CN202915767U - Material condensation recovery device - Google Patents
Material condensation recovery device Download PDFInfo
- Publication number
- CN202915767U CN202915767U CN 201220579302 CN201220579302U CN202915767U CN 202915767 U CN202915767 U CN 202915767U CN 201220579302 CN201220579302 CN 201220579302 CN 201220579302 U CN201220579302 U CN 201220579302U CN 202915767 U CN202915767 U CN 202915767U
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- Prior art keywords
- condenser
- recycling device
- recovery device
- tube connector
- condensate recycling
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Abstract
The utility model discloses a material condensation recovery device. The material condensation recovery device is characterized by comprising a condenser, wherein the condenser is connected with an outlet of a material rector, an upper pipe plate and a lower pipe plate are arranged inside the condenser, heat transfer components are installed on the upper pipe plate and the lower pipe plate, the condenser is connected with a hot water tank by pressurizing to a water pump, and a water outlet of the condenser is connected with a pipe network in a factory. The material condensation recovery device not only enables reaction technology gas and material waste heat to be recovered, can reduce running cost, optimizes waste heat recovery system flow, but also can generate water with a certain temperature and flow or low pressure steam to be supplied to a user who needs, brings convenience to heat energy comprehensive utilization, and meets demands of energy conservation and emission reduction.
Description
Technical field
The utility model relates to the energy recovery recycling, relates in particular to a kind of material condensate recycling device.
Background technology
Reactor, destilling tower etc. are a kind of very important technological equipments of present chemical industry, petrochemical industry and pharmaceuticals industry.The process gas of the generation 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 assurance conduction oil and recirculating cooling water system normally move and consume a large amount of electric energy, 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 device operating cost because buying steam simultaneously.
The utility model content
The technical problem that the utility model solves is: a kind of material condensate recycling device is provided, better utilizes residual heat resources.
For reaching this purpose, the utility model by the following technical solutions:
A kind of material condensate recycling device, comprise condenser, described condenser connects the material reactor outlet, be provided with upper perforated plate and lower perforated plate in the described condenser, on described upper perforated plate and the lower perforated plate heat transfer element is installed, described condenser also connects boiler by the pressurizing feedwater pump, and described condenser delivery port connects plant area's pipe network.
Further, described pressurizing feedwater pump discharge links to each other with the water inlet of described condenser by the first tube connector.
Further, described heat transfer element is light pipe or finned tube.
Further, described condenser be vertical be arranged vertically or the bedroom horizontally disposed.
Further, be provided with the first control valve on described the first tube connector.
Further, described condenser delivery port connects plant area's pipe network by the second tube connector, is provided with the second control valve on described the second tube connector.
The beneficial effects of the utility model are: native system is adjusted and is optimized in design cycle, can reduce plant investment expense and operating cost, makes things convenient for the actual motion operation, and flow process is reasonable, advanced, can satisfy the needs of actual production.
The utility model not only reclaims reaction process gas and material waste heat, can reduce operating cost, has optimized the residual neat recovering system flow process; Hot water or the low-pressure steam that can also produce uniform temperature, flow are provided with the user who needs, and heat integration is provided convenience, and satisfy the needs of energy-saving and emission-reduction.
Description of drawings
The below is described in further detail the utility model with embodiment with reference to the accompanying drawings.
Fig. 1 is material condensate recycling device structural representation.
Among the figure:
1, material reaction device; 2, condenser; 3, upper perforated plate; 4, lower perforated plate; 5, heat transfer element; 6, pressurizing feedwater pump; 7, boiler; 8, condenser delivery port; 9, the first tube connector; 10, the second tube connector; 11, the first control valve; 12, the second control valve.
The specific embodiment
Further specify the technical solution of the utility model below in conjunction with accompanying drawing and by the specific embodiment.
As shown in Figure 1, in present embodiment, a kind of material condensate recycling device described in the utility model, comprise the condenser 2, the pressurizing feedwater pump 6 that link to each other with material reaction device 1, the outlet of pressurizing feedwater pump 6 is connected with the condenser water inlet by the first tube connector 9, hot water or low-pressure steam link to each other with condenser delivery port 8 by the second tube connector 10, thereby form residual neat recovering system.Condenser 2 is preferably vertical and is arranged vertically, but also Horizontal type is arranged.
Condenser 2 is equipped with heat transfer element 5 by upper perforated plate 3 and lower perforated plate 4, and this heat transfer element 5 is heat pipe or finned tube.Wherein condenser 2 belows link to each other with described material reaction device 1 by flange.
During use, the low-temperature water heating in the boiler 7 is given by pressurizing feedwater pump 6 and is sent into plant area's pipe network after condenser 2 is preheating to 90 ~ 95 ℃, is provided with the temperature of charge sensor in condenser 2 bottoms; Be provided with pressure sensor at the second tube connector 10, be provided with the first control valve 11 at the first tube connector 9, so just can realize satisfying the subsequent technique requirement to entering the adjusting of condenser 2 cold fluid flows to guarantee the cooled temperature of condenser 2 interior materials.The second tube connector 10 is provided with the second control valve 12, realizes being sent to the adjusting of the required low-pressure steam pressure of user by controlling opening of valve.Wherein the first control valve 11 and the second control valve 12 can be electronic or pneumatic control valve.
Be provided with respectively the first by-passing valve and the second by-passing valve at the first control valve 11 and the second control valve 12 places, under normal circumstances, by-passing valve is in closed condition, when control valve breaks down, can by close former and later two valves of control valve, open simultaneously by-passing valve and realize manually control.
Above-mentioned condenser 2 cold fluids also can adopt heat conduction wet goods medium to carry out heat exchange.
What need statement is; the above-mentioned specific embodiment only is preferred embodiment of the present utility model and institute's application technology principle; in technical scope disclosed in the utility model; the variation that any those skilled in the art of being familiar with expected easily or replacement all should be encompassed in the protection domain of the present utility model.
Claims (6)
1. material condensate recycling device, it is characterized in that, comprise condenser, described condenser connects the material reactor outlet, be provided with upper perforated plate and lower perforated plate in the described condenser, on described upper perforated plate and the lower perforated plate heat transfer element is installed, described condenser also connects boiler by the pressurizing feedwater pump, and described condenser delivery port connects plant area's pipe network.
2. material condensate recycling device according to claim 1 is characterized in that, described pressurizing feedwater pump discharge links to each other with the water inlet of described condenser by the first tube connector.
3. material condensate recycling device according to claim 1 is characterized in that, described heat transfer element is light pipe or finned tube.
4. material condensate recycling device according to claim 1 is characterized in that, described condenser be vertical be arranged vertically or the bedroom horizontally disposed.
5. material condensate recycling device according to claim 1 is characterized in that, is provided with the first control valve on described the first tube connector.
6. material condensate recycling device according to claim 1 is characterized in that, described condenser delivery port connects plant area's pipe network by the second tube connector, is provided with the second control valve on described the second tube connector.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220579302 CN202915767U (en) | 2012-11-06 | 2012-11-06 | Material condensation recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220579302 CN202915767U (en) | 2012-11-06 | 2012-11-06 | Material condensation recovery device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202915767U true CN202915767U (en) | 2013-05-01 |
Family
ID=48164075
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220579302 Expired - Fee Related CN202915767U (en) | 2012-11-06 | 2012-11-06 | Material condensation recovery device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202915767U (en) |
-
2012
- 2012-11-06 CN CN 201220579302 patent/CN202915767U/en not_active Expired - Fee Related
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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: 20130501 Termination date: 20151106 |
|
| EXPY | Termination of patent right or utility model |