CN202869332U - Heat pipe type material condenser device - Google Patents

Heat pipe type material condenser device Download PDF

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Publication number
CN202869332U
CN202869332U CN 201220398639 CN201220398639U CN202869332U CN 202869332 U CN202869332 U CN 202869332U CN 201220398639 CN201220398639 CN 201220398639 CN 201220398639 U CN201220398639 U CN 201220398639U CN 202869332 U CN202869332 U CN 202869332U
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CN
China
Prior art keywords
heat
heat pipe
tube
condenser body
type material
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
CN 201220398639
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Chinese (zh)
Inventor
蔡国海
管欣
沙仙众
张彤
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.)
Jurong Hualian Special Equipment Manufacture Co Ltd
Original Assignee
Jurong Hualian Special Equipment Manufacture Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Jurong Hualian Special Equipment Manufacture Co Ltd filed Critical Jurong Hualian Special Equipment Manufacture Co Ltd
Priority to CN 201220398639 priority Critical patent/CN202869332U/en
Application granted granted Critical
Publication of CN202869332U publication Critical patent/CN202869332U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses a heat pipe type material condenser device which comprises a condenser body, a hot water tank and a pressurization feed pump, wherein a material inlet is arranged at the bottom of the condenser body, a hot water or low-pressure steam outlet is arranged on the top of the condenser body, a material air lack outlet, a water inlet and a water outlet are arranged in the middle of the condenser body, the material inlet is connected with a material outlet of a material reactor, the hot water or low-pressure steam outlet is connected with a factory pipe network through a first pipeline, the material air lack outlet is connected with a follow-up material pipe network through a second pipeline, the water inlet is connected with the pressurization feed pump through a connecting pipe, the pressurization feed pump is connected with the hot water tank, and besides, the interior of the heat pipe type condenser body is further provided with a heat transfer element and a middle pipe plate transversely arranged in the middle of the heat pipe type condenser body. The heat pipe type material condenser device not only enables reaction process gas and material waste heat to be recycled and reduces operating cost, but also brings convenience to comprehensive utilization of heat energy, meets requirement for energy saving and emission reduction, and has certain economic benefit and social benefit.

