CN205593597U - Slurry tank liquid level measurement device - Google Patents
Slurry tank liquid level measurement device Download PDFInfo
- Publication number
- CN205593597U CN205593597U CN201620240460.6U CN201620240460U CN205593597U CN 205593597 U CN205593597 U CN 205593597U CN 201620240460 U CN201620240460 U CN 201620240460U CN 205593597 U CN205593597 U CN 205593597U
- Authority
- CN
- China
- Prior art keywords
- flange
- slurry tank
- liquid level
- tank liquid
- emasuring device
- 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
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 51
- 239000002002 slurry Substances 0.000 title claims abstract description 38
- 238000005259 measurement Methods 0.000 title abstract description 8
- 239000012530 fluid Substances 0.000 claims description 14
- 238000005406 washing Methods 0.000 claims description 13
- 238000010521 absorption reaction Methods 0.000 claims description 9
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 7
- 230000000903 blocking effect Effects 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000006477 desulfuration reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 230000003009 desulfurizing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model relates to a slurry tank liquid level measurement device, the device and slurry tank are connected, include: the liquid taking tube way, its entry sets up for the slurry tank slope to be the fixed first flange of 42~45, liquid taking tube way export with the slurry tank horizontal direction, door once, the second flange fix to its one end, first flange and the 2nd flange joint, once door one end is through first flange, second flange and liquid taking tube way exit linkage, and once the third flange is fixed to the door other end, the liquid level changer, the fourth flange is fixed to its one end, wash the ring, its one end is passed through the fourth flange and is connected with liquid level changer one end, washes the ring other end and passes through the third flange and be connected third flange and fourth flange joint with an other end once. The beneficial effect of the utility model: the slope of liquid taking tube way sets up, the extension thick liquid wall built -up time, liquid level changer leakproofness is good, and accuracy is high, the reliability is high, the scope is big, it accessible time washs sedimentary thick liquid to wash the ring, the exhaust -valve can further reduce the jam.
Description
Technical field
This utility model relates to technical field of desulfurization, is specifically related to a kind of slurry tank liquid level emasuring device.
Background technology
In sulfur removal technology, in absorption tower, liquid level of slurry is the important operational factor of wet method fume desulfurizing system,
Absorbing tower liquid-level control planning is to desulphurization system safety and economic operation.If liquid level of slurry is too high, can cause
Absorption tower serosity overflow；If liquid level of slurry is too low, then can reduce desulfuration efficiency.Therefore, how to measure
In absorption tower, liquid level of slurry is the steps necessary of conservative control liquid level of slurry.
The measuring method currently used is:
1, using differential pressure examination diaphragm pressure transmitter to measure, but serosity easily blocks pipeline, liquid level is normal
The measurement time is relatively short；
2, use radar level timing, its easy fouling of guided wave bar, affect echo；
3, using capacitance level gauge, when having stirring or slip fluctuation is big, electric capacity bar is easily broken off,
Technique can not be effectively instructed to produce.
Utility model content
For weak point present in the problems referred to above, this utility model provides one can accurately measure absorption
Liquid level of slurry the slurry tank liquid level emasuring device of blocking can be prevented effectively from tower.
For achieving the above object, this utility model provides a kind of slurry tank liquid level emasuring device, described serosity
Case liquid level emasuring device is connected with the slurry tank bottom absorption tower, and described slurry tank liquid level emasuring device includes:
Liquid flowing tube road, its entrance relative to described slurry tank sidewall slope arrange, and with described slurry tank
Horizontal direction be 42 °～45 °, the outlet on described liquid flowing tube road is fixed with the first flange；
Once door, it is fixing even that its one end is fixed with the second flange, described first flange and described second flange
Connecing, one end of described once door is by described first flange, described second flange and described liquid flowing tube road
Outlet connects, and the other end of described once door is fixed with three-flange；
Fluid level transmitter, its one end is fixed with the 4th flange；
Washing ring, its one end is connected with one end of described fluid level transmitter by described 4th flange, described
The other end of washing ring is connected with the other end of described once door by described three-flange, described 3rd method
Blue and described 4th flange is fixing to be connected.
Improving further as this utility model, also include exhaust-valve, one end of described exhaust-valve is with described
Washing ring connects.
Improve further as this utility model, also include emptying pipeline, described emptying pipeline and described row
The other end of empty valve connects.
Improving further as this utility model, described first flange and described second flange are solid by bolt
Fixed connection.
Improve further as this utility model, between described first flange and described second flange, be provided with method
Blue sealing gasket.
