CN205850812U - A kind of reburner condensate recovery device - Google Patents
A kind of reburner condensate recovery device Download PDFInfo
- Publication number
- CN205850812U CN205850812U CN201620651200.8U CN201620651200U CN205850812U CN 205850812 U CN205850812 U CN 205850812U CN 201620651200 U CN201620651200 U CN 201620651200U CN 205850812 U CN205850812 U CN 205850812U
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- CN
- China
- Prior art keywords
- reburner
- pump
- recovery device
- tank
- condensate recovery
- 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
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- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model discloses a kind of reburner condensate recovery device, including the reburner being provided with chuck on outer wall, described chuck connects surge tank by steam pipe, surge tank is connected with Sedimentation tank by condensate line again, described Sedimentation tank connects water tank by pipeline, it is provided with self priming pump between Sedimentation tank and water tank, recycling by the desalted water steam in chuck on reburner outer wall being carried out condensation sedimentation, efficiently solving in prior art by the natural evaporation waste to desalted water.
Description
Technical field
This utility model belongs to chemical production technical field, is specifically related to a kind of reburner condensate recovery device.
Background technology
When Chemical Manufacture uses oven gas to prepare methanol, need to use reburner to carry out partial oxidation combustion under the conditions of pure oxygen
Burning reaction and steam reforming reaction, in course of reaction, hot(test)-spot temperature reaches 1200-1400 DEG C, owing to temperature is higher so needing
Designing water leg on reburner outer wall uses desalted water entrance chuck to dispel the heat in the way of natural evaporation, to ensure equipment
Safely and steadily run, but in prior art, use about 12 tons desalted waters every about hour, take the shape of natural evaporation
Formula, makes substantial amounts of desalted water be evaporated consumption, causes the waste of resource, increase manufacturing cost.
Summary of the invention
In order to solve the problems referred to above, this utility model provides a kind of reburner condensate recovery device, by outside reburner
Desalted water in wall chuck collect carry out condensing through surge tank, Sedimentation tank and cooling water tank, settle, cool down after recycle,
Solve the technology carrying out desalted water in the way of natural evaporation in prior art dispelling the heat and cause desalted water to waste in a large number to ask
Topic.
To achieve these goals, the technical solution adopted in the utility model is:
A kind of reburner condensate recovery device, including being provided with the reburner of chuck on outer wall, described chuck is by steaming
Steam pipe connection surge tank, surge tank is connected with Sedimentation tank by condensate line again, and described Sedimentation tank cools down water by pipeline communication
Case.
Further, being provided with pump between Sedimentation tank and cooling water tank, pump intake is connected with Sedimentation tank by inlet pipeline,
Pump discharge is connected with water tank by outlet conduit.
Further, Sedimentation tank is also connected with evaporative type cooler by pipeline.
Further, Sedimentation tank is additionally provided with overflow pipe.
Further, described condensate line is provided with the first stop valve.
Further, pump is self priming pump.
Further, described outlet conduit is provided with the second stop valve for regulating pump discharge pressure.
Further, described second stop valve and between outlet conduit on be provided with for preventing pump discharge aqueous reflux
Check (non-return) valve.
Compared with prior art, this utility model at least has the advantages that, by by chuck on reburner outer wall
In desalted water steam collect surge tank and carry out cooling and condense into liquid, this liquid desalted water is again by Sedimentation tank, profit
With expansion chamber, the dust impurities in desalted water is carried out subsiding and purifying, finally flow into cooling water tank and reclaim, again with, this
Sample has reached energy-saving and cost-reducing purpose, and this reburner condensate recovery device simple in construction, and easy and simple to handle, practicality is the highest.
Further, being provided with self priming pump between Sedimentation tank and cooling water tank, easy to operate, operate steadily, efficiency is high, work
Quantitative desalted water is contained, it becomes possible to be transported in cooling water tank by the desalted water after sedimentation in only need to ensureing the pump housing before making, it is ensured that
Desalted water can be recovered in cooling water tank by whole retracting device smoothly.
Further, condensate line and outlet conduit are respectively arranged with stop valve, it is possible to control condensation desalted water at any time
Flow and speed.
Further, the outlet conduit between stop valve and pump being provided with check (non-return) valve, check (non-return) valve ensures condensation desalted water
Can only one-way flow, prevent pump discharge liquid desalted water from flowing backwards, affect the properly functioning of whole device.
Further, jacket of converter overflow pipe can guarantee that a certain amount of liquid level of energy, in order to when liquid level exceedes, unnecessary liquid
The rapid overflow of physical ability is discharged.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In accompanying drawing: 1, reburner, 2, surge tank, 3, Sedimentation tank, 4, pump, 5, chuck, a, steam pipe, b, condensate line, c,
Inlet pipeline, d, outlet conduit, e, overflow pipe, f, the first stop valve, h, the second stop valve, g, check (non-return) valve.
