JPS58104712A - Mixed solution supply device - Google Patents

Mixed solution supply device

Info

Publication number
JPS58104712A
JPS58104712A JP56180308A JP18030881A JPS58104712A JP S58104712 A JPS58104712 A JP S58104712A JP 56180308 A JP56180308 A JP 56180308A JP 18030881 A JP18030881 A JP 18030881A JP S58104712 A JPS58104712 A JP S58104712A
Authority
JP
Japan
Prior art keywords
tank
mixed solution
supply
supply pipe
mixed liquid
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
JP56180308A
Other languages
Japanese (ja)
Other versions
JPS6243845B2 (en
Inventor
Yukio Komura
幸夫 香村
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.)
Furukawa Electric Co Ltd
Original Assignee
Furukawa Electric Co 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 Furukawa Electric Co Ltd filed Critical Furukawa Electric Co Ltd
Priority to JP56180308A priority Critical patent/JPS58104712A/en
Publication of JPS58104712A publication Critical patent/JPS58104712A/en
Publication of JPS6243845B2 publication Critical patent/JPS6243845B2/ja
Granted 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/285Feeding the extrusion material to the extruder
    • B29C48/286Raw material dosing
    • 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/285Feeding the extrusion material to the extruder
    • B29C48/29Feeding the extrusion material to the extruder in liquid form
    • 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/0005Condition, form or state of moulded material or of the material to be shaped containing compounding ingredients

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Abstract

PURPOSE:To prevent mixed solution from stagnating in the supply pipe, in a mixed solution supply device, by a method wherein a return pipe is provided to connect a point near the end of a supply pipe for mixed solution from a tank to the point to be supplied with the tank so that the mixed solution flows through a circulating passage. CONSTITUTION:In a mixed solution supply device, a mixed solution supply pipe 10 for connecting the bottom of a tank 2 with an extruder cylinder 9 is provided in order to supply a mixed solution 1 from the tank 2 to the extruder 8. A mixed solution supply pump 11 is provided in the middle of this supply pipe 10 to supply the solution 1 by a fixed amount. A return pipe 12 is connected between a point near the end of the supply pipe 10 and the tank 2 and when the solution 1 is not supplied to the extruder 8, the solution 1 is returned to the tank 2. In this manner, the component of the mixed solution is prevented from accumulating and stagnating in the supply pipe.

Description

【発明の詳細な説明】 本発明は比重の異なる複数成分の混合液の供給装置に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for supplying a liquid mixture of a plurality of components having different specific gravities.

例えば、架橋ケーブルを製造する押出機には、架橋剤と
老化防止剤とを供給し1.これらを押出機シリンダー内
で押出用プラスチック材と混練してケーブル導体の外周
に押出すようになっている。
For example, an extruder for producing a crosslinked cable is supplied with a crosslinking agent and an anti-aging agent.1. These are kneaded with an extrusion plastic material in an extruder cylinder and extruded onto the outer periphery of the cable conductor.

この場合、架橋剤として使われ′Cいる例えばジク建ル
バーオキサイドの融点は約40℃、比、重はα984(
70°C)であり、老化防止剤として使われている例え
ば4 、4’−チオビス(6−ターシャルブチル−5−
メチルフェノール)の融点は約170℃、比重は1.0
7 (70℃)であり、これら両者をタンク内で約70
℃に加熱すると、相溶効果により老化防止剤も溶融する
。この混合液をタンク内で攪拌しつつ供給管を経て押出
機シリンダーに供給するのであるが、ラインの停止時等
の混合液の供給停止時に融点の高い老化防止剤が供給管
内で析出し、供給管が詰ま9易い欠点がある。
In this case, the melting point of the dichloromethane used as a crosslinking agent, for example, is about 40°C, and the specific weight is α984 (
For example, 4,4'-thiobis(6-tertbutyl-5-
The melting point of methylphenol is approximately 170℃, and the specific gravity is 1.0.
7 (70℃), and both of these were heated in a tank at about 70℃.
When heated to ℃, the anti-aging agent also melts due to the compatibility effect. This mixed solution is fed into the extruder cylinder through the supply pipe while being stirred in the tank, but when the supply of the mixed solution is stopped, such as when the line is stopped, the anti-aging agent with a high melting point precipitates in the supply pipe. The disadvantage is that the pipes are easily clogged.

本発明の目的は、供給管内での混合液の詰まりを防止で
きる混合液供給装置を提供するにある。
An object of the present invention is to provide a mixed liquid supply device that can prevent clogging of the mixed liquid in a supply pipe.

本発明に係る混合液供給装置社、タンクから被供給箇所
に混合液を供給する供給管の末端寄りの箇所とタンクと
を結ぶリターン管を設け、供給管→リターン管→タンク
からなる循環路に混合液を流し、供給管内に混合液が詰
らないようにしたも、、のである。
The mixed liquid supply equipment company according to the present invention provides a return pipe that connects the tank and a point near the end of the supply pipe that supplies the mixed liquid from the tank to the supplied location, and connects the tank to the circulation path consisting of the supply pipe → return pipe → tank. Even if you let the mixed liquid flow and make sure that the mixed liquid does not clog the supply pipe.

以下本発FII4t−押出様の架橋剤と老化防止剤との
混合液の供給装置に適用したsm例により詳細に説明す
る。第1図に示すように本実施例の混合液供給装置は、
架橋剤と老化防止剤との混合液It収容するタンク2を
有し、このタンク2の外周には加熱ジャケットるが鋏着
され、この加熱ジャケラ)MKは配管4,5を経て温水
勢の加熱媒体が循環して供給され、タンク2内の混合液
1の加熱を行うようになっている。加熱ジャケットるの
外11には熱が逃げないように保温材6が被覆されてい
る・混合液1は攪拌機7で攪拌されるようになっている
。タンク2から押出機8に混合液を供給するためにタン
ク2の゛庭部と押出機シリンダー9とをつなぐ混合液供
給管10が設けられ、この供給管10の途中には混合液
供給ポンプ11が設けられ、混合液1が一定量ずつ供給
されるようになっている。供給管10の末端寄シの筒所
とタンク2との間には、リターン管12が接続され、押
出機8に混合液1會供給しないときその混合液1をタン
ク1に戻すようになっている。リターン管12の分岐接
続箇所より末端側即ち押出機シリンダー9側の供給管1
0と、リターン管12の途中(例えば分岐接続箇所寄シ
の位置)とにはそれぞれメイン切換弁14とリターン切
換弁16とが接続され、これら切換弁15.14は弁制
御器15゜16によp制御されるようになっている。
The present invention will be described in detail below using an example of SM applied to a feeding device for a mixed liquid of a crosslinking agent and an anti-aging agent in the FII4t-extrusion type according to the present invention. As shown in FIG. 1, the mixed liquid supply device of this example is as follows:
It has a tank 2 containing a mixture of a cross-linking agent and an anti-aging agent, and a heating jacket is attached to the outer circumference of the tank 2. A medium is circulated and supplied to heat the mixed liquid 1 in the tank 2. The outside 11 of the heating jacket is covered with a heat insulating material 6 to prevent heat from escaping.The mixed liquid 1 is stirred by a stirrer 7. In order to supply the mixed liquid from the tank 2 to the extruder 8, a mixed liquid supply pipe 10 is provided that connects the garden part of the tank 2 and the extruder cylinder 9, and a mixed liquid supply pump 11 is installed in the middle of this supply pipe 10. is provided, and the mixed liquid 1 is supplied in a fixed amount at a time. A return pipe 12 is connected between the tube at the end of the supply pipe 10 and the tank 2, and is configured to return the mixed liquid 1 to the tank 1 when the mixed liquid 1 is not supplied to the extruder 8. There is. The supply pipe 1 on the end side of the branch connection point of the return pipe 12, that is, on the side of the extruder cylinder 9
A main switching valve 14 and a return switching valve 16 are connected to the terminal 0 and the middle of the return pipe 12 (for example, at a position near a branch connection point). It is designed to be closely controlled.