Description

Heat pipe-type material condenser device
Technical field
The utility model relates to a kind of heat pipe-type material condenser device, relates in particular to a kind of heat pipe-type material condenser device that designs for the residual neat recovering system such as process gas or reaction mass in chemical industry, petrochemical industry and the pharmaceuticals industry specially.
Background technology
Reactor, destilling tower etc. are a kind of very important technological equipments in present chemical industry, petrochemical industry and the pharmaceuticals industry.The process gas that produces in the reaction tower and material produce physical and chemical reaction heat in course of reaction, the reaction mass temperature reaches 150 ~ 350 ℃, the general conduction oil that adopts cools off reaction mass at present, and the conduction oil after the heat absorption cools off by heat exchanger access recirculated cooling water again.
But the technical scheme that adopts conduction oil+recirculated cooling water has only played the effect to process gas and reaction mass cooling, but can not fully effectively reclaim process gas and material waste heat, and can be because of guaranteeing the normal operation of conduction oil and recirculating cooling water system and consume a large amount of electric energy that the operation of whole device is very uneconomical.A large amount of process gas and material waste heats can not access fully, effectively recycles simultaneously, caused the waste of residual heat resources yet.
And in present stage, also need hot water or low-pressure steam in the explained hereafter, take at present to obtain with the mode of steam heating water the hot water of required uniform temperature, flow, be about to steam and the direct or indirect heat exchange of water, the hot water of technological requirement is satisfied in generation, guarantees the normal operation of production system, needs by external steam heating water but do like this, both waste the device by utilizing waste heat resource, also increased simultaneously the operating cost of device because buying steam.
The utility model content
Be the solution the deficiencies in the prior art, but the purpose of this utility model is to provide a kind of heat pipe-type material condenser device of energy-conserving and environment-protective effective recycling residual heat resources.
The technical scheme that the utility model adopts is:
A kind of heat pipe-type material condenser device, it is characterized in that, comprise heat pipe-type material condenser body, boiler and pressurizing feedwater pump, the bottom of described heat tube type cold condenser body is provided with material inlet, the top is provided with hot water or low-pressure steam outlet, the middle part then is provided with the weary gas outlet of material, water inlet and sewage draining exit, described material inlet is connected with the material outlet of the material reaction device that is arranged on heat tube type cold condenser body bottom, the outlet of hot water or low-pressure steam is connected with the plant area pipe network by the first pipeline, the weary gas outlet of material is connected with follow-up material pipe network by second pipe, water inlet is connected with the pressurizing feedwater pump by tube connector, and described pressurizing feedwater pump is connected with boiler, in addition, the inside of described heat tube type cold condenser body also is provided with heat transfer element and is used for separating the tube sheet of material and cooling water, and described middle tube sheet is horizontally installed on the middle part of heat tube type cold condenser body.
Further, described heat transfer element is heat exchanger tube or finned tube.And work as, when described heat transfer element was heat exchanger tube, described heat exchanger tube is vertical vertical setting or horizontal type level setting in heat tube type cold condenser body.
And when described heat transfer element was heat exchanger tube, the bottom of described heat exchanger tube also was provided with for the fixing lower perforated plate of heat exchanger tube, and described lower perforated plate is fixedly connected with heat tube type cold condenser body.
Further, satisfy the subsequent technique requirement in order to ensure the material outlet temperature of heat pipe-type material condenser body, be provided with the first control valve that enters the intrinsic cold fluid flow of heat tube type cold condenser for control on the described tube connector.And also being provided with the first by-passing valve on the described tube connector, described the first by-passing valve and the first control valve are set up in parallel.
Further, in order to realize the hot water temperature that is sent to plant area's pipe network or the adjusting of low-pressure steam pressure are provided with the second control valve that enters the cold fluid pressure in plant area's pipe network for control on described the first pipeline.And also being provided with the second by-passing valve on described the first pipeline, described the second by-passing valve and the second control valve are set up in parallel.
In addition, the bottom of described heat pipe-type material condenser body also is provided with the temperature of charge sensor, and described temperature of charge sensor is communicated with described the first control valve simultaneously.
And also being provided with pressure sensor on described the first pipeline, described pressure sensor is communicated with the second control valve simultaneously.
The beneficial effects of the utility model are: the utility model is adjusted and is optimized in design cycle in terms of existing technologies, can reduce investment cost and the operating cost of device, make things convenient for the actual motion operation, and flow process is reasonable, advanced, can satisfy the needs of actual production.
In addition, the utility model not only reclaims reaction process gas and material waste heat (condensation sensible heat and latent heat), has reduced operating cost, has optimized the residual neat recovering system flow process; Can also produce hot water or the low-pressure steam of uniform temperature and flow, with supply the user who needs be arranged, provide convenience for the comprehensive utilization of heat energy, satisfy the needs of energy-saving and emission-reduction, have certain economic benefit and social benefit.
Description of drawings
Fig. 1 is the structural representation of the utility model one embodiment.
The specific embodiment
Below in conjunction with the drawings and specific embodiments the utility model is done concrete introduction.
Fig. 1 is the structural representation of the utility model one embodiment.
As shown in Figure 1: heat pipe-type material condenser device, comprise heat pipe-type material condenser body 2, boiler 11 and pressurizing feedwater pump 12, the bottom of described heat tube type cold condenser body 2 is provided with material inlet, the top is provided with hot water or low-pressure steam outlet, the middle part then is provided with the weary gas outlet of material, water inlet and sewage draining exit 7, described material inlet is connected with the material outlet of the material reaction device 1 that is arranged on heat tube type cold condenser body 2 bottoms, the outlet of hot water or low-pressure steam is connected with the plant area pipe network by the first pipeline 6, the weary gas outlet of material is connected with follow-up material pipe network by second pipe 3, water inlet is connected with pressurizing feedwater pump 12 by tube connector 4, and described pressurizing feedwater pump 12 is connected with boiler 11, in addition, the inside of described heat tube type cold condenser body 2 also is provided with heat transfer element 5 and is used for separating the tube sheet 8 of material and cooling water, and described middle tube sheet 8 is horizontally installed on the middle part of heat tube type cold condenser body 2.
In the present embodiment, described heat transfer element 5 is heat exchanger tube, and described heat exchanger tube is in the 2 interior vertical vertical settings of heat tube type cold condenser body, can certainly the horizontal type level setting, and the bottom of described heat exchanger tube also is provided with for the fixing lower perforated plate 9 of heat exchanger tube, and described lower perforated plate 9 is fixedly connected with heat tube type cold condenser body 2.In addition, described heat transfer element 5 also can be finned tube.
Be provided with the first control valve 13 that enters the cold fluid flow in the heat tube type cold condenser body 2 for control on the described tube connector 4, so just can realize the adjusting to the cold fluid flow that enters heat pipe-type material condenser body 2, satisfy the subsequent technique requirement to guarantee the cooled temperature of heat pipe-type material condenser body 2 interior materials.And also being provided with the first by-passing valve 15 on the described tube connector 4, described the first by-passing valve 15 and the first control valve 13 are set up in parallel.
And be provided with the second control valve 14 that enters the cold fluid pressure in plant area's pipe network for control on described the first pipeline 6, realize being sent to the adjusting of the required low-pressure steam pressure of user by the aperture of regulating the second control valve 14.And also being provided with the second by-passing valve 16 on described the first pipeline 6, described the second by-passing valve 16 and the second control valve 14 are set up in parallel.Under normal circumstances, the first by-passing valve 15 and the second by-passing valve 16 are in closed condition, when the first control valve 13 or the second control valve 14 break down, can be by closing former and later two valves of the control valve that breaks down, the by-passing valve that open simultaneously on its pipeline is realized manually control.
The first above-mentioned control valve 13 and the second control valve 14 are electronic (or pneumatic) control valve.
In addition, the bottom of described heat pipe-type material condenser body 2 also is provided with temperature of charge sensor 101, and described temperature of charge sensor 101 is communicated with described the first control valve 13 simultaneously.
And also being provided with pressure sensor 102 on described the first pipeline, described pressure sensor 102 is communicated with the second control valve 14 simultaneously.
The cold side cold fluid of above-mentioned heat pipe-type material condenser body 2 also can adopt heat conduction wet goods medium to carry out heat exchange.
The course of work of the present utility model is: the material by 2 pairs of material reaction devices 1 of heat pipe-type material condenser body carries out waste heat recovery first, by pressurizing feedwater pump 12 cold water is delivered to hot water or the low-pressure steam that produces uniform temperature and flow in the heat pipe-type material condenser body 2, again this hot water or low-pressure steam is delivered to the user's use that needs hot water or low-pressure steam.
The utility model is adjusted and is optimized in design cycle in terms of existing technologies, can reduce investment cost and the operating cost of device, make things convenient for the actual motion operation, and flow process is reasonable, advanced, can satisfy the needs of actual production.
In addition, the utility model not only reclaims reaction process gas and material waste heat (condensation sensible heat and latent heat), has reduced operating cost, has optimized the residual neat recovering system flow process; Can also produce hot water or the low-pressure steam of uniform temperature and flow, with supply the user who needs be arranged, provide convenience for the comprehensive utilization of heat energy, satisfy the needs of energy-saving and emission-reduction, have certain economic benefit and social benefit.
Above-described embodiment does not limit the utility model in any form, and all employings are equal to replaces or technical scheme that the mode of equivalent transformation obtains, all drops in the protection domain of the present utility model.

