CN219709425U - Acetylene concentration tank safe operation device - Google Patents
Acetylene concentration tank safe operation device Download PDFInfo
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- CN219709425U CN219709425U CN202321289516.3U CN202321289516U CN219709425U CN 219709425 U CN219709425 U CN 219709425U CN 202321289516 U CN202321289516 U CN 202321289516U CN 219709425 U CN219709425 U CN 219709425U
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- China
- Prior art keywords
- concentration
- pump
- pipeline
- treatment pipeline
- treatment
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- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 title claims abstract description 17
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 title claims abstract description 17
- 239000007788 liquid Substances 0.000 claims abstract description 30
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 238000009825 accumulation Methods 0.000 claims abstract description 16
- 239000006228 supernatant Substances 0.000 claims abstract description 11
- 239000002893 slag Substances 0.000 claims abstract description 9
- 230000008676 import Effects 0.000 claims description 6
- 238000011084 recovery Methods 0.000 claims description 4
- 230000001105 regulatory effect Effects 0.000 claims description 4
- 241000521257 Hydrops Species 0.000 claims description 2
- 206010030113 Oedema Diseases 0.000 claims description 2
- 239000002002 slurry Substances 0.000 abstract description 14
- 230000005540 biological transmission Effects 0.000 abstract description 8
- 230000006378 damage Effects 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 10
- 239000005997 Calcium carbide Substances 0.000 description 4
- CLZWAWBPWVRRGI-UHFFFAOYSA-N tert-butyl 2-[2-[2-[2-[bis[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]amino]-5-bromophenoxy]ethoxy]-4-methyl-n-[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]anilino]acetate Chemical compound CC1=CC=C(N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)C(OCCOC=2C(=CC=C(Br)C=2)N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)=C1 CLZWAWBPWVRRGI-UHFFFAOYSA-N 0.000 description 4
- 238000003825 pressing Methods 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 229910000519 Ferrosilicon Inorganic materials 0.000 description 1
- 238000006424 Flood reaction Methods 0.000 description 1
- 208000027418 Wounds and injury Diseases 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 208000014674 injury Diseases 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001960 triggered effect Effects 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
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- Accessories For Mixers (AREA)
Abstract
The utility model relates to the technical field of acetylene concentration tank treatment, in particular to a safe operation device of an acetylene concentration tank, which comprises a concentration tank and a first concentration pump, wherein an inlet at the upper part of the concentration tank is fixedly communicated with a carbide slag slurry inlet pipeline, an outlet at the upper part of the concentration tank is fixedly communicated with a supernatant liquid outlet pipeline, a first treatment pipeline is fixedly communicated between a first outlet at the bottom of the concentration tank and the inlet of the first concentration pump, and an outlet of the first concentration pump is fixedly communicated with a second treatment pipeline. The utility model has reasonable and compact structure and convenient use, and can solve the problem of damage to the pump body of the concentration pump caused by leakage of a large amount of concentrated slurry due to leakage of the concentration pump at the first time by arranging the submersible pump and the remote transmission liquid level meter in the water accumulation pit and realizing interlocking control of the submersible pump and the remote transmission liquid level meter, thereby avoiding safety production accidents, improving the safety coefficient of the device and having the characteristics of safety, labor saving, simplicity, convenience and high efficiency.
Description
Technical Field
The utility model relates to the technical field of acetylene concentration tank treatment, in particular to a safe operation device of an acetylene concentration tank.
Background
In the PVC process by the calcium carbide wet method acetylene, the waste water of the calcium carbide slag is correctly treated, the sewage discharge is reduced, the sewage treatment cost is saved, and the comprehensive utilization is achieved. The calcium carbide and water react in the generator to generate acetylene gas, and the generated calcium carbide slag slurry overflows to the concentration tank through the overflow pipe of the generator to be subjected to sedimentation separation, supernatant flows into the supernatant tank, and is conveyed to the generator for recycling through the supernatant pump, and concentrated slurry at the bottom of the concentration tank is conveyed to the filter pressing process for treatment through the concentration pump. The concentrated pump is arranged in a pit of 5 meters below the ground, and in the operation process, as the concentrated slurry contains ferrosilicon, the spiral casing and the pipeline of the concentrated pump are scoured and thinned after long-time operation, so that a large amount of leaked concentrated slurry floods the pit, the pump body of the concentrated pump is damaged, economic loss is generated, and personnel are easily corroded and burned by the concentrated slurry during emergency treatment, thereby causing personal injury and other accidents.
Disclosure of Invention
The utility model provides a safe operation device of an acetylene concentration tank, which overcomes the defects of the prior art, and can effectively solve the problem that a large amount of concentrated slurry leaks to damage a pump body of a concentration pump in the operation process of treating the concentrated slurry in the prior acetylene concentration tank.
The technical scheme of the utility model is realized by the following measures: the utility model provides an acetylene concentration pond safe operation device, including concentrated pond and first concentrated pump, the fixed intercommunication in concentrated pond upper portion import has carbide slag thick liquid feed liquor pipeline, the fixed intercommunication in concentrated pond upper portion export has supernatant drain line, fixed intercommunication has first processing pipeline between concentrated pond bottom first export and the first concentrated pump import, the fixed intercommunication in first concentrated pump export has the second processing pipeline, it is provided with the water accumulation pit to correspond first concentrated pump below, fixed mounting has immersible pump and teletransmission level gauge in the water accumulation pit, fixed intercommunication has the hydrops recovery pipeline between immersible pump and the concentrated pond top import, the electricity is connected between immersible pump and the teletransmission level gauge.
The following are further optimizations and/or improvements to the above-described inventive solution:
the device further comprises a second concentration pump, a third treatment pipeline is fixedly communicated between a second outlet at the bottom of the concentration tank and an inlet of the second concentration pump, and a fourth treatment pipeline is fixedly communicated between an outlet of the second concentration pump and the second treatment pipeline.
The third concentrating pump is fixedly communicated with a fifth treating pipeline between a third outlet at the bottom of the concentrating pool and an inlet of the third concentrating pump, and a sixth treating pipeline is fixedly communicated between an outlet of the third concentrating pump and the fourth treating pipeline.
The first treatment pipeline, the third treatment pipeline and the fifth treatment pipeline are respectively and fixedly provided with a flow regulating valve and a stop valve, the sixth treatment pipeline is fixedly provided with a stop valve, the fourth treatment pipeline between the sixth treatment pipeline and the second concentration pump is fixedly provided with a stop valve, and the second treatment pipeline between the fourth treatment pipeline and the first concentration pump is fixedly provided with a stop valve.
The utility model has reasonable and compact structure and convenient use, and can solve the problem of damage to the pump body of the concentration pump caused by leakage of a large amount of concentrated slurry due to leakage of the concentration pump at the first time by arranging the submersible pump and the remote transmission liquid level meter in the water accumulation pit and realizing interlocking control of the submersible pump and the remote transmission liquid level meter, thereby avoiding safety production accidents, improving the safety coefficient of the device and having the characteristics of safety, labor saving, simplicity, convenience and high efficiency.
Drawings
FIG. 1 is a schematic process flow diagram of a preferred embodiment of the present utility model.
The codes in the drawings are respectively: 1 is a concentration tank, 2 is a first concentration pump, 3 is a second concentration pump, 4 is a third concentration pump, 5 is a submersible pump, 6 is a remote transmission liquid level meter, 7 is a carbide slag slurry inlet pipeline, 8 is a supernatant liquid outlet pipeline, 9 is a first treatment pipeline, 10 is a second treatment pipeline, 11 is a third treatment pipeline, 12 is a fourth treatment pipeline, 13 is a fifth treatment pipeline, 14 is a sixth treatment pipeline, 15 is a effusion recovery pipeline, 16 is a flow regulating valve, and 17 is a stop valve.
Detailed Description
The present utility model is not limited by the following examples, and specific embodiments can be determined according to the technical scheme and practical situations of the present utility model.
In the present utility model, for convenience of description, the description of the relative positional relationship of each component is described according to the layout manner of fig. 1 of the specification, for example: the positional relationship of front, rear, upper, lower, left, right, etc. is determined in accordance with the layout direction of fig. 1 of the specification.
The utility model is further described below with reference to examples and figures:
as shown in figure 1, the acetylene concentration tank safe operation device comprises a concentration tank 1 and a first concentration pump 2, wherein an inlet at the upper part of the concentration tank 1 is fixedly communicated with a carbide slag slurry liquid inlet pipeline 7, an outlet at the upper part of the concentration tank 1 is fixedly communicated with a supernatant liquid outlet pipeline 8, a first treatment pipeline 9 is fixedly communicated between a first outlet at the bottom of the concentration tank 1 and an inlet of the first concentration pump 2, a second treatment pipeline 10 is fixedly communicated with an outlet of the first concentration pump 2, a water accumulation pit is arranged below the corresponding first concentration pump 2, a submersible pump 5 and a remote liquid level meter 6 are fixedly arranged in the water accumulation pit, a liquid accumulation recovery pipeline 15 is fixedly communicated between the submersible pump 5 and the inlet at the top of the concentration tank 1, and the submersible pump 5 and the remote liquid level meter 6 are electrically connected.
According to the utility model, the submersible pump 5 and the remote liquid level meter 6 are arranged in the water accumulation pit, meanwhile, the submersible pump 5 and the remote liquid level meter 6 realize interlocking control, so that the problem of damage to the pump body of the first concentration pump 2 caused by leakage of a large amount of thick liquid due to leakage of the first concentration pump 2 can be solved in the first time, when the first concentration pump 2 leaks, a large amount of accumulated water is accumulated in the water accumulation pit within a certain time, the liquid level of the water accumulation pit is monitored by the remote liquid level meter 6, and when the liquid level of the remote liquid level meter 6 in the water accumulation pit reaches a certain height, the interlocking is triggered, the submersible pump 5 is automatically started, accumulated water in the water accumulation pit is timely pumped away, safety production accidents are avoided, and the safety coefficient of the device is improved.
