JPS58175637A - Manufacture of stable foamed object - Google Patents
Manufacture of stable foamed objectInfo
- Publication number
- JPS58175637A JPS58175637A JP57058492A JP5849282A JPS58175637A JP S58175637 A JPS58175637 A JP S58175637A JP 57058492 A JP57058492 A JP 57058492A JP 5849282 A JP5849282 A JP 5849282A JP S58175637 A JPS58175637 A JP S58175637A
- Authority
- JP
- Japan
- Prior art keywords
- shaft
- foam
- resin
- foaming
- agent
- 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
Links
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
- B29B7/00—Mixing; Kneading
- B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
- B29B7/7404—Mixing devices specially adapted for foamable substances
- B29B7/7409—Mixing devices specially adapted for foamable substances with supply of gas
- B29B7/7414—Mixing devices specially adapted for foamable substances with supply of gas with rotatable stirrer, e.g. using an intermeshing rotor-stator system
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/27—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices
- B01F27/271—Mixers 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
- B01F27/2711—Mixers 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F2025/91—Direction of flow or arrangement of feed and discharge openings
- B01F2025/912—Radial flow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/19—Stirrers with two or more mixing elements mounted in sequence on the same axis
- B01F27/191—Stirrers with two or more mixing elements mounted in sequence on the same axis with similar elements
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (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)
Abstract
Description
【発明の詳細な説明】
本発明は、水溶性または水分散性を有する熱硬化性樹脂
を原料とし、メカニカル70ス発泡機を用いて、発泡体
を安定的に製造する方法に関する1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、省エネルギー、
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
まっている。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for stably producing a foam using a water-soluble or water-dispersible thermosetting resin as a raw material and using a mechanical 70 bath foaming machine. The body has excellent performance as an insulator, saving energy and
Large demand is expected due to the need to conserve resources. In addition, 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、樹脂発泡体原料、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剤、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
的であった。Conventional methods for producing highly foamed materials include resin foam raw materials, curing agents, and blowing agents that are liquid at room temperature and pressure but vaporize when the temperature rises, or liquid under pressure but at room temperature and pressure. A common method has been to mix a gaseous foaming agent (hereinafter simply referred to as a liquid foaming agent) and then foam and harden the mixture.
しかしながら、このような方法では、発泡倍率音大きく
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桟等により区切られている場
合には、11
未充填部分を生じる等トラ氷ルの原因となり易い。However, such a method has the disadvantage that a large amount of foaming agent must be used in order to increase the foaming magnification sound, which increases the cost of producing the foam. In addition, when manufacturing a foam using a liquid foaming agent, the foaming rate differs depending on the temperature of the atmosphere, making quality control difficult. It is easy to cause parts to freeze.
一方、親水性熱硬化性樹脂は、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犬で
ある。On the other hand, hydrophilic thermosetting resins can be foamed using air as a foaming agent, and in this method, there is almost no volumetric expansion after discharge from a foaming machine, making quality control easy. As described above, there is a strong demand for hydrophilic thermosetting resins because they use air as a blowing agent, so the manufacturing cost is low and 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、及び、空気、硬化剤を発泡機に
よって発泡し、硬化させるが、この際の発泡機としては
、メカニカルクロス発泡機を使用するのが最も好ましい
。このメカニカルフロス発泡機の構造を第1図に示した
。In the method of producing foam from 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 foaming machine is used. The structure of this mechanical floss foaming machine is shown in FIG.
従来、主剤(樹脂液)R1硬化剤H5発泡用エアーAの
各成分をシャフト1周辺に設けた注入口2より注入する
ためにあたり、シャフト部、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
法の政体を製造するにあたり、シャフト周辺部に設けら
れた注入口より主剤をシャフト中心部に向は注入し、硬
化剤は、単独又は発泡用エアーと共にシャフトの外周方
向に注入することにより上記諸問題が解決し、安定した
発泡体製造方法を発明するに至ったものである。Conventionally, when injecting each component of base resin (resin liquid) R1 curing agent H5 and foaming air A through the injection port 2 provided around the shaft 1, the shaft part, especially the curing agent inlet part, was frequently clogged, and the composition ratio There were concerns about instability in production and quality due to changes in foam, contamination of gelled substances, reduction in expansion ratio, and reduction in yield. The above problems can be solved by injecting the base agent toward the center of the shaft from the injection port provided at the periphery, and the curing agent alone or together with foaming air toward the outer circumference of the shaft, resulting in a stable foam. This led to the invention of a manufacturing method.