さて、スタート時にはリターン切換弁16は一度が例え
ば第2図に示すように制御し、メイン切換弁14は開度
が例えば第5図に示すように制御する。即ち、ポンプ1
1によって押出機8に供給される混合液1の流量は一定
であ)、スタート時からT1時間の間はリターン管12
のみに混合液1を流し、混合液1を循環させる。そして
、11時間俵にメイン切換弁14を開くにつれてリター
ン切換弁するを徐々に閉じてTm時間後にはリターン切
換弁16を完全に閉じて混合液1を押出機8に総て供給
するようにする。
Now, at the time of starting, the return switching valve 16 is controlled once as shown in FIG. 2, for example, and the opening degree of the main switching valve 14 is controlled as shown in FIG. 5, for example. That is, pump 1
The flow rate of the mixed liquid 1 supplied to the extruder 8 by the extruder 1 is constant), and the return pipe 12 is
Flow the mixed liquid 1 through the pipes and circulate the mixed liquid 1. Then, as the main switching valve 14 is opened for 11 hours, the return switching valve is gradually closed, and after Tm time, the return switching valve 16 is completely closed to supply all of the mixed liquid 1 to the extruder 8. .

実験例1 ポンプ11の流量をt0t/mとしてライン停□やは、
イ、扁、換弁14を閉じ、’)p−’切換弁16を開い
て混合液1を循環させ、ラインのスタート時からポンプ
11の流量を2.0t/IIIIとして、第2図、第5
図の流量−IIIK従った弁操作は弁制御器15.16
により行つ九、この場合は、’r4 m5〜4分、T雪
−’〜2分とした。押出機8は内径115■φのものを
用い、押出材料はポ・リエチレンを使用し、架橋剤はジ
クミルバーオキサイド、老化防止剤は4,4′−チオビ
ス(6−ターシャルブチル−5−メチルフェノール)を
使用した。
Experimental example 1 The flow rate of the pump 11 is set to t0t/m, and the line is stopped □ or
A, close the switch valve 14, open the 'p-' switch valve 16 to circulate the mixed liquid 1, set the flow rate of the pump 11 to 2.0t/III from the start of the line,
Figure Flow Rate - IIIK The valve operation according to the valve controller 15.16
In this case, 'r4 m5 ~ 4 minutes, T snow ~ 2 minutes. The extruder 8 used had an inner diameter of 115 mm, the extrusion material used was polyethylene, the crosslinking agent was dicumyl peroxide, and the anti-aging agent was 4,4'-thiobis(6-tert-butyl-5- methylphenol) was used.

実験例2 ラインの停止時にはポンプ11を止め、ラインのスター
ト時からポンプ11を動かした。この際、タンク2.供
給管10.リターン管12はスタート時には十分加熱し
、リターン切換弁18を開き、メイン切換弁14を閉じ
良、このようにして供給管10中KtIF、出或は堆積
している拠金fillをリターン管12を通してタンク
2内に戻し、新−良な混合液1をタンク2−供給管10
−リターン管12なる循環路に循環させて供給管10を
漬浸化し、その後、リターン切換弁1δを閉じ、メイン
切換弁14を開いて混合液1を押出機8に供給し良。
Experimental Example 2 The pump 11 was stopped when the line stopped, and the pump 11 was started when the line started. At this time, tank 2. Supply pipe 10. The return pipe 12 is sufficiently heated at the start, the return switching valve 18 is opened, and the main switching valve 14 is closed. Return to tank 2 and add new good mixed liquid 1 to tank 2 - supply pipe 10
- The supply pipe 10 is immersed by circulating through the return pipe 12, and then the return switching valve 1δ is closed and the main switching valve 14 is opened to supply the mixed liquid 1 to the extruder 8.

