JPH0343057B2 - - Google Patents

Info

Publication number
JPH0343057B2
JPH0343057B2 JP57082698A JP8269882A JPH0343057B2 JP H0343057 B2 JPH0343057 B2 JP H0343057B2 JP 57082698 A JP57082698 A JP 57082698A JP 8269882 A JP8269882 A JP 8269882A JP H0343057 B2 JPH0343057 B2 JP H0343057B2
Authority
JP
Japan
Prior art keywords
shaft
rotor
foaming machine
blades
foam
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.)
Expired - Lifetime
Application number
JP57082698A
Other languages
Japanese (ja)
Other versions
JPS58199126A (en
Inventor
Mikio Kitahara
Tadashi Ishioka
Muneo Nagaoka
Masaichi Izumida
Yukinari Fujii
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP57082698A priority Critical patent/JPS58199126A/en
Publication of JPS58199126A publication Critical patent/JPS58199126A/en
Publication of JPH0343057B2 publication Critical patent/JPH0343057B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/74Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
    • B29B7/7404Mixing devices specially adapted for foamable substances
    • B29B7/7409Mixing devices specially adapted for foamable substances with supply of gas
    • B29B7/7414Mixing devices specially adapted for foamable substances with supply of gas with rotatable stirrer, e.g. using an intermeshing rotor-stator system
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/27Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices
    • B01F27/271Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator
    • B01F27/2711Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator provided with intermeshing elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F2025/91Direction of flow or arrangement of feed and discharge openings
    • B01F2025/912Radial flow
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05Stirrers
    • B01F27/11Stirrers characterised by the configuration of the stirrers
    • B01F27/19Stirrers with two or more mixing elements mounted in sequence on the same axis
    • B01F27/191Stirrers with two or more mixing elements mounted in sequence on the same axis with similar elements

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
  • Molding Of Porous Articles (AREA)

Description

【発明の詳細な説明】 本発明はシヤフト周辺部から発泡体原料を注入
して発泡体を製造する発泡機において、品質の安
定した発泡体を生産性よく製造するために、シヤ
フト周辺部に傾斜羽根を付設した発泡機に関す
る。
Detailed Description of the Invention The present invention provides a foaming machine that manufactures foam by injecting foam raw materials from the periphery of the shaft. Regarding a foaming machine equipped with blades.

合成樹脂発泡体は断熱材としてすぐれた性能を
有しており、省ネルギー、省資源の必要性から大
きな需要が見込まれている。また省資源の意味か
ら高発泡倍率の発泡体に対する要求が強まつてい
る。
Synthetic resin foam has excellent performance as a heat insulating material, and is expected to be in great demand due to the need to save energy and resources. Furthermore, from the perspective of resource conservation, there is an increasing demand for foams with a high expansion ratio.

従来高発泡体の製造方法としては、発泡体原料
樹脂、硬化剤および常温、常圧においては液体で
あるが、温度上昇により気化する発泡、または加
圧下では液体であるが常温、常圧では気体である
発泡剤(以下単に液状発泡剤という。)を混合し
た後、発泡硬化させる方法が一般的であつた。し
かしながら、このような方法では、発泡倍率を大
きくするためには、多量の発泡剤を使用する必要
があり、発泡体製造コストが高くなるという欠点
を有している。また、液状発泡剤による発泡体の
製造は雰囲気の温度により、その発泡が異なるた
め、品質管理が難かしく、特に住宅用パネル等内
部空間が棧等により区切られている場合には、未
充填部分を生じる等トラブルの原因となり易い。
Conventional methods for manufacturing highly foamed materials include foaming, which is a foam raw material resin, a curing agent, and a foam that is liquid at room temperature and pressure, but vaporizes when the temperature rises, or liquid under pressure, but becomes gas at room temperature and pressure. A common method was to mix a foaming agent (hereinafter simply referred to as a liquid foaming agent) and then foam and harden the mixture. However, this method has the disadvantage that in order to increase the expansion ratio, it is necessary to use a large amount of foaming agent, which increases the cost of producing the foam. In addition, when producing foam using a liquid foaming agent, the foaming rate differs depending on the temperature of the atmosphere, making quality control difficult.Especially when the interior space of a residential panel is divided by slats, etc., unfilled areas may be difficult to control. This can easily cause problems such as .

一方、水溶性又は水分散性を有する熱硬化性樹
脂(以下、親水性熱硬化性樹脂という。)は、空
気を発泡剤とした発泡方法が可能で、しかもこの
方法では発泡機より吐出後殆んど体積膨張がな
く、品質の管理が容易である。この様に空気を発
泡剤とするため製造コストも安く、作業性も良い
こと等から親水性熱硬化性樹脂に対する要望は大
である。
On the other hand, water-soluble or water-dispersible thermosetting resins (hereinafter referred to as hydrophilic thermosetting resins) can be foamed using air as a foaming agent. There is no volume expansion, and quality control is easy. There is a great demand for hydrophilic thermosetting resins because they use air as a blowing agent, which makes the manufacturing cost low and the workability is good.

親水性熱硬化性樹脂より空気を発泡剤として発
泡体を製造する方法は、樹脂液、空気、及び硬化
剤を発泡機によつて発泡し、硬化させるが、この
際の発泡機としては、メカニカルフロス発泡機を
使用するのが最も好ましい。メカニカルフロス発
泡機はオークス型連続ミキサー等とも呼ばれ(特
願昭56−138604号、特公昭40−17143号)、第1図
に示すように、内壁に多数の突起1を有する混合
室内を多数の羽根2を有する回転子3が回転し、
羽根2が突起1に接触することなく突起間を回転
子3の回転と共に回転する構造を有しており、混
合室内で発泡体主剤と硬化剤と空気が均一に分散
して含泡状態となる。ところが、従来、主剤(樹
脂液)R、硬化剤H、発泡用エアーAの各成分を
シヤフト4周辺に設けた注入口5より注入するに
あたり、シヤフト部、特に硬化剤入口部分での詰
まりが激しく、組成比の変化や、ゲル化物の混
入、発泡倍率の低下、収率の減少などが起り、製
造および品質の不安定が懸念されたので、より安
定した発泡体の製造方法の改良が強く望まれてい
た。
In the method of manufacturing a foam from a hydrophilic thermosetting resin using air as a foaming agent, resin liquid, air, and a curing agent are foamed and cured using a foaming machine. Most preferably, a floss foamer is used. The mechanical floss foaming machine is also called an Oaks-type continuous mixer (Japanese Patent Application No. 138604/1983, Patent Publication No. 17143/1973), and as shown in Figure 1, it has a mixing chamber with many protrusions 1 on the inner wall. A rotor 3 having blades 2 rotates,
It has a structure in which the blades 2 rotate between the protrusions together with the rotation of the rotor 3 without contacting the protrusions 1, and the foam base material, curing agent, and air are uniformly dispersed in the mixing chamber, resulting in a foam-containing state. . However, conventionally, when injecting the main resin (resin liquid) R, curing agent H, and foaming air A through the injection port 5 provided around the shaft 4, the shaft part, especially the curing agent inlet part, was frequently clogged. However, there were concerns about instability in production and quality due to changes in the composition ratio, contamination of gelled substances, decrease in expansion ratio, and decrease in yield.Therefore, there was a strong desire to improve the production method to produce more stable foams. It was rare.

本発明者は、メカニカルフロス発泡機のシヤフ
ト4周辺部に、シヤフト軸方向に対して傾斜した
傾斜羽根6を取付けることによりシヤフト周辺部
での詰まりを防止することが出来ることを見出し
本発明を完成するに至つたものである。
The present inventor discovered that clogging in the shaft periphery can be prevented by attaching inclined blades 6 inclined with respect to the shaft axis direction to the shaft 4 periphery of a mechanical floss foaming machine, and completed the present invention. This is what I came to do.

以下、図面を用いて本発明を説明する。第1図
は本発明発泡機の長手方向断面図、第2図は軸に
対して直角方向断面図、および第3図は、傾斜羽
根の傾斜角度の説明図である。第1図および第2
図において、注入口5よりそれぞれ注入された発
泡体原料は、シヤフト4の周辺部の空間を通つて
矢印の如く進行し、回転子3の回転によつて機械
的に混合泡立て処理され含泡状態となし、発泡機
より吐出せしめて、その後硬化が進む。第1,2
図で発泡体原料R、H、Aの注入の1例を示して
いるが、各原料が供給され、混合室に至る迄のシ
ヤフト周辺の空間部では、従来各原料がほとんど
混合されない為比較的層をなして流れ部分的に、
硬化剤過剰状態が発生し屡々詰りとなつてあらわ
れていた。本発明ではシヤフト周辺の空間部を傾
斜羽根6を使用して撹拌し、部分的な硬化剤過剰
状態の発生を防止し、同時に混合室への流れを促
進し空間部分に於ける原料の滞留時間を短くする
ことによつて詰まりを防止する。傾斜羽根6は第
3図に示したようにシヤフト軸方向に対して5〜
15゜の傾斜角(θ)をもつてらせん状に取付けら
れている。θが小さいと原料の混合室への流れを
促進し詰まりを防止する効果が少なく、大きすぎ
ると分解掃除の際傾斜羽根6がじやまになり、シ
ヤフト4周辺部の掃除が困難となる。好ましくは
5〜7゜の範囲である。傾斜羽根6に取付枚数は、
特に制限はないが詰まり防止効果及び分解掃除の
面から2〜4枚が好ましい。従来シヤフト周辺部
の詰まりのために、この部分の分解掃除間隔は約
1週間であつたが、本発明の場合、約1ケ月間に
延長でき品質の安定した発泡体を長時間供給する
事が可能となり、しかも生産性も向上する等効果
は顕著であつた。傾斜羽根6をシヤフト4に取付
ける方法は、シヤフト4自体に溶接等で取付けて
もよいが、第2図に示すように、円筒形の取付金
具7をシヤフト4に嵌合させる方法でもよい。
The present invention will be explained below using the drawings. FIG. 1 is a longitudinal sectional view of the foaming machine of the present invention, FIG. 2 is a sectional view perpendicular to the axis, and FIG. 3 is an explanatory diagram of the inclination angle of the inclined blade. Figures 1 and 2
In the figure, the foam raw materials injected from the injection ports 5 advance as shown by the arrows through the space around the shaft 4, and are mechanically mixed and foamed by the rotation of the rotor 3 to form a foamed state. Then, it is discharged from a foaming machine, and then curing proceeds. 1st, 2nd
The figure shows an example of injection of foam raw materials R, H, and A, but in the space around the shaft where each raw material is supplied and reaches the mixing chamber, conventionally, each raw material is hardly mixed, so it is relatively Partially flowing in layers,
An excess amount of curing agent occurred, often resulting in clogging. In the present invention, the space around the shaft is stirred using inclined blades 6 to prevent the occurrence of a partial curing agent excess state, and at the same time promote the flow to the mixing chamber, thereby increasing the residence time of the raw material in the space. Prevent clogging by shortening. As shown in FIG. 3, the inclined blade 6 has an angle of 5 to
It is installed in a spiral shape with an inclination angle (θ) of 15°. If θ is small, the effect of promoting the flow of raw materials into the mixing chamber and preventing clogging will be small; if it is too large, the inclined blades 6 will become jammed during disassembly and cleaning, making it difficult to clean the area around the shaft 4. Preferably it is in the range of 5 to 7 degrees. The number of blades attached to the inclined blade 6 is
Although there is no particular limit, 2 to 4 sheets is preferable from the viewpoint of clogging prevention effect and disassembly and cleaning. Conventionally, due to clogging around the shaft, the interval for disassembling and cleaning this area was about one week, but with the present invention, this can be extended to about one month, making it possible to supply foam with stable quality for a long time. In addition, the effects were remarkable, such as improved productivity. The inclined blade 6 may be attached to the shaft 4 by welding or the like, or alternatively, as shown in FIG. 2, a cylindrical attachment fitting 7 may be fitted onto the shaft 4.

なお、本発明の親水性熱硬化性樹脂としてはユ
リア樹脂、フエノール樹脂、ウレタン樹脂等が代
表的である。
Note that typical examples of the hydrophilic thermosetting resin of the present invention include urea resin, phenol resin, and urethane resin.

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

第1,2図は本発明実施例の断面図、第3図
は、傾斜羽根の取付状態の説明図である。 1……突起、2……羽根、3……回転子、4…
…シヤフト、5……注入口、6……傾斜羽根、7
……取付金具。
1 and 2 are sectional views of the embodiment of the present invention, and FIG. 3 is an explanatory view of the state in which the inclined blades are attached. 1...Protrusion, 2...Blade, 3...Rotor, 4...
...Shaft, 5...Inlet, 6...Slanted blade, 7
...Mounting bracket.

Claims (1)

【特許請求の範囲】[Claims] 1 内壁に多数の突起を有する混合室内を多数の
羽根を有する回転子が回転し、羽根が突起に接触
することなく突起間を回転子の回転と共に回転す
る構造を有する発泡機内に、水溶性又は水分散性
を有する熱硬化性樹脂液、空気及び硬化剤を主成
分とする発泡体原料を回転子につながるシヤフト
周辺部より注入し、発泡させる発泡機において、
発泡体原料を混合室内へ進行せしめるよう、シヤ
フト軸方向に対して5〜15゜の傾斜角をなした傾
斜羽根をシヤフトに取り付けたことを特徴とする
発泡機。
1. A foaming machine with a structure in which a rotor with a large number of blades rotates in a mixing chamber with a large number of projections on the inner wall, and the blades rotate between the projections together with the rotation of the rotor without contacting the projections. In a foaming machine that injects a foam raw material whose main components are a water-dispersible thermosetting resin liquid, air, and a hardening agent from the periphery of a shaft connected to a rotor and foams the material.
A foaming machine characterized by having inclined blades attached to a shaft at an angle of inclination of 5 to 15 degrees with respect to the shaft axis direction so as to advance foam raw materials into a mixing chamber.
JP57082698A 1982-05-17 1982-05-17 Foaming machine Granted JPS58199126A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57082698A JPS58199126A (en) 1982-05-17 1982-05-17 Foaming machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57082698A JPS58199126A (en) 1982-05-17 1982-05-17 Foaming machine

Publications (2)

Publication Number Publication Date
JPS58199126A JPS58199126A (en) 1983-11-19
JPH0343057B2 true JPH0343057B2 (en) 1991-07-01

Family

ID=13781623

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57082698A Granted JPS58199126A (en) 1982-05-17 1982-05-17 Foaming machine

Country Status (1)

Country Link
JP (1) JPS58199126A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT516946B1 (en) * 2015-07-03 2016-10-15 Sonderhoff Eng Gmbh mixing device

Also Published As

Publication number Publication date
JPS58199126A (en) 1983-11-19

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