これを図面により説明する。第1図はメカ二カ/l/7
0ス発泡機の断面図で、メカニカルフロス発泡機は、内
壁に多数の突起3を有する円筒容器内を、多数の羽根(
突起)4を有する回転子5が回転し、羽根4が突起3に
接触することなく突起間を回転子5の回転と共に回転す
る構造で、回転子5に連なり、シール6を有し軸受7に
よって支えられたシャフト1の主として周辺から、注入
された発泡体原料が羽根4と突起3の間で機械的に混合
泡立たせ処理され含泡状態となる。This will be explained using drawings. Figure 1 is Mechanica/l/7
This is a cross-sectional view of the 0-s foaming machine. The mechanical floss foaming machine moves a large number of blades (
It has a structure in which a rotor 5 having projections) 4 rotates, and the blades 4 rotate between the projections together with the rotation of the rotor 5 without contacting the projections 3. The foam raw material injected mainly from the periphery of the supported shaft 1 is mechanically mixed and foamed between the blades 4 and the protrusions 3 to form a foamed state.
第2図および第3図は、第1図におけるX−X’断面図
で、従来は、たとえば第1〜2図のA、R2、鴇の矢印
に示す箇所より、それぞれ、空気、硬化剤、主剤をシャ
フト中心部へ向けて注入した。ところが、前記したよう
に硬化剤入口部分での、詰まりが起った。そのため硬化
剤の注入口ヲH8〜。2 and 3 are XX' cross-sectional views in FIG. 1. Conventionally, for example, air, curing agent, The main agent was injected toward the center of the shaft. However, as mentioned above, clogging occurred at the curing agent inlet. Therefore, the hardening agent injection port is H8~.
の如く、円筒容器部分から注入する方法も試みられたが
、同様tζ部分硬化が起こり、不都合であった。A method of injecting from the cylindrical container portion was also attempted, but this also resulted in curing of the tζ portion, which was inconvenient.
本発明は、これに対し、第1および3図のA、Hlおよ
びR,の矢印に示す箇所より、それぞれ空気、硬化剤お
よび主剤を注入するもので、硬化剤を発泡機のシャフト
の外周方向に向けて注入する。この際、硬化剤H1′f
c空気Aと共に注入してもよい。In contrast, the present invention injects air, a hardening agent, and a base agent from the locations indicated by arrows A, Hl, and R in FIGS. Inject towards. At this time, the curing agent H1'f
c May be injected together with air A.
硬化剤を外周方向に向けて注入することにより、発泡体
の製造、品質が安定向上した。By injecting the curing agent toward the outer circumference, the production and quality of the foam were stably improved.
本発明の熱硬化性樹脂発泡体としてはユリア樹脂、フェ
ノール樹脂、ウレタン樹脂等がある。Examples of the thermosetting resin foam of the present invention include urea resin, phenol resin, and urethane resin.
つぎに実施例によりさらに具体的に説明する。Next, a more specific explanation will be given with reference to Examples.
部又はチとあるのは断りのない限り重量部又は重量%と
さす。Unless otherwise specified, "parts" or "chi" refer to parts by weight or percent by weight.
実施例及び比較例
実施例及び比較1例に使用した尿素樹脂初期縮合−物は
次のようにして製造した。市販の尿素樹脂ユーロフォー
ムRIOI (三井東圧化学■製)を、減圧濃縮するこ
とにより、粘度2500センチボイズ、不揮発分73%
の尿素樹脂初期縮合物を得た。この尿素樹脂初期縮合物
に水を加え、不揮発分52q6としたもの100部に対
し、アルキルジフエニルエーテルジスルフオン酸ソーダ
1部を加えて混合し樹(5)
胆液とした。一方硬化液としては燐酸2.0%、レゾル
シノール10%、アルキルジフェニルエーテルジスルフ
オン酸ソーダ1チを含む水溶液を使用した。Examples and Comparative Examples The urea resin initial condensates used in Examples and Comparative Example 1 were produced as follows. By concentrating commercially available urea resin Euroform RIOI (manufactured by Mitsui Toatsu Chemical Co., Ltd.) under reduced pressure, it has a viscosity of 2500 centiboise and a non-volatile content of 73%.