Improving further as this utility model, described three-flange and described 4th flange are solid by bolt
Fixed connection.
Improve further as this utility model, between described three-flange and described 4th flange, be provided with method
Blue sealing gasket.
The beneficial effects of the utility model are:
1, liquid flowing tube road is obliquely installed, extends the serosity wall built-up time, effectively reduce blocking；
2, fluid level transmitter is completely isolated with serosity, good airproof performance, accuracy of measurement is higher, reliability more
High；
3, the measurement scope of fluid level transmitter is relatively big, is not limited by absorption tower height；
4, the serosity being deposited on fluid level transmitter can be carried out by the setting of washing ring in time；
5, exhaust-valve is used can to reduce pipeline blockage further.
Accompanying drawing explanation
Fig. 1 is the structural representation of this utility model a kind of slurry tank liquid level emasuring device.
In figure:
1, washing ring；2, flange gasket；3, fluid level transmitter；4, bolt；5, exhaust-valve；6、
Once door；71, the first flange；72, the second flange；73, three-flange；74, the 4th flange.
Detailed description of the invention
As it is shown in figure 1, a kind of slurry tank liquid level emasuring device of this utility model embodiment, this slurry tank
Liquid level emasuring device is connected with the slurry tank bottom absorption tower.Slurry tank liquid level emasuring device includes liquid flowing tube
Road, once door 6, washing ring 1 and fluid level transmitter 3.Wherein, the entrance on liquid flowing tube road is relative to serosity
The sidewall slope of case is arranged, and is 42 °～45 ° with the horizontal direction of slurry tank, and the outlet on liquid flowing tube road is solid
Surely there is the first flange 71.Once one end of door 6 is fixed with the second flange 72, the first flange 71 and second
Flange 72 connects by bolt 4 is fixing, is provided with flange seal between the first flange 71 and the second flange 72
Pad 2.Once one end of door 6 is connected with the outlet on liquid flowing tube road by first flange the 71, second flange 72,
Once the other end of door 6 is fixed with three-flange 73.One end of fluid level transmitter 3 is fixed with the 4th flange
74.One end of washing ring 1 is connected with one end of fluid level transmitter 3 by the 4th flange 74, washing ring 1
The other end be connected with the other end of once door 6 by three-flange 73, three-flange 73 and the 4th method
Blue 74 connect by bolt 4 is fixing, are provided with flange gasket between three-flange 73 and the 4th flange 74
2。
Further, in order to prevent blocking, also include exhaust-valve 5, one end of exhaust-valve 5 and washing ring 1
Connecting, the other end of exhaust-valve 5 is connected with emptying pipeline.
Time specifically used, liquid flowing tube road arranged relative to absorption tower sidewall slope, extends the extension of serosity
The wall time, effectively reduce pipeline blockage；Fluid level transmitter is completely isolated with serosity, better tightness,
Accuracy of measurement is higher, reliability is higher, and meanwhile, the measurement scope of fluid level transmitter is relatively big, is not inhaled
Receive the restriction of tower height degree；Owing to serosity has viscosity, liquid level can be gathered in through deposition after a while and become
Sending at device diaphragm, can affect measurement effect, the setting of washing ring can be in time to being deposited on fluid level transmitter
Serosity be carried out；Use exhaust-valve and emptying pipeline can clear up slurry plugs in time, reduce further
Pipeline blockage.
The foregoing is only preferred embodiment of the present utility model, be not limited to this utility model,
For a person skilled in the art, this utility model can have various modifications and variations.All in this reality
Within novel spirit and principle, any modification, equivalent substitution and improvement etc. made, all should comprise
Within protection domain of the present utility model.
Claims (7)
1. a slurry tank liquid level emasuring device, it is characterised in that described slurry tank liquid level emasuring device is connected with the slurry tank bottom absorption tower, described slurry tank liquid level emasuring device includes:
Liquid flowing tube road, its entrance is arranged relative to the sidewall slope of described slurry tank, and is 42 °～45 ° with the horizontal direction of described slurry tank, and the outlet on described liquid flowing tube road is fixed with the first flange (71)；
Once door (6), its one end is fixed with the second flange (72), described first flange (71) and the fixing connection of described second flange (72), one end of described once door (6) is connected with the outlet on described liquid flowing tube road by described first flange (71), described second flange (72), and the other end of described once door (6) is fixed with three-flange (73)；
Fluid level transmitter (3), its one end is fixed with the 4th flange (74)；
Washing ring (1), its one end is connected with one end of described fluid level transmitter (3) by described 4th flange (74), the other end of described washing ring (1) is connected with the other end of described once door (6) by described three-flange (73), described three-flange (73) and the fixing connection of described 4th flange (74).
Slurry tank liquid level emasuring device the most according to claim 1, it is characterised in that also include that exhaust-valve (5), one end of described exhaust-valve (5) are connected with described washing ring (1).
Slurry tank liquid level emasuring device the most according to claim 2, it is characterised in that also including emptying pipeline, described emptying pipeline is connected with the other end of described exhaust-valve (5).
Slurry tank liquid level emasuring device the most according to claim 1, it is characterised in that described first flange (71) and described second flange (72) connect by bolt (4) is fixing.
Slurry tank liquid level emasuring device the most according to claim 4, it is characterised in that be provided with flange gasket (2) between described first flange (71) and described second flange (72).
Slurry tank liquid level emasuring device the most according to claim 1, it is characterised in that described three-flange (73) and described 4th flange (74) connect by bolt (4) is fixing.
Slurry tank liquid level emasuring device the most according to claim 6, it is characterised in that be provided with flange gasket (2) between described three-flange (73) and described 4th flange (74).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620240460.6U CN205593597U (en) | 2016-03-25 | 2016-03-25 | Slurry tank liquid level measurement device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620240460.6U CN205593597U (en) | 2016-03-25 | 2016-03-25 | Slurry tank liquid level measurement device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205593597U true CN205593597U (en) | 2016-09-21 |
Family
ID=56930079
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620240460.6U Expired - Fee Related CN205593597U (en) | 2016-03-25 | 2016-03-25 | Slurry tank liquid level measurement device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205593597U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106768163A (en) * | 2016-12-28 | 2017-05-31 | 安徽六国化工股份有限公司 | The liquid level detection device and the detection method using the device of slag bath are dragged for for gasifying |
| CN109442206A (en) * | 2018-12-21 | 2019-03-08 | 张家港富瑞深冷科技有限公司 | A kind of vacuum insulation deep cooling pressure vessel |
-
2016
- 2016-03-25 CN CN201620240460.6U patent/CN205593597U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106768163A (en) * | 2016-12-28 | 2017-05-31 | 安徽六国化工股份有限公司 | The liquid level detection device and the detection method using the device of slag bath are dragged for for gasifying |
| CN109442206A (en) * | 2018-12-21 | 2019-03-08 | 张家港富瑞深冷科技有限公司 | A kind of vacuum insulation deep cooling pressure vessel |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205562498U (en) | Sealed pH meter interface | |
| CN205593597U (en) | Slurry tank liquid level measurement device | |
| CN108333078A (en) | Fully-automatic on-line sampling formula slurry density measurement device | |
| CN208187625U (en) | Anti-blocking device for pressure measurement suitable for wet flue gas pressure measurement | |
| CN201852720U (en) | Closed liquid sampler | |
| CN204831860U (en) | Associated gas hydrogen sulfide sampling device | |
| CN205593596U (en) | Desulfurization absorption tower liquid level measurement device | |
| CN206945475U (en) | Wet flue gas desulfurization tower serum density and pH measurement apparatus | |
| CN204816195U (en) | Desulfurizing tower with formula of input liquid level measurement ware | |
| CN103630578A (en) | pH on-line measurement method and device of desulfurizing absorption tower | |
| CN208109629U (en) | Fully-automatic on-line sampling formula slurry density measurement device | |
| CN207779502U (en) | With the device for rinsing double flange diaphragm differential pressure transmitters measurement viscous medium liquid levels | |
| CN203274845U (en) | Liquid level detection device for slurry | |
| CN204085644U (en) | A kind of flow calibrating device | |
| CN205593598U (en) | Slurry tank's multistage liquid level measurement device | |
| CN205593595U (en) | Water tank liquid level measurement device | |
| CN108593196A (en) | A kind of anti-blocking device for pressure measurement suitable for wet flue gas pressure measurement | |
| CN205861277U (en) | A kind of instrument pressure spacing container | |
| CN203772778U (en) | PH online measuring device for desulfurization absorption tower | |
| CN209656494U (en) | Slurry density measurement device in a kind of desulfurizing tower suitable for calcium method desulfurization | |
| CN204649667U (en) | The measurement mechanism of slurry pH value in absorption tower | |
| CN208594906U (en) | Normal pressure oil wellhead chemical agent adding device | |
| CN205535896U (en) | Flue gas liquid seal device based on S type pipeline | |
| CN211783735U (en) | Liquid level measuring device of wet desulphurization tower | |
| CN205593696U (en) | Differential pressure measuring device |
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: 20160921 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |