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CN207703297U - High viscosity liquid level emasuring device containing solvent - Google Patents

High viscosity liquid level emasuring device containing solvent Download PDF

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Publication number
CN207703297U
CN207703297U CN201820084283.6U CN201820084283U CN207703297U CN 207703297 U CN207703297 U CN 207703297U CN 201820084283 U CN201820084283 U CN 201820084283U CN 207703297 U CN207703297 U CN 207703297U
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China
Prior art keywords
liquid level
level gauge
pipeline
differential pressure
connect
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Active
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CN201820084283.6U
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Chinese (zh)
Inventor
陈晓霞
于星玉
廉燕
赵代利
郭希武
王恩峰
魏锋
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QILONG CHEMICAL CO Ltd SHANDONG
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QILONG CHEMICAL CO Ltd SHANDONG
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Priority to CN201820084283.6U priority Critical patent/CN207703297U/en
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Abstract

The utility model is related to a kind of liquid level emasuring devices, more particularly, to a kind of high viscosity liquid level emasuring device containing solvent.The utility model provides circulation flushing function by the way that condenser is arranged, for liquid level gauge, realizes the level gauging of the high-viscosity material with solvent.The utility model includes reaction kettle, liquid level gauge, differential pressure transmitter, the reaction kettle upper orifice is connect by the first pipeline with liquid level gauge top, reaction kettle lower nozzle is connect by the second pipeline with liquid level gauge lower part, described differential pressure transmitter one end is connect with liquid level gauge top nozzle, the differential pressure transmitter other end is connect with liquid level gauge bottom nozzle, first pipeline tilts down in the horizontal direction, liquid level gauge is located at the first pipeline compared with downside, condenser and the first valve switch are connected on first pipeline, and the second valve switch is set on the second pipeline.

Description

High viscosity liquid level emasuring device containing solvent
Technical field
The utility model is related to a kind of liquid level emasuring devices, more particularly, to a kind of high viscosity level gauging containing solvent Device.
Background technology
Liquid level gauge is widely used in various pilot plant units, is installed in liquid tank or is carried out in reaction vessel liquid level Observation.But highly viscous material, because its viscosity is high, poor fluidity is easy blocking pipeline, is especially using differential pressure type When liquid level gauge, high-viscosity material enters in liquid level gauge, is attached to liquid level gauge inner surface, and liquid level is made to be difficult to measure, however uses and be situated between Enter formula liquid level gauge be easy because stirring problem hold caused by disturbance cause to measure it is unstable.
Utility model content
The purpose of this utility model is that proposing a kind of high viscosity liquid level emasuring device containing solvent, condensed by being arranged Device provides circulation flushing function for liquid level gauge, realizes the level gauging of the high-viscosity material with solvent.
The utility model includes reaction kettle, liquid level gauge, differential pressure transmitter, and the reaction kettle upper orifice passes through the first pipeline It is connect with liquid level gauge top, reaction kettle lower nozzle is connect by the second pipeline with liquid level gauge lower part, the differential pressure transmitter one End is connect with liquid level gauge top nozzle, and the differential pressure transmitter other end is connect with liquid level gauge bottom nozzle, and first pipeline is along water Square to tilting down, liquid level gauge is located at the first pipeline compared with downside, connection condenser and the first valve switch on the first pipeline, the Second valve switch is set on two pipelines.
Reactor bottom is the high viscosity liquid phase with solvent, and top is gas phase, under the action of condenser, vapor phase solvent It liquefies within the condenser, since the first pipeline is in tilted layout, the vapor phase solvent after liquefaction flows into liquid level gauge, liquid certainly along the first pipeline Liquid level is higher than liquid level in reaction kettle in the meter of position, and according to law of connected vessels, liquid level is calculated as keeping liquid level constant, by liquid level Meter bottom liquid phases are expelled to reaction kettle, and since vapor phase solvent viscosity is small, the liquid phase viscosity after liquefaction is low, to liquid phase in liquid level gauge Diluting effect is played, and then realizes the level gauging of high-viscosity material.
Described, the angle that the first pipeline tilts down in the horizontal direction is 2-5 degree.
It is flowed into liquid level gauge convenient for the gas phase after liquefaction.
Described, liquid level gauge top nozzle, liquid level gauge bottom nozzle are respectively provided with triple valve, the both ends of the differential pressure transmitter It is connected respectively with corresponding triple valve valve port.
When normal measurement, the pressure difference for the differential pressure transmitter detection differential pressure transmitter both sides being connected to triple valve valve port is used for The output of liquid level data;When liquid level gauge is cleaned and purged, turns off triple valve valve port, the first valve being connect with differential pressure transmitter and open It closes, the second valve switch, the valve port being not turned off by triple valve is cleaned and purged to liquid level gauge.
The utility model has the beneficial effects that:
(1) the high viscosity liquid level emasuring device described in the utility model containing solvent is provided with condenser and the first pipe Road makes the vapor phase solvent on reaction kettle top liquefy and flows automatically into liquid level gauge, plays circulation flushing function to liquid level gauge, and then realize The level gauging of high-viscosity material;
(2) the high viscosity liquid level emasuring device described in the utility model containing solvent is provided with the first valve switch, Two valve switch, triple valve realize the dredging and cleaning of liquid level gauge by turning off corresponding valve port.
Description of the drawings
Fig. 1 is a kind of example structure schematic diagram;
In figure:1, reaction kettle;2, liquid level gauge;3, differential pressure transmitter;4, the first pipeline;5, the second pipeline;6, condenser;7、 First valve switch;8, the second valve switch;9, triple valve.
Specific implementation mode
The utility model is described in further detail below in conjunction with the accompanying drawings.
As shown in Figure 1, the high viscosity liquid level emasuring device described in the utility model containing solvent, including reaction kettle 1, liquid Position meter 2, differential pressure transmitter 3,1 upper orifice of the reaction kettle is connect by the first pipeline 4 with 2 top of liquid level gauge, under reaction kettle 1 Portion's nozzle is connect by the second pipeline 5 with 2 lower part of liquid level gauge, and 3 one end of the differential pressure transmitter connects with 2 top nozzle of liquid level gauge It connects, 3 other end of differential pressure transmitter is connect with 2 bottom nozzle of liquid level gauge, and first pipeline 4 tilts down in the horizontal direction, liquid Position meter 2 is located at the first pipeline 4 compared with downside, connection condenser 6 and the first valve switch 7 on the first pipeline 4, is set on the second pipeline 5 Set the second valve switch 8;The angle that first pipeline 4 tilts down in the horizontal direction is 3 degree;2 head tube of the liquid level gauge Mouthful, 2 bottom nozzle of liquid level gauge be respectively provided with triple valve 9, the both ends of the differential pressure transmitter 3 respectively with 9 valve port of corresponding triple valve Connection.
1 bottom of reaction kettle is the high viscosity liquid phase with solvent, and top is gas phase, and under the action of condenser 6, gas phase is molten Agent is liquefied in condenser 6, and since the first pipeline 4 is in tilted layout, the vapor phase solvent after liquefaction flows into liquid level certainly along the first pipeline 4 In meter 2, liquid level is higher than liquid level in reaction kettle 1 in liquid level gauge 2, and according to law of connected vessels, liquid level gauge 2 is to keep liquid level It is constant, 2 bottom liquid phases of liquid level gauge are expelled to reaction kettle 1, since vapor phase solvent viscosity is small, the liquid phase viscosity after liquefaction is low, Diluting effect is played to liquid phase in liquid level gauge 2, with the continuous liquefaction of vapor phase solvent, liquid concentration is diluted in liquid level gauge 2, will not It is attached on liquid level gauge inner wall, and then realizes the level gauging of high-viscosity material;When normal measurement, it is connected to 9 valve port of triple valve Differential pressure transmitter 3 detect the pressure differences of differential pressure transmitter 3 both sides, be used for the output of liquid level data;It cleans and purges in liquid level gauge 2 When, 9 valve port of triple valve, the first valve switch 7, the second valve switch 8 being connect with differential pressure transmitter 3 are turned off, triple valve 9 is passed through Valve port solvent washing or the nitrogen purging being not turned off.
The utility model use process is as follows described:When measurement, condenser, vapor phase solvent liquid within the condenser are opened Change, make the dilution of liquid phase in liquid level gauge, complete liquid level gauge circulation flushing, liquid level data is exported using differential pressure transmitter, realizes high The level gauging of viscous material;When liquid level gauge is cleaned and purged, triple valve valve port, the first valve being connect with differential pressure transmitter are turned off Door switch, the second valve switch, the valve port solvent washing being not turned off by triple valve or nitrogen purging.
Certainly, the above is only the preferred embodiment of the utility model, be should not be construed as limiting new to this practicality The scope of embodiments of type.The utility model is also not limited to the example above, and those skilled in the art are in this reality With all the changes and improvements etc. made in novel essential scope, the patent covering scope of the utility model should all be belonged to It is interior.

Claims (3)

1. a kind of high viscosity liquid level emasuring device containing solvent, including reaction kettle (1), liquid level gauge (2), differential pressure transmitter (3), Reaction kettle (1) upper orifice is connect by the first pipeline (4) with liquid level gauge (2) top, and reaction kettle (1) lower nozzle passes through Second pipeline (5) is connect with liquid level gauge (2) lower part, and described differential pressure transmitter (3) one end is connect with liquid level gauge (2) top nozzle, Differential pressure transmitter (3) other end is connect with liquid level gauge (2) bottom nozzle, it is characterised in that:First pipeline (4) is along level side To tilting down, liquid level gauge (2) is located at the first pipeline (4) compared with downside, connection condenser (6) and the first valve on the first pipeline (4) The second valve switch (8) is arranged on the second pipeline (5) in door switch (7).
2. the high viscosity liquid level emasuring device according to claim 1 containing solvent, it is characterised in that:First pipeline (4) angle tilted down in the horizontal direction is 2-5 degree.
3. the high viscosity liquid level emasuring device according to claim 1 containing solvent, it is characterised in that:The liquid level gauge (2) top nozzle, liquid level gauge (2) bottom nozzle are respectively provided with triple valve (9), the both ends of the differential pressure transmitter (3) respectively with it is right Triple valve (9) valve port connection answered.
CN201820084283.6U 2018-01-18 2018-01-18 High viscosity liquid level emasuring device containing solvent Active CN207703297U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820084283.6U CN207703297U (en) 2018-01-18 2018-01-18 High viscosity liquid level emasuring device containing solvent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820084283.6U CN207703297U (en) 2018-01-18 2018-01-18 High viscosity liquid level emasuring device containing solvent

Publications (1)

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CN207703297U true CN207703297U (en) 2018-08-07

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CN (1) CN207703297U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110712902A (en) * 2019-11-19 2020-01-21 乐山市益洁环保科技有限公司 Kitchen garbage truck
GB2585374A (en) * 2019-07-04 2021-01-13 Linde Ag Measurement instrumentation for a process vessel and process vessel system
CN113588040A (en) * 2021-07-30 2021-11-02 中国石油天然气股份有限公司 Pressure measuring device, liquid level measuring system, interlocking protection system and method
CN115979374A (en) * 2022-12-22 2023-04-18 四川惠科达仪表制造有限公司 A differential pressure measuring liquid level gauge and measuring system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2585374A (en) * 2019-07-04 2021-01-13 Linde Ag Measurement instrumentation for a process vessel and process vessel system
CN110712902A (en) * 2019-11-19 2020-01-21 乐山市益洁环保科技有限公司 Kitchen garbage truck
CN113588040A (en) * 2021-07-30 2021-11-02 中国石油天然气股份有限公司 Pressure measuring device, liquid level measuring system, interlocking protection system and method
CN113588040B (en) * 2021-07-30 2024-04-26 中国石油天然气股份有限公司 A pressure taking device, liquid level measurement system, interlocking protection system and method
CN115979374A (en) * 2022-12-22 2023-04-18 四川惠科达仪表制造有限公司 A differential pressure measuring liquid level gauge and measuring system

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