A urea resin initial condensate was obtained. Water was added to this urea resin initial condensate to give a non-volatile content of 52q6, and 1 part of sodium alkyl diphenyl ether disulfonate was added and mixed to 100 parts to obtain Tree (5) bile fluid. On the other hand, as the curing liquid, an aqueous solution containing 2.0% phosphoric acid, 10% resorcinol, and 1% sodium alkyldiphenyl ether disulfonate was used.
実施例および比較例に於いては第1図及び第3図、第1
図及び第2図に示したメカニカル70ス発泡機(東邦機
械工業■製、東邦’IM302型、円筒容器の内壁には
多数の突起3を有し、また多数の攪拌羽根4(突起状)
を有する回転子5が容器内(6)
で突起3と近接して回転する構造)中に樹脂液と硬化液
との重量比100/35の流量で注入し、又圧縮空気を
発泡機中の内圧ヲ35〜45kf/cIIに保つ様に連
続的に注入し、発泡機の回転子5を45Orpmの回転
数で回転した。実施例に於いては第1図及び第3図に於
いて樹脂液を注入口R1より、硬化液をHlよりまた圧
縮空気を注入口Aより注入した。In Examples and Comparative Examples, Figures 1 and 3, Figure 1
The mechanical 70s foaming machine (manufactured by Toho Kikai Kogyo ■, model Toho' IM302, shown in Figures and Figure 2) has many protrusions 3 on the inner wall of the cylindrical container, and a large number of stirring blades 4 (protrusions).
A rotor 5 having a rotor 5 is injected into the container (6) (a structure in which it rotates close to the protrusions 3) at a flow rate of a weight ratio of resin liquid and curing liquid of 100/35, and compressed air is injected into the foaming machine. The mixture was continuously injected so as to keep the internal pressure at 35 to 45 kf/cII, and the rotor 5 of the foaming machine was rotated at a rotation speed of 45 Orpm. In the example, as shown in FIGS. 1 and 3, the resin liquid was injected through the inlet R1, the curing liquid was injected through the inlet H1, and the compressed air was injected through the inlet A.
一方比較例に於いては、第1図及び第2図に於いて樹脂
液k I(’2より、硬化液ヲH2より又圧縮空気を注
入口Aより注入した。On the other hand, in the comparative example, in FIGS. 1 and 2, compressed air was injected from the resin liquid K I ('2) through the injection port A rather than the curing liquid H2.
発泡機の吐出口3及び図外の注入用ホースを通じて連続
吐出を開始し、一定時間毎に含泡状混合物f 30 c
m角のダンボール箱中で硬化させた。得られた発泡体の
性状及び乾燥後の密度を第1表に示した。Continuous discharge is started through the discharge port 3 of the foaming machine and an injection hose (not shown), and the foam-containing mixture f 30 c is pumped out at regular intervals.
It was cured in an m square cardboard box. Table 1 shows the properties of the obtained foam and the density after drying.
更に実施例については、1日8時間連続運転した後水洗
し、翌日再使用する方法により分解掃除せずに延ベア日
間運転した所、発泡体密度は約17klf/ln”に達
し、発泡体の性状がやや不均一となった為分解掃除の必
要が生じた。Furthermore, in the example, the foam density reached approximately 17 klf/ln'' when the foam was operated continuously for 8 hours a day, washed with water, and then reused the next day without disassembly and cleaning. Because the properties became somewhat uneven, it became necessary to disassemble and clean it.
