CN214319397U - Novel sediment thick liquid desorption is retrieved device - Google Patents
Novel sediment thick liquid desorption is retrieved device Download PDFInfo
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- CN214319397U CN214319397U CN202022195262.1U CN202022195262U CN214319397U CN 214319397 U CN214319397 U CN 214319397U CN 202022195262 U CN202022195262 U CN 202022195262U CN 214319397 U CN214319397 U CN 214319397U
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Abstract
A novel slag slurry desorption recovery device comprises a slag slurry buffer tank, wherein the slag slurry buffer tank is connected with a carbide slurry discharge pipe through a pipeline, the bottom of the slag slurry buffer tank is provided with a carbide discharge pipe, a supernatant input pipeline is arranged on the slag slurry buffer tank, the slag slurry buffer tank is connected with a slag slurry pump through a pipeline, the output end of the slag slurry pump is connected with a desorption tower through a pipeline, the output end of the desorption tower is connected with a cooler through a pipeline, the cooler is connected with a vacuum pump through a pipeline, and the vacuum pump is connected with an acetylene buffer tank through a pipeline; the utility model discloses simple structure, convenient to use, low in cost and easy to maintain have solved among the prior art problem that sediment thick liquid recovery system pressure balance is slow, and ageing is low, through simple structure, very big improvement production safety, make the operation of whole equipment more reliable and more stable.
Description
Technical Field
The utility model relates to a chemical industry field especially relates to a novel sediment thick liquid desorption recovery device.
Background
The influence of the slag discharging of the acetylene generator and the slag slurry buffer tank on the pressure and the liquid level of the slag slurry buffer tank is large, the conventional slag slurry backflow pipeline and the conventional pressure balance pipeline are slow in regulation process, the normal operation of the slag slurry desorption and recovery device is seriously influenced, and great potential safety hazards are generated on safety production.
SUMMERY OF THE UTILITY MODEL
The utility model aims to overcome the defects of the prior art, and provides a novel slag slurry desorption and recovery device which has simple structure, convenient use, stable operation and reliable use.
Novel sediment thick liquid desorption recovery unit includes the sediment thick liquid buffer tank, the pipe is arranged into to the sediment thick liquid buffer tank pipe connection carbide thick liquid, that is to say, through the carbide thick liquid pipeline row pipe in the sediment thick liquid buffer tank, sediment thick liquid buffer tank bottom is equipped with the carbide discharge pipe, and the carbide discharge pipe is used for discharging solid-state carbide.
And a supernatant liquid input pipeline is arranged on the slag slurry buffer tank and is used for supplementing liquid when the liquid level in the slag slurry buffer tank is too low.
The slurry buffer tank is connected with a slurry pump through a pipeline, the output end of the slurry pump is connected with a desorption tower through a pipeline, the output end of the desorption tower is connected with a cooler through a pipeline, the cooler is connected with a vacuum pump through a pipeline, and acetylene gas in the cooler is separated through the vacuum pump and is discharged into the acetylene buffer tank.
The pipeline connection pressure compensating pipe on the sediment thick liquid buffer tank, the pressure compensating pipe makes the pipeline UNICOM between sediment thick liquid buffer tank and sediment thick liquid pump to the desorption tower, be equipped with the pneumatic valve on the pressure compensating pipe. The purpose of the arrangement form is to avoid overhigh negative pressure difference in the slag pulp buffer tank, and the opening degree of the pneumatic valve is adjusted to control the pressure of the pneumatic valve within a certain range, so that the influence on the operation stability and the production safety is avoided.
Further, a filter is arranged between the slurry buffer tank and the slurry pump. The purpose of this arrangement is to prevent plugging of the slurry pump for slurry filtration.
The utility model has the advantages that: the utility model discloses simple structure, convenient to use, low in cost and easy to maintain have solved among the prior art problem that sediment thick liquid recovery system pressure balance is slow, and ageing is low, through simple structure, very big improvement production safety, make the operation of whole equipment more reliable and more stable.
Drawings
FIG. 1 is a schematic structural view of a novel slurry desorption and recovery device according to the present invention;
reference numerals:
1-carbide slag slurry discharge pipe 2-supernatant liquid input pipeline 3-carbide discharge pipe 4-slag slurry buffer tank 5-pressure compensating pipe 6-desorption tower 7-cooler 8-acetylene buffer tank 9-vacuum pump 10-slag slurry pump 11-filter
The objects, features and advantages of the present invention will be further described with reference to the accompanying drawings.
