CN203240927U - Conical heat exchanger - Google Patents

Conical heat exchanger Download PDF

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Publication number
CN203240927U
CN203240927U CN 201320079163 CN201320079163U CN203240927U CN 203240927 U CN203240927 U CN 203240927U CN 201320079163 CN201320079163 CN 201320079163 CN 201320079163 U CN201320079163 U CN 201320079163U CN 203240927 U CN203240927 U CN 203240927U
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CN
China
Prior art keywords
conical
cooling liquid
heat exchanger
pass
tube
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Expired - Lifetime
Application number
CN 201320079163
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Chinese (zh)
Inventor
闫玉兰
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Shanghai Guangjian Transmission Control Equipment Co Ltd
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Shanghai Guangjian Transmission Control Equipment Co Ltd
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Priority to CN 201320079163 priority Critical patent/CN203240927U/en
Application granted granted Critical
Publication of CN203240927U publication Critical patent/CN203240927U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model relates to the technical field of heat exchange equipment, in particular to a conical heat exchanger. The conical heat exchanger comprises a shell pass, a tube pass, a cooling liquid inlet and a cooling liquid outlet. The conical heat exchanger is characterized in that the shell pass is conical or the upper portion of the shell pass is cylindrical, the lower portion of the shell pass is conical, the tube pass is arranged inside the shell pass, the sectional area of the top of the conical part of the shell pass is larger than the sectional area of the bottom part of the conical part of the shell pass, the cooling liquid inlet is formed in the top of the shell pass, the cooling liquid outlet is formed in the bottom of the shell pass, the tube pass is spiral, and the spiral diameter of the top of the tube pass is larger than the spiral diameter of the bottom of the tube pass. According to the conical heat exchanger, the conical big-end-up structures are adopted by both the shell pass and the tube pass, the function of gravity and the function of centrifugal force are used, flowing speed of fluid gradually becomes faster, intensity of pressure is decreased, impurities in the cooling liquid are effectively taken away, the outer wall of the tube pass and the inner wall of the shell pass are washed and brushed to enable the heat exchanger not to be prone to forming scaling to be blocked, heat exchange effect is improved, ordinary sewage or demineralized water is used as the cooling liquid, operating cost is saved to the greatest extent, and the energy-saving and consumption-reducing effect is achieved.

Description

Conical heat exchanger
[technical field]
The utility model relates to the heat-exchange apparatus technical field, specifically a kind of conical heat exchanger.
[background technology]
The cold exchange device of using in the industry technological processes such as the present oil of China, chemical industry is shell-and-tube heat exchanger in a large number, this class has the advantages such as simple in structure, lightweight, that cost is low, be applicable to the stringent process conditions such as various high temperature, high pressure, complex dielectrics, in the numerous kinds heat transmission equipment, occupy an leading position.But existing shell-and-tube tubular heat exchanger, its heat exchanger tube mostly are greatly all smooth common steel tubes of inside and outside surface, easily exist heat exchange efficiency lower, easily the problems such as fouling and obstruction.
The problems referred to above that exist in order to solve the shell-and-tube tubular heat exchanger, consider utilize flow through the time itself deposit tool impulsive force can remove the heat exchanger tube inwall and stop up, therefore the scheme that the heat exchanging tube shape is transformed has appearred, such as the disclosed a kind of cone-shaped telescopic tube for shell-and-tube heat exchanger of domestic patent CN202074869U, its heat exchange principle is to utilize the special construction of this inner-walls of duct, utilize specifically the conical tube of continuous intussusception, the miner diameter end of a upper pitch circle Taper Pipe is plugged in the bigger diameter end of next conical tube, so move in circles, utilize the conical tube bigger diameter end to consist of the crest of this heat exchanger inner tube, miner diameter end consists of the trough of this heat exchanger inner tube.Therefore when flow through the time because the ripple on the inner-walls of duct, thereby form strong turbulent flow and strong disturbance, thus the heat transfer coefficient of raising heat exchanger tube.But the fluctuation of this heat exchanger tube inner wall shape only can change the flow through path of fluid on traffic direction, but can not change in fact the speed of flow warp, therefore still has defective.
[summary of the invention]
The purpose of this utility model is improved at the architecture basics that has heat exchanger shell pass and tube side now, provides a kind of and can prevent effectively that shell wall from blocking, the conical heat exchanger of fouling.
For achieving the above object, design a kind of conical heat exchanger, comprise shell side, tube side, cooling liquid inlet and cooling liquid outlet, it is characterized in that described shell side is conical, be provided with tube side in the shell side, shell side top cross-sectional area is greater than the bottom transverse sectional area, the shell side top is provided with cooling liquid inlet, shell side bottom is provided with cooling liquid outlet, described tube side in the shape of a spiral, described tube side top screw diameter is greater than the bottom screw diameter.
A kind of conical heat exchanger, comprise shell side, tube side, cooling liquid inlet and cooling liquid outlet, it is characterized in that described shell side top is cylindrical, the shell side bottom is conical, is provided with tube side in the shell side, and shell side lower cone shape top cross-sectional area is greater than the conical lower section cross-sectional area, shell side top cylinder-shaped top is provided with cooling liquid inlet, shell side lower cone shape bottom is provided with cooling liquid outlet, described tube side in the shape of a spiral, described tube side top screw diameter is greater than the bottom screw diameter.
Cooling fluid in the above-mentioned heat exchanger is upper entering and lower leaving.
In the heat exchanger of the present utility model, shell side and tube side all adopt tepee structure, up big and down small taper shape specifically, when cooling fluid enters the middle flow process that end opening flows out from suitable for reading, the tube side of the shell side inner conical of need to flowing through, owing to being subject to the effect of gravity and centrifugal force, the flow velocity of coolant fluid can be more and more fast, the liquid outlet flow velocity strengthens, pressure reduces not only can effectively take away in the cooling fluid impurity to reduce sediment, flow velocity strengthens the effect of washing away tube side outer wall and shell side inwall of playing, advantage is that heat exchanger is difficult for forming fouling and is difficult to stop up, and conical top is because heat exchange area increases, and heat transfer effect is improved;
By using this new type heat exchanger, can use general sewage or demineralized water as cooling fluid, and needn't cause that because water quality is not good the fouling of heat exchangers blockage problem removes to be replaced with fresh water (domestic use of water) as cooling fluid or increase the fund input that other improve water treatment schemes (improving quality problem), need not change original state of arts and under the prerequisite that guarantees the equipment operational reliability maximum saving equipment operating cost so that the input-output ratio optimum becomes a reality---namely reach performance and the result of a kind of " saving energy and reduce the cost ".
[description of drawings]
Fig. 1 is the structural representation of the conical heat exchanger of the utility model;
Fig. 2 is another structural representation for the conical heat exchanger of the utility model;
1. cooling liquid inlets, 2. shell sides, 3. tube sides, 4. cooling liquid outlets among the figure.
[specific embodiment]
For making the purpose of this utility model, principle and product configurations more cheer and bright, now be further elaborated in conjunction with the drawings and the specific embodiments, believe for a person skilled in the art and can realize, the realization of technical solutions of the utility model specifies with the following example:
Embodiment one
Conical heat exchanger in the present embodiment as shown in Figure 1, critical piece has: the shell side 2 of the conical one configuration of being made by metal material, shell side 2 top cross-sectional areas are greater than the bottom transverse sectional area, described shell side 2 contains cavity, is used for installing fixedly tube side 3; The tube side 3 of being made by metal pipe material bends to helical form with described tube side 3 and forms the conical structure of hollow out, and described tube side 2 top screw diameters are greater than the bottom screw diameter;
Tube side 3 is being installed in the cavity of shell side 2, be provided with a cooling liquid inlet 1 at shell side 2 tops, be used for injecting cooling fluid or connect the coolant duct outlet, shell side 2 bottoms are provided with a cooling liquid outlet 4, are used for the discharge of cooling fluid or connect coolant duct entering the interruption-forming circular flow.
Above-mentioned heat exchanger in use, the flow direction of cooling fluid is upper entering and lower leaving.
Embodiment two
Conical heat exchanger in the present embodiment as shown in Figure 2, critical piece has: the top of being made by metal material is shell side 2 cylindrical, that the bottom is conical one configuration, shell side 2 lower cone shape top cross-sectional areas are greater than the conical lower section cross-sectional area, described shell side 2 contains cavity, is used for installing fixedly tube side 3; The tube side 3 of being made by metal pipe material bends to helical form with described tube side 3 and forms the conical structure of hollow out, and the tube side 3 top screw diameters in the described shell side 2 lower cone shapes are greater than end screw diameter;
Tube side 3 is installed in the cavity of shell side 2, be provided with a cooling liquid inlet 1 at shell side 2 top cylinder-shaped tops, be used for injecting cooling fluid or connect the coolant duct outlet, shell side 2 lower cone shapes bottom is provided with cooling liquid outlet 4, is used for the discharge of cooling fluid or connects coolant duct entering the interruption-forming circular flow.
Above-mentioned heat exchanger in use, the flow direction of cooling fluid is upper entering and lower leaving.

Claims (3)

1. conical heat exchanger, comprise shell side, tube side, cooling liquid inlet and cooling liquid outlet, it is characterized in that described shell side is conical, be provided with tube side in the shell side, shell side top cross-sectional area is greater than the bottom transverse sectional area, and the shell side top is provided with cooling liquid inlet, and the shell side bottom is provided with cooling liquid outlet, described tube side in the shape of a spiral, described tube side top screw diameter is greater than the bottom screw diameter.
2. conical heat exchanger, comprise shell side, tube side, cooling liquid inlet and cooling liquid outlet, it is characterized in that described shell side top is cylindrical, the shell side bottom is conical, is provided with tube side in the shell side, and shell side lower cone shape top cross-sectional area is greater than the conical lower section cross-sectional area, shell side top cylinder-shaped top is provided with cooling liquid inlet, shell side lower cone shape bottom is provided with cooling liquid outlet, described tube side in the shape of a spiral, tube side top screw diameter is greater than the bottom screw diameter.
3. a kind of conical heat exchanger as claimed in claim 1 or 2 is characterized in that the cooling fluid in the described heat exchanger is upper entering and lower leaving.
CN 201320079163 2013-02-20 2013-02-20 Conical heat exchanger Expired - Lifetime CN203240927U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201320079163 CN203240927U (en) 2013-02-20 2013-02-20 Conical heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201320079163 CN203240927U (en) 2013-02-20 2013-02-20 Conical heat exchanger

Publications (1)

Publication Number Publication Date
CN203240927U true CN203240927U (en) 2013-10-16

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201320079163 Expired - Lifetime CN203240927U (en) 2013-02-20 2013-02-20 Conical heat exchanger

Country Status (1)

Country Link
CN (1) CN203240927U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108262459A (en) * 2018-01-24 2018-07-10 宁波隆源精密机械有限公司 A kind of thermal center Quick cooling structure of die casting
CN110220409A (en) * 2019-06-25 2019-09-10 杭州富尔顿热能设备有限公司 Rotary table needle recuperator

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108262459A (en) * 2018-01-24 2018-07-10 宁波隆源精密机械有限公司 A kind of thermal center Quick cooling structure of die casting
CN110220409A (en) * 2019-06-25 2019-09-10 杭州富尔顿热能设备有限公司 Rotary table needle recuperator

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Granted publication date: 20131016