JPH04118035A - Mix-stirring apparatus - Google Patents
Mix-stirring apparatusInfo
- Publication number
- JPH04118035A JPH04118035A JP2237726A JP23772690A JPH04118035A JP H04118035 A JPH04118035 A JP H04118035A JP 2237726 A JP2237726 A JP 2237726A JP 23772690 A JP23772690 A JP 23772690A JP H04118035 A JPH04118035 A JP H04118035A
- Authority
- JP
- Japan
- Prior art keywords
- chamber
- liquid
- rotor
- discharge 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
Links
- 238000003756 stirring Methods 0.000 title claims abstract description 34
- 239000007788 liquid Substances 0.000 claims abstract description 58
- 239000011344 liquid material Substances 0.000 claims abstract description 26
- 238000001816 cooling Methods 0.000 claims abstract description 14
- 238000007599 discharging Methods 0.000 claims description 4
- 239000002826 coolant Substances 0.000 abstract description 7
- 238000006243 chemical reaction Methods 0.000 abstract description 4
- 230000002093 peripheral effect Effects 0.000 abstract description 4
- 230000020169 heat generation Effects 0.000 abstract description 3
- 230000003247 decreasing effect Effects 0.000 abstract description 2
- 230000000717 retained effect Effects 0.000 abstract 1
- 229920005989 resin Polymers 0.000 description 19
- 239000011347 resin Substances 0.000 description 19
- 239000003795 chemical substances by application Substances 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 6
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- RAXXELZNTBOGNW-UHFFFAOYSA-N imidazole Natural products C1=CNC=N1 RAXXELZNTBOGNW-UHFFFAOYSA-N 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 229920005862 polyol Polymers 0.000 description 3
- 150000003077 polyols Chemical class 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229920002635 polyurethane Polymers 0.000 description 2
- 239000004814 polyurethane Substances 0.000 description 2
- 229920005749 polyurethane resin Polymers 0.000 description 2
- ZJCCRDAZUWHFQH-UHFFFAOYSA-N Trimethylolpropane Chemical compound CCC(CO)(CO)CO ZJCCRDAZUWHFQH-UHFFFAOYSA-N 0.000 description 1
- OMOVVBIIQSXZSZ-UHFFFAOYSA-N [6-(4-acetyloxy-5,9a-dimethyl-2,7-dioxo-4,5a,6,9-tetrahydro-3h-pyrano[3,4-b]oxepin-5-yl)-5-formyloxy-3-(furan-3-yl)-3a-methyl-7-methylidene-1a,2,3,4,5,6-hexahydroindeno[1,7a-b]oxiren-4-yl] 2-hydroxy-3-methylpentanoate Chemical compound CC12C(OC(=O)C(O)C(C)CC)C(OC=O)C(C3(C)C(CC(=O)OC4(C)COC(=O)CC43)OC(C)=O)C(=C)C32OC3CC1C=1C=COC=1 OMOVVBIIQSXZSZ-UHFFFAOYSA-N 0.000 description 1
- 239000000499 gel Substances 0.000 description 1
- 239000002075 main ingredient Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000005056 polyisocyanate Substances 0.000 description 1
- 229920001228 polyisocyanate Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
- B29B7/401—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft having a casing closely surrounding the rotor, e.g. with a plunger for feeding the material
-
- 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
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
- B29B7/405—Mixing heads
- B29B7/407—Mixing heads with a casing closely surrounding the rotor, e.g. with conical rotor
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
この発明は、ポリウレタン樹脂溶液などの樹脂液を用い
て樹脂製品を成形する際に、2種類以上の液状物を撹拌
混合して金型などに吐出(注入)させるための混合撹拌
装置に関し、詳しくは、高温(100℃以上)で硬化す
る熱硬化性の樹脂液の混合撹拌に好適な装置に関するも
のである。[Detailed Description of the Invention] [Industrial Application Field] This invention is applicable to molding of molds, etc. by stirring and mixing two or more types of liquid materials when molding resin products using resin liquids such as polyurethane resin solutions. The present invention relates to a mixing and stirring device for discharging (injecting) liquid, and more specifically, to a device suitable for mixing and stirring a thermosetting resin liquid that hardens at high temperatures (100° C. or higher).