Claims (10)

1. heat pipe-type material condenser device, it is characterized in that, comprise heat pipe-type material condenser body (2), boiler (11) and pressurizing feedwater pump (12), the bottom of described heat tube type cold condenser body (2) is provided with material inlet, the top is provided with hot water or low-pressure steam outlet, the middle part then is provided with the weary gas outlet of material, water inlet and sewage draining exit (7), described material inlet is connected with the material outlet of the material reaction device (1) that is arranged on heat tube type cold condenser body (2) bottom, the outlet of hot water or low-pressure steam is connected with the plant area pipe network by the first pipeline (6), the weary gas outlet of material is connected with follow-up material pipe network by second pipe (3), water inlet is connected with pressurizing feedwater pump (12) by tube connector (4), and described pressurizing feedwater pump (12) is connected with boiler (11), in addition, the inside of described heat tube type cold condenser body (2) also is provided with heat transfer element (5) and is used for separating the tube sheet (8) of material and cooling water, and described middle tube sheet (8) is horizontally installed on the middle part of heat tube type cold condenser body (2).
2. heat pipe-type material condenser device according to claim 1 is characterized in that, described heat transfer element (5) is heat exchanger tube or finned tube.
3. heat pipe-type material condenser device according to claim 2 is characterized in that, described heat exchanger tube is vertical vertical setting or horizontal type level setting in heat tube type cold condenser body (2).
4. heat pipe-type material condenser device according to claim 2 is characterized in that, the bottom of described heat exchanger tube also is provided with for the fixing lower perforated plate of heat exchanger tube (9), and described lower perforated plate (9) is fixedly connected with heat tube type cold condenser body (2).
5. heat pipe-type material condenser device according to claim 1 is characterized in that, is provided with the first control valve (13) that enters the cold fluid flow in the heat tube type cold condenser body (2) for control on the described tube connector (4).
6. heat pipe-type material condenser device according to claim 5 is characterized in that, also is provided with the first by-passing valve (15) on the described tube connector (4), and described the first by-passing valve (15) is set up in parallel with the first control valve (13).
7. heat pipe-type material condenser device according to claim 1 is characterized in that, is provided with the second control valve (14) that enters the cold fluid pressure in plant area's pipe network for control on described the first pipeline (6).
8. heat pipe-type material condenser device according to claim 7 is characterized in that, also is provided with the second by-passing valve (16) on described the first pipeline (6), and described the second by-passing valve (16) is set up in parallel with the second control valve (14).
9. heat pipe-type material condenser device according to claim 1, it is characterized in that, the bottom of described heat pipe-type material condenser body (2) also is provided with temperature of charge sensor (101), and described temperature of charge sensor (101) is communicated with described the first control valve (13) simultaneously.
10. heat pipe-type material condenser device according to claim 1 is characterized in that, also is provided with pressure sensor (102) on described the first pipeline (6), and described pressure sensor (102) is communicated with the second control valve (14) simultaneously.
CN 201220398639 2012-08-13 2012-08-13 Heat pipe type material condenser device Expired - Fee Related CN202869332U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220398639 CN202869332U (en) 2012-08-13 2012-08-13 Heat pipe type material condenser device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220398639 CN202869332U (en) 2012-08-13 2012-08-13 Heat pipe type material condenser device

Publications (1)

Publication Number Publication Date
CN202869332U true CN202869332U (en) 2013-04-10

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201220398639 Expired - Fee Related CN202869332U (en) 2012-08-13 2012-08-13 Heat pipe type material condenser device

Country Status (1)

Country Link
CN (1) CN202869332U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113405394A (en) * 2021-06-29 2021-09-17 连云港临海新材料有限公司 High-grade waste heat recovery device and process for high-temperature calcined petroleum coke

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113405394A (en) * 2021-06-29 2021-09-17 连云港临海新材料有限公司 High-grade waste heat recovery device and process for high-temperature calcined petroleum coke

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

Granted publication date: 20130410

Termination date: 20200813