CN203837525U - Medium pressure and high temperature steam heating heat exchanger - Google Patents

Medium pressure and high temperature steam heating heat exchanger Download PDF

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Publication number
CN203837525U
CN203837525U CN201420178654.9U CN201420178654U CN203837525U CN 203837525 U CN203837525 U CN 203837525U CN 201420178654 U CN201420178654 U CN 201420178654U CN 203837525 U CN203837525 U CN 203837525U
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CN
China
Prior art keywords
heat exchanger
flange
outlet
discharge
high temperature
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201420178654.9U
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Chinese (zh)
Inventor
陆宝夫
陆伟峰
虞卫兴
陶家明
方安兴
高火林
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ZHEJIANG JINGBAO MACHINERY CO Ltd
Original Assignee
ZHEJIANG JINGBAO MACHINERY CO Ltd
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Filing date
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Priority to CN201420178654.9U priority Critical patent/CN203837525U/en
Application granted granted Critical
Publication of CN203837525U publication Critical patent/CN203837525U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The utility model relates to a medium pressure and high temperature steam heating heat exchanger which comprises a plurality of heat conduction pipe connected heat exchange sheets. The heat conduction pipe connected heat exchange sheets are metal seamless heat conduction pipe connected heat exchange sheets and are wrapped with cooling fins. The two ends of each heat conduction pipe connected heat exchange sheet are respectively provided with a heat conduction pipe linkage plate. The outer portions of the heat conduction pipe linkage plate are provided with an end socket. The heat exchanger is further provided with an inlet flange, an outlet flange and a drainage port, wherein the inlet flange, the outlet flange and the drainage port are installed on the end socket. The medium pressure and high temperature steam heating heat exchanger can bear about 30 kilograms, the maximum pressure is 36 kilograms, the highest temperature can reach 320 DEG C, and the requirement that medium pressure and high temperature are needed in industrial production can be met. Steam heating is adopted, steam of industrial waste heat can be adopted as a heat exchange source, the step utilization of waste heat can be achieved, a great contribution is made to utilization of new energy resources, haze in the burning process of a boiler is effectively avoided, a haze source is eliminated, and the medium pressure and high temperature steam heating heat exchanger accords with the theme of environmental protection and is low in price and cost and easy to operate.

Description

A kind of middle super pressure-high temperature Steam Heating heat exchanger
Technical field
The utility model relates to a kind of heat exchanger, specifically relates to a kind of middle super pressure-high temperature Steam Heating heat exchanger, is applied to weaving, printing and dyeing, rubber, process hides, timber processing, oil and foodstuffs processing, the fields such as application baking vanish.
Background technology
Radiator is widely used in industrial every field.As weaving, printing and dyeing, rubber, process hides, timber processing, oil and foodstuffs processing, has been widely applied in the industries such as application baking vanish, all obtains satisfied effect.Heat exchanger in the market mainly be take heating liquid as main, and Some Enterprises adopts flue gas as heat exchange source, but flue gas need to produce by boiler combustion coal, for the source that haze produces, disagrees with the theme of current environment protection.Some Enterprises has proposed take natural gas as raw material, although the temperature that natural gas produces is faster than heating liquid, it is high that efficiency is wanted, and Gas Prices is expensive, and production cost is too expensive, cannot on market, popularize.
Based on this, the utility model is proposed.
Utility model content
For the above-mentioned technical problem of prior art, the purpose of this utility model is to provide a kind of middle super pressure-high temperature Steam Heating heat exchanger, can bear the pressure of 30 kilograms of left and right; heat exchange by steam had both met industrial needs; meet again the requirement of environmental protection, and with low cost, simple to operate.
For achieving the above object, the utility model is achieved through the following technical solutions:
A kind of middle super pressure-high temperature Steam Heating heat exchanger, comprise some heat pipe connection heat exchanger fins, described heat pipe connection heat exchanger fin is metal seamless heat pipe connection heat exchanger fin, the outside of heat pipe connection heat exchanger fin is coated with fin, and the two ends of heat pipe connection heat exchanger fin are all provided with heat pipe gusset piece, described heat pipe gusset piece outside is provided with end socket, and described heat exchanger is also provided with suction flange, outlet(discharge) flange and dewatering outlet, and described suction flange, outlet(discharge) flange and dewatering outlet are installed on end socket.
Described some heat pipe connection heat exchanger fins are that tandem is installed, described suction flange and outlet(discharge) flange are arranged on respectively on two end sockets, described dewatering outlet and outlet(discharge) flange are arranged on same end socket, and dewatering outlet is positioned at outlet(discharge) flange top, and suction flange is relative with dewatering outlet.
Described some heat pipes connection heat exchanger fins are parallel installation, and described suction flange, outlet(discharge) flange and dewatering outlet are arranged on same end socket, and suction flange is positioned at the top of outlet(discharge) flange, and dewatering outlet is arranged on the bottom of end socket.
Described heat exchanger is first horizontal, described some heat pipe connection heat exchanger fins are horizontal and arrange left and right, described suction flange, outlet(discharge) flange and dewatering outlet are arranged on same end socket, and suction flange is positioned at the top of outlet(discharge) flange, and dewatering outlet is arranged on the bottom of end socket.
Described heat exchanger is second horizontal, described some heat pipe connection heat exchanger fins are longitudinal and arrange left and right, described suction flange and outlet(discharge) flange are arranged on same end socket, and described dewatering outlet is arranged on different end sockets from outlet(discharge) flange, and outlet(discharge) flange is relative with dewatering outlet.
Described heat exchanger is vertical, described some heat pipe connection heat exchanger fins are laterally and are arranged above and below, described suction flange and outlet(discharge) flange are arranged on same end socket, suction flange is positioned at outlet(discharge) flange top, described dewatering outlet is arranged on different end sockets from outlet(discharge) flange, and outlet(discharge) flange is relative with dewatering outlet, described heat pipe connection heat exchanger fin outside is provided with support, and described support two ends are all connected with heat pipe gusset piece.
Described fin is circular, square, oval, semicircle or oval nest plate shape.
For increasing radiating effect, as preferably, described fin be ellipse.
The beneficial effects of the utility model are as follows:
1, middle super pressure-high temperature Steam Heating heat exchanger of the present utility model, can bear 30 kilograms of left and right, and maximum pressure is 36 kilograms, and temperature can reach 320 ℃, can meet the needs of the middle super pressure-high temperature of needs in industrial production.
2, the utility model adopts Steam Heating; can adopt industrial exhaust heat steam as heat exchange source; realize step UTILIZATION OF VESIDUAL HEAT IN; not only for very large contribution is made in the utilization of new forms of energy, and effectively avoid the haze in boiler combustion, eliminated the source of haze; consistent with the theme of environmental protection; and low price, cost is low, simple to operate.
3, in the utility model, heat pipe joins the fin that heat exchanger fin outside is coated with circle, square, oval, semicircle or oval nest plate shape, and radiating effect is very good.
4, the utility model can become tandem, parallel, first horizontal, second horizontal or vertical according to the different Demand Design of commercial Application, meets the arrangement of different industrial production systems.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation of the utility model embodiment 1;
Fig. 3 is the structural representation of the utility model embodiment 2;
Fig. 4 is the structural representation of the utility model embodiment 3;
Fig. 5 is the structural representation of the utility model embodiment 4;
Fig. 6 is the structural representation of the utility model embodiment 5;
Fig. 7-11 are the shape schematic diagram of fin in the utility model;
Wherein, 1 is that heat pipe joins heat exchanger fin, and 2 is that heat pipe gusset piece, 3 is that end socket, 4 is that suction flange, 5 is that outlet(discharge) flange, 6 is that dewatering outlet, 7 is that support, 8 is fin.