Detailed description of the invention
With detailed description of the invention, this utility model is described further below in conjunction with the accompanying drawings.
See Fig. 1, a kind of reburner condensate recovery device, including being provided with the reburner 1 of chuck 5 on outer wall, chuck 5
Connecting surge tank 2 by steam pipe a, surge tank 2 is connected with Sedimentation tank 3 by condensate line b again, and Sedimentation tank 3 is by pipeline even
Water flowing case, condensate line b is provided with the first stop valve f, is provided with pump 4 between Sedimentation tank 3 and water tank, and pump 4 is self priming pump, pump
4 entrances are connected with Sedimentation tank 3 by inlet pipeline c, and pump 4 is exported and connected with water tank by outlet conduit d, and outlet conduit d sets
Be equipped with the second stop valve h for regulating pump 4 outlet pressure, the outlet conduit d between stop valve h and pump 4 is provided with for
Preventing the check (non-return) valve g that pump 4 water outlet flows backwards, Sedimentation tank 3 from also connecting evaporative type cooler by pipeline, Sedimentation tank 3 is additionally provided with
Overflow pipe e.
A kind of reburner condensate recovery device that this utility model provides, when reburner 1 normally works, to reburner
The chuck 5 arranged on 1 outer wall inputs desalted water, owing to the operating temperature of reburner 1 is 1200-1400 DEG C, and the desalination in chuck 5
Steam turns to gaseous state, opens and is provided with the second stop valve h on the first stop valve f and outlet conduit d arranged on condensate line b,
Desalted water steam enters surge tank 2 by steam pipe a and condenses, and it is heavy that the desalted water after condensation is entered by condensate line b again
Fall pond 3 carries out sedimentation cooling, is settled by the dust impurities in desalted water, opens pump 4, uses the second stop valve h regulation pump 4 to export
Pressure, the desalted water in Sedimentation tank 3 is transported in water tank recycle, thus is avoided that the side by natural evaporation by pump 4
Substantial amounts of desalted water is wasted by formula.
Claims (8)
1. a reburner condensate recovery device, it is characterised in that include the reburner (1) being provided with chuck (5) on outer wall,
Described chuck (5) is by steam pipe (a) connection surge tank (2), and surge tank (2) is again by condensate line (b) with Sedimentation tank (3) even
Logical, described Sedimentation tank (3) passes through pipeline communication water tank.
A kind of reburner condensate recovery device the most according to claim 1, it is characterised in that described Sedimentation tank (3) with
Being provided with pump (4) between water tank, pump (4) entrance is connected with Sedimentation tank (3) by inlet pipeline (c), and pump (4) outlet is by outlet
Pipeline (d) connects with water tank.
A kind of reburner condensate recovery device the most according to claim 1, it is characterised in that described Sedimentation tank (3) leads to
Piping also connects evaporative type cooler.
A kind of reburner condensate recovery device the most according to claim 1, it is characterised in that described Sedimentation tank (3) is also
It is provided with overflow pipe (e).
A kind of reburner condensate recovery device the most according to claim 1, it is characterised in that described condensate line
The first stop valve (f) it is provided with on (b).
A kind of reburner condensate recovery device the most according to claim 2, it is characterised in that described pump (4) is self-priming
Pump.
A kind of reburner condensate recovery device the most according to claim 2, it is characterised in that described outlet conduit
The second stop valve (h) for regulating pump (4) outlet pressure it is provided with on (d).
A kind of reburner condensate recovery device the most according to claim 7, it is characterised in that described second stop valve
The check (non-return) valve (g) for preventing pump (4) water outlet from flowing backwards it is provided with on outlet conduit (d) between (h) and pump (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620651200.8U CN205850812U (en) | 2016-06-27 | 2016-06-27 | A kind of reburner condensate recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620651200.8U CN205850812U (en) | 2016-06-27 | 2016-06-27 | A kind of reburner condensate recovery device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205850812U true CN205850812U (en) | 2017-01-04 |
Family
ID=57637551
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620651200.8U Expired - Fee Related CN205850812U (en) | 2016-06-27 | 2016-06-27 | A kind of reburner condensate recovery device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205850812U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108854167A (en) * | 2018-09-17 | 2018-11-23 | 陕西黑猫焦化股份有限公司 | The cyclic utilization system of methane steam reforming rear condensate liquid in coke-stove gas |
-
2016
- 2016-06-27 CN CN201620651200.8U patent/CN205850812U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108854167A (en) * | 2018-09-17 | 2018-11-23 | 陕西黑猫焦化股份有限公司 | The cyclic utilization system of methane steam reforming rear condensate liquid in coke-stove gas |
| CN108854167B (en) * | 2018-09-17 | 2023-12-05 | 陕西黑猫焦化股份有限公司 | Recycling system of condensate after methane steam conversion in coke oven gas |
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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: 20170104 Termination date: 20190627 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |