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CN201138106Y - A liquid nitrogen heat exchange device for liquid nitrogen-assisted freeze-drying equipment - Google Patents

A liquid nitrogen heat exchange device for liquid nitrogen-assisted freeze-drying equipment Download PDF

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CN201138106Y
CN201138106Y CNU2007200770632U CN200720077063U CN201138106Y CN 201138106 Y CN201138106 Y CN 201138106Y CN U2007200770632 U CNU2007200770632 U CN U2007200770632U CN 200720077063 U CN200720077063 U CN 200720077063U CN 201138106 Y CN201138106 Y CN 201138106Y
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liquid nitrogen
nitrogen
outlet
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heat conduction
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郑效东
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Praxair China Investment Co Ltd
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Shanghai Tofflon Science and Technology Co Ltd
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Abstract

本实用新型涉及一种液氮辅助制冷冻干设备的液氮换热装置,其特征在于,由液氮气化管、导热循环油管、折流板和筒体组成,在筒体内壁设有一圈液氮气化管,液氮气化管下端与筒体中部的液氮进口和氮气出口连接,在液氮气化管中间设有至少两根U形导热循环油管,U形导热循环油管顶端穿过筒体盖一端与导热循环油进口连接,另一端与导热循环油出口连接,液氮气化管和导热循环油管中间通过折流板固定,导热油温度探头分别设于导热循环油进口和导热循环油出口上,氮气温度探头及上液位接口设于筒体上端一侧,在液氮进口和液氮出口的上端设有安全阀及下液位接口,在筒体底部分别设有氮气出口和氮气出口温度探头。本实用新型的优点是能实现液氮能安全的与循环导热油进行热交换。

Figure 200720077063

The utility model relates to a liquid nitrogen heat exchange device for liquid nitrogen auxiliary freeze-drying equipment. Nitrogen gasification tube, the lower end of the liquid nitrogen gasification tube is connected to the liquid nitrogen inlet and nitrogen outlet in the middle of the cylinder, at least two U-shaped heat conduction circulation oil pipes are arranged in the middle of the liquid nitrogen vaporization pipe, and the top of the U-shaped heat conduction circulation oil pipe passes through the cylinder cover One end is connected to the heat transfer circulating oil inlet, and the other end is connected to the heat transfer circulating oil outlet. The middle of the liquid nitrogen gasification pipe and the heat transfer circulating oil pipe is fixed by a baffle plate. The heat transfer oil temperature probes are respectively installed on the heat transfer circulating oil inlet and the heat transfer circulating oil outlet. The nitrogen temperature probe and the upper liquid level interface are set on the upper side of the cylinder, and the safety valve and the lower liquid level interface are installed at the upper end of the liquid nitrogen inlet and liquid nitrogen outlet, and the nitrogen outlet and nitrogen outlet temperature probes are respectively installed at the bottom of the cylinder . The utility model has the advantage that the liquid nitrogen can safely exchange heat with the circulating heat-conducting oil.

Figure 200720077063

Description

一种液氮辅助制冷冻干设备的液氮换热装置 A liquid nitrogen heat exchange device for liquid nitrogen-assisted freeze-drying equipment

技术领域technical field

本实用新型涉及一种液氮辅助制冷冻干设备的液氮换热装置,尤其涉及一种把来自于储罐的液氮通过此换热装置进行气化并且与液氮真空冷冻干燥机的循环导热油进行热交换的一种换热器,属于换热器技术领域。The utility model relates to a liquid nitrogen heat exchange device for liquid nitrogen auxiliary freeze-drying equipment, in particular to a liquid nitrogen from a storage tank that is vaporized through the heat exchange device and circulated with a liquid nitrogen vacuum freeze dryer. The invention relates to a heat exchanger for conducting heat exchange with heat transfer oil, which belongs to the technical field of heat exchangers.

背景技术Background technique

真空冷冻干燥机就是利用冷冻干燥原理将含水物质进行降温冻结成固态,然后在真空的条件下使水蒸汽直接从固态中升华出来的用于冻干含水物质的机器。Vacuum freeze dryer is a machine for freeze-drying water-containing substances by using the principle of freeze-drying to cool and freeze water-containing substances into a solid state, and then sublimate water vapor directly from the solid state under vacuum conditions.

目前真空冷冻干燥机从制冷方式来分主要分为二大类:1、利用制冷剂氟利昂的压缩机来制冷;2、利用液氮来制冷。At present, vacuum freeze dryers are mainly divided into two categories in terms of refrigeration methods: 1. Refrigeration using refrigerant Freon compressors; 2. Refrigeration using liquid nitrogen.

而目前利用液氮制冷存在着以下缺点:At present, the use of liquid nitrogen refrigeration has the following disadvantages:

1、液氮的温度极低,在一定的压力下液氮的温度在-196℃,这么低的温度与真空冷冻干燥机的循环导热油不能直接进行热交换,否则就会发生循环导热油冻结现象;1. The temperature of liquid nitrogen is extremely low. Under a certain pressure, the temperature of liquid nitrogen is -196°C. Such a low temperature cannot directly exchange heat with the circulating heat transfer oil of the vacuum freeze dryer, otherwise the circulating heat transfer oil will freeze Phenomenon;

2、液氮在其它领域的应用已经很广泛了,但用在液氮真空冷冻干燥机这种制药机械领域应用才刚起步,目前还没有一种成熟的高效的液氮换热装置。2. Liquid nitrogen has been widely used in other fields, but it has just started to be used in the field of pharmaceutical machinery such as liquid nitrogen vacuum freeze dryer. At present, there is no mature and efficient liquid nitrogen heat exchange device.

发明内容Contents of the invention

本实用新型的目的是提供一种实现液氮能安全的与循环导热油进行热交换的液氮辅助制冷冻干设备的液氮换热装置。The purpose of the utility model is to provide a liquid nitrogen heat exchange device for liquid nitrogen assisted freeze-drying equipment that can safely exchange heat with circulating heat transfer oil.

为实现以上目的,本实用新型的技术方案是提供一种液氮辅助制冷冻干设备的液氮换热装置,其特征在于,由液氮气化管、导热循环油管、折流板和筒体组成,在筒体内壁设有一圈液氮气化管,液氮气化管下端与筒体中部的液氮进口和氮气出口连接,在液氮气化管中间设有至少两根U形导热循环油管,U形导热循环油管顶端穿过筒体盖一端与导热循环油进口连接,另一端与导热循环油出口连接,液氮气化管和导热循环油管中间通过折流板固定,导热油温度探头分别设于导热循环油进口和导热循环油出口上,氮气温度探头及上液位接口设于筒体上端一侧,在液氮进口和液氮出口的上端设有安全阀及下液位接口,在筒体底部分别设有氮气出口和氮气出口温度探头。In order to achieve the above objectives, the technical solution of this utility model is to provide a liquid nitrogen heat exchange device for liquid nitrogen assisted freeze-drying equipment, which is characterized in that it consists of a liquid nitrogen gasification tube, a heat conduction circulation oil tube, a baffle plate and a cylinder , there is a ring of liquid nitrogen gasification tubes on the inner wall of the cylinder, the lower end of the liquid nitrogen gasification tubes is connected with the liquid nitrogen inlet and nitrogen outlet in the middle of the cylinder body, and at least two U-shaped heat conduction circulation oil pipes are arranged in the middle of the liquid nitrogen gasification tubes, U-shaped The top end of the heat conduction circulation oil pipe passes through the cylinder cover, and one end is connected to the heat conduction circulation oil inlet, and the other end is connected to the heat conduction circulation oil outlet. On the oil inlet and the heat conduction circulating oil outlet, the nitrogen temperature probe and the upper liquid level interface are set on the upper side of the cylinder, and the safety valve and the lower liquid level interface are installed on the upper end of the liquid nitrogen inlet and liquid nitrogen outlet, respectively. Equipped with nitrogen outlet and nitrogen outlet temperature probe.

本实用新型把来自于储罐的液氮气化并与导热循环油进行热交换,把液氮气化成低温氮气,低温氮气与导热循环油进行热交换,避免液氮冻结循环导热油的现象,而且充分利用了液氮潜热和显热,高效率、安全地与循环导热油进行热交换。The utility model gasifies the liquid nitrogen from the storage tank and conducts heat exchange with the heat-conducting circulating oil, turns the liquid nitrogen into low-temperature nitrogen, and performs heat exchange between the low-temperature nitrogen and the heat-conducting circulating oil, avoids the phenomenon that the liquid nitrogen freezes the circulating heat-conducting oil, and fully The latent and sensible heat of liquid nitrogen is used to exchange heat with circulating heat transfer oil efficiently and safely.

本实用新型的优点是能实现液氮能安全地与循环导热油进行热交换。The utility model has the advantage that the liquid nitrogen can safely exchange heat with the circulating heat-conducting oil.

附图说明Description of drawings

图1为一种液氮辅助制冷冻干设备的液氮换热装置结构示意图;Fig. 1 is a schematic structural diagram of a liquid nitrogen heat exchange device of a liquid nitrogen-assisted freeze-drying equipment;

图2为一种液氮辅助制冷冻干设备的液氮换热装置A-A剖视图。Fig. 2 is a sectional view of a liquid nitrogen heat exchange device A-A of a liquid nitrogen assisted freeze-drying equipment.

具体实施方式Detailed ways

以下结合附图和实施例对本实用新型作进一步说明。Below in conjunction with accompanying drawing and embodiment the utility model is described further.

实施例Example

如图1、2所示,为一种液氮辅助制冷冻干设备的液氮换热装置结构示意图,所述的一种液氮辅助制冷冻干设备的液氮换热装置由液氮气化管1、导热循环油管2、折流板3和筒体4组成,在筒体4内壁安装一圈12根液氮气化管1,液氮气化管1下端与筒体4中部的液氮进口10和氮气出口11连接,在液氮气化管1间安装10根U形导热循环油管2,U形导热循环油管2顶端穿过筒体4盖一端与导热循环油进口5连接,另一端与导热循环油出口6连接,液氮气化管1和导热循环油管2中间通过折流板3固定,导热油温度探头7分别安装在导热循环油进口5和导热循环油出口6上,氮气温度探头及上液位接口8安装在筒体4上端一侧,在液氮进口10和液氮出口11的上端安装安全阀及下液位接口9,在筒体4底部分别设有氮气出口12和氮气出口温度探头13。As shown in Figures 1 and 2, it is a schematic structural diagram of a liquid nitrogen heat exchange device for a liquid nitrogen-assisted freeze-drying equipment. The liquid nitrogen heat exchange device for a liquid nitrogen-assisted freeze-drying equipment consists of a liquid nitrogen gasification tube 1. The heat conduction circulation oil pipe 2, the baffle plate 3 and the cylinder body 4 are composed of 12 liquid nitrogen gasification tubes 1 in a circle on the inner wall of the cylinder body 4, the lower end of the liquid nitrogen gasification tube 1 and the liquid nitrogen inlet 10 in the middle of the cylinder body 4 and The nitrogen outlet 11 is connected, and 10 U-shaped heat-conducting circulating oil pipes 2 are installed between the liquid nitrogen gasification pipes 1. The top of the U-shaped heat-conducting circulating oil pipe 2 passes through the cylinder body 4. One end of the cover is connected to the heat-conducting circulating oil inlet 5, and the other end is connected to the heat-conducting circulating oil. The outlet 6 is connected, the middle of the liquid nitrogen gasification pipe 1 and the heat conduction circulation oil pipe 2 is fixed by the baffle plate 3, the heat conduction oil temperature probe 7 is respectively installed on the heat conduction circulation oil inlet 5 and the heat conduction circulation oil outlet 6, the nitrogen temperature probe and the upper liquid level The interface 8 is installed on one side of the upper end of the cylinder 4, a safety valve and a lower liquid level interface 9 are installed on the upper end of the liquid nitrogen inlet 10 and the liquid nitrogen outlet 11, and a nitrogen outlet 12 and a nitrogen outlet temperature probe 13 are respectively provided at the bottom of the cylinder 4 .

工作时,液氮从贮罐过来进入液氮进口10,进入到换热器内的液氮气化管1内,液氮在液氮气化管1内上升的过程中由于压力降低而发生气化,从液态变成气态,因为氮气气液二相的体积比是800∶1,所以这个过程要吸收大量的热,这个热量由循环导热油来提供,当循环导热油从导热循环油进口5进入到换热器内,沿着导热循环油管2一端向下流动,到达底部时折弯180°再向上流动,从导热循环油出口6流出,在这一个过程中,气化成的氮气到达顶部后再向下流动,在下行流动的过程中经过很多的折流板3,以增加氮气的流通路径,这样更加高效地进行热交换,导热循环油在流动的过程中热量被液氮气化成的氮气吸收,温度降低,而氮气最后从氮气出口12排出,完成这一热交换过程。During operation, liquid nitrogen enters the liquid nitrogen inlet 10 from the storage tank and enters the liquid nitrogen gasification tube 1 in the heat exchanger. The liquid nitrogen gasifies due to pressure drop during the process of rising in the liquid nitrogen gasification tube 1. From liquid state to gaseous state, because the volume ratio of nitrogen gas-liquid two-phase is 800:1, so this process will absorb a lot of heat, this heat is provided by circulating heat transfer oil, when the circulating heat transfer oil enters from the heat transfer circulating oil inlet 5 to In the heat exchanger, it flows down along one end of the heat conduction circulation oil pipe 2, bends 180° when it reaches the bottom, then flows upward, and flows out from the heat conduction circulation oil outlet 6. During this process, the gasified nitrogen reaches the top and then flows Downward flow, through a lot of baffles 3 in the process of downward flow, to increase the flow path of nitrogen gas, so as to perform heat exchange more efficiently, and the heat of the heat conduction circulating oil is absorbed by the nitrogen gas formed by liquid nitrogen gas during the flow process, and the temperature Reduce, and nitrogen is discharged from nitrogen outlet 12 at last, completes this heat exchange process.

从上面的工作原理上来看,液氮并不与导热循环油直接接触,而是液氮气化后的氮气与导热循环油管接触,避免了发生导热循环油冻结现象,另外利用液氮气化这一物理现象来制冷,利用了体积膨胀要吸收大量的热,同时利用各处温度探头采集温度信号,以及通过上下液位差输出信号以便于合理地控制液氮的进入量,充分高效地利用了液氮。From the above working principle, liquid nitrogen is not in direct contact with the heat transfer circulating oil, but the nitrogen gas after liquid nitrogen vaporization is in contact with the heat transfer circulating oil tube, which avoids the freezing of the heat transfer circulating oil. Phenomena to refrigerate, using volume expansion to absorb a large amount of heat, and using temperature probes everywhere to collect temperature signals, and output signals through the upper and lower liquid level differences to reasonably control the amount of liquid nitrogen entering, making full and efficient use of liquid nitrogen .

Claims (1)

1. the liquid nitrogen heat-exchanger rig of a liquid nitrogen auxiliary cooling freeze-drier, it is characterized in that, by liquid nitrogen gasification pipe (1), heat conduction circulating pipe (2), deflection plate (3) and cylindrical shell (4) are formed, be provided with a circle liquid nitrogen gasification pipe (1) at cylindrical shell (4) inwall, liquid nitrogen gasification pipe (1) lower end is connected with nitrogen outlet (11) with the liquid nitrogen import (10) at cylindrical shell (4) middle part, in the middle of liquid nitrogen gasification pipe (1), be provided with at least two U-shaped heat conduction circulating pipes (2), U-shaped heat conduction circulating pipe (2) top is passed cylindrical shell (4) Gai Yiduan and is connected with heat conduction recycle oil import (5), the other end is connected with heat conduction recycle oil outlet (6), fixing in the middle of liquid nitrogen gasification pipe (1) and the heat conduction circulating pipe (2) by deflection plate (3), conduction oil temp probe (7) is located at respectively in heat conduction recycle oil import (5) and the heat conduction recycle oil outlet (6), nitrogen temperature is popped one's head in and is gone up liquid level interface (8) and be located at cylindrical shell (4) upper end one side, be provided with safety valve in the upper end of liquid nitrogen import (10) and liquid nitrogen outlet (11) and reach liquid level interface (9) down, be respectively equipped with nitrogen outlet (12) and nitrogen outlet temp probe (13) in cylindrical shell (4) bottom.
CNU2007200770632U 2007-12-24 2007-12-24 A liquid nitrogen heat exchange device for liquid nitrogen-assisted freeze-drying equipment Expired - Fee Related CN201138106Y (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101871720A (en) * 2010-06-11 2010-10-27 上海东富龙科技股份有限公司 Liquid nitrogen freeze dryer direct-expansion cold trap
CN102012141A (en) * 2010-11-01 2011-04-13 江苏永能光伏科技有限公司 Liquid nitrogen vaporization cold recycling device
CN102472590A (en) * 2009-08-04 2012-05-23 大阳日酸株式会社 Reaction device
CN109373783A (en) * 2018-12-16 2019-02-22 江苏世林博尔制冷设备有限公司 One kind is convenient for automatic adjustment oil cooler
CN109959196A (en) * 2019-03-07 2019-07-02 西安航天动力研究所 A wide-range temperature regulation heat exchange device for methane cryogenic treatment

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102472590A (en) * 2009-08-04 2012-05-23 大阳日酸株式会社 Reaction device
US8721982B2 (en) 2009-08-04 2014-05-13 Taiyo Nippon Sanso Corporation Reaction device
CN102472590B (en) * 2009-08-04 2014-07-30 大阳日酸株式会社 Reaction device
CN101871720A (en) * 2010-06-11 2010-10-27 上海东富龙科技股份有限公司 Liquid nitrogen freeze dryer direct-expansion cold trap
CN101871720B (en) * 2010-06-11 2011-11-30 上海东富龙科技股份有限公司 Liquid nitrogen freeze dryer direct-expansion cold trap
CN102012141A (en) * 2010-11-01 2011-04-13 江苏永能光伏科技有限公司 Liquid nitrogen vaporization cold recycling device
CN102012141B (en) * 2010-11-01 2012-05-02 江苏永能光伏科技有限公司 Liquid nitrogen vaporization cold recycling device
CN109373783A (en) * 2018-12-16 2019-02-22 江苏世林博尔制冷设备有限公司 One kind is convenient for automatic adjustment oil cooler
CN109959196A (en) * 2019-03-07 2019-07-02 西安航天动力研究所 A wide-range temperature regulation heat exchange device for methane cryogenic treatment

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