[従来の技術]
例えば、ポリウレタン製の電子写真式複写機用クリーニ
ングプレートを金型で成形する場合、その原料としての
樹脂液には、ウレタンプレポリマーに低分子量ポリオー
ルなどの硬化剤を混合して撹拌したものが一般に用いら
れる。[Prior Art] For example, when molding a polyurethane cleaning plate for an electrophotographic copying machine using a mold, the resin liquid used as the raw material is mixed with a urethane prepolymer and a curing agent such as a low molecular weight polyol. It is generally used after stirring.
本出願人は、上記のような2種類以上の液状物を混合撹
拌して金型に注入する装置として、次のような構造の装
置を既に開発している。すなわち、第4図に示すように
、チャンバー51内に撹拌用回転子(ロータ)57が上
端より回転軸58に支持さて配設されており、チャンバ
ー51の上端側に設られた複数の導入口52.53から
液状物が導入さ回転子57により混合撹拌された後、チ
ャンバーの下端に設けられた吐出管54から吐出される
。The present applicant has already developed an apparatus having the following structure as an apparatus for mixing and stirring two or more types of liquid substances as described above and injecting the mixture into a mold. That is, as shown in FIG. 4, a stirring rotor 57 is disposed in the chamber 51 and is supported by a rotating shaft 58 from the upper end, and a plurality of inlets provided at the upper end of the chamber 51 are provided. A liquid substance is introduced from 52 and 53, mixed and stirred by a rotor 57, and then discharged from a discharge pipe 54 provided at the lower end of the chamber.
転子57の側周面には、多数の突起部57aが間隔あけ
て突設され、回転子57の下端部は、チャンー−Stの
底部形状に対応して円錐形に形成されてる。さらに、底
部を除くチャンバー51の周囲に:冷却用ジャケット5
5が設けられている。A large number of protrusions 57a are provided at intervals on the side peripheral surface of the rotor 57, and the lower end of the rotor 57 is formed into a conical shape corresponding to the bottom shape of the chamber. Furthermore, around the chamber 51 except for the bottom: cooling jacket 5
5 is provided.
[発明が解決しようとする課題」
第4図に示した混合撹拌装置は、チャンバー5の周囲に
設けられた冷却用ジャケット55で、内fの液状物を冷
却しながら混合撹拌するので、つ1タンブレポリマーに
緩硬化剤を混合撹拌する時jは、液状物の温度が大幅に
上昇したり反応が急4に促進されたりして液状物が硬化
しチャンバー5内に付着することはほとんどない。[Problems to be Solved by the Invention] The mixing and stirring device shown in FIG. When mixing and stirring the slow curing agent into the tumble polymer, the temperature of the liquid material rises significantly or the reaction is suddenly accelerated, so that the liquid material hardly hardens and adheres to the inside of the chamber 5. .
しかしながら、樹脂製品の成型時間を大幅に匁縮して生
産効率の向上や製造コストの低減を図イために、速硬化
性の樹脂液を混合撹拌しようとすると、上記の装置では
、次のような問題点が生じた。すなわち、
低分子量ポリオールなどの上記硬化剤に、イミダゾール
系などの硬化触媒を添加したものを硬化剤として、ウレ
タンプレポリマーと混合撹拌させて、所定の複数の金型
に順番に間欠吐出させていくと、混合液が次第にゲル化
してチャンバー内壁および吐出口付近に付着し、7〜l
O分間で吐出量が減少すると共に、混合液の比率不良が
生じた。However, when trying to mix and stir a fast-curing resin liquid in order to significantly shorten the molding time of resin products to improve production efficiency and reduce manufacturing costs, the above equipment does not work as described below. A problem arose. That is, a curing agent such as an imidazole type curing catalyst is added to the curing agent such as a low molecular weight polyol, which is mixed with the urethane prepolymer and stirred, and then intermittently discharged into a plurality of predetermined molds in order. Then, the mixed liquid gradually gels and adheres to the inner wall of the chamber and the vicinity of the discharge port, and from 7 to 1
The discharge amount decreased in 0 minutes, and a ratio failure of the mixed liquid occurred.
この主な原因として、第4図の混合撹拌装置では、■チ
ャンバー51内壁と撹拌用回転子57との間の空隙部に
一種のデッドスペースがあり、そのデッドスペース部分
で混合液の流れが停滞して滞留すること、■吐出管54
の周辺には、冷却用ジャケット55が設けられていない
ので、混合液の吐出を中止した際に硬化し易いこと、が
考えられる。The main reason for this is that in the mixing and stirring device shown in Fig. 4, there is a kind of dead space in the gap between the inner wall of the chamber 51 and the stirring rotor 57, and the flow of the mixed liquid stagnates in the dead space. ■Discharge pipe 54
Since the cooling jacket 55 is not provided around the mixed liquid, it is considered that the mixed liquid is likely to harden when discharging is stopped.
この発明は上述の点に鑑みなされたもので、第4図の混
合撹拌装置において上記した問題点を解消して、速硬化
性の樹脂液を混合撹拌する場合にも、チャンバー内で混
合液が硬化して付着することがなく、長時間安定して混
合撹拌が行われ、樹脂製品の生産効率を向上し得る混合
撹拌装置を提供することを目的としている。This invention was made in view of the above-mentioned points, and it solves the above-mentioned problems in the mixing and stirring device shown in FIG. It is an object of the present invention to provide a mixing and stirring device that does not harden and adhere, stably performs mixing and stirring for a long time, and can improve the production efficiency of resin products.
[課題を解決するための手段]
上記目的を達成するためにこの発明の混合撹拌装置は、
a)上端部に液状物の導入口を、下端部中央に液状物の
吐出管を備えた装置本体のチャンバー内に、撹拌用回転
子をその上端中央部で支持して回転可能に配備した、2
種類以上の液状物を撹拌混合して吐出させる混合撹拌装
置であって、b)前記チャンバーの底部を前記吐出管の
入口に向けて傾斜させると共に、c)その底部形状に対
応する形状に前記回転子の下端部を形成して、d)その
下端部に液状物搬送用の複数の羽根部を、正転時に吐出
管へ液状物が搬送される向きに傾斜させて設け、e)前
記回転子の側周面に多数の突起部を突設し、f)正転時
に液状物を吐出させる向きにネジ部を刻設したネジ杆を
回転子の下端中央部に突設して前記吐出管内に挿入し、
g)前記装置本体のチャンバーおよび吐出管の周囲に、
冷却用ジャケットを配設している。[Means for Solving the Problems] In order to achieve the above object, the mixing and stirring device of the present invention has the following features:
a) A stirring rotor is supported at the center of the upper end and rotatably disposed in the chamber of the main body of the device, which has a liquid material inlet at the upper end and a liquid material discharge pipe at the center of the lower end. 2
A mixing and stirring device that stirs and mixes and discharges more than one type of liquid material, wherein b) the bottom of the chamber is inclined toward the inlet of the discharge pipe, and c) the rotation is made into a shape corresponding to the shape of the bottom. d) a plurality of blades for transporting the liquid are provided at the lower end of the rotor so as to be inclined in a direction in which the liquid is transported to the discharge pipe during forward rotation; e) the rotor f) a threaded rod with a threaded portion carved in the direction in which the liquid material is discharged during forward rotation is provided protrudingly in the center of the lower end of the rotor, and is inserted into the discharge pipe; Insert
g) Around the chamber and discharge pipe of the device main body,
A cooling jacket is provided.
[作用]
上記構成を有するこの発明の混合撹拌装置によれば、チ
ャンバー内に導入された2種以上の液状物は、チャンバ
ー内壁に沿って流下しながら回転子の多数の突起部で撹
拌され、相互に混合される。[Function] According to the mixing and stirring device of the present invention having the above configuration, two or more types of liquid substances introduced into the chamber are stirred by the numerous protrusions of the rotor while flowing down along the inner wall of the chamber, mixed with each other.
このとき、周囲の冷却ジャケットに流入する冷却媒体に
よって、混合液(樹脂液)が冷却され、混合時の化学反
応や発熱が抑えられる。混合液は十分に撹拌されて、チ
ャンバーの底部まで達すると、回転子の下端部に設けら
れた複数の羽根部によって、吐出管へ送られ同時に撹拌
されるので、チャンバー底部での混合液の滞留が阻止さ
れる。そして、吐出管内では、ネジ杆によってその下端
の吐出口へ向けて混合液が送られ同時に撹拌される。At this time, the mixed liquid (resin liquid) is cooled by the cooling medium flowing into the surrounding cooling jacket, and chemical reactions and heat generation during mixing are suppressed. When the mixed liquid is sufficiently stirred and reaches the bottom of the chamber, it is sent to the discharge pipe and stirred at the same time by multiple blades provided at the lower end of the rotor, so that the mixed liquid remains at the bottom of the chamber. is prevented. In the discharge pipe, the mixed liquid is sent toward the discharge port at the lower end of the pipe by a threaded rod and is stirred at the same time.
また、上記チャンバーおよび吐出管の周囲の冷却ジャケ
ットに流入する冷却媒体によって、混合液が冷却され、
混合時の化学反応や発熱が抑えられる。したがって、混
合撹拌した混合液を多数の金型へ間欠吐出する際に、混
合液の吐出が一時的に中止された場合でも、吐出管内や
吐出管の入口付近での混合液の硬化や付着が阻止される
。In addition, the mixed liquid is cooled by the cooling medium flowing into the cooling jacket around the chamber and the discharge pipe,
Chemical reactions and heat generation during mixing are suppressed. Therefore, when discharging mixed and stirred liquid mixture intermittently to a large number of molds, even if the discharge of the mixed liquid is temporarily stopped, the mixed liquid will not harden or adhere in the discharge pipe or near the entrance of the discharge pipe. blocked.
[実施例コ 以下、この発明の実施例を図面に基づいて説明する。[Example code] Embodiments of the present invention will be described below based on the drawings.
第1図は実施例にかかる混合撹拌装置を示す一部を断面
で表した正面図、第2図は回転子の平面図、第3図は回
転子の底面図である。FIG. 1 is a partially sectional front view showing a mixing and stirring device according to an embodiment, FIG. 2 is a plan view of a rotor, and FIG. 3 is a bottom view of the rotor.
第1図に示すように、装置本体1は、下方に向は漸次口
径を縮小した内周壁を備えた円筒状の胴部ケーシング2
と、この胴部ケーシング2の下端開口部にバッキング1
1を介して連結される半球形状の底部ケーシング3と、
胴部ケーシング2の上端開口部にバッキング12を介し
て連結される蓋体4とから構成される。As shown in FIG. 1, the device main body 1 includes a cylindrical body casing 2 having an inner circumferential wall whose diameter is gradually reduced in the downward direction.
And, the backing 1 is attached to the lower end opening of the body casing 2.
a hemispherical bottom casing 3 connected via 1;
The lid body 4 is connected to the upper end opening of the body casing 2 via a backing 12.
蓋体4の中央部には開口4aが開設され、その周囲に液
状物Aの導入口4bと液状物Bの導入口4cとかそれぞ
れ開設されている。また胴部ケーシング2の周囲には冷
却ジャケット5か形設され、冷却ジャケット5の一方に
冷却媒体(空気や水など)の流入口5aが、その他方に
冷却媒体の排出口5bが開設されている。さらに底部ケ
ーシング3の中央部には嘴状の吐出管3aが下向けに延
設され、吐出管3aの周囲を含む底部ケーシング3の周
囲に、冷却ジャケット6が形設されている。また冷却ジ
ャケット6の一方に冷却媒体の流入口6aが、その他方
に冷却媒体の排出口6bがそれぞれ開設されている。An opening 4a is provided in the center of the lid 4, and an inlet 4b for liquid A and an inlet 4c for liquid B are provided around the opening 4a. Further, a cooling jacket 5 is formed around the body casing 2, and one side of the cooling jacket 5 has an inlet 5a for a cooling medium (air, water, etc.), and the other side has an outlet 5b for the cooling medium. There is. Furthermore, a beak-shaped discharge pipe 3a extends downward in the center of the bottom casing 3, and a cooling jacket 6 is formed around the bottom casing 3 including the periphery of the discharge pipe 3a. Further, a cooling medium inlet 6a is provided on one side of the cooling jacket 6, and a cooling medium outlet 6b is provided on the other side.
前記装置本体1のチャンバー1a内に、撹拌用回転子7
が回転自在に配備されているが、回転子7は前記開口4
aを貫通する回転軸8に支持されている。回転軸8と開
口4aとの間隙には、軸受ンール部材8aが介装され、
スプリング8cで下向けに付勢された押し金具8bを介
して軸受シール部材8aの上端が押圧されている。A stirring rotor 7 is provided in the chamber 1a of the apparatus main body 1.
is arranged rotatably, and the rotor 7 is located in the opening 4.
It is supported by a rotating shaft 8 passing through a. A bearing ring member 8a is interposed in the gap between the rotating shaft 8 and the opening 4a,
The upper end of the bearing seal member 8a is pressed through a push metal fitting 8b that is urged downward by a spring 8c.
回転子7は、第2図のように上端中央部に回転軸8が螺
着されるネジ孔7aが穿設され、上端面の周縁部が下向
きに僅かに傾斜させである。回転子7の側周面には、円
周方向に等間隔に且つ上下方向に一定の間隔をあけて多
数の突起部7bが突設されている。As shown in FIG. 2, the rotor 7 has a screw hole 7a in the center of its upper end into which the rotating shaft 8 is screwed, and the peripheral edge of the upper end surface is slightly inclined downward. A large number of protrusions 7b are protruded from the side peripheral surface of the rotor 7 at equal intervals in the circumferential direction and at regular intervals in the vertical direction.
回転子7の底部は、前記底部ケーシング3の形状に対応
させて半球形状に形成され、第3図のように複数の羽根
部9が風車状に一体に形設されている。羽根部9の向き
は、回転子7の正回転時にチャン/<−1a内の液状物
が吐出管3aに送られるように設定されている。The bottom of the rotor 7 is formed into a hemispherical shape corresponding to the shape of the bottom casing 3, and as shown in FIG. 3, a plurality of blades 9 are integrally formed in the shape of a windmill. The direction of the blade portion 9 is set so that the liquid material in the chamber /<-1a is sent to the discharge pipe 3a when the rotor 7 rotates forward.
回転子7の底部の中央部には、ドリル状のネジ杆10が
下向きに突設され、前記吐出管3a内に挿入されている
。このネジ杆10のネジ部10aの向きは、回転子7の
正回転時に吐出管3a内の液状物を吐出させるように設
定されている。A drill-shaped threaded rod 10 is provided at the center of the bottom of the rotor 7 to protrude downward and is inserted into the discharge pipe 3a. The direction of the threaded portion 10a of the threaded rod 10 is set so that the liquid in the discharge pipe 3a is discharged when the rotor 7 rotates forward.
次に、上記のように構成した実施例の混合撹拌装置につ
いてその具体的使用例を説明する。Next, a specific usage example of the mixing/stirring device of the embodiment configured as described above will be explained.
ポリウレタン製のクリーニングプレートの製造過程にお
いて、チャンバー内容量:30ccの混合撹拌装置を使
用し、回転子7の回転速度:1500rpm。In the process of manufacturing a polyurethane cleaning plate, a mixing and stirring device with a chamber internal capacity of 30 cc was used, and the rotation speed of the rotor 7 was 1500 rpm.
吐出量:90g/l1linで運転した。It was operated at a discharge rate of 90 g/l lin.
本装置で混合撹拌する液状物として、液状物Aと液状物
Bとを用いた。主剤としての液状物A(ウレタンプレポ
リマー)には、高分子量ポリオール(100重量部)と
ポリイソシアネート(41重量部)を温度70℃の下に
反応させたものを用いた。Liquid material A and liquid material B were used as liquid materials to be mixed and stirred in this apparatus. Liquid material A (urethane prepolymer) as a main ingredient was prepared by reacting a high molecular weight polyol (100 parts by weight) with a polyisocyanate (41 parts by weight) at a temperature of 70°C.
また硬化剤としての液状物Bには、1.4−ブタンジオ
ール(5,9重量f15)およびトリメチロールプロパ
ン(3,9重量部)に、硬化促進用触媒としての1,2
−ジメチルイミダゾール(0,15重量部)を温度10
0℃の下に混ぜ合わせたものを用いた。Liquid substance B as a curing agent contains 1,4-butanediol (5,9 weight f15) and trimethylolpropane (3,9 parts by weight), and 1,2 as a curing accelerating catalyst.
-dimethylimidazole (0.15 parts by weight) at a temperature of 10
The mixture was used at 0°C.
そして、導入口4bから温度70℃、粘度2000セン
チボイスに保持した前記液状物Aを、また導入口4cか
ら温度50℃、粘度100センチボイズに保持した液状
物Bをそれぞれチャンバー1a内に導入した。Then, the liquid A maintained at a temperature of 70° C. and a viscosity of 2000 centivoise was introduced into the chamber 1a through the inlet 4b, and the liquid B maintained at a temperature of 50° C. and a viscosity of 100 centivoise was introduced into the chamber 1a through the inlet 4c.
両者の割合(重量比)は、液状物A 液状物B=100
: 6.9に設定した。The ratio (weight ratio) of both is Liquid A Liquid B = 100
: It was set to 6.9.
クリーニングブレード用成形金型は多数準備したうえ、
各金型をあらかしめ145℃に加熱しておき、混合撹拌
装置で混合撹拌した液状物を吐出管3aから各金型へ順
次間欠的に吐出させて注入した。In addition to preparing a large number of molds for cleaning blades,
Each mold was preheated to 145° C., and a liquid material mixed and stirred using a mixing and stirring device was intermittently discharged from the discharge pipe 3a into each mold.
液状物の吐出時間は6秒、吐出中止時間は6秒であった
。これにより、各金型内のウレタンプレポリマーは約2
〜3分で硬化し、脱型できた。The liquid material discharge time was 6 seconds, and the discharge stop time was 6 seconds. This results in approximately 20% of the urethane prepolymer in each mold.
It hardened in ~3 minutes and was able to be demolded.
上記のような速硬化性樹脂液を用いることにより短時間
でクリーニングブレードを成形することができた。By using the above-mentioned fast-curing resin liquid, a cleaning blade could be molded in a short time.
しかも、本装置のチャンバー18内壁や吐出管3a内壁
への樹脂液の付着は、第4図の装置に比べて非常に緩慢
で、150分間は連続使用可能であった。Moreover, the adhesion of the resin liquid to the inner wall of the chamber 18 and the inner wall of the discharge pipe 3a of this apparatus was much slower than that of the apparatus shown in FIG. 4, and the apparatus could be used continuously for 150 minutes.
すなわち、吐出管3aから吐出される樹脂液は、150
分間は混合比率および吐出量ともに適正であった。この
ように連続使用可能な時間が150分に延長されたので
、十分に実用化できるようになった。That is, the resin liquid discharged from the discharge pipe 3a is 150
Both the mixing ratio and discharge amount were appropriate. In this way, the continuous usable time has been extended to 150 minutes, making it fully practical.
また上記した使用データは、液状物Aと液状物Bとの完
全プレポリマー法により混合したものであるか、擬プレ
ポリマー法により概ね1 lの割合で且つ近似の粘度に
調整した両液状物を混合した樹脂液を用いるようにすれ
ば、連続使用時間か更に延長されることは明らかである
。In addition, the above usage data indicates whether liquid A and liquid B were mixed using the complete prepolymer method, or both liquids were mixed using the pseudo prepolymer method at a ratio of approximately 1 liter and adjusted to a similar viscosity. It is clear that if a mixed resin solution is used, the continuous use time will be further extended.
ところで、連続使用可能な時間の判定は、下記の方法て
行った。すなわち、供給タンク(図示せず)内の液状物
A(主剤)と液状物B(硬化剤)とをそれぞれポンプ(
図示せず)で送って導入口4b、4cからチャンバー1
a内に導入するが、運転開始時において、ポンプを介し
て供給タンクに循環される圧力と各導入口4b、4cか
らチャンバー1a内へ導入される圧力とを合わせておく
。そして、そのときの圧力を基準にしたうえて、ポンプ
の性能データに基づき、液状物A側が2.0kg/cm
″あるいは液状物B側が0.3kg/am”へ上昇する
までの範囲を、連続使用可能な時間と想定して判定した
。運転開始後から時間の経過に伴って、液状物A側およ
び液状物B側の導入圧がそれぞれ徐々に上昇していき、
液状物A側の導入圧が2.0kg/am”になる前に液
状物B側の導入圧が0.3kg/am’を超えにが、そ
の時点までの時間か150分であった。但し、この限界
圧力は使用する液状物AおよびBの粘度、ポンプの性能
、配管口径、単位時間当たりの吐出量等によって変化す
るものであり、一定の値ではない。なお、この直前に金
型に注入された樹脂液の混合比率を検査したが、その比
率は適正(許容)範囲にあり、またその成形品(樹脂製
品)も規格に合格するものであった。By the way, the continuous usable time was determined by the following method. That is, liquid material A (main agent) and liquid material B (curing agent) in a supply tank (not shown) are pumped (
(not shown) to the chamber 1 from the inlets 4b and 4c.
However, at the start of operation, the pressure circulated to the supply tank via the pump and the pressure introduced into the chamber 1a from the respective introduction ports 4b and 4c are matched. Based on the pressure at that time and the performance data of the pump, the liquid A side is 2.0 kg/cm.
The determination was made assuming that the range until the liquid B side rose to 0.3 kg/am was considered to be the period of continuous use. As time passes after the start of operation, the introduction pressures of the liquid A side and the liquid B side gradually increase,
It took 150 minutes for the introduction pressure on the liquid material B side to exceed 0.3 kg/am' before the introduction pressure on the liquid material A side reached 2.0 kg/am'. This limit pressure varies depending on the viscosity of the liquid materials A and B used, the performance of the pump, the diameter of the piping, the discharge amount per unit time, etc., and is not a constant value. The mixing ratio of the injected resin liquid was inspected, and it was found to be within an appropriate (tolerable) range, and the molded product (resin product) also passed the standards.