Detailed Description
Referring to fig. 1, a novel sediment thick liquid desorption recovery unit, including sediment thick liquid buffer tank 4, 4 pipe connections carbide thick liquid of sediment thick liquid buffer tank arrange into pipe 1, that is to say, through carbide thick liquid pipeline arrange into in the pipe arranges into sediment thick liquid buffer tank 4, 4 bottoms of sediment thick liquid buffer tank are equipped with carbide discharge pipe 3, carbide discharge pipe 3 is used for discharging solid-state carbide.
And a supernatant input pipeline 2 is arranged on the slag slurry buffer tank 4, and the supernatant input pipeline 2 is used for liquid supplement when the liquid level in the slag slurry buffer tank 4 is too low.
4 pipe connection sediment stuff pumps 10 of sediment thick liquid buffer tank, sediment thick liquid pump 10 output end pipe connection desorption tower 6, 6 output end pipe connection coolers 7 of desorption tower, 7 pipe connection vacuum pump 9 of cooler, the acetylene gas in the cooler 7 is deviate from through vacuum pump 9, and the acetylene buffer tank 8 is gone into to the side by side.
The pipeline connection pressure compensating pipe 5 is gone up to sediment thick liquid buffer tank 4, pressure compensating pipe 5 makes the pipeline UNICOM between sediment thick liquid buffer tank 4 and sediment thick liquid pump 10 to desorption tower 6, be equipped with the pneumatic valve on the pressure compensating pipe 5. The purpose of this kind of arrangement form is to avoid the sediment thick liquid surge tank 4 in negative pressure differential pressure too high, through the aperture regulation of pneumatic valve, makes its pressure control in certain extent, avoids influencing operation stability and production safety.
Further, a filter 11 is arranged between the slurry buffer tank 4 and the slurry pump 10. The purpose of this arrangement is to prevent plugging of the slurry pump 10 for slurry filtration.
The basic principles and the main features of the invention and the advantages of the invention have been shown and described above, it will be evident to those skilled in the art that the invention is not limited to the details of the foregoing illustrative embodiments, but that the invention may be embodied in other specific forms without departing from the spirit or essential characteristics of the invention. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention 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. Any reference sign in a claim should not be construed as limiting the claim concerned.
Furthermore, it should be understood that although the present description refers to embodiments, not every embodiment may contain only a single embodiment, and such description is for clarity only, and those skilled in the art should integrate the description, and the embodiments may be combined as appropriate to form other embodiments understood by those skilled in the art.
Claims (2)
1. The utility model provides a novel sediment thick liquid desorption recovery unit, includes the sediment thick liquid buffer tank, sediment thick liquid buffer tank pipe connection carbide thick liquid discharge pipe, sediment thick liquid buffer tank bottom is equipped with carbide discharge pipe, its characterized in that: a supernatant liquid input pipeline is arranged on the slurry buffer tank, the slurry buffer tank is connected with a slurry pump through a pipeline, the output end of the slurry pump is connected with a desorption tower through a pipeline, the output end of the desorption tower is connected with a cooler through a pipeline, the cooler is connected with a vacuum pump through a pipeline, and the vacuum pump is connected with an acetylene buffer tank through a pipeline;
the pipeline connection pressure compensating pipe on the sediment thick liquid buffer tank, the pressure compensating pipe makes the pipeline UNICOM between sediment thick liquid buffer tank and sediment thick liquid pump to the desorption tower, be equipped with the pneumatic valve on the pressure compensating pipe.
2. The novel slurry desorption recovery device as claimed in claim 1, wherein a filter is arranged between the slurry buffer tank and the slurry pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022195262.1U CN214319397U (en) | 2020-09-30 | 2020-09-30 | Novel sediment thick liquid desorption is retrieved device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022195262.1U CN214319397U (en) | 2020-09-30 | 2020-09-30 | Novel sediment thick liquid desorption is retrieved device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN214319397U true CN214319397U (en) | 2021-10-01 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202022195262.1U Active CN214319397U (en) | 2020-09-30 | 2020-09-30 | Novel sediment thick liquid desorption is retrieved device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN214319397U (en) |
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2020
- 2020-09-30 CN CN202022195262.1U patent/CN214319397U/en active Active
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