第1図はメカニカル70ス発泡機の断面図である。
第2図は第1図X−X断面における従来注入方法のlf
l説明する説明図、第3図は第1図X−X′断面におけ
る本発明方法の1例を説明する説明図である。
1・・・シャフト、2・・・注入口、3・・・突起、4
・・・羽根、5・・・回転子、6・・・軸承、A・・・
空気、H・・・硬化剤、R・・・主剤。
特許出願人 三井東圧化学株式会社
代理人弁理士 井 上 雅 主
筒2図
第3図FIG. 1 is a sectional view of a mechanical 70 bath foaming machine. Figure 2 shows lf of the conventional injection method taken along the line XX in Figure 1.
FIG. 3 is an explanatory diagram illustrating an example of the method of the present invention taken along the line XX' in FIG. 1. 1...Shaft, 2...Inlet, 3...Protrusion, 4
...Blade, 5...Rotor, 6...Bearing, A...
Air, H...hardening agent, R...main agent. Patent applicant: Mitsui Toatsu Chemical Co., Ltd. Representative patent attorney: Masaru Inoue Main tube 2 Figure 3
Claims (1)
るにあたり、シャフト周辺部に設けられた注入口より主
剤をシャフト中心部に向は注入し、硬化剤は単独又は空
気と共にシャフトの外周方向に向けて注入することを特
徴とする水溶性または水分散性を有する熱硬化性樹脂発
泡体の製造方法。1. When producing foam using a mechanical floss foaming machine, the main agent is injected toward the center of the shaft from the injection port provided around the shaft, and the curing agent is injected alone or together with air toward the outer circumference of the shaft. 1. A method for producing a water-soluble or water-dispersible thermosetting resin foam, the method comprising injecting a water-soluble or water-dispersible thermosetting resin foam.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57058492A JPS58175637A (en) | 1982-04-08 | 1982-04-08 | Manufacture of stable foamed object |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57058492A JPS58175637A (en) | 1982-04-08 | 1982-04-08 | Manufacture of stable foamed object |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58175637A true JPS58175637A (en) | 1983-10-14 |
JPH0343056B2 JPH0343056B2 (en) | 1991-07-01 |
Family
ID=13085916
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57058492A Granted JPS58175637A (en) | 1982-04-08 | 1982-04-08 | Manufacture of stable foamed object |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58175637A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20150003773A (en) * | 2012-05-02 | 2015-01-09 | 다우 글로벌 테크놀로지스 엘엘씨 | Radial-flow rotor-stator mixer and process to produce polymeric froths |
JP2018520856A (en) * | 2015-07-03 | 2018-08-02 | ゾンダホフ エンジニアリング ゲゼルシャフト ミット ベシュレンクテル ハフツングSonderhoff Engineering GmbH | Mixing device for mixing liquid plastic components with gas |
-
1982
- 1982-04-08 JP JP57058492A patent/JPS58175637A/en active Granted
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20150003773A (en) * | 2012-05-02 | 2015-01-09 | 다우 글로벌 테크놀로지스 엘엘씨 | Radial-flow rotor-stator mixer and process to produce polymeric froths |
CN104411393A (en) * | 2012-05-02 | 2015-03-11 | 陶氏环球技术有限责任公司 | Radial-flow rotor-stator mixer and process to produce polymeric froths |
JP2015517399A (en) * | 2012-05-02 | 2015-06-22 | ダウ グローバル テクノロジーズ エルエルシー | Radial flow rotor-stator mixer and method for producing polymeric foam |
EP2844381B1 (en) * | 2012-05-02 | 2018-09-19 | Dow Global Technologies LLC | Radial-flow rotor-stator mixer and process to produce polymeric froths |
JP2018520856A (en) * | 2015-07-03 | 2018-08-02 | ゾンダホフ エンジニアリング ゲゼルシャフト ミット ベシュレンクテル ハフツングSonderhoff Engineering GmbH | Mixing device for mixing liquid plastic components with gas |
US10946350B2 (en) | 2015-07-03 | 2021-03-16 | Henkel Ag & Co. Kgaa | Mixing device for mixing a liquid plastics component with a gas |
Also Published As
Publication number | Publication date |
---|---|
JPH0343056B2 (en) | 1991-07-01 |
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