting Ltd
Original Assignee
Mitsuboshi Belting Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsuboshi Belting Ltd filed Critical Mitsuboshi Belting Ltd
Priority to JP5259026A priority Critical patent/JP2622075B2/en
Publication of JPH0788864A publication Critical patent/JPH0788864A/en
Application granted granted Critical
Publication of JP2622075B2 publication Critical patent/JP2622075B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C41/00Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
    • B29C41/34Component parts, details or accessories; Auxiliary operations
    • B29C41/52Measuring, controlling or regulating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C41/00Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
    • B29C41/02Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor for making articles of definite length, i.e. discrete articles
    • B29C41/18Slush casting, i.e. pouring moulding material into a hollow mould with excess material being poured off
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C37/00Component parts, details, accessories or auxiliary operations, not covered by group B29C33/00 or B29C35/00
    • B29C2037/90Measuring, controlling or regulating
    • B29C2037/903Measuring, controlling or regulating by means of a computer

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Moulding By Coating Moulds (AREA)

Abstract

PURPOSE:To obtain proper mold temp. by measuring the temp. of a mold temp. change factor at every process and substituting the measured value for a relational expression of the temp. of the factor preliminarily calculated by multiple regression analysis and the quantity and supply time of a supply heat source and changing the quantity and time of the supply heat source on the basis of the calculated value. CONSTITUTION:In a heating furnace 2, hot air is sprayed on the single surface of a mold 1 from the inner wall of the furnace in a preheating process 1 and sprayed on the upper and rear surfaces of the mold in a process 2'' and sprayed on the single surface of the mold 1 in a process 3' to heat the mold 1 to proper temp. Therefore, the hot air is adjusted by a heating medium supply device Q and a supply time control valve X. In a molding process II, a powder material is bonded to the mold l and, in a curing process III, hot air is sprayed on the mold to control the temp. of the mold so as to hold the same to temp. suitable for curing to perform curing. The temp. of the factor related to the change of mold temp. calculated by multiple regression analysis is substituted for the relational expression of the temp. of the factor, the quantity of a heating medium and the supply time of the heating medium and, on the basis of the calculated value, the quantity Q and time X of the heating medium are adjusted to obtain proper mold temp.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、自動車等のインストル
メントパネルや、ヘッドレスト、アームレスト、又は、
コンソールボックス、その他クッション類や玩具類の表
皮乃至カバーとして使用される樹脂成形品の成形方法で
あるパウダスラッシュ成形方法に係わり、特に、その型
温度の調整方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an instrument panel of an automobile, a headrest, an armrest, or
The present invention relates to a powder slush molding method, which is a molding method of a resin molded product used as a cover or cover of a console box, other cushions and toys, and particularly to a method of adjusting the mold temperature thereof.

【0002】[0002]

【従来の技術】パウダスラッシュ成形方法を図3のグラ
フに基づいて説明する。図3において、横軸に時間の経
過に伴い順次行われる成形の各工程を示し、縦軸に前記
各工程での型温度を示している。パウダスラッシュ成形
方法は、スラッシュ成形型を加熱する予熱工程と、型表
面に樹脂パウダを供給する成形工程と、この樹脂パウダ
を加熱溶融して架橋させて安定した状態に変えるキュア
工程と、キュアされた樹脂を冷却固化する冷却工程と、
固化した樹脂を型から外す脱型工程とを1サイクルとし
て順次繰り返し、製品を成形する。
2. Description of the Related Art A powder slush molding method will be described with reference to the graph of FIG. In FIG. 3, the abscissa axis represents the respective molding steps sequentially performed with the passage of time, and the ordinate axis represents the mold temperature in each of the steps. The powder slush molding method includes a preheating step of heating the slush molding die, a molding step of supplying resin powder to the mold surface, and a curing step of heating and melting the resin powder to crosslink the resin powder to a stable state. A cooling step of cooling and solidifying the resin
A product is molded by sequentially repeating the demolding step of removing the solidified resin from the mold as one cycle.

【0003】この時、良質の成形品を安定して量産する
には、成形型の型温度を各工程毎に一定の適切な温度に
することが重要なポイントとなる。特に、予熱工程では
次工程である成形に適した温度αになるまで予熱し、キ
ュア工程ではキュアに適した温度βを保つように、冷却
工程では次工程である脱型が容易になる温度γにまで下
げるようにしなければならない。そのため、従来のパウ
ダスラッシュ成形方法は、型別に各工程で供給する熱媒
の量若しくは熱媒又は冷媒の供給時間を一律に定めてい
た。
At this time, in order to stably mass-produce high-quality molded products, it is important to set the mold temperature of the mold to a constant and appropriate temperature for each process. In particular, in the preheating step, preheating is performed until the temperature becomes a temperature suitable for molding, which is the next step, and in the curing step, the temperature β that is suitable for curing is maintained. You have to lower it to. Therefore, in the conventional powder slush molding method, the amount of the heat medium to be supplied in each step or the supply time of the heat medium or the refrigerant is uniformly determined for each mold.

【0004】ところが、熱媒の量若しくは熱媒又は冷媒
の供給時間を一律に定めていても、型温度昇降曲線は、
図3中の実線に示すように、夏場と冬場とでは推移する
温度範囲が異なり、予熱後、キュア直前、脱型直前の温
度にかなりの幅α′、β′、γ′が生じ、又、この温度
の幅は、季節のみならず1日内の状況変化によっても生
じる。更に、予熱工程前の型温度においては、型替え直
後や休日、休憩後等の一旦、成形を中断して再開する時
の型温度と、成形サイクルを繰り返し継続中の型温度と
ではかなりちがってくる。そのため、従来のパウダスラ
ッシュ成形方法のように、各工程で供給する熱媒の量若
しくは熱媒又は冷媒の供給時間を型毎に一律に定める方
法では、良質の成形品を安定して量産するために、成形
型の型温度を各工程毎に一定な適切な温度にすることが
困難であった。
However, even if the amount of the heat medium or the supply time of the heat medium or the refrigerant is uniformly set, the mold temperature rising / falling curve is
As shown by the solid line in FIG. 3, the temperature range in which it changes in summer and winter is different, and there are considerable widths α ′, β ′, γ ′ in the temperatures after preheating, immediately before curing, and immediately before demolding. This temperature range is caused not only by the season but also by changes in the conditions within one day. Furthermore, in the mold temperature before the preheating step, there is a considerable difference between the mold temperature when the molding is temporarily stopped and restarted immediately after the mold change, after a holiday, after a break, and the mold temperature during which the molding cycle is repeated. come. Therefore, as in the conventional powder slush molding method, a method of uniformly setting the amount of heat medium to be supplied in each step or the supply time of heat medium or refrigerant for each mold is used for stable mass production of high-quality molded products. In addition, it is difficult to keep the mold temperature of the mold constant and appropriate for each process.

【0005】そこで、採られた従来の型温度調整方法
は、予熱工程後、上昇した型温度を成形前に測定し、成
形に適した許容温度範囲となっている場合にだけ、成形
工程に移り、許容温度範囲を上に越えている場合は、許
容温度範囲内に型温度が下がるまで放置し、又、許容温
度範囲を下に越えた場合は、予熱後の全工程、即ち、成
形工程、キュア工程、冷却工程、脱型工程と空運転する
という方法が採られた。
Therefore, the conventional mold temperature adjusting method adopted is to measure the increased mold temperature after the preheating process and before the molding, and move to the molding process only when the allowable temperature range suitable for the molding is obtained. If the temperature exceeds the allowable temperature range, the mold temperature is left to fall within the allowable temperature range.If the temperature exceeds the allowable temperature range, all the steps after preheating, that is, the molding step, A method of idle operation including a curing step, a cooling step, a demolding step was adopted.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、このよ
うな従来の型温度調整方法では、成形品質の規格が厳し
くなり、許容温度範囲の幅が狭まると、予熱後の許容温
度範囲内に型温度がおさまらないことが頻繁になり、許
容温度範囲内に型温度がおさまるまで、型を放置した
り、空運転したりする回数が増え、稼働率の低下、エネ
ルギーロス等が増大するという問題を有していた。
However, in such a conventional mold temperature adjusting method, when the specification of the molding quality becomes strict and the width of the allowable temperature range is narrowed, the mold temperature falls within the allowable temperature range after preheating. There is a problem that the number of times molds are left unattended or run idle until the mold temperature falls within the allowable temperature range, which reduces the operating rate and increases energy loss, etc. Was there.

【0007】本発明は、上記問題を鑑みてなされたもの
であって、その目的とするところは、成形型の型温度を
各工程毎に一定の適切な温度にすることを容易にし、良
質の成形品を安定して量産することが可能なパウダスラ
ッシュ成形方法を提供するものである。
The present invention has been made in view of the above problems, and it is an object of the present invention to make it easy to set the mold temperature of the molding die to a constant and appropriate temperature for each process, and Provided is a powder slush molding method capable of stably mass-producing molded products.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するため
に本発明のパウダスラッシュ成形方法は、予熱工程、キ
ュア工程、冷却工程とを含み前記各工程で熱媒又は冷媒
を供給しながら製品を成形するパウダスラッシュ成形方
法において、各工程で適切な型温度を得るように、各工
程毎に型温度の昇降に関係する因子の温度を計測し、そ
の計測値を、予め重回帰分析により求められた型温度の
昇降に関係する因子の温度と各工程で供給する熱媒の
量、若しくは熱媒又は冷媒の供給時間との関係式に代入
し、この関係式により各工程で算出された値に基づいて
各工程で供給する熱媒の量、若しくは熱媒又は冷媒の供
給時間を変動させて成形する方法で、前記関係式が、予
熱工程、キュア工程では、熱媒の量又はその供給時間を
型温度と雰囲気温度の二次関数、及び、供給する熱媒温
度、炉内壁温度、材料の温度の一次関数として表したも
のであり、冷却工程では、冷媒の供給時間を雰囲気温度
と冷媒温度の一次関数として表したものである。
In order to achieve the above object, the powder slush molding method of the present invention includes a preheating step, a curing step, and a cooling step to produce a product while supplying a heat medium or a refrigerant in each step. In the powder slush molding method for molding, in order to obtain an appropriate mold temperature in each process, the temperature of a factor related to the rise and fall of the mold temperature is measured in each process, and the measured value is obtained in advance by multiple regression analysis. Substituting in the relational expression between the temperature of the factors related to the rise and fall of the mold temperature and the amount of heat medium supplied in each process, or the supply time of the heat medium or the refrigerant, the value calculated in each process by this relational expression Based on the amount of heat medium to be supplied in each step, or a method of molding by varying the supply time of the heat medium or the refrigerant, the relational expression, in the preheating step, curing step, the amount of heat medium or its supply time. Mold temperature and ambient temperature A quadratic function, and a heating medium temperature to be supplied, a furnace inner wall temperature, and a linear function of the material temperature. In the cooling step, the supply time of the refrigerant is expressed as a linear function of the ambient temperature and the refrigerant temperature. Is.

【0009】[0009]

【作用】上記手段によると、重回帰分析によって、各工
程毎に型温度の昇降に関係する因子の温度と、供給する
熱媒の量、若しくは熱媒又は冷媒の供給時間とが定量的
に関係づけられているので、前記温度因子から各工程で
適切な型温度を得るために必要な熱媒の量、若しくは熱
媒又は冷媒の供給時間を算出することができ、そして前
記算出された値に基づいて各工程で供給する熱媒の量、
若しくは熱媒又は冷媒の供給時間を変動させると、各工
程毎に一定の適切な型温度にすることが容易になる。
According to the above means, the multiple regression analysis quantitatively correlates the temperature of the factors related to the rise and fall of the mold temperature in each step with the amount of the heat medium to be supplied or the supply time of the heat medium or the refrigerant. Since it is attached, it is possible to calculate the amount of heat medium required to obtain an appropriate mold temperature in each step from the temperature factor, or the supply time of the heat medium or the refrigerant, and to the calculated value. Based on the amount of heat medium supplied in each process,
Alternatively, if the supply time of the heat medium or the refrigerant is changed, it becomes easy to maintain a constant and appropriate mold temperature for each process.

【0010】[0010]

【実施例】以下本発明の実施例を図面に基づいて説明す
る。図1は本発明のパウダスラッシュ成形方法の設備形
態の一例である。図1に示す設備は、複数の成形用金型
をオンラインし、I予熱、II成形、IIIキュア、I
V冷却、V脱型と順次搬送を繰り返すことにより成形を
行う方式で、特に、I予熱工程がからの三段階に分
かれているものが示されている。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is an example of the equipment form of the powder slush molding method of the present invention. The equipment shown in FIG. 1 has a plurality of molding dies online, I preheating, II molding, III cure, I
A method of performing molding by repeating V cooling, V demolding, and sequential conveyance, in particular, a method in which the I preheating step is divided into three stages, is shown.

【0011】図1において、1は成形型、2及び3は予
熱及びキュア工程での加熱炉、4は冷却装置、5は材料
であり、加熱炉2のI予熱工程では、成形型1の上下
(表裏)から加熱する加熱炉となっている。そして、成
形型1の型温度を各工程毎に適切な温度にするための装
置として、熱風供給装置Q、上Q、下Q、Q、
Qキと、熱風供給時間を調節するバルブX、上X、
下X、X、Xキと、冷却水供給時間を調節するバル
ブX冷とが設置されている。
In FIG. 1, 1 is a mold, 2 and 3 are heating furnaces in preheating and curing processes, 4 is a cooling device, and 5 is a material. It is a heating furnace that heats from the front and back. Then, hot air supply devices Q, upper Q, lower Q, Q, as devices for making the mold temperature of the mold 1 appropriate for each process.
Q key and valve X, upper X, which adjusts hot air supply time
Lower X, X, X keys and a valve X cooling for adjusting the cooling water supply time are installed.

【0012】型温度の昇降に関係する因子の温度を測定
する温度計としては、各工程直前の型温度を測定するた
めの温度計T1、上T1、下T1、T1、T1
キと、各工程直前での熱媒温度を測定するための温度計
T2、上T2、下T2、T2、T2キと、IV
冷却工程直前での冷媒温度を測定するための温度計T2
冷と、各工程直前での炉内壁の温度を測定するための温
度計T3、上T3、下T3、T3、T3キと、
設備内の雰囲気温度を測定するための温度計T4と、材
料温度を測定するための温度計T5が設置されている。
As a thermometer for measuring the temperature of a factor related to the rise and fall of the mold temperature, a thermometer T1, an upper T1, a lower T1, T1, T1 for measuring the mold temperature immediately before each step is used.
G, a thermometer T2 for measuring the temperature of the heat medium immediately before each step, upper T2, lower T2, T2, T2, and IV
Thermometer T2 for measuring the refrigerant temperature immediately before the cooling process
Cooling, and a thermometer T3 for measuring the temperature of the furnace inner wall immediately before each step, an upper T3, a lower T3, T3, T3 key,
A thermometer T4 for measuring the ambient temperature in the facility and a thermometer T5 for measuring the material temperature are installed.

【0013】上記パウダスラッシュ成形設備では、成形
型1がオンラインされた各工程設備を矢印方向に移動す
る。加熱炉2においては、I予熱工程で成形型1の片
面に炉内壁2aから熱媒である熱風を吹きつけ、I予熱
工程で成形型1の表裏(上下)に炉内壁2aから熱媒
である熱風を吹きつけ、I予熱工程で成形型1の片面
に炉内壁2aから熱媒である熱風を吹きつけるようにし
て、I予熱工程を経ると成形型1が成形に適した
温度αになるように、各工程の熱媒供給装置Q、上Q
、下Q、Qと、熱媒供給時間調節用バルブX、
上X、下X、Xとで熱風が調整されて徐々に昇温
していく。
In the powder slush molding equipment, the molding equipment 1 is moved in the direction of the arrow in each process equipment where the molding die 1 is online. In the heating furnace 2, hot air, which is a heating medium, is blown from one side of the mold 1 in the I preheating step from the furnace inner wall 2a, and the inside and outside (upper and lower) sides of the molding die 1 are heated from the furnace inner wall 2a in the I preheating step. Hot air is blown, and hot air as a heating medium is blown from the furnace inner wall 2a to one surface of the molding die 1 in the I preheating step so that the molding die 1 reaches a temperature α suitable for molding after the I preheating step. In addition, the heat medium supply device Q of each process, the upper Q
, Lower Q, Q and heat medium supply time adjusting valve X,
The hot air is adjusted by the upper X, lower X, and X to gradually raise the temperature.

【0014】次に、II成形工程で、成形に適した温度
αに昇温された成形型1に樹脂パウダの材料5を付着さ
せ、IIIキュア工程において、加熱炉3内で成形型1
に炉内壁3aから熱媒である熱風を吹きつけ、型温度が
キュアに適した温度βを保ように熱媒供給装置Qキ及び
熱媒供給時間調節用バルブXキとで調整しながらキュア
を行う。そして、IV冷却工程で、冷媒供給時間調節用
バルブX冷によって、冷媒である冷却水が調整され脱型
に適した温度γにまで下げられた後、V脱型がされる。
Next, in the II molding step, the resin powder material 5 is attached to the molding die 1 heated to the temperature α suitable for molding, and in the III curing step, the molding die 1 is heated in the heating furnace 3.
Hot air, which is a heat medium, is blown from the furnace inner wall 3a to the mold while adjusting the mold temperature with the heat medium supply device Q and the heat medium supply time adjusting valve X to maintain the temperature β suitable for the cure. To do. Then, in the IV cooling step, the cooling water, which is the refrigerant, is adjusted by the cooling valve X for cooling the refrigerant supply time to be lowered to the temperature γ suitable for demolding, and then the V demolding is performed.

【0015】このようなパウダスラッシュ成形設備での
本発明のパウダスラッシュ成形方法による型温度調整方
法は、重回帰分析における重回帰式から求められた型温
度の昇降に関係する因子の温度と各工程で供給する熱媒
の量、若しくは熱媒又は冷媒の供給時間との関係式であ
る数1に示す関係式に、型温度の昇降に関係する因子の
温度T1、T2、T3、T4、T5を代入し、算出され
た値に基づいて、供給する熱媒の量Q、若しくは熱媒又
は冷媒の供給時間X、X冷を調整するものである。
The mold temperature adjusting method according to the powder slush molding method of the present invention in such a powder slush molding facility has a temperature of a factor related to the rise and fall of the mold temperature obtained from the multiple regression equation in the multiple regression analysis and each step. In the relational expression shown in the equation 1 which is a relational expression with the amount of heat medium supplied in step 1 or the supply time of the heat medium or the refrigerant, The amount Q of the heat medium to be supplied or the supply time X, X cooling of the heat medium or the refrigerant is adjusted based on the calculated value.

【0016】[0016]

【数1】 [Equation 1]

【0017】ここで、T1、T2、T3、T4、T5は
それぞれ、各工程直前の型、熱媒又は冷媒、炉内壁、雰
囲気、材料の型温度に関係する因子を示している。2及
び2′式の熱媒供給時間Xは、算出された1及び1′式
の熱媒供給量Qが最高限度値を越えて供給時間により必
要な熱量を補う場合の式であり、通常、熱媒供時間は所
定値になっている。1式、2式及び1′式、2′式は、
図2に示すように一定の適正な昇降曲線を型温度が描く
ように、後述する重回帰式のT6(工程後の型温度)を
各工程毎の適切な型温度α、β(成形型によって異なる
定数値)に設定して得られたもので、3式も同様に冷却
工程における重回帰式の型温度を冷却工程に適切な型温
度γ(成形型によって異なる定数値)に設定して得られ
たものである。又、上記A、A′、B、B′C、及びa
乃至qそして、a′乃至q′の定数も、重回帰式によっ
て導かれた成形型毎に設定される定数である。
Here, T1, T2, T3, T4, and T5 represent factors related to the mold temperature, the heat medium or the refrigerant, the furnace inner wall, the atmosphere, and the mold temperature immediately before each step, respectively. The heat medium supply time X of the formulas 2 and 2'is a formula in the case where the calculated heat medium supply amount Q of the formulas 1 and 1'exceeds the maximum limit value and supplements the necessary heat amount by the supply time. The heating medium service time is a predetermined value. Formula 1, Formula 2 and Formula 1 ', Formula 2'are
As shown in FIG. 2, T6 (the mold temperature after the process) of the multiple regression equation described later is set to an appropriate mold temperature α, β (depending on the molding mold) so that the mold temperature draws a certain appropriate rising and falling curve. Different constant values) were obtained by setting the mold temperature of the multiple regression equation in the cooling process to the mold temperature γ (constant value that differs depending on the mold) suitable for the cooling process. It has been done. Also, the above A, A ', B, B'C, and a
To q and a ′ to q ′ are also constants set for each mold, which are derived by the multiple regression equation.

【0018】このような本発明のパウダスラッシュ成形
方法によれば、成形型の型温度を各工程毎に一定の適切
な温度にすることが容易になり、その結果、良質の成形
品を安定して量産することが可能である。本発明実施に
より、色規格の厳しい製品、又は、硬度規格の厳しい発
泡パウダスラッシュにおいては、従来よりも不良率が8
%から0.5%に激減し、通常の製品関しては、従来よ
りも不良率が3%から0%に激減した。
According to the powder slush molding method of the present invention as described above, it becomes easy to make the mold temperature of the molding die constant and appropriate for each step, and as a result, a good quality molded product is stabilized. Mass production is possible. By implementing the present invention, in a product with a strict color standard or a foamed powder slash with a strict hardness standard, the defective rate is 8 than that of the conventional product.
% From 0.5% to 0.5%, and with respect to ordinary products, the defective rate has drastically decreased from 3% to 0%.

【0019】又、各測定値の代入、供給する熱媒の量、
若しくは熱媒又は冷媒の供給時間の算出は、各温度計に
接続されたコンピュータによって、各工程毎に瞬時に行
われ、その算出された値に基づいて速やかに熱媒や冷媒
が調整されるようになっているので、予熱後の型温度を
成形に適した許容温度範囲内におさめるために、作業者
が頻繁に各工程で供給する熱媒の量、若しくは熱媒又は
冷媒の供給時間の設定条件を変更してまわる必要がな
い。
Substitution of each measured value, amount of heat medium supplied,
Alternatively, the calculation of the supply time of the heat medium or the refrigerant is instantaneously performed for each process by the computer connected to each thermometer so that the heat medium or the refrigerant can be quickly adjusted based on the calculated value. Therefore, in order to keep the mold temperature after preheating within the allowable temperature range suitable for molding, the operator often sets the amount of heat medium to be supplied in each process, or the supply time of heat medium or refrigerant. There is no need to change the conditions.

【0020】例えば、表1を参照して説明すると、I予
熱工程においては、工程前の型温度T1として温度計
T1によって測定された測定値が代入され、熱媒温度
T2として温度計T2によって測定された測定値が代
入され、炉内壁温度T3としては温度計T3によって
測定された測定値が代入され、雰囲気温度T4として温
度計T4によって測定された測定値が代入され、材料温
度T5として温度計T5によって測定された測定値が代
入され、そして、各測定値の代入によって算出された熱
媒供給量又は時間に基づいて、予熱I工程での熱媒供
装置Q又はバルブXが作動することを示している。
このような作業が本発明のパウダスラッシュ成形方法で
は、各温度計に接続されたコンピュータによって、各工
程毎に瞬時に行われ、その算出された値に基づいて速や
かに熱媒や冷媒が調整されるようになっている。
For example, referring to Table 1, in the I preheating step, the measured value measured by the thermometer T1 is substituted as the mold temperature T1 before the step, and the heat medium temperature T2 is measured by the thermometer T2. The measured value measured by the thermometer T3 is substituted as the furnace inner wall temperature T3, the measured value measured by the thermometer T4 is substituted as the ambient temperature T4, and the thermometer is measured as the material temperature T5. The measurement value measured by T5 is substituted, and the heat medium supplying device Q or the valve X in the preheating I step is operated based on the heat medium supply amount or time calculated by the substitution of each measurement value. Shows.
In the powder slush molding method of the present invention, such a work is instantaneously performed in each step by a computer connected to each thermometer, and the heat medium and the refrigerant are quickly adjusted based on the calculated value. It has become so.

【0021】[0021]

【表1】 [Table 1]

【0022】ここで、各工程毎の型温度の昇降に関係す
る因子の温度と、供給する熱媒の量、若しくは熱媒又は
冷媒の供給時間とを定量的に関係づける関係式の求め方
について説明する。型温度の昇降に関係する因子とし
て、各工程直前の型温度T1と、熱媒又は冷媒温度T2
と、炉内壁の温度T3と、設備内の雰囲気温度T4と、
材料温度T5とを取り上げ、種々の実験を重ねた結果、
熱媒の供給量及び時間は、予熱工程、キュア工程におい
ては、型温度と雰囲気温度の二次関数、及び、供給する
熱媒温度、炉内壁温度、材料の温度の一次関数として表
されることが判明し、冷却工程においては、冷媒の供給
時間を雰囲気温度と冷媒温度の一次関数として表される
ことが判明した。
Here, a method of obtaining a relational expression quantitatively relating the temperature of a factor relating to the rise and fall of the mold temperature in each step and the amount of the heat medium to be supplied or the supply time of the heat medium or the refrigerant explain. As factors related to the rise and fall of the mold temperature, the mold temperature T1 immediately before each process and the heat medium or refrigerant temperature T2
And the temperature T3 of the furnace inner wall and the ambient temperature T4 of the equipment,
Taking the material temperature T5 and repeating various experiments,
In the preheating process and the curing process, the supply amount and time of the heating medium are expressed as a quadratic function of the mold temperature and the ambient temperature, and the heating medium temperature to be supplied, the furnace inner wall temperature, and the material temperature. It has been found that in the cooling step, the supply time of the refrigerant is expressed as a linear function of the ambient temperature and the refrigerant temperature.

【0023】そこで、予熱I工程での重回帰式を T6=D+rQ+sX+tT12 +uT1+vT2+w
T3+xT42 +yT4+zT5 (ここで、T1は工程前の型温度、T6は工程後の型温
度を示し、Dとrからzは重回帰式を満たす定数であ
る。)とし、重回帰式の各工程後の型温度T6に、予熱
I工程後の所望型温度α(成形型により異なる定数)を
設定し、更に、X=(所定時間)を設定して得られたも
のが Q=E−rX−aT12 −bT1−cT2−dT3−eT42 −fT4−gT5 ・・・1式 であり、Q=(最高値)を設定したものが X=B−hT12 −jT1−kT2−lT3−mT42 −nT4−oT5 ・・・2式 である。
Therefore, the multiple regression equation in the preheating I step is given by T6 = D + rQ + sX + tT1 2 + uT1 + vT2 + w
T3 + xT4 2 + yT4 + zT5 (where T1 is the mold temperature before the process, T6 is the mold temperature after the process, and D and r to z are constants that satisfy the multiple regression equation), and after each step of the multiple regression equation Q = E-rX-aT1 is obtained by setting the desired mold temperature α (constant that differs depending on the mold) after the preheating I step to the mold temperature T6 of No. 1 and further setting X = (predetermined time). 2- bT1-cT2-dT3-eT4 2- fT4-gT5 ... 1 formula, and what sets Q = (highest value) is X = B-hT1 2 -jT1-kT2-1T3-mT4 2 -nT4 -OT5 ... It is a 2 type | formula.

【0024】IIIキュア工程において用いられる1′
式及び2′式は、上記重回帰式のT6にIIIキュア工
程の所望型温度β(成形型により異なる定数)を設定
し、更に、X=(所定時間)を設定したものが1′式で
あり、Q=(最高値)を設定したものが2′式である。
IV冷却工程において用いられる3式も同様に冷却工程
における重回帰式の型温度を冷却工程に適切な型温度γ
(成形型によって異なる定数値)に設定して求められ
る。ここで、上記A、A′、B、B′C、及びa乃至q
そして、a′乃至q′は成形型毎に設定される定数であ
る。
III 'used in the III cure process
The formulas and 2'formulas are 1'formulas in which the desired mold temperature β (constant that differs depending on the molding mold) of the III curing process is set in T6 of the above multiple regression formula and further X = (predetermined time) is set. Yes, there is a formula 2'when Q = (highest value) is set.
Similarly, for the three equations used in the IV cooling step, the mold temperature of the multiple regression equation in the cooling step is set to the mold temperature γ suitable for the cooling step.
(Constant value that differs depending on the molding die). Here, A, A ′, B, B′C, and a to q
Then, a'to q'are constants set for each mold.

【0025】尚、成形型の型温度を各工程毎に適切な温
度にするための調節方式としては、熱媒に熱風のみなら
ずオイル、金属粉等を使用して型を加熱する方式におい
ても、又、パウダスラッシュ成形方法の設備形態が、上
記記載のオンライン方式と異なり、各型固有に加熱、冷
却媒体経路、調整機能を有し、専属の回転装置にて材料
を供給スラッシュ成形するモジュール方式においても、
各工程毎に、型温度の昇降に関係する因子の温度を測定
し、その測定値を重回帰分析によって得られた関係式に
代入して熱媒の量、若しくは熱媒又は冷媒の供給時間を
算出し、その算出値に基づいて、前記各工程毎の供給す
る熱媒の量、若しくは熱媒又は冷媒の供給時間を変動さ
せ調節すると、成形型の型温度を各工程毎に一定の適切
な温度にすることが容易になる。
As a method of adjusting the mold temperature of the molding mold to an appropriate temperature for each step, not only hot air but also oil, metal powder or the like is used as a heating medium to heat the mold. In addition, the equipment form of the powder slush molding method is different from the online system described above, and has a heating, cooling medium path and adjusting function unique to each mold, and a modular system for supplying slush molding with a dedicated rotating device Even in
For each step, measure the temperature of the factors related to the rise and fall of the mold temperature, and substitute the measured value into the relational expression obtained by multiple regression analysis to determine the amount of heat medium or the supply time of heat medium or refrigerant. If the amount of the heat medium to be supplied in each of the steps, or the supply time of the heat medium or the refrigerant is varied and adjusted based on the calculated value, the mold temperature of the molding die is adjusted to a certain appropriate value for each step. Easy to reach temperature.

【0026】[0026]

【発明の効果】このように、本発明のパウダスラッシュ
成形方法は、各工程で適切な型温度を得るために必要な
熱媒の量、若しくは熱媒又は冷媒の供給時間が、重回帰
分析によって定量的に関係づけられた型温度の昇降に関
係する因子の温度から算出でき、その算出値に基づい
て、前記各工程毎の供給する熱媒の量、若しくは熱媒又
は冷媒の供給時間を変動させているので、成形型の型温
度を各工程毎に一定の適切な温度にすることが容易にな
り、その結果、良質の成形品を必要最小限のエネルギー
で安定して量産することが可能である。
As described above, according to the powder slush molding method of the present invention, the amount of the heat medium necessary to obtain an appropriate mold temperature in each step, or the supply time of the heat medium or the refrigerant is determined by multiple regression analysis. It can be calculated from the temperature of a factor related to the rise and fall of the mold temperature that is quantitatively related, and based on the calculated value, the amount of heat medium supplied for each process, or the supply time of the heat medium or refrigerant is changed. As a result, it becomes easy to set the mold temperature to a constant and appropriate temperature for each process, and as a result, it is possible to stably mass-produce high-quality molded products with the minimum required energy. Is.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明実施のパウダスラッシュ成形方法の設備
を示す図である。
FIG. 1 is a diagram showing equipment of a powder slush molding method according to the present invention.

【図2】本発明における型温度昇降曲線を示すグラフで
ある。
FIG. 2 is a graph showing a mold temperature rise / fall curve in the present invention.

【図3】従来の型温度昇降曲線を示すグラフである。FIG. 3 is a graph showing a conventional mold temperature rise / fall curve.

【符号の説明】[Explanation of symbols]

1 成形型 2、3 加熱炉 4 冷却装置 5 材料 I 予熱工程 II 成形工程 III キュア工程 IV 冷却工程 V 脱型工程 T1、上T1、下T1、T1、T1キ 型温度
計 T2、上T2、下T2、T2、T2キ 熱媒温
度計 T2冷 冷媒温度計 T3、上T3、下T3、T3、T3キ 炉内壁
温度計 T4 雰囲気温度計 T5 材料温度計 Q、上Q、下Q、Q、Qキ 熱風供給装置 X、上X、下X、X、Xキ、X冷 バルブ
1 Mold 2, 3 Heating Furnace 4 Cooling Device 5 Material I Preheating Process II Molding Process III Cure Process IV Cooling Process V Demolding Process T1, Upper T1, Lower T1, T1, T1 Key Thermometer T2, Upper T2, Lower T2, T2, T2 key heat medium thermometer T2 cold refrigerant thermometer T3, upper T3, lower T3, T3, T3 key furnace inner wall thermometer T4 atmosphere thermometer T5 material thermometer Q, upper Q, lower Q, Q, Q Hot air supply device X, upper X, lower X, X, X key, X cold valve

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 予熱工程、キュア工程、冷却工程とを含
み前記各工程で熱媒又は冷媒を供給しながら製品を成形
するパウダスラッシュ成形方法において、各工程で適切
な型温度を得るように、各工程毎に型温度の昇降に関係
する因子の温度を計測し、その計測値を、予め重回帰分
析により求められた型温度の昇降に関係する因子の温度
と各工程で供給する熱媒の量、若しくは熱媒又は冷媒の
供給時間との関係式に代入し、この関係式により各工程
で算出された値に基づいて各工程で供給する熱媒の量、
若しくは熱媒又は冷媒の供給時間を変動させるパウダス
ラッシュ成形方法。
1. A powder slush molding method, comprising a preheating step, a curing step, and a cooling step, for molding a product while supplying a heat medium or a refrigerant in each of the steps so as to obtain an appropriate mold temperature in each step, The temperature of the factor related to the rise and fall of the mold temperature is measured for each process, and the measured value is the temperature of the factor related to the rise and fall of the mold temperature previously obtained by the multiple regression analysis and the heat medium supplied in each process. Substituting in the relational expression with the amount, or the heating medium or the supply time of the refrigerant, the amount of the heating medium supplied in each step based on the value calculated in each step by this relational expression,
Alternatively, a powder slush molding method in which the supply time of the heat medium or the refrigerant is varied.
【請求項2】 重回帰分析により求められた型温度の昇
降に関係する因子の温度と各工程で供給する熱媒の量、
若しくは熱媒又は冷媒の供給時間との関係式が、予熱工
程、キュア工程では、熱媒の供給量又はその供給時間
を、型温度と雰囲気温度の二次関数、及び、供給する熱
媒温度、炉内壁温度、材料の温度の一次関数として表し
たものであり、冷却工程では、冷媒の供給時間を雰囲気
温度と冷媒温度の一次関数として表したものである請求
項1記載のパウダスラッシュ成形方法。
2. The temperature of a factor related to the rise and fall of the mold temperature obtained by multiple regression analysis and the amount of heat medium supplied in each step,
Alternatively, the relational expression with the supply time of the heat medium or the refrigerant, in the preheating step, the curing step, the supply amount of the heat medium or its supply time is a quadratic function of the mold temperature and the ambient temperature, and the heat medium temperature to be supplied, The powder slush molding method according to claim 1, wherein the temperature is expressed as a linear function of the furnace inner wall temperature and the material temperature, and in the cooling step, the supply time of the refrigerant is expressed as a linear function of the ambient temperature and the refrigerant temperature.
JP5259026A 1993-09-21 1993-09-21 Powder slush molding method Expired - Fee Related JP2622075B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5259026A JP2622075B2 (en) 1993-09-21 1993-09-21 Powder slush molding method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5259026A JP2622075B2 (en) 1993-09-21 1993-09-21 Powder slush molding method

Publications (2)

Publication Number Publication Date
JPH0788864A true JPH0788864A (en) 1995-04-04
JP2622075B2 JP2622075B2 (en) 1997-06-18

Family

ID=17328318

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2622075B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998042487A1 (en) * 1997-03-21 1998-10-01 Remcon Plastics, Inc. Rotational molding apparatus using infrared thermometry feedback
WO2018025442A1 (en) * 2016-08-02 2018-02-08 株式会社仲田コーティング Powder slush molding machine and powder slush molding method

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61127315A (en) * 1984-11-21 1986-06-14 エク‐セル‐オー・コーポレーシヨン Method and device for molding article from heat fusion material
JPH04355108A (en) * 1991-06-03 1992-12-09 Honda Motor Co Ltd Temperature control of molding tool

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61127315A (en) * 1984-11-21 1986-06-14 エク‐セル‐オー・コーポレーシヨン Method and device for molding article from heat fusion material
JPH04355108A (en) * 1991-06-03 1992-12-09 Honda Motor Co Ltd Temperature control of molding tool

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998042487A1 (en) * 1997-03-21 1998-10-01 Remcon Plastics, Inc. Rotational molding apparatus using infrared thermometry feedback
US6036897A (en) * 1997-03-21 2000-03-14 Remcon Plastics, Inc. Rotational molding apparatus and method using infrared thermometry
WO2018025442A1 (en) * 2016-08-02 2018-02-08 株式会社仲田コーティング Powder slush molding machine and powder slush molding method
JPWO2018025442A1 (en) * 2016-08-02 2019-03-14 株式会社仲田コーティング Powder slush molding machine and powder slush molding method

Also Published As

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