上記実施例では、速硬化性のポリウレタン樹脂溶液を混
合撹拌する場合を例にとって説明したが、本発明の装置
に使用可能な樹脂液は実施例に限定されるものではなく
、各種の樹脂液の混合撹拌に使用できる。In the above example, the case where a fast-curing polyurethane resin solution is mixed and stirred was explained as an example, but the resin liquid that can be used in the apparatus of the present invention is not limited to the example, and various resin liquids can be used. Can be used for mixing and stirring.
〔発明の効果]
以上説明したことから明らかなように、この発明の混合
撹拌装置は下記のような効果がある。[Effects of the Invention] As is clear from the above explanation, the mixing and stirring device of the present invention has the following effects.
すなわち、チャンバー内で液状物が停滞したり滞留した
りする箇所を極力少なくすると共に、チャンバー内だけ
でなく、吐出管内も冷却するようにしたので、特に速硬
化性の樹脂液を混合撹拌する場合にも、チャンバー内や
吐出管内で混合液が短時間に硬化して内壁に付着するこ
とが防止され、液状物の混合撹拌を長時間安定して行う
ことかできる。したがって、速硬化性の樹脂液を使用す
ることにより、樹脂製品の生産効率を大幅に向上し得て
、大量生産を可能にすると共に、製品コストの低減を図
れる。In other words, we have minimized the number of places in the chamber where the liquid material stagnates or accumulates, and also cooled not only the chamber but also the discharge pipe, especially when mixing and stirring fast-curing resin liquids. Also, the mixed liquid is prevented from hardening in a short time and adhering to the inner wall in the chamber or the discharge pipe, and the liquid can be mixed and stirred stably for a long time. Therefore, by using a fast-curing resin liquid, the production efficiency of resin products can be greatly improved, mass production becomes possible, and product costs can be reduced.
第1図はこの発明の実施例にかかる混合撹拌装置を示す
一部を断面で表した正面図、第2図は回転子の平面図、
第3図は回転子の底面図である。
第4図は本出願人が先に開発した混合撹拌装置を示す断
面図である。
1・・・装置本体、1a・・・チャンバー、2・胴部ケ
ーシング、3・・底部ケーシング、38・吐出管、4・
・蓋体、4b、4c・・・導入口、5.6・・・冷却ジ
ャケット、7・・・回転子、7b・・突起部、8 回転
軸、9・・・羽根部、10・・ネジ杆。FIG. 1 is a partially sectional front view showing a mixing and stirring device according to an embodiment of the present invention, FIG. 2 is a plan view of a rotor,
FIG. 3 is a bottom view of the rotor. FIG. 4 is a sectional view showing a mixing and stirring device previously developed by the applicant. DESCRIPTION OF SYMBOLS 1...Device body, 1a...Chamber, 2.Body casing, 3.Bottom casing, 38.Discharge pipe, 4.
・Lid, 4b, 4c...Inlet, 5.6...Cooling jacket, 7...Rotor, 7b...Protrusion, 8 Rotating shaft, 9...Blade part, 10...Screw Rod.
Claims (1)
管を備えた装置本体のチャンバー内に、撹拌用回転子を
その上端中央部で支持して回転可能に配備した、2種類
以上の液状物を撹拌混合して吐出させる混合撹拌装置で
あって、前記チャンバーの底部を前記吐出管の入口に向
けて傾斜させると共に、その底部形状に対応する形状に
前記回転子の下端部を形成して、その下端部に液状物搬
送用の複数の羽根部を、正転時に吐出管へ液状物が搬送
される向きに傾斜させて設け、 前記回転子の側周面に多数の突起部を突設し、正転時に
液状物を吐出させる向きにネジ部を刻設したネジ杆を、
前記回転子の下端中央部に突設して前記吐出管内に挿入
し、 前記装置本体のチャンバーおよび吐出管の周囲に、冷却
用ジャケットを配設したことを特徴とする混合撹拌装置
。[Claims] A stirring rotor is supported at the center of the upper end and is rotatable in the chamber of the main body of the device, which has a liquid material inlet at the upper end and a liquid material discharge pipe at the center of the lower end. A mixing/stirring device for agitating and discharging two or more types of liquid materials installed in a chamber, wherein the bottom of the chamber is inclined toward the inlet of the discharge pipe, and the bottom of the chamber is shaped to correspond to the shape of the bottom. A lower end of the rotor is formed, and a plurality of blades for transporting the liquid are provided on the lower end so as to be inclined in a direction in which the liquid is transported to the discharge pipe during forward rotation, and a side periphery of the rotor is provided. A threaded rod with many protrusions protruding from the surface and a threaded part engraved in the direction that discharges liquid during normal rotation.