The acetylene concentration tank safe operation device can be further optimized or/and improved according to actual needs:
as shown in fig. 1, the device further comprises a second concentration pump 3, a third treatment pipeline 11 is fixedly communicated between a second outlet at the bottom of the concentration tank 1 and an inlet of the second concentration pump 3, and a fourth treatment pipeline 12 is fixedly communicated between an outlet of the second concentration pump 3 and the second treatment pipeline 10. In the use process, when the first concentration pump 2 fails and is damaged, the second concentration pump 3 can be switched in time and replaced or repaired in time.
As shown in fig. 1, the device further comprises a third concentration pump 4, a fifth treatment pipeline 13 is fixedly communicated between a third outlet at the bottom of the concentration tank 1 and an inlet of the third concentration pump 4, and a sixth treatment pipeline 14 is fixedly communicated between an outlet of the third concentration pump 4 and the fourth treatment pipeline 12. In the use process, the third concentration pump 4 is used as a standby pump and can be switched at any time.
As shown in fig. 1, the first, third and fifth treatment lines 9, 11 and 13 are respectively and fixedly provided with a flow regulating valve 16 and a stop valve 17, the sixth treatment line 14 is fixedly provided with a stop valve 17, the fourth treatment line 12 between the sixth treatment line 14 and the second concentration pump 3 is fixedly provided with a stop valve 17, and the second treatment line 10 between the fourth treatment line 12 and the first concentration pump 2 is fixedly provided with a stop valve 17.
The technical characteristics form the optimal embodiment of the utility model, have stronger adaptability and optimal implementation effect, and can increase or decrease unnecessary technical characteristics according to actual needs so as to meet the requirements of different situations.
The use process of the best embodiment of the utility model comprises the following steps: the carbide slag slurry is sent to a concentration tank 1 through a carbide slag slurry liquid inlet pipeline 7, sedimentation separation is carried out in the concentration tank 1, supernatant is sent to a supernatant liquid pond through a supernatant liquid outlet pipeline 8 for treatment, and concentrated liquid at the bottom is sent to a subsequent filter pressing process for treatment through a first treatment pipeline 9 and a second treatment pipeline 10.
When the liquid level of the remote transmission liquid level meter 6 in the water accumulation pit reaches a certain height, the remote transmission liquid level meter 6 is interlocked with the submersible pump 5 to be automatically started, accumulated water in the water accumulation pit is sent into the concentration tank 1 by the submersible pump 5, and when the liquid level of the remote transmission liquid level meter 6 is reduced to a certain height, the submersible pump 5 is automatically stopped.
Claims (4)
1. The utility model provides an acetylene concentration pond safe operation device, its characterized in that includes concentration pond and first concentration pump, concentration pond upper portion import fixed intercommunication has carbide slag thick liquid feed liquor pipeline, concentration pond upper portion export fixed intercommunication has supernatant drain line, fixed intercommunication has first processing pipeline between concentration pond bottom first export and the first concentration pump import, fixed intercommunication of first concentration pump export has the second processing pipeline, be provided with the water accumulation pit corresponding first concentration pump below, fixed mounting has immersible pump and teletransmission level gauge in the water accumulation pit, fixed intercommunication has the hydrops recovery pipeline between immersible pump and the concentration pond top import, electric connection between immersible pump and the teletransmission level gauge.
2. The acetylene concentration tank safety operation device according to claim 1, further comprising a second concentration pump, wherein a third treatment pipeline is fixedly communicated between a second outlet at the bottom of the concentration tank and an inlet of the second concentration pump, and a fourth treatment pipeline is fixedly communicated between an outlet of the second concentration pump and the second treatment pipeline.
3. The acetylene concentration tank safe operation device according to claim 1 or 2, further comprising a third concentration pump, wherein a fifth treatment pipeline is fixedly communicated between a third outlet at the bottom of the concentration tank and an inlet of the third concentration pump, and a sixth treatment pipeline is fixedly communicated between an outlet of the third concentration pump and the fourth treatment pipeline.
4. The acetylene concentration tank safety operation device according to claim 3, wherein the first treatment pipeline, the third treatment pipeline and the fifth treatment pipeline are respectively fixedly provided with a flow regulating valve and a stop valve, the sixth treatment pipeline is fixedly provided with a stop valve, the fourth treatment pipeline between the sixth treatment pipeline and the second concentration pump is fixedly provided with a stop valve, and the second treatment pipeline between the fourth treatment pipeline and the first concentration pump is fixedly provided with a stop valve.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN202321289516.3U CN219709425U (en) | 2023-05-25 | 2023-05-25 | Acetylene concentration tank safe operation device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202321289516.3U CN219709425U (en) | 2023-05-25 | 2023-05-25 | Acetylene concentration tank safe operation device |
Publications (1)
Publication Number | Publication Date |
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CN219709425U true CN219709425U (en) | 2023-09-19 |
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Family Applications (1)
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CN202321289516.3U Active CN219709425U (en) | 2023-05-25 | 2023-05-25 | Acetylene concentration tank safe operation device |
Country Status (1)
Country | Link |
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CN (1) | CN219709425U (en) |
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2023
- 2023-05-25 CN CN202321289516.3U patent/CN219709425U/en active Active
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