CN219333204U - Steam condensate recycling system - Google Patents
Steam condensate recycling system Download PDFInfo
- Publication number
- CN219333204U CN219333204U CN202223432089.8U CN202223432089U CN219333204U CN 219333204 U CN219333204 U CN 219333204U CN 202223432089 U CN202223432089 U CN 202223432089U CN 219333204 U CN219333204 U CN 219333204U
- Authority
- CN
- China
- Prior art keywords
- steam condensate
- pipeline
- utility
- model
- desalted water
- 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.)
- Active
Links
- 238000004064 recycling Methods 0.000 title claims abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 27
- 230000001105 regulatory effect Effects 0.000 claims description 6
- 238000000034 method Methods 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 4
- 238000005406 washing Methods 0.000 description 3
- 238000010612 desalination reaction Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 2
- 230000001502 supplementing effect Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000011033 desalting Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 235000010344 sodium nitrate Nutrition 0.000 description 1
- 239000004317 sodium nitrate Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
Images
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The utility model discloses a steam condensate recycling system, which belongs to the technical field of steam condensate recycling, and particularly relates to a steam condensate recycling system.
Description
Technical Field
The utility model relates to the technical field of steam condensate recovery, in particular to a steam condensate recovery and utilization system.
Background
In the preparation process of the Fischer-Tropsch synthesis catalyst, sodium nitrate as a byproduct is generated through evaporation and crystallization, in the evaporation process, steam is required to be used for heating, condensed steam condensate can be used for heating desalted water after heat exchange of the steam, the heated desalted water is used for the catalyst water washing process, but because the temperature of the steam condensate is about 100 ℃ which is too high, the temperature of the heated desalted water is above 90 ℃, the water washing process requires that the temperature of the desalted water is 85-87 ℃, otherwise, the quality of a catalyst product can be influenced, the temperature can be controlled only by discharging a part of the steam condensate and supplementing the desalted water, so that certain waste is caused, meanwhile, the temperature controlling process is unstable, and personnel are required to monitor and operate for a long time.
Disclosure of Invention
The utility model aims to provide a steam condensate recycling system, which solves the problems that the temperature of the steam condensate is over 100 ℃ and is above 90 ℃ after being mixed with desalted water, the temperature of the desalted water is required to be 85-87 ℃ in a water washing process, otherwise, the quality of a catalyst product can be influenced, the temperature can be controlled by discharging a part of steam condensate and supplementing the desalted water, so that certain waste is caused, meanwhile, the temperature control process is unstable, and long-time monitoring and operation of personnel are required.
In order to achieve the above purpose, the present utility model provides the following technical solutions: the utility model provides a steam condensate recycle system, includes desalination water pipeline and steam condensate pipeline, the right-hand member of desalination water pipeline is provided with temperature feedback governing valve, the right-hand member of steam condensate pipeline is provided with steam condensate collecting vat, the left end connection of steam condensate collecting vat is provided with overflow pipeline, the right-hand member of steam condensate collecting vat is provided with the delivery pump, the upper end connection of delivery pump is provided with the teletransmission thermometer.
Preferably, the output end of the temperature feedback regulating valve is respectively connected and fixed with the input end of the remote thermometer and the output end of the steam condensate collecting tank.
Compared with the prior art, the utility model has the beneficial effects that:
the utility model can effectively recycle the steam condensate, reduce the consumption of desalted water, effectively control the water temperature, bring a certain economic value and have wider practicability.
Drawings
FIG. 1 is a schematic diagram of the structure of the present utility model.
In the figure: a desalting water pipeline 1, a steam condensate pipeline 2, an overflow pipeline 3, a steam condensate collecting tank 4, a conveying pump 5, a remote transmission thermometer 6 and a temperature feedback regulating valve 7.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
In the description of the present utility model, it should be understood that the terms "upper," "lower," "front," "rear," "left," "right," "top," "bottom," "inner," "outer," and the like indicate or are based on the orientation or positional relationship shown in the drawings, merely to facilitate description of the present utility model and to simplify the description, and do not indicate or imply that the devices or elements referred to must have a specific orientation, be configured and operated in a specific orientation, and thus should not be construed as limiting the present utility model.
Examples:
referring to fig. 1, the present utility model provides a technical solution: the utility model provides a steam condensate recycle system, includes desalted water pipeline 1 and steam condensate pipeline 2, the right-hand member of desalted water pipeline 1 is provided with temperature feedback governing valve 7, the right-hand member of steam condensate pipeline 2 is provided with steam condensate collecting vat 4, the left end connection of steam condensate collecting vat 4 is provided with overflow pipeline 3, the right-hand member of steam condensate collecting vat 4 is provided with delivery pump 5, the upper end connection of delivery pump 5 is provided with teletransmission thermometer 6.
The output end of the temperature feedback regulating valve 7 is respectively connected and fixed with the input end of the remote thermometer 6 and the output end of the steam condensate collecting tank 4.
Working principle: the steam condensate is pumped out of the steam condensate pipeline 2 through the previous working procedure and is fully conveyed into the steam condensate collecting tank 4, desalted water is conveyed to the inlet of the conveying pump 5 through the desalted water pipeline 1 after passing through the temperature feedback regulating valve 7, when the desalted water is washed, the conveying pump 5 is started to control the water inflow of the desalted water by utilizing the feedback temperature of the pump outlet remote thermometer 6 and the interlocking of the temperature feedback regulating valve 7 in the desalted water pipeline 1, the temperature is ensured to be maintained at 85-87 ℃ for the next working procedure, when the collected steam condensate is surplus, the collected steam condensate can be discharged through the overflow pipeline 3, wherein the overflow pipeline 3 is an inverted U-shaped pipe with the height of 3m, and when the overflow pipeline is 3m, the desalted water can be discharged in an overflow mode, and the operation is not monitored by personnel.
While the fundamental and principal features of the utility model and advantages of the utility model have been shown and described, it will be apparent to those skilled in the art that the utility model is not limited to the details of the foregoing exemplary embodiments, but may be embodied in other specific forms without departing from the spirit or essential characteristics thereof; the present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the utility model being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein.
Although embodiments of the present utility model have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made therein without departing from the principles and spirit of the utility model, the scope of which is defined in the appended claims and their equivalents.
Claims (2)
1. The utility model provides a steam condensate recycle system, includes desalted water pipeline (1) and steam condensate pipeline (2), its characterized in that, the right-hand member of desalted water pipeline (1) is provided with temperature feedback governing valve (7), the right-hand member of steam condensate pipeline (2) is provided with steam condensate collecting vat (4), the left end connection of steam condensate collecting vat (4) is provided with overflow pipeline (3), the right-hand member of steam condensate collecting vat (4) is provided with delivery pump (5), the upper end connection of delivery pump (5) is provided with teletransmission thermometer (6).
2. The steam condensate recycling system of claim 1, wherein: the output end of the temperature feedback regulating valve (7) is respectively connected and fixed with the input end of the remote thermometer (6) and the output end of the steam condensate collecting tank (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202223432089.8U CN219333204U (en) | 2022-12-21 | 2022-12-21 | Steam condensate recycling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202223432089.8U CN219333204U (en) | 2022-12-21 | 2022-12-21 | Steam condensate recycling system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219333204U true CN219333204U (en) | 2023-07-14 |
Family
ID=87110539
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202223432089.8U Active CN219333204U (en) | 2022-12-21 | 2022-12-21 | Steam condensate recycling system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219333204U (en) |
-
2022
- 2022-12-21 CN CN202223432089.8U patent/CN219333204U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN114277393B (en) | A heat energy recycling system for producing hydrogen by electrolysis and a control method thereof | |
| CN102557225A (en) | Method for adjusting pH value of secondary circuit of nuclear power plant | |
| CN219333204U (en) | Steam condensate recycling system | |
| CN208426672U (en) | A kind of steam condensate recovery system | |
| CN220939129U (en) | Waste acid concentration device | |
| CN201367397Y (en) | Device for producing naphthalene series based water reducing agent or homologous dispersion agent thereof | |
| CN220939130U (en) | Concentrated spent acid joins in marriage sour device | |
| CN207608511U (en) | A kind of butyraldehyde stripping recovery system of PVB waste water | |
| CN218755115U (en) | Stainless steel pickling waste liquid treatment device | |
| CN111606867A (en) | Differential urea co-production melamine device and production method | |
| CN109678819A (en) | A kind of ketene dimer optimization production capacity production method | |
| CN213112908U (en) | Low-temperature multi-effect seawater desalination decarbonization antiscaling device | |
| CN213652670U (en) | Circulating temperature regulating system of ion membrane electrolytic cell | |
| CN203487063U (en) | Device for preparing polyoxymethylene dimethyl ethers | |
| CN220245632U (en) | Washing water system for phosphoric acid production | |
| CN211004598U (en) | Continuous quality-separating crystallization and purification device for sodium chloride and ammonium chloride in industrial mixed salt wastewater | |
| CN210367047U (en) | Multistage flash distillation desulfurization effluent treatment plant | |
| CN209291967U (en) | A kind of equipment for preparing polyphosphoric acid by microwave flash evaporation of phosphoric acid | |
| CN116023250A (en) | PTA process waste heat recovery system, PTA process system and PTA process | |
| CN216549657U (en) | Stannous chloride production system | |
| CN223342459U (en) | Titanium white powder production waste liquid recycle device | |
| CN110496413A (en) | A kind of Increasing Production and Energy Saving technological transformation method and device of vulcanized sodium multi-effect evaporation system | |
| CN222969517U (en) | A device for capturing tail gas materials from chlorination kettle | |
| CN116371320B (en) | A system and method for continuously producing dimethylol urea with high purity | |
| CN120717660B (en) | NMMO waste glue solution recycling treatment system in lyocell fiber production |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |