CN201200888Y - High-efficiency chemical reactor combined with stirred tank and static mixer - Google Patents
High-efficiency chemical reactor combined with stirred tank and static mixer Download PDFInfo
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- CN201200888Y CN201200888Y CNU2008200364633U CN200820036463U CN201200888Y CN 201200888 Y CN201200888 Y CN 201200888Y CN U2008200364633 U CNU2008200364633 U CN U2008200364633U CN 200820036463 U CN200820036463 U CN 200820036463U CN 201200888 Y CN201200888 Y CN 201200888Y
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Abstract
Description
技术领域 technical field
本实用新型涉及一种用于沥青化学改性的工业反应装置。属于化学反应设备制造的技术领域。The utility model relates to an industrial reaction device for asphalt chemical modification. The invention belongs to the technical field of chemical reaction equipment manufacture.
背景技术 Background technique
对于两相反应或三相反应来说,宏观反应速率取决于相间传质速率和化学反应速率中的慢者。如果一个多相反应的决速步骤是相间传质,毫无疑问要提高整个反应的速率就要从强化传质入手。在环氧沥青的生产中,沥青的功能化就是一个比较典型的多相反应,而且控制步骤是传质;将残留的对沥青进行功能化改性的小分子化合物进行转换的反应也是一种相间传质控制的快速反应,如果温度控制不当或传质速率不够就会严重影响反应产物的性能,最终影响环氧沥青的性能。可见,在环氧沥青的生产中强化传质是获得质量稳定可靠,性能优异的最终产品的关键,而传质的强化跟化学反应器的设计有着直接的关系。许多其它物料的反应体系也是如此。For two-phase or three-phase reactions, the macroscopic reaction rate depends on the slower of the mass transfer rate between the phases and the chemical reaction rate. If the rate-determining step of a heterogeneous reaction is mass transfer between phases, there is no doubt that to increase the rate of the entire reaction, we must start with the enhancement of mass transfer. In the production of epoxy asphalt, the functionalization of asphalt is a typical heterogeneous reaction, and the control step is mass transfer; the reaction of converting the remaining small molecular compounds that functionally modify asphalt is also an interphase reaction. The rapid response of mass transfer control, if the temperature is not properly controlled or the mass transfer rate is not enough, it will seriously affect the performance of the reaction product, and finally affect the performance of epoxy asphalt. It can be seen that the enhancement of mass transfer in the production of epoxy asphalt is the key to obtain a final product with stable and reliable quality and excellent performance, and the enhancement of mass transfer has a direct relationship with the design of the chemical reactor. The same is true for reaction systems of many other materials.
CN01810595.5给出了一种用来制备聚苯胺的方法和装置,该装置是几个并联的装有静态混合器的管式反应器、一个搅拌釜和循环泵串联构成的回路;其中在管式反应器外部设置了夹套控温。ZL200420023052.2提供了类似的方法,区别在于为了应对高黏度物料造成的传热问题在回路中增加了一个换热器。CN1056895A则公开了一种适用于微生物发酵方面的装置,其突出特点是反应器中没有搅拌桨,而是设置了适合生物发酵的挡板配合静态混合器和循环泵使用。CN01810595.5 provides a kind of method and device for preparing polyaniline, and this device is the loop that several parallel tubular reactors equipped with static mixers, a stirred tank and circulation pump are connected in series; A jacket was installed outside the reactor for temperature control. ZL200420023052.2 provides a similar method, the difference is that a heat exchanger is added in the loop to deal with the heat transfer problem caused by high-viscosity materials. CN1056895A discloses a device suitable for microbial fermentation. Its outstanding feature is that there is no stirring paddle in the reactor, but a baffle suitable for biological fermentation is provided to cooperate with a static mixer and a circulation pump.
总的看来,在间歇式反应釜中,为了增强传质效果采用静态混合器和外循环是一种趋势;采用的反应釜则是根据各个反应体系自身的特点量身定做。In general, in batch reactors, it is a trend to use static mixers and external circulation in order to enhance the mass transfer effect; the reactors used are tailored according to the characteristics of each reaction system.
发明内容 Contents of the invention
技术问题:本实用新型旨在提供一种结构简单,性能稳定可靠,经济适用的搅拌釜与静态混合器组合的高效化学反应器,能够满足反应体系的快速步骤是相间传质的多相快速反应体系的间歇式高效化学反应器。Technical problem: The purpose of this utility model is to provide a simple structure, stable and reliable performance, an economical and applicable high-efficiency chemical reactor combined with a stirred tank and a static mixer, which can meet the fast step of the reaction system is the multiphase rapid reaction of mass transfer between phases System of intermittent high-efficiency chemical reactors.
技术方案:本实用新型的搅拌釜与静态混合器组合的高效化学反应器包括搅拌釜、物料循环泵和静态混合器以及构成回路的连接管道;其中:搅拌釜、物料循环泵和静态混合器由连接管道将其连接成一个闭合的回路,反应釜的上部为进料口,下部为出料口,反应釜中设有搅拌桨。Technical solution: The high-efficiency chemical reactor combined with a stirred tank and a static mixer of the utility model includes a stirred tank, a material circulation pump, a static mixer and connecting pipes forming a loop; wherein: the stirred tank, the material circulation pump and the static mixer are composed of The connecting pipe connects it into a closed circuit, the upper part of the reactor is the inlet, the lower part is the outlet, and the reactor is equipped with a stirring paddle.
搅拌反应釜的顶部设有冷凝回流装置。搅拌反应釜的搅拌桨根据各种反应特征和物料特性,为涡轮式,或桨式,或推进式,或锚式以及螺杆螺带式中的一种或组合。静态混合器为波纹板型,或单螺旋型,或双螺旋型或横条型静态混合器,静态混合器外包覆保温层。搅拌反应釜为夹套结构,管道外包覆保温层。静态混合器和物料循环泵的安装位置可以互换。The top of the stirred reactor is equipped with a condensation reflux device. According to various reaction characteristics and material characteristics, the stirring paddle of the stirred reactor is one or a combination of turbine type, paddle type, pusher type, anchor type and screw ribbon type. The static mixer is a corrugated plate type, or a single helix type, or a double helix type or a horizontal strip type static mixer, and the static mixer is covered with an insulating layer. The stirred reactor is a jacketed structure, and the pipe is covered with an insulation layer. The installation positions of the static mixer and material circulation pump can be interchanged.
有益效果:通过釜内搅拌和外循环两种措施强化了传质和传热,通过静态混合器进一步加速了传质和传热过程,大大提高了设备的利用率、在最大程度上削弱了放大效应,提高了产品质量;结构简单,性能稳定可靠,经济适用。Beneficial effects: the mass transfer and heat transfer are enhanced through the two measures of internal stirring and external circulation, and the mass transfer and heat transfer process is further accelerated through the static mixer, which greatly improves the utilization rate of the equipment and weakens the amplification to the greatest extent. Effect, improved product quality; simple structure, stable and reliable performance, economical and applicable.
附图说明 Description of drawings
图1是本实用新型实施方式1的结构示意图。Fig. 1 is a schematic structural view of Embodiment 1 of the present utility model.
图2是本是用新型实施方式2的结构示意图。Fig. 2 is a schematic structural view of the second embodiment of the present invention.
具体实施方式 Detailed ways
下面通过具体的实施例对本发明进一步说明,但是实施例不是对本实用新型的限制。The present invention is further described below by specific examples, but the examples are not limitations of the present utility model.
搅拌釜与静态混合器组合的高效化学反应器,其特征在于该反应器包括搅拌釜1、物料循环泵3和静态混合器2以及构成回路的连接管道;其中:搅拌釜1、物料循环泵3和静态混合器2由连接管道将其连接成一个闭合的回路,反应釜1的上部为进料口,下部为出料口,反应釜1中设有搅拌桨。A high-efficiency chemical reactor combined with a stirred tank and a static mixer is characterized in that the reactor includes a stirred tank 1, a
所述的搅拌釜的顶部可以根据需要增设冷凝回流装置。A condensation reflux device can be added on the top of the stirred tank as required.
所述的搅拌釜与静态混合器组合的高效化学反应器中的静态混合器和物料循环泵的安装位置可以互换。The installation positions of the static mixer and the material circulation pump in the high-efficiency chemical reactor combining the stirred tank and the static mixer can be interchanged.
所述的搅拌釜的搅拌桨型式可选,以满足各种反应特征和物料特性。The stirring paddle type of the stirring tank is optional to meet various reaction characteristics and material characteristics.
所述的搅拌釜的搅拌桨型式可以是:涡轮式,桨式,推进式及锚式的一种或组合。The paddle type of the stirring tank can be one or a combination of turbine type, paddle type, propulsion type and anchor type.
所述的静态混合器的型号可以是:波纹板型,单螺旋型,双螺旋型或横条型。比较好的是采用波纹板型。The model of the static mixer can be: corrugated plate type, single helix type, double helix type or horizontal bar type. It is better to use corrugated plate type.
本是用新型所述的搅拌釜与静态混合器组合的高效化学反应器,其特征在于反应釜为夹套结构,管道外包覆保温层。This is a high-efficiency chemical reactor combined with a new type of stirred tank and a static mixer. It is characterized in that the reactor is a jacket structure, and the pipe is covered with an insulating layer.
实施例1:Example 1:
参看图1,主要包括:反应釜,循环泵,静态混合器及其相连的管道。其中反应釜中的搅拌桨采用下层锚式、上层六直叶涡轮式双层搅拌桨,循环泵采用专用沥青泵,静态混合器采用波纹板型。Referring to Figure 1, it mainly includes: reactor, circulating pump, static mixer and its connected pipelines. Among them, the stirring paddle in the reaction kettle adopts the lower anchor type, the upper layer has six straight blade turbine type double-layer stirring paddles, the circulation pump adopts a special asphalt pump, and the static mixer adopts a corrugated plate type.
实施例2:Example 2:
参看图2,主要包括:反应釜,循环泵,静态混合器及相连管道。其中反应釜上增设冷凝回流装置,搅拌桨采用下层框式、上层涡轮式双层搅拌桨,循环泵采用无泄漏流程泵,静态混合器采用双螺旋型。Referring to Figure 2, it mainly includes: reactor, circulation pump, static mixer and connected pipelines. Among them, a condensation reflux device is added to the reaction kettle, the stirring impeller adopts the lower frame type, the upper layer turbine type double-layer stirring impeller, the circulation pump adopts a non-leakage process pump, and the static mixer adopts a double-helix type.
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Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102285918A (en) * | 2011-07-29 | 2011-12-21 | 上海福达精细化工有限公司 | Method for producing ethoxy quinoline |
| CN102908966A (en) * | 2012-10-11 | 2013-02-06 | 四川省精细化工研究设计院 | Environment-friendly liquid circulation reactor |
| CN103816846A (en) * | 2014-02-26 | 2014-05-28 | 山东富达装饰工程有限公司 | Production system for anti-pollution chemical coating on surface of metal in water |
| CN105032316A (en) * | 2015-08-31 | 2015-11-11 | 句容宁武科技开发有限公司 | Pipeline reactor combined device for modified asphalt |
| CN105062535A (en) * | 2015-08-31 | 2015-11-18 | 句容宁武科技开发有限公司 | Method for continuously producing modified asphalt |
| CN106010962A (en) * | 2016-06-17 | 2016-10-12 | 山东宝莫生物化工股份有限公司 | Catalytic hydration reactor and method for producing acrylamide through same |
| CN107399993A (en) * | 2017-08-31 | 2017-11-28 | 北京沃尔夫斯科技有限公司 | A kind of kitchen garbage aerobic sigestion system |
| CN107803156A (en) * | 2017-11-09 | 2018-03-16 | 大丰鑫源达化工有限公司 | A kind of new speed up gas and liquid or the device of liquid liquid mixing |
| CN108745026A (en) * | 2018-08-01 | 2018-11-06 | 上海优华系统集成技术股份有限公司 | A kind of homogeneous pretreatment system and method for being adapted to pyrogenic process and handling clear tank sludge |
| CN110302736A (en) * | 2019-08-07 | 2019-10-08 | 上海蓝科石化环保科技股份有限公司 | Exchange heat polymerization reaction system and method in a kind of kettle for strongly exothermic polymerization reaction |
| CN112844180A (en) * | 2020-12-29 | 2021-05-28 | 煤炭科学技术研究院有限公司 | External forced dispersing device for improving dispersing and mixing capacity of stirring kettle |
| CN112980644A (en) * | 2021-02-20 | 2021-06-18 | 四川乐智机电工程有限公司 | Zero-wine-loss beer high-concentration dilution system and dilution method |
| WO2023118971A1 (en) * | 2021-12-24 | 2023-06-29 | Vinati Organics Limited | An buffer reactor for the preparation of acrn-sulphate for synthesis of acrylamido tertiary butyl sulfonic acid and process implemented thereon |
-
2008
- 2008-06-06 CN CNU2008200364633U patent/CN201200888Y/en not_active Expired - Lifetime
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102285918A (en) * | 2011-07-29 | 2011-12-21 | 上海福达精细化工有限公司 | Method for producing ethoxy quinoline |
| CN102908966A (en) * | 2012-10-11 | 2013-02-06 | 四川省精细化工研究设计院 | Environment-friendly liquid circulation reactor |
| CN102908966B (en) * | 2012-10-11 | 2015-04-08 | 四川省精细化工研究设计院 | Environment-friendly liquid circulation reactor |
| CN103816846A (en) * | 2014-02-26 | 2014-05-28 | 山东富达装饰工程有限公司 | Production system for anti-pollution chemical coating on surface of metal in water |
| CN103816846B (en) * | 2014-02-26 | 2015-03-18 | 山东富达装饰工程有限公司 | Production system for anti-pollution chemical coating on surface of metal in water |
| CN105032316A (en) * | 2015-08-31 | 2015-11-11 | 句容宁武科技开发有限公司 | Pipeline reactor combined device for modified asphalt |
| CN105062535A (en) * | 2015-08-31 | 2015-11-18 | 句容宁武科技开发有限公司 | Method for continuously producing modified asphalt |
| CN106010962A (en) * | 2016-06-17 | 2016-10-12 | 山东宝莫生物化工股份有限公司 | Catalytic hydration reactor and method for producing acrylamide through same |
| CN107399993A (en) * | 2017-08-31 | 2017-11-28 | 北京沃尔夫斯科技有限公司 | A kind of kitchen garbage aerobic sigestion system |
| CN107803156A (en) * | 2017-11-09 | 2018-03-16 | 大丰鑫源达化工有限公司 | A kind of new speed up gas and liquid or the device of liquid liquid mixing |
| CN108745026A (en) * | 2018-08-01 | 2018-11-06 | 上海优华系统集成技术股份有限公司 | A kind of homogeneous pretreatment system and method for being adapted to pyrogenic process and handling clear tank sludge |
| CN108745026B (en) * | 2018-08-01 | 2024-04-05 | 上海优华系统集成技术股份有限公司 | Homogenizing pretreatment system and method suitable for treating clean tank sludge by coking method |
| CN110302736A (en) * | 2019-08-07 | 2019-10-08 | 上海蓝科石化环保科技股份有限公司 | Exchange heat polymerization reaction system and method in a kind of kettle for strongly exothermic polymerization reaction |
| CN112844180A (en) * | 2020-12-29 | 2021-05-28 | 煤炭科学技术研究院有限公司 | External forced dispersing device for improving dispersing and mixing capacity of stirring kettle |
| CN112980644A (en) * | 2021-02-20 | 2021-06-18 | 四川乐智机电工程有限公司 | Zero-wine-loss beer high-concentration dilution system and dilution method |
| WO2023118971A1 (en) * | 2021-12-24 | 2023-06-29 | Vinati Organics Limited | An buffer reactor for the preparation of acrn-sulphate for synthesis of acrylamido tertiary butyl sulfonic acid and process implemented thereon |
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