A mixing and stirring device, characterized in that a cooling jacket is provided protruding from the center of the lower end of the rotor and inserted into the discharge pipe, and a cooling jacket is provided around the chamber of the device main body and the discharge pipe.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2237726A JPH0611389B2 (en) | 1990-09-07 | 1990-09-07 | Mixing and stirring device |
TW080106665A TW197958B (en) | 1990-09-07 | 1991-08-22 | |
DE4128549A DE4128549A1 (en) | 1990-09-07 | 1991-08-28 | Polyurethane doctor blade mfr. without gel deposit forming - involves mixing and stirring 2 or more liquids within vessel having inclined floor toward the outlet through which rotor screw protrudes |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2237726A JPH0611389B2 (en) | 1990-09-07 | 1990-09-07 | Mixing and stirring device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04118035A true JPH04118035A (en) | 1992-04-20 |
JPH0611389B2 JPH0611389B2 (en) | 1994-02-16 |
Family
ID=17019582
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2237726A Expired - Lifetime JPH0611389B2 (en) | 1990-09-07 | 1990-09-07 | Mixing and stirring device |
Country Status (3)
Country | Link |
---|---|
JP (1) | JPH0611389B2 (en) |
DE (1) | DE4128549A1 (en) |
TW (1) | TW197958B (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008068206A (en) * | 2006-09-14 | 2008-03-27 | Aisin Seiki Co Ltd | Two-liquid mixing device |
US8275302B2 (en) | 2007-01-29 | 2012-09-25 | Bando Chemical Industries, Ltd. | Blade for electrophotographic device with elastic rubber member constituted by edge/nip and base portions of different materials |
CN107685455A (en) * | 2017-10-23 | 2018-02-13 | 河南科技大学 | A kind of agitating paddle and the type vacuum injecting and forming machine using the agitating paddle |
CN111645216A (en) * | 2020-06-24 | 2020-09-11 | 宫恒桃 | Heating device for polystyrene processing |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0689865B1 (en) * | 1994-06-28 | 1998-09-30 | MTA Automation AG | Dynamic mixing head |
DE4433039B4 (en) * | 1994-09-16 | 2006-11-16 | Richard Frisse Gmbh | Devices for processing dispersions |
SE9802350D0 (en) | 1998-07-01 | 1998-07-01 | Borealis As | Mixing device |
CN112440401A (en) * | 2020-10-30 | 2021-03-05 | 江苏淼泓环保新材料科技有限公司 | Polyurethane mixing and stirring mechanism |
-
1990
- 1990-09-07 JP JP2237726A patent/JPH0611389B2/en not_active Expired - Lifetime
-
1991
- 1991-08-22 TW TW080106665A patent/TW197958B/zh active
- 1991-08-28 DE DE4128549A patent/DE4128549A1/en not_active Withdrawn
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008068206A (en) * | 2006-09-14 | 2008-03-27 | Aisin Seiki Co Ltd | Two-liquid mixing device |
US8275302B2 (en) | 2007-01-29 | 2012-09-25 | Bando Chemical Industries, Ltd. | Blade for electrophotographic device with elastic rubber member constituted by edge/nip and base portions of different materials |
CN107685455A (en) * | 2017-10-23 | 2018-02-13 | 河南科技大学 | A kind of agitating paddle and the type vacuum injecting and forming machine using the agitating paddle |
CN107685455B (en) * | 2017-10-23 | 2023-04-28 | 河南科技大学 | Stirring paddle and vacuum injection machine using same |
CN111645216A (en) * | 2020-06-24 | 2020-09-11 | 宫恒桃 | Heating device for polystyrene processing |
Also Published As
Publication number | Publication date |
---|---|
DE4128549A1 (en) | 1992-03-12 |
TW197958B (en) | 1993-01-11 |
JPH0611389B2 (en) | 1994-02-16 |
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