CN201172020Y - Internal mixing pneumatic atomizing nozzle with extended diverging section - Google Patents
Internal mixing pneumatic atomizing nozzle with extended diverging section Download PDFInfo
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- CN201172020Y CN201172020Y CNU2007203060156U CN200720306015U CN201172020Y CN 201172020 Y CN201172020 Y CN 201172020Y CN U2007203060156 U CNU2007203060156 U CN U2007203060156U CN 200720306015 U CN200720306015 U CN 200720306015U CN 201172020 Y CN201172020 Y CN 201172020Y
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Abstract
Description
一、技术领域 1. Technical field
本实用新型涉及一种带有加长扩张段的内混式气动雾化喷嘴,属于对以气(汽)体为雾化介质的液体雾化喷嘴所进行的改进。The utility model relates to an internal mixing pneumatic atomizing nozzle with an extended expansion section, which belongs to the improvement of the liquid atomizing nozzle with gas (steam) body as the atomizing medium.
二、背景技术 2. Background technology
在催化裂化等反应中,原料油的雾化是关键问题。它对提高反应速度和反应选择性、减少生焦和干气起着重要的作用;在燃烧中,燃油的雾化对提高燃烧效率,降低污染起着重要作用。尤其对原料油重质化和劣质化,原料雾化的影响更加明显,良好的原料雾化需要优良的雾化喷嘴。目前常用的雾化喷嘴为内混式气动雾化喷嘴,如中国科学院的KH-3催化雾化喷嘴,中国石化总公司洛阳工程的LPC催化雾化喷嘴、美国石伟公司靶式雾化喷嘴、北京神火雾化喷嘴等,这类喷嘴充分利用了蒸汽(气体)的能量,雾化油料细度较细(一般水-空气冷模实验、质量平均粒度约为60μm左右)。有的喷嘴也考虑了反应或燃烧所需要的雾矩形状,但均未考虑周围反应环境高温对物化的影响。近几年来,重油、渣油催化裂化或燃烧已成趋势,对产品的选择性、节能和环保的要求越来越高。原有的液体雾化喷嘴已不能适应这种新的要求。针对新的要求,利用新的重油雾化理论,设计一种能够充分利用雾化介质能量和周围反应环境的高温条件、雾化粒度细、粒度分布范围窄、雾矩形状适合反应要求的高效液体雾化喷嘴,一直是有关科技工作者研究的课题。In reactions such as catalytic cracking, the atomization of raw oil is a key issue. It plays an important role in improving reaction speed and reaction selectivity, reducing coke and dry gas; in combustion, fuel atomization plays an important role in improving combustion efficiency and reducing pollution. Especially for heavy and inferior raw material oil, the impact of raw material atomization is more obvious, and good raw material atomization requires excellent atomizing nozzles. At present, the commonly used atomizing nozzles are internal mixing pneumatic atomizing nozzles, such as the KH-3 catalytic atomizing nozzle of the Chinese Academy of Sciences, the LPC catalytic atomizing nozzle of the Luoyang Project of Sinopec Corporation, the target atomizing nozzle of the American Shiwei Company, Beijing Shenhuo atomizing nozzle, etc., this type of nozzle makes full use of the energy of steam (gas), and the fineness of atomized oil is finer (general water-air cold model experiment, the mass average particle size is about 60 μm). Some nozzles also consider the shape of the fog rectangle required for reaction or combustion, but none of them consider the influence of the high temperature of the surrounding reaction environment on the physicochemical properties. In recent years, catalytic cracking or combustion of heavy oil and residual oil has become a trend, and the requirements for product selectivity, energy saving and environmental protection are getting higher and higher. The original liquid atomizing nozzle can no longer meet this new requirement. In response to new requirements, using the new heavy oil atomization theory, design a high-efficiency liquid that can make full use of the energy of the atomization medium and the high-temperature conditions of the surrounding reaction environment, fine atomization particle size, narrow particle size distribution range, and rectangular shape of the fog suitable for the reaction requirements Atomizing nozzles have always been a subject of research by relevant scientific and technological workers.
三、发明内容 3. Contents of the invention
本实用新型的目的就在于避免现有技术的不足,而提供一种带有加长扩张段的内混式气动雾化喷嘴。The purpose of the utility model is to avoid the deficiencies of the prior art, and provide an internal mixing pneumatic atomizing nozzle with an extended expansion section.
本实用新型的目的这样实现的,主要由套管、错流式多点注汽喷管、油气混合室、雾化喷头、加长扩张段依次同轴串联连接而成。套管入口段设计有原料油的入口,错流式多点注汽喷管设计有3~8排交错排列的注汽小孔,它通过凸台与套管同轴连接并封闭入口端,凸台上设计有和第一排注汽小孔孔数相同、交错垂直相碰撞的注油小孔,错流式多点注汽喷管安装在油气混合室之前,雾化喷头连接在油气混合室之后,雾化喷头由收缩段、喉部和扩张段构成,雾化喷头的扩张段再连接一段扩张加长段,雾化喷头和扩张加长段的截面形状可以是圆形、环形、扁平形。The purpose of this utility model is realized in this way, mainly by sleeve pipe, cross-flow type multi-point steam injection nozzle, oil-gas mixing chamber, atomizing spray nozzle, lengthened expansion section successively coaxially connected in series to form. The casing inlet section is designed with the inlet of raw material oil, and the cross-flow multi-point steam injection nozzle is designed with 3 to 8 rows of staggered steam injection holes, which are coaxially connected with the casing through the boss and close the inlet end. The platform is designed with the same number of small steam injection holes as the first row of small steam injection holes, which are staggered and vertically collided with each other. The cross-flow multi-point steam injection nozzle is installed before the oil-gas mixing chamber, and the atomizing nozzle is connected after the oil-gas mixing chamber. , the atomizing nozzle is composed of a constriction section, a throat and an expansion section, and the expansion section of the atomization nozzle is connected with an expansion extension section, and the cross-sectional shape of the atomization nozzle and the expansion extension section can be circular, circular, or flat.
依据本实用新型的设计,可以利用少量蒸汽(气体)通过错流式多点注汽喷管和从凸台高速注入的原料油在油气混合室内交错混合形成良好的空间混合和雾化,此时,雾化后的油气进入喷管锥形头与雾化喷头的收缩段形成环形喉部和喷头喉部两次变细,并经扩张加长段与周围反应环境的高温换热,油雾温度升高,可以更加充分的反应或燃烧,提高反应速度和反应选择性,减少干气和生焦,提高燃烧效率,减少污染。According to the design of the utility model, a small amount of steam (gas) can be used to pass through the cross-flow multi-point steam injection nozzle and the raw material oil injected at high speed from the boss in the oil-gas mixing chamber to form good spatial mixing and atomization. , the atomized oil and gas enter the conical head of the nozzle and the contraction section of the atomization nozzle to form an annular throat and the throat of the nozzle is thinned twice, and exchange heat with the high temperature of the surrounding reaction environment through the expansion and extension section, and the temperature of the oil mist rises High, can react or burn more fully, increase reaction speed and reaction selectivity, reduce dry gas and coke, improve combustion efficiency, and reduce pollution.
四、附图说明 4. Description of drawings
附图是本实用新型的结构示意图。Accompanying drawing is the structural representation of the utility model.
附图的图面设明如下;The drawings of the accompanying drawings are set as follows;
1.套管 2.错流式多点注汽喷管 3.油汽混合室 4.雾化喷头 5.扩张加长段 6.原料油入口1.
下面结合附图和实施例来详细描述依据本实用新型所提供的带有加长扩张段的内混式气动雾化喷嘴的具体结构。The specific structure of the internal mixing pneumatic atomizing nozzle with extended expansion section provided by the utility model will be described in detail below with reference to the drawings and embodiments.
五、具体实施方式 5. Specific implementation
本实用新型所提出的带有加长扩张段的内混式气动雾化喷嘴是由套管(1)、错流式多点注汽喷管(2)、油气混合室(3)、雾化喷头(4)、加长扩张段(5)依次同轴串联连接而成。套管(1)入口段设计有原料油的入口(6),错流式多点注汽喷管(2)设计有3~8排交错排列的注汽小孔,它通过凸台与套管(1)同轴连接并封闭入口端,凸台上设计有和第一排注汽小孔孔数相同、交错垂直相碰撞的注油小孔,错流式多点注汽喷管(2)安装在油气混合室(3)之前,雾化喷头(4)连接在油气混合室(5)之后,雾化喷头(4)由收缩段、喉部和扩张段串联而成,雾化喷头(4)的扩张段再连接一段扩张加长段(5),雾化喷头和扩张加长段的截面形状可以是圆形、环形、扁平形。The internal mixing pneumatic atomizing nozzle with extended expansion section proposed by the utility model is composed of a casing (1), a cross-flow multi-point steam injection nozzle (2), an oil-gas mixing chamber (3), and an atomizing nozzle. (4), lengthened expansion section (5) are connected in series coaxially successively and form. The inlet section of casing (1) is designed with feed oil inlet (6), and the cross-flow multi-point steam injection nozzle (2) is designed with 3 to 8 rows of staggered steam injection holes, which pass through the boss and the casing. (1) Coaxially connect and close the inlet end, the boss is designed with the same number of small steam injection holes as the first row of small steam injection holes, staggered and vertically collided with each other, and the cross-flow multi-point steam injection nozzle (2) is installed Before the oil-gas mixing chamber (3), the atomizing nozzle (4) is connected after the oil-gas mixing chamber (5). The expansion section connects a section of expansion extension section (5) again, and the cross-sectional shape of atomizing nozzle and expansion extension section can be circular, annular, flat shape.
实施本实用新型可以实现以下优点:(1)雾化蒸汽用量少,通常为原料油的2-5%;(2)多次雾化,雾化粒度细,分布范围窄,与同类喷嘴相比,雾化效果明显提高;(3)利用高速蒸汽(气体)垂直错流雾化,使得重油的雾化效果好,同时也适用于各种原料油;(4)增加了扩张加长段,充分利用了周围反应环境的高温条件,提高油雾温度,得以蒸发汽化,再次使粒度变细;(5)优化了喷嘴结构,充分利用了蒸汽能量,油雾矩截面可为多种形状,适用于不同反应或燃烧之需要;(6)操作弹性大、结构简单、制造安装方便。Implementing the utility model can realize the following advantages: (1) the amount of atomized steam is less, usually 2-5% of the raw oil; The atomization effect is significantly improved; (3) The use of high-speed steam (gas) vertical cross-flow atomization makes the atomization effect of heavy oil better, and it is also suitable for various raw material oils; The high temperature conditions of the surrounding reaction environment are used to increase the temperature of the oil mist, so that it can be evaporated and vaporized, and the particle size is thinned again; (5) The nozzle structure is optimized, and the steam energy is fully utilized. The oil mist moment cross section can be in various shapes, suitable for Different reactions or combustion needs; (6) Large operating flexibility, simple structure, and convenient manufacturing and installation.
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Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CNU2007203060156U CN201172020Y (en) | 2007-11-23 | 2007-11-23 | Internal mixing pneumatic atomizing nozzle with extended diverging section |
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| CNU2007203060156U CN201172020Y (en) | 2007-11-23 | 2007-11-23 | Internal mixing pneumatic atomizing nozzle with extended diverging section |
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| CN201172020Y true CN201172020Y (en) | 2008-12-31 |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102553748A (en) * | 2012-02-24 | 2012-07-11 | 青岛科技大学 | Ejection type atomization drying device |
| CN103160309A (en) * | 2011-12-16 | 2013-06-19 | 洛阳瑞泽石化工程有限公司 | Feeding nozzle for catalytic cracking test unit |
| CN105921295A (en) * | 2016-06-27 | 2016-09-07 | 石宝珍 | Feed atomization nozzle |
| CN105950208A (en) * | 2016-06-27 | 2016-09-21 | 石宝珍 | Multistage-atomization feed nozzle |
| CN107930883A (en) * | 2018-01-24 | 2018-04-20 | 深圳市山水乐环保科技有限公司 | A liquid micro-nano atomization device and method |
| CN107999297A (en) * | 2018-01-24 | 2018-05-08 | 深圳市山水乐环保科技有限公司 | Plurality of liquid is pre-mixed micro-nano atomising device and method |
| CN108793075A (en) * | 2018-06-15 | 2018-11-13 | 西南科技大学 | A kind of hydroreactive metal fuel eddy flow punching press controllable hydrogen preparation system |
| CN109578806A (en) * | 2018-12-07 | 2019-04-05 | 江苏中圣压力容器装备制造有限公司 | A kind of process unit of LNG flash steam (BOG) pressurization condensing recovery |
| CN114007377A (en) * | 2021-09-29 | 2022-02-01 | 歌尔光学科技有限公司 | VR equipment heat dissipation device, VR equipment and control method |
-
2007
- 2007-11-23 CN CNU2007203060156U patent/CN201172020Y/en not_active Expired - Fee Related
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103160309A (en) * | 2011-12-16 | 2013-06-19 | 洛阳瑞泽石化工程有限公司 | Feeding nozzle for catalytic cracking test unit |
| CN102553748A (en) * | 2012-02-24 | 2012-07-11 | 青岛科技大学 | Ejection type atomization drying device |
| CN102553748B (en) * | 2012-02-24 | 2013-12-11 | 青岛科技大学 | Ejection type atomization drying device |
| CN105921295B (en) * | 2016-06-27 | 2019-03-26 | 石宝珍 | A kind of atomizing feed nozzle |
| CN105950208A (en) * | 2016-06-27 | 2016-09-21 | 石宝珍 | Multistage-atomization feed nozzle |
| CN105950208B (en) * | 2016-06-27 | 2017-11-10 | 石宝珍 | A kind of multistage atomizing feed nozzle |
| CN105921295A (en) * | 2016-06-27 | 2016-09-07 | 石宝珍 | Feed atomization nozzle |
| CN107930883A (en) * | 2018-01-24 | 2018-04-20 | 深圳市山水乐环保科技有限公司 | A liquid micro-nano atomization device and method |
| CN107999297A (en) * | 2018-01-24 | 2018-05-08 | 深圳市山水乐环保科技有限公司 | Plurality of liquid is pre-mixed micro-nano atomising device and method |
| CN108793075A (en) * | 2018-06-15 | 2018-11-13 | 西南科技大学 | A kind of hydroreactive metal fuel eddy flow punching press controllable hydrogen preparation system |
| CN108793075B (en) * | 2018-06-15 | 2021-08-06 | 西南科技大学 | A water-reactive metal fuel swirl stamping controllable hydrogen production system |
| CN109578806A (en) * | 2018-12-07 | 2019-04-05 | 江苏中圣压力容器装备制造有限公司 | A kind of process unit of LNG flash steam (BOG) pressurization condensing recovery |
| CN109578806B (en) * | 2018-12-07 | 2024-01-23 | 江苏中圣压力容器装备制造有限公司 | LNG flash evaporation vapour (BOG) supercharging condensation recovery process device |
| CN114007377A (en) * | 2021-09-29 | 2022-02-01 | 歌尔光学科技有限公司 | VR equipment heat dissipation device, VR equipment and control method |
| CN114007377B (en) * | 2021-09-29 | 2025-02-11 | 歌尔科技有限公司 | VR device heat dissipation device, VR device and control method |
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Granted publication date: 20081231 Termination date: 20111123 |