CN100484743C - Frother mixing head - Google Patents
Frother mixing head Download PDFInfo
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- CN100484743C CN100484743C CNB2004100008315A CN200410000831A CN100484743C CN 100484743 C CN100484743 C CN 100484743C CN B2004100008315 A CNB2004100008315 A CN B2004100008315A CN 200410000831 A CN200410000831 A CN 200410000831A CN 100484743 C CN100484743 C CN 100484743C
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Abstract
本发明涉及一种主要用于各种树脂泡沫塑料连续发泡生产,特别是适合酚醛树脂等高粘度树脂的连续发泡以及其他需要高速搅拌的、多组份的流体搅拌与发泡生产的发泡机混合头。设有电动机、叶轮、物料混合腔和至少1根进料管,叶轮轴与电动机联接,叶轮置于物料混合腔内,进料管与物料混合腔由轴向进料口连接,物料混合腔的前端设混合料喷嘴。与现有的设备相比,巧妙地采用沿轴向进料口进料的方法,避开了旋转流场外围的高压,克服了现有的弊端。叶轮头部设有螺旋推进段,有助于物料进入混合腔,同时也进一步避免了物料倒灌问题。采用电动机与叶轮直联的结构,不经过增速机构,简化了机械传动结构,提高了传动效率。容易实现高转速,从而大大提高产品质量。
The invention relates to a foaming foaming machine mainly used for the continuous foaming production of various resin foams, especially suitable for the continuous foaming of high-viscosity resins such as phenolic resin and other multi-component fluid stirring and foaming production that require high-speed stirring. Bubble machine mixing head. It is equipped with a motor, an impeller, a material mixing chamber and at least one feeding pipe, the impeller shaft is connected with the motor, the impeller is placed in the material mixing chamber, the feeding pipe and the material mixing chamber are connected by an axial feed port, and the material mixing chamber The front end is provided with a mixing nozzle. Compared with the existing equipment, the method of feeding material along the axial feed port is skillfully adopted, which avoids the high pressure around the swirling flow field and overcomes the existing disadvantages. The head of the impeller is equipped with a spiral propulsion section, which helps the material to enter the mixing chamber and further avoids the problem of material backflow. The structure of direct connection between the motor and the impeller is adopted, without a speed-increasing mechanism, which simplifies the mechanical transmission structure and improves the transmission efficiency. It is easy to achieve high speed, thus greatly improving product quality.
Description
技术领域 technical field
本发明涉及一种塑料压力发泡成型设备,主要用于各种树脂泡沫塑料的连续发泡生产,特别是适合酚醛树脂等高粘度树脂的连续发泡以及其他需要高速搅拌的、多组份的流体搅拌与发泡生产的发泡机混合头。The invention relates to a plastic pressure foam molding equipment, which is mainly used for the continuous foaming production of various resin foams, especially for the continuous foaming of high-viscosity resins such as phenolic resins and other multi-component products that require high-speed stirring. Foaming machine mixing head for fluid mixing and foaming production.
背景技术 Background technique
酚醛泡沫材料是一种新型阻燃性的泡沫保温材料,其生产设备由于原料粘度的不同,与目前已很成熟的聚氨酯发泡设备有很大的区别。目前已有很多厂家以原有的聚氨酯连续发泡设备,将其主要部件改为采用防腐蚀材料制作,用于酚醛泡沫材料的生产,由于酚醛树脂的粘度很高、密度很大,常发生进料口堵塞、树脂原料及混合物向其他物料管道回流等问题,实际上无法实现正常连续生产。此外由于混合头的叶轮转速越高,产品质量就越好,现有的设备常采用皮带或齿轮增速,有体积笨重、效率低等问题,而且所能够达到的最高转速非常有限。CN 1345656号专利公开了一种酚醛树脂低温发泡机,由三套储料罐、配量泵、配量齿轮泵、带马达的混合头、电磁阀、放料阀、输料管和回流管等组成。其中,混合头由混合室及装在混合室内由马达带转的转子及其上的涡叶片组成,其中,混合头使用OOCr17Ni14Mo2材料制成,转子与涡叶片使用OCr17Ni13Mo5材料制成。Phenolic foam material is a new type of flame-retardant foam insulation material. Due to the difference in raw material viscosity, its production equipment is very different from the current mature polyurethane foam equipment. At present, many manufacturers have changed the main parts of the original polyurethane continuous foaming equipment to anti-corrosion materials for the production of phenolic foam materials. Due to the high viscosity and high density of phenolic resin, it often occurs Problems such as blockage of the feed port, backflow of resin raw materials and mixtures to other material pipelines, etc., actually cannot achieve normal continuous production. In addition, the higher the speed of the impeller of the mixing head, the better the product quality. The existing equipment often adopts belt or gear speed increase, which has problems such as bulky size and low efficiency, and the maximum speed that can be achieved is very limited. CN 1345656 patent discloses a phenolic resin low-temperature foaming machine, which consists of three sets of storage tanks, metering pumps, metering gear pumps, mixing heads with motors, solenoid valves, discharge valves, feeding pipes and return pipes and so on. Among them, the mixing head is composed of a mixing chamber, a rotor driven by a motor in the mixing chamber and a vortex blade on it. The mixing head is made of OOCr17Ni14Mo2 material, and the rotor and vortex blade are made of OCr17Ni13Mo5 material.
发明内容 Contents of the invention
本发明旨在克服上述已有连续发泡设备存在的问题,提供一种主要用于各种树脂泡沫塑料的连续发泡生产,特别是适合酚醛树脂等高黏度树脂的连续发泡以及其他需要高速搅拌的、多组份的流体搅拌与发泡生产的发泡机混合头。The present invention aims to overcome the problems existing in the above-mentioned existing continuous foaming equipment, and provides a continuous foaming production mainly used for various resin foams, especially suitable for continuous foaming of high-viscosity resins such as phenolic resins, and other equipment that require high speed. Foamer mixing head for agitated, multi-component fluid agitation and foaming production.
本发明设有电动机、叶轮、物料混合腔和至少1根进料管,叶轮轴与电动机联接,叶轮置于物料混合腔内,进料管与物料混合腔由轴向进料口连接,物料混合腔的前端设混合料喷嘴(或挤出嘴)。The invention is provided with a motor, an impeller, a material mixing chamber and at least one feeding pipe, the impeller shaft is connected with the motor, the impeller is placed in the material mixing chamber, the feeding pipe and the material mixing chamber are connected by an axial feeding port, and the materials are mixed The front end of the cavity is provided with a mixing nozzle (or extrusion nozzle).
叶轮轴可由联轴器与电动机联接。用于物料搅拌混合的叶轮最好设推进段和混合段两个功能段,推进段可呈螺旋状结构;混合段可采用叶片式结构。在物料混合腔上除了轴向进料口之外尚可设径向进料口。The impeller shaft can be connected with the motor by a coupling. The impeller used for material stirring and mixing is preferably provided with two functional sections, a propulsion section and a mixing section. The propulsion section can be in a spiral structure; the mixing section can adopt a blade-type structure. In addition to the axial feed port, a radial feed port can also be set on the material mixing chamber.
与现有的可以进行酚醛泡沫连续生产的设备相比,现有的树脂发泡机混合头均采用径向进料口,在一种物料的密度和粘度较高的情况下,由于旋转流场外围的高压,容易造成混合物向密度和粘度较低的物料进料口倒灌、不同组份的物料在进料口附近的管道内混串、凝固、堵塞等问题。本发明巧妙地采用沿轴向进料口进料的方法,避开了旋转流场外围的高压,克服了现有的弊端。Compared with the existing equipment capable of continuous production of phenolic foam, the mixing heads of the existing resin foaming machines all use radial feed ports. The high pressure in the periphery will easily cause the mixture to pour back into the feed port of the material with lower density and viscosity, and the materials of different components will mix, solidify, and block in the pipeline near the feed port. The present invention skillfully adopts the method of feeding material along the axial feeding port, avoids the high pressure on the periphery of the rotating flow field, and overcomes the existing disadvantages.
现有的树脂发泡机混合头叶轮没有明确的、独立的推进功能段,整个混合腔沿轴向的压力分布没有合理的梯度。物料混合发泡时所产生的高压,一方面使混合物从挤出嘴喷出,另一方面也使混合物沿密度和粘度较低的物料进料口附近侵入。本发明在混合叶轮头部设计了一个螺旋推进段,在每分钟数千转的高转速下,推进段靠近进料口一端产生了低压甚至负压,有助于物料进入混合腔,同时也进一步避免了物料倒灌问题。The existing impeller of the mixing head of the resin foaming machine has no clear and independent propulsion function section, and the pressure distribution along the axial direction of the entire mixing chamber has no reasonable gradient. The high pressure generated when the materials are mixed and foamed, on the one hand, the mixture is ejected from the extrusion nozzle, and on the other hand, the mixture is invaded near the material inlet with lower density and viscosity. In the present invention, a screw propulsion section is designed at the head of the mixing impeller. Under the high speed of thousands of revolutions per minute, the end of the propulsion section near the feed inlet generates low pressure or even negative pressure, which helps the material to enter the mixing chamber and further The problem of material backflow is avoided.
现有的树脂发泡机混合头由电动机通过增速机构驱动,以取得高质量混合所需的高转速。本发明采用电动机与叶轮直联的结构,不经过增速机构,简化了机械传动结构,提高了传动效率。容易实现高转速,从而大大提高产品质量。高转速可由一般的变频技术取得。The mixing head of the existing resin foaming machine is driven by a motor through a speed increasing mechanism to obtain the high speed required for high-quality mixing. The invention adopts the structure in which the motor and the impeller are directly connected without passing through a speed-increasing mechanism, simplifies the mechanical transmission structure, and improves the transmission efficiency. It is easy to achieve high speed, thus greatly improving product quality. High speed can be obtained by general frequency conversion technology.
附图说明 Description of drawings
图1为本发明的原理示意图。Fig. 1 is a schematic diagram of the principle of the present invention.
图2为本发明实施例的结构示意图。Fig. 2 is a schematic structural diagram of an embodiment of the present invention.
具体实施方式 Detailed ways
实施例1Example 1
如图1,2所示,本发明设有电动机1、联轴器2、叶轮轴3、叶轮4、3根轴向进料管5、物料混合腔6和喷嘴7,叶轮轴3通过联轴器2与电动机1联接,叶轮4置于物料混合腔6内,轴向进料管5与物料混合腔6由轴向进料口连接,物料混合腔6的前端与混合料喷嘴7连接。叶轮4分为螺旋状推进段4.1和叶片式混合段4.2两个功能段。As shown in Figures 1 and 2, the present invention is provided with a
实施例2Example 2
与实施例1类似,其区别在于可设径向进料管,径向进料管与物料混合腔通过径向进料口连接。Similar to
可采用转速3600转/分以上的电动机,并采用与叶轮轴直联的结构,不经过增速机构。A motor with a speed of 3600 r/min or more can be used, and the structure directly connected with the impeller shaft is adopted without passing through the speed increasing mechanism.
参见图1,2,多种液态物料由3根轴向进料管5通过轴向进料口进入混合腔6。因为叶轮螺旋推进段4.1的高速旋转,造成进料口附近的负压,使物料顺利进入混合腔。若主料的粘度和密度特别高,可由位于混合段的径向进料管通过径向进料口直接进入混合腔,而低密度物料仍然经由轴向进料管5进入混合腔。这时,螺旋推进段4.1起着旋转密封件的作用,可有效防止物料倒灌现象。物料经高速旋转的叶轮混合段4.2混合后,由喷嘴7输出。Referring to Figures 1 and 2, a variety of liquid materials enter the
显然,本发明可用于各种树脂泡沫塑料的连续发泡生产,特别适合酚醛树脂等高粘度树脂的连续发泡工艺,也适用于其他需要高速搅拌的、多组份的流体搅拌及发泡工艺。Obviously, the present invention can be used in the continuous foaming production of various resin foams, especially suitable for the continuous foaming process of high-viscosity resins such as phenolic resin, and also suitable for other multi-component fluid stirring and foaming processes that require high-speed stirring .
Claims (3)
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| Application Number | Priority Date | Filing Date | Title |
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| CNB2004100008315A CN100484743C (en) | 2004-01-02 | 2004-01-02 | Frother mixing head |
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| Application Number | Priority Date | Filing Date | Title |
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| CNB2004100008315A CN100484743C (en) | 2004-01-02 | 2004-01-02 | Frother mixing head |
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| CN1555926A CN1555926A (en) | 2004-12-22 |
| CN100484743C true CN100484743C (en) | 2009-05-06 |
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| CNB2004100008315A Expired - Fee Related CN100484743C (en) | 2004-01-02 | 2004-01-02 | Frother mixing head |
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Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103273609A (en) * | 2013-05-21 | 2013-09-04 | 济南圣泉集团股份有限公司 | Mixing device |
| CN104353373B (en) * | 2014-11-03 | 2017-10-31 | 吕国成 | Foaming machine |
| CN106493894A (en) * | 2016-10-17 | 2017-03-15 | 郑州峰泰纳米材料有限公司 | A kind of online dynamic mixer |
| DE102018122797A1 (en) * | 2018-09-18 | 2020-03-19 | Kraussmaffei Technologies Gmbh | Device for molding a plastic component |
| CN109772613A (en) * | 2019-01-30 | 2019-05-21 | 江苏安全技术职业学院 | A foam slurry injection device |
| CN117065957B (en) * | 2023-10-13 | 2023-12-22 | 山东泰宇消防科技集团有限公司 | Rotary mixing convection adjustable spray head |
Citations (7)
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| US4515908A (en) * | 1979-05-11 | 1985-05-07 | Snia Viscosa Societa Nazionale Industria Applicazioni Viscosa S.P.A. | Liquid foams of reinforced unsaturated polyester resins and process for making the same |
| CN2128581Y (en) * | 1992-08-05 | 1993-03-24 | 陈运进 | Polyurethane foam machine spray gun head |
| CN2304525Y (en) * | 1998-02-25 | 1999-01-20 | 浙江天屹集团有限公司 | Pressure reducing foaming device of plastic injection machine |
| CN2405739Y (en) * | 1999-11-19 | 2000-11-15 | 王启宇 | Head mixing device of polyurethane foaming machine |
| CN2465814Y (en) * | 2001-02-21 | 2001-12-19 | 玉环县富达电器厂 | Spray gun of polyurethane foaming apparatus |
| CN1345656A (en) * | 2000-09-26 | 2002-04-24 | 广州擎天新材料研究开发有限公司 | Phenolic resin low temp. foaming machine |
| CN2562956Y (en) * | 2002-08-09 | 2003-07-30 | 凯力实业股份有限公司 | Double-layer secondary mixing foaming filling machine |
-
2004
- 2004-01-02 CN CNB2004100008315A patent/CN100484743C/en not_active Expired - Fee Related
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4515908A (en) * | 1979-05-11 | 1985-05-07 | Snia Viscosa Societa Nazionale Industria Applicazioni Viscosa S.P.A. | Liquid foams of reinforced unsaturated polyester resins and process for making the same |
| CN2128581Y (en) * | 1992-08-05 | 1993-03-24 | 陈运进 | Polyurethane foam machine spray gun head |
| CN2304525Y (en) * | 1998-02-25 | 1999-01-20 | 浙江天屹集团有限公司 | Pressure reducing foaming device of plastic injection machine |
| CN2405739Y (en) * | 1999-11-19 | 2000-11-15 | 王启宇 | Head mixing device of polyurethane foaming machine |
| CN1345656A (en) * | 2000-09-26 | 2002-04-24 | 广州擎天新材料研究开发有限公司 | Phenolic resin low temp. foaming machine |
| CN2465814Y (en) * | 2001-02-21 | 2001-12-19 | 玉环县富达电器厂 | Spray gun of polyurethane foaming apparatus |
| CN2562956Y (en) * | 2002-08-09 | 2003-07-30 | 凯力实业股份有限公司 | Double-layer secondary mixing foaming filling machine |
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| CN1555926A (en) | 2004-12-22 |
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