The specific embodiment
Below in conjunction with specific embodiment, the utility model is further described, but protection domain of the present utility model is not limited to this.
As shown in Fig. 7-11, the fin 8 in the utility model can be circular, square, oval, semicircle or oval nest plate shape.When fin 8 is circular, inside and outside being with fin 8, heat pipe connection heat exchanger fin 1 is round shape; When fin 8 is square, heat pipe connection heat exchanger fin 1 and fin 8 are the shape of inner circle foreign side; When fin 8 is oval, heat pipe connection heat exchanger fin 1 is inside and outside equal oval shape with fin 8; When fin 8 is semicircle, heat pipe connection heat exchanger fin 1 and fin 8 are the shape of the outer semicircle of inner circle; When fin 8 is oval nest plate shape, heat pipe connection heat exchanger fin 1 and fin 8 are the shape of interior a plurality of oval foreign sides.
When wherein fin 8 is oval, radiating effect is best.With regard to other structure of super pressure-high temperature Steam Heating heat exchanger in the utility model, do concrete introduction below, in all the utility model, there is no the structure of appearance and the known property general knowledge that connected mode is this area.
embodiment 1
As illustrated in fig. 1 and 2, middle super pressure-high temperature Steam Heating heat exchanger of the present utility model, comprise some heat pipe connection heat exchanger fins 1, heat pipe connection heat exchanger fin 1 is metal seamless heat pipe connection heat exchanger fin, can bear 30 kilograms of even larger pressure, also can bear high temperature, the outside of heat pipe connection heat exchanger fin 1 is coated with fin 8, and the two ends of heat pipe connection heat exchanger fin 1 are all provided with heat pipe gusset piece 2, heat pipe gusset piece 2 outsides are provided with end socket 3, heat exchanger of the present utility model is also provided with suction flange 4, outlet(discharge) flange 5 and dewatering outlet 6, suction flange 4, outlet(discharge) flange 5 and dewatering outlet 6 are installed on end socket 3.
In the present embodiment 1, heat pipe connection heat exchanger fin 1 is tandem installation, suction flange 4 and outlet(discharge) flange 5 are arranged on respectively on two end sockets 3, dewatering outlet 6 is arranged on same end socket 3 with outlet(discharge) flange 5, and dewatering outlet 6 is positioned at outlet(discharge) flange 5 tops, and suction flange 4 is relative with dewatering outlet 6.
embodiment 2
As shown in Figure 3, in the present embodiment 2, some heat pipes connection heat exchanger fins 1 are parallel installation, and suction flange 4, outlet(discharge) flange 5 and dewatering outlet 6 are arranged on same end socket 3, and suction flange 4 is positioned at the top of outlet(discharge) flange 5, and dewatering outlet 6 is arranged on the bottom of end socket 3.
Other structure and the connected mode of the present embodiment 2 are identical with embodiment 1, do not repeat herein.
embodiment 3
As shown in Figure 4, heat exchanger in the present embodiment 3 is first horizontal, some heat pipe connection heat exchanger fins 1 are horizontal and arrange left and right, suction flange 4, outlet(discharge) flange 5 and dewatering outlet 6 are arranged on same end socket 3, and suction flange 4 is positioned at the top of outlet(discharge) flange 5, dewatering outlet 6 is arranged on the bottom of end socket 3.
Other structure and the connected mode of the present embodiment 3 are identical with embodiment 1, do not repeat herein.
embodiment 4
As shown in Figure 5, heat exchanger in the present embodiment 4 is second horizontal, some heat pipe connection heat exchanger fins 1 are longitudinal and arrange left and right, suction flange 4 is arranged on same end socket 3 with outlet(discharge) flange 5, dewatering outlet 6 is arranged on different end socket 3 from outlet(discharge) flange 5, and outlet(discharge) flange 5 is relative with dewatering outlet 6.
Other structure and the connected mode of the present embodiment 4 are identical with embodiment 1, do not repeat herein.
embodiment 5
As shown in Figure 6, heat exchanger in the present embodiment 5 is vertical, some heat pipe connection heat exchanger fins 1 are laterally and are arranged above and below, suction flange 4 is arranged on same end socket 3 with outlet(discharge) flange 5, suction flange 4 is positioned at outlet(discharge) flange 5 tops, and dewatering outlet 6 is arranged on different end socket 3 from outlet(discharge) flange 5, and outlet(discharge) flange 5 is relative with dewatering outlet 6, heat pipe connection heat exchanger fin 1 outside is provided with support 7, and support 7 two ends are all connected with heat pipe gusset piece 2.
Other structure and the connected mode of the present embodiment 5 are identical with embodiment 1, do not repeat herein.
Middle super pressure-high temperature Steam Heating heat exchanger of the present utility model, can bear 30 kilograms of left and right, and maximum pressure is 36 kilograms, and temperature can reach 320 ℃, can meet the needs of the middle super pressure-high temperature of needs in industrial production.Adopt Steam Heating; can adopt industrial exhaust heat steam as heat exchange source; realize step UTILIZATION OF VESIDUAL HEAT IN; not only for very large contribution is made in the utilization of new forms of energy, and effectively avoid the haze in boiler combustion, eliminated the source of haze; consistent with the theme of environmental protection; and low price, cost is low, simple to operate.Heat pipe connection heat exchanger fin 1 outside is coated with the fin 8 of circle, square, oval, semicircle or oval nest plate shape, and radiating effect is very good, and wherein oval-shaped fin 8 radiating effects are best.The utility model can become tandem, parallel, first horizontal, second horizontal or vertical according to the different Demand Design of commercial Application, meets the arrangement of different industrial production systems.
Above-described embodiment is only for the inventive concept of the present utility model of explaining; but not restriction to the utility model rights protection; as allly in change of suction flange 4, outlet(discharge) flange 5 and dewatering outlet 6 installation site in end socket 3 etc. utilize this design to carry out the change of unsubstantiality to the utility model, all should fall into protection domain of the present utility model.

Claims (8)

1. super pressure-high temperature Steam Heating heat exchanger in a kind, it is characterized in that: comprise some heat pipe connection heat exchanger fins, described heat pipe connection heat exchanger fin is metal seamless heat pipe connection heat exchanger fin, the outside of heat pipe connection heat exchanger fin is coated with fin, and the two ends of heat pipe connection heat exchanger fin are all provided with heat pipe gusset piece, described heat pipe gusset piece outside is provided with end socket, described heat exchanger is also provided with suction flange, outlet(discharge) flange and dewatering outlet, and described suction flange, outlet(discharge) flange and dewatering outlet are installed on end socket.
2. middle super pressure-high temperature Steam Heating heat exchanger as claimed in claim 1, it is characterized in that: described some heat pipe connection heat exchanger fins are that tandem is installed, described suction flange and outlet(discharge) flange are arranged on respectively on two end sockets, described dewatering outlet and outlet(discharge) flange are arranged on same end socket, and dewatering outlet is positioned at outlet(discharge) flange top, and suction flange is relative with dewatering outlet.
3. middle super pressure-high temperature Steam Heating heat exchanger as claimed in claim 1, it is characterized in that: described some heat pipe connection heat exchanger fins are parallel installation, described suction flange, outlet(discharge) flange and dewatering outlet are arranged on same end socket, and suction flange is positioned at the top of outlet(discharge) flange, dewatering outlet is arranged on the bottom of end socket.
4. middle super pressure-high temperature Steam Heating heat exchanger as claimed in claim 1, it is characterized in that: described heat exchanger is first horizontal, described some heat pipe connection heat exchanger fins are horizontal and arrange left and right, described suction flange, outlet(discharge) flange and dewatering outlet are arranged on same end socket, and suction flange is positioned at the top of outlet(discharge) flange, dewatering outlet is arranged on the bottom of end socket.
5. middle super pressure-high temperature Steam Heating heat exchanger as claimed in claim 1, it is characterized in that: described heat exchanger is second horizontal, described some heat pipe connection heat exchanger fins are longitudinal and arrange left and right, described suction flange and outlet(discharge) flange are arranged on same end socket, described dewatering outlet is arranged on different end sockets from outlet(discharge) flange, and outlet(discharge) flange is relative with dewatering outlet.
6. middle super pressure-high temperature Steam Heating heat exchanger as claimed in claim 1, it is characterized in that: described heat exchanger is vertical, described some heat pipe connection heat exchanger fins are laterally and are arranged above and below, described suction flange and outlet(discharge) flange are arranged on same end socket, suction flange is positioned at outlet(discharge) flange top, described dewatering outlet is arranged on different end sockets from outlet(discharge) flange, and outlet(discharge) flange is relative with dewatering outlet, described heat pipe connection heat exchanger fin outside is provided with support, and described support two ends are all connected with heat pipe gusset piece.
7. the middle super pressure-high temperature Steam Heating heat exchanger as described in claim as arbitrary in claim 1-6, is characterized in that: described fin is circular, square, oval, semicircle or oval nest plate shape.
8. middle super pressure-high temperature Steam Heating heat exchanger as claimed in claim 7, is characterized in that: described fin is for oval.
CN201420178654.9U 2014-04-14 2014-04-14 Medium pressure and high temperature steam heating heat exchanger Expired - Fee Related CN203837525U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420178654.9U CN203837525U (en) 2014-04-14 2014-04-14 Medium pressure and high temperature steam heating heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420178654.9U CN203837525U (en) 2014-04-14 2014-04-14 Medium pressure and high temperature steam heating heat exchanger

Publications (1)

Publication Number Publication Date
CN203837525U true CN203837525U (en) 2014-09-17

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ID=51515351

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420178654.9U Expired - Fee Related CN203837525U (en) 2014-04-14 2014-04-14 Medium pressure and high temperature steam heating heat exchanger

Country Status (1)

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CN (1) CN203837525U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103954148A (en) * 2014-04-14 2014-07-30 浙江精宝机械有限公司 Medium-pressure high-temperature steam heating heat exchanger
CN105332973A (en) * 2015-10-16 2016-02-17 北京精密机电控制设备研究所 Embedded cooler for electro-hydraulic servo mechanism and cooling method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103954148A (en) * 2014-04-14 2014-07-30 浙江精宝机械有限公司 Medium-pressure high-temperature steam heating heat exchanger
CN103954148B (en) * 2014-04-14 2015-04-29 浙江精宝机械有限公司 Medium-pressure high-temperature steam heating heat exchanger
CN105332973A (en) * 2015-10-16 2016-02-17 北京精密机电控制设备研究所 Embedded cooler for electro-hydraulic servo mechanism and cooling method

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20140917

Termination date: 20190414

CF01 Termination of patent right due to non-payment of annual fee