この場合、7.=1Q分、T3−5〜4分とし九・押出
機8は内径115■φのものを用い、押出材料紘ポリエ
チレンを使用し、架橋剤はジクミルバーオキサイド、老
化防止材は4.4′−チオビス(6−ターシャルブチル
−3−メチルフェノール)を使用しえ。老化防止剤は架
橋剤内1(1/10  の割合で混入した。
In this case, 7. = 1Q minute, T3-5 to 4 minutes. 9. The extruder 8 has an inner diameter of 115 mm, the extrusion material is Hiropolyethylene, the crosslinking agent is dicumyl peroxide, and the anti-aging material is 4.4' - Thiobis(6-tert-butyl-3-methylphenol) may be used. The anti-aging agent was mixed into the crosslinking agent at a ratio of 1/10.

上記実施例では押出機用の混合液供給装置について説明
したが、本発明はこれに限定されるものではなく、例え
ばインクジェット式印刷機への顔料系インクの供給装置
にも同様に適用することができる。
Although the above embodiment describes a mixed liquid supply device for an extruder, the present invention is not limited thereto, and can be similarly applied to, for example, a pigment-based ink supply device to an inkjet printing machine. can.

以上説明し良ように本発明に係る混合液供給装置によれ
ば、供給管内に混合液の成分が堆積して詰まるのを防止
することができる。1+本発明によれば、単に弁の切換
えで制御できるので、作業性がよい利点がある。
As explained above, according to the mixed liquid supply device according to the present invention, it is possible to prevent components of the mixed liquid from accumulating and clogging the supply pipe. 1+According to the present invention, control can be performed simply by switching valves, so there is an advantage of good workability.

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

第1図は本発明に係る装置の一実施例の概略構成を示す
断面図、第2図及び第S図は6弁の曲量特性を示す流量
曲線図であや。 1・・・混合液、2・・・タンク、10・・・供給管、
11・・・ポンプ、12・・・リターン管、する、14
・・・切換弁・ @1図 第2図   第3図
FIG. 1 is a sectional view showing a schematic configuration of an embodiment of the device according to the present invention, and FIGS. 2 and S are flow curve diagrams showing the bending characteristics of six valves. 1... Mixed liquid, 2... Tank, 10... Supply pipe,
11...Pump, 12...Return pipe, Yes, 14
...Switching valve・@Fig. 1 Fig. 2 Fig. 3

Claims (1)

【特許請求の範囲】[Claims] タンクから供給管を経て被供給箇所に混合液を供給する
混合液供給装置において、前記供給管の末端寄シの箇所
と前記タンクとを結ぶリターン管を設け、前記リターン
管の分岐接続箇所より末端側の前記供給管と、前記リタ
ーン管の途中とには、それぞれ切換弁を設けたことを特
徴とする混合液供給装置。
In a mixed liquid supply device that supplies a mixed liquid from a tank to a supplied location via a supply pipe, a return pipe is provided that connects the end of the supply pipe to the tank, and a return pipe is provided that connects the end of the supply pipe with the tank. A mixed liquid supply device characterized in that switching valves are provided in the side supply pipe and in the middle of the return pipe, respectively.
JP56180308A 1981-11-12 1981-11-12 Mixed solution supply device Granted JPS58104712A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56180308A JPS58104712A (en) 1981-11-12 1981-11-12 Mixed solution supply device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56180308A JPS58104712A (en) 1981-11-12 1981-11-12 Mixed solution supply device

Publications (2)

Publication Number Publication Date
JPS58104712A true JPS58104712A (en) 1983-06-22
JPS6243845B2 JPS6243845B2 (en) 1987-09-17

Family

ID=16080934

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56180308A Granted JPS58104712A (en) 1981-11-12 1981-11-12 Mixed solution supply device

Country Status (1)

Country Link
JP (1) JPS58104712A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104552860A (en) * 2014-12-24 2015-04-29 浙江天禾生态科技有限公司 Device and method for producing fiber-filled starch-based fully-biodegradable material
JP2019171356A (en) * 2018-03-28 2019-10-10 王磊 Rubber material device

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0539970Y2 (en) * 1988-06-20 1993-10-12

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4947920A (en) * 1972-09-14 1974-05-09
JPS5541890A (en) * 1978-07-24 1980-03-24 Gen Electric Liquid supply mixing method and its device
JPS5545337A (en) * 1978-09-28 1980-03-31 Kagome Kk Method of germ-free agitation of germ-free storage tank
JPS5621593A (en) * 1979-07-27 1981-02-28 Nitto Chem Ind Co Ltd Microbial preparation of monohydroxycarboxylic acid

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4947920A (en) * 1972-09-14 1974-05-09
JPS5541890A (en) * 1978-07-24 1980-03-24 Gen Electric Liquid supply mixing method and its device
JPS5545337A (en) * 1978-09-28 1980-03-31 Kagome Kk Method of germ-free agitation of germ-free storage tank
JPS5621593A (en) * 1979-07-27 1981-02-28 Nitto Chem Ind Co Ltd Microbial preparation of monohydroxycarboxylic acid

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104552860A (en) * 2014-12-24 2015-04-29 浙江天禾生态科技有限公司 Device and method for producing fiber-filled starch-based fully-biodegradable material
CN104552860B (en) * 2014-12-24 2017-06-16 浙江天禾生态科技有限公司 Production fiber fills the device and method of starch base full-biodegradable material
JP2019171356A (en) * 2018-03-28 2019-10-10 王磊 Rubber material device

Also Published As

Publication number Publication date
JPS6243845B2 (en) 1987-09-17

Similar Documents

Publication Publication Date Title
US4217325A (en) Method using modular slush molding machine
JPS58104712A (en) Mixed solution supply device
DE19737849A1 (en) Device and method for heating a liquid or viscous polishing agent and device for polishing wafers
US4155690A (en) Continuous production of cross-linked polyethylene
US2732592A (en) Extrusion of thermoplastic material
DE3027200A1 (en) METHOD AND DEVICE FOR EXTRUDING RUBBER AND THERMALLY CROSSLINKED RESIN
US4351664A (en) Furnace delivery system
CZ318192A3 (en) Process for producing plastic tube and apparatus for making the same
US4356143A (en) Apparatus for and a method of curing a continuous length of curable material
DE60218907T2 (en) METHOD AND APPARATUS FOR PRODUCING LENGTHS OF PREISOLATED PIPES
US4331626A (en) Method useful for rotational molding articles where successful runs are of different colors
US5281124A (en) Arrangement for pressurizing a plurality of molds with one or more pressurized fluids for molding synthetic materials and maintaining said materials at a predetermined temperature in the molds
US4663096A (en) Apparatus and method of heating melt spinning head structure
US3369873A (en) Apparatus and method for continuously melting a solid reactant
JP6660666B2 (en) Hot coating method of silylated adhesive composition
CN106182575A (en) Stealthy optical cable production technology and coating equipment
JPH09168758A (en) Viscosity control device for paint in tank in automatic painting apparatus
US4353861A (en) Process and plant for vulcanizing a continuous length of curable material
DE2131253A1 (en) Manufacture of rubber or plastic insulated cables
US2684050A (en) Apparatus for coating cables
JPH0372170B2 (en)
CA1039915A (en) Quick-chilling method of filling a stranded article with a waterproofing composition
CN205275468U (en) Condensation kettle
JPS59175507A (en) Method of producing crosslinked rubber and plastic insulatedwire
JPS54160240A (en) Ink jet head of ink jet recorder