CN211528168U - Long-life high-temperature jet type liquid-solid dual-phase flow erosion corrosion experimental device - Google Patents
Long-life high-temperature jet type liquid-solid dual-phase flow erosion corrosion experimental device Download PDFInfo
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- CN211528168U CN211528168U CN201922081498.XU CN201922081498U CN211528168U CN 211528168 U CN211528168 U CN 211528168U CN 201922081498 U CN201922081498 U CN 201922081498U CN 211528168 U CN211528168 U CN 211528168U
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- 230000007797 corrosion Effects 0.000 title claims abstract description 29
- 238000005260 corrosion Methods 0.000 title claims abstract description 29
- 230000003628 erosive effect Effects 0.000 title claims abstract description 25
- 239000007787 solid Substances 0.000 title claims abstract description 18
- 239000002002 slurry Substances 0.000 claims abstract description 30
- 238000010438 heat treatment Methods 0.000 claims abstract description 28
- 238000002347 injection Methods 0.000 claims abstract description 26
- 239000007924 injection Substances 0.000 claims abstract description 26
- 238000010992 reflux Methods 0.000 claims abstract description 14
- 239000007921 spray Substances 0.000 claims abstract description 14
- 239000000523 sample Substances 0.000 claims description 15
- 238000003756 stirring Methods 0.000 claims description 12
- 230000005514 two-phase flow Effects 0.000 claims description 9
- 238000007599 discharging Methods 0.000 claims description 8
- 238000002474 experimental method Methods 0.000 claims description 7
- 239000000498 cooling water Substances 0.000 claims description 5
- 238000001816 cooling Methods 0.000 abstract description 12
- 239000012530 fluid Substances 0.000 abstract description 11
- 239000007788 liquid Substances 0.000 abstract description 5
- 238000009510 drug design Methods 0.000 abstract description 2
- 239000012071 phase Substances 0.000 description 5
- 238000005507 spraying Methods 0.000 description 5
- 239000000919 ceramic Substances 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 230000005518 electrochemistry Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000002035 prolonged effect Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000002848 electrochemical method Methods 0.000 description 1
- 230000003028 elevating effect Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000010349 pulsation Effects 0.000 description 1
- 238000009991 scouring Methods 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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Abstract
The utility model relates to a erode corrosion device specifically is a long-life high temperature jet type liquid solid diphase flow erode corrosion experimental apparatus, solves the problem that equipment service cycle is short under the higher temperature among the prior art. The input end of the motor is connected with the frequency converter, the output end of the motor is provided with a cam pump, the outlet of the cam pump is connected with the inlet of the three-stage heating system through a pipeline, the outlet of the three-stage heating system extends into the injection chamber through a pipeline, the pipeline is provided with an electromagnetic flowmeter, one end of the pipeline extending into the injection chamber is provided with a nozzle, and one side of the pipeline part positioned at the inlet at the top of the injection chamber is connected with the lifting screw rod; the bottom outlet of the spray chamber is connected with one end of a reflux cooler through a pipeline, the other end of the reflux cooler arranged in the slurry tank extends to the lower part in the slurry tank, and the slurry tank is communicated with the inlet of the cam pump through a pipeline. The utility model discloses a rational design heating and cooling position, separately hot-fluid and driving pump, make the stable labour in service of injection formula erosion corrosion experimental apparatus realization phase.
Description
Technical Field
The utility model relates to an erosion corrosion device, in particular to a long-life high-temperature jet type liquid-solid dual-phase flow erosion corrosion experimental device.
Background
In the prior art, the jet erosion corrosion experimental device is used in the multiphase flow erosion corrosion research, but is mostly applied to the normal temperature condition. Erosion corrosion under different temperatures is also often listed in the research scope, but because hot-fluid can produce great damage to it through the driving pump, the research under the higher temperature often designs into shorter experimental time, even so, experimental apparatus's in service life also shortens greatly. Therefore, a unique heating and cooling system is designed, high-temperature fluid is prevented from passing through a driving pump while high-temperature injection is realized, and the service life of the injection type erosion corrosion experiment device is greatly prolonged.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a long-life high temperature sprays formula liquid solid diphase flow erosion corrosion experimental apparatus solves among the prior art because the hot-fluid passes through the driving pump and makes the problem that experimental apparatus is in service life-span shortens by a wide margin.
The technical scheme of the utility model is that:
a long-life high-temperature injection type liquid-solid two-phase flow erosion corrosion experimental device is characterized in that an input end of a motor is connected with a frequency converter, an output end of the motor is provided with a cam pump, an outlet of the cam pump is connected with an inlet of a three-stage heating system through a pipeline, an outlet of the three-stage heating system extends into an injection chamber through the pipeline, the pipeline is provided with an electromagnetic flowmeter, one end of the pipeline, which extends into the injection chamber, is provided with a nozzle, and one side of a pipeline part, which is positioned at an inlet at the top of; the bottom outlet of the spray chamber is connected with one end of a reflux cooler through a pipeline, the other end of the reflux cooler arranged in the slurry tank extends to the lower part in the slurry tank, and the slurry tank is communicated with the inlet of the cam pump through a pipeline.
The long-life high-temperature jet type liquid-solid two-phase flow erosion corrosion experimental device is characterized in that a cooling water pipe is installed at the lower part of the side face of a slurry tank, the upper part of the side face of the slurry tank is connected with an inlet of an overflow cooler through a pipeline, and an outlet of the overflow cooler is communicated with the lower part of the side face of a jet chamber through an overflow pipe.
The long-life high-temperature injection type liquid-solid two-phase flow erosion corrosion experiment device is characterized in that a thermocouple I is inserted into an injection chamber, an attack angle measurer, a nozzle, a reference electrode, an auxiliary electrode, a working electrode and an acidimeter probe are arranged in the injection chamber, the attack angle measurer corresponds to the working electrode, the reference electrode, the auxiliary electrode and the working electrode are connected to an electrochemical workstation through leads, the electrochemical workstation is connected with a computer, and the acidimeter probe is connected to an acidimeter through leads.
The long-life high-temperature jet type liquid-solid dual-phase flow erosion corrosion experiment device is characterized in that a thermocouple II is inserted into a slurry tank, the slurry tank is communicated with an inlet of a stirring and discharging pump through a pipeline, an outlet of the stirring and discharging pump is divided into two branches, one branch is communicated with the slurry tank, a ball valve II is arranged on the branch, and a ball valve I is arranged on the other branch.
The long-life high-temperature jet type liquid-solid two-phase flow erosion corrosion experimental device is characterized in that a ball valve III is arranged on a pipeline, wherein the bottom outlet of the jet chamber is connected with a reflux cooler.
The design idea of the utility model is that: the utility model discloses try to make the driving pump avoid the erosion and corrosion of hot-fluid to improve the long-term stable in service of system under the high temperature erosion and corrosion condition.
The utility model has the advantages of as follows and beneficial effect:
1. the utility model discloses a heating system installs the play water end after the driving pump, has avoided high temperature fluid to pass through the driving pump, has prolonged the life of driving pump by a wide margin, realizes the injection of hot-fluid. Therefore, the hot fluid can realize the jet type erosion corrosion test of the high-temperature hot fluid without passing through a driving pump.
2. The utility model discloses a cooling system installs after the spray chamber, adopts at the refrigerated design of spray chamber rear end, has guaranteed the realization that the high temperature flows the injection experiment, realizes the cooling of backward flow liquid, and the liquid of having guaranteed the backward flow driving pump simultaneously is in the lower temperature, and the protection driving pump is avoided high temperature erosion and corrosion. The cooling system adopts a way of cooling by a return pipe and an overflow pipe in a shunting way so as to improve the cooling efficiency.
3. The utility model discloses a heating system adopts multistage heating, multistage accuse temperature, realizes the accurate control of export hot-fluid temperature.
4. The utility model discloses a cooling system adopts the mode of back flow, overflow pipe cooling down along separate routes, and cooling efficiency is high.
Drawings
Fig. 1 is a schematic structural diagram of the present invention. In the figure, 1, a control cabinet, 2, a frequency converter, 3, a motor, 4, a cam pump, 5, a stirring and discharging pump, 6, a ball valve I, 7, a ball valve II, 8, a ball valve III, 9, an injection chamber, 10, a thermocouple I, 11, a thermocouple II, 12, an electromagnetic flowmeter, 13, a lifting screw rod, 14, an attack angle measurer, 15, a nozzle, 16, a reference electrode, 17, an auxiliary electrode, 18, a working electrode, 19, an acidimeter probe, 20, an overflow pipe, 21, a slurry tank, 22, a cooling water pipe, 23, an acidimeter, 24, an electrochemical workstation, 25, a computer, 26, a three-stage heating system, 27, a reflux cooler and 28, an overflow cooler are arranged.
Detailed Description
The structure and operation of the present invention will be further described in detail with reference to the accompanying drawings.
As shown in fig. 1, the long-life high-temperature jet type liquid-solid dual-phase flow erosion corrosion experimental device of the present invention mainly comprises: control cabinet 1, converter 2, motor 3, lobe pump 4, stirring discharge pump 5, ball valve I6, ball valve II 7, ball valve III 8, spray chamber 9, thermocouple I10, thermocouple II 11, electromagnetic flowmeter 12, elevating screw 13, angle of attack caliber 14, nozzle 15, reference electrode 16, auxiliary electrode 17, working electrode 18 (sample), acidimeter probe 19, overflow pipe 20, slurry tank 21, condenser tube 22, acidimeter 23, electrochemistry workstation 24, computer 25, tertiary heating system 26, reflux cooler 27, overflow cooler 28 etc. concrete structure is as follows:
the input end of a motor 3 is connected with a frequency converter 2 on a control cabinet 1, the output end of the motor 3 is provided with a cam pump 4, the outlet of the cam pump 4 is connected with the inlet of a three-stage heating system 26 through a pipeline, the outlet of the three-stage heating system 26 extends into an injection chamber 9 through a pipeline, the pipeline is provided with an electromagnetic flowmeter 12, one end of the pipeline extending into the injection chamber 9 is provided with a nozzle 15, and one side of the pipeline part positioned at the inlet at the top of the injection chamber 9 is connected with a lifting screw 13; the bottom outlet of the injection chamber 9 is connected with one end of a reflux cooler 27 through a pipeline (a ball valve III 8 is arranged on the pipeline), the other end of the reflux cooler 27 arranged in the slurry tank 21 extends to the lower part in the slurry tank 21, and the slurry tank 21 is communicated with the inlet of the cam pump 4 through a pipeline.
The lower part of the side surface of the slurry tank 21 is provided with a cooling water pipe 22, the upper part of the side surface of the slurry tank 21 is connected with the inlet of an overflow cooler 28 through a pipeline, and the outlet of the overflow cooler 28 is communicated with the lower part of the side surface of the spraying chamber 9 through an overflow pipe 20. The thermocouple I10 is inserted in the spraying chamber 9, an attack angle measurer 14, a nozzle 15, a reference electrode 16, an auxiliary electrode 17, a working electrode 18 and an acidimeter probe 19 are arranged in the spraying chamber 9, the attack angle measurer 14 corresponds to the working electrode 18, the reference electrode 16, the auxiliary electrode 17 and the working electrode 18 are connected to an electrochemical workstation 24 through leads, the electrochemical workstation 24 is connected with a computer 25, and the acidimeter probe 19 is connected to an acidimeter 23 through a lead.
The thermocouple II 11 is inserted in the slurry tank 21, the slurry tank 21 is communicated with an inlet of the stirring and discharging pump 5 through a pipeline, an outlet of the stirring and discharging pump 5 is divided into two branches, one branch (provided with the ball valve II 7) is communicated with the slurry tank 21, and the other branch is provided with the ball valve I6.
The utility model adopts the cam pump 4 driven by the motor 3 provided with the frequency converter 2 as a driving pump, the electromagnetic flowmeter 12 is arranged in the output pipeline of the cam pump 4, and the electromagnetic flowmeter 12 displays the flow velocity in the pipeline in real time; the tertiary heating system 26 is installed after the lobe pump 4 and before the injection chamber 9; the nozzle 15 is installed in the spray chamber 9 and is provided with a spray distance adjusting device (a lifting screw 13), an attack angle measurer 14 is also installed in the spray chamber 9, the attack angle measurer 14 adjusts the attack angle, and the sample is controlled by the attack angle measurer and can be used for adjusting the sprayed angle of the sample; the bottom of the working electrode (sample) 18 is connected with a lead, and the reference electrode 16, the auxiliary electrode 17 and the working electrode (sample) 18 are connected to an electrochemical workstation 24 through leads so as to realize electrochemical parameter measurement. The side wall of the spraying chamber 9 is provided with an overflow pipe 20, the rear part of the overflow pipe 20 is connected with an overflow cooler 28, and the bottom of the spraying chamber 9 is provided with a drain ball valve III 8 which is communicated with a reflux cooler 27 and then returned to the slurry tank 21. The utility model discloses still be equipped with stirring discharge pump 5, the export of stirring discharge pump 5 is divided into two the tunnel, is controlled by ball valve I6, ball valve II 7 respectively, realizes the stirring to the material when opening all the way of feed back thick liquid jar 21, accesss to the outside and realizes the emission of waste material when opening all the way.
The utility model discloses in, lobe pump 4 has a great deal of advantage in the transport that contains the solid particle medium: the flow rate of the cam pump is controlled by the frequency converter, the pulsation problem of a common high-pressure plunger pump is avoided, and the scouring corrosion experiment can be performed under the harsh medium conditions of high solid content, corrosivity and the like. The use of a lobe pump allows the testing of systems containing larger solid phase particles.
The utility model discloses in, tertiary heating system adopts high temperature ceramic heating rope and high power heating pipe as heating element. The first stage is that a high-temperature ceramic heating rope is wound outside a stainless steel pipe for heating, the pipe pass is designed to be 2 meters, the tail end adopts a thermocouple for measuring the temperature, and the temperature of a first stage outlet at the tail end is controlled to reach 80 ℃ in cooperation with a temperature relay; in the second stage, a high-power high-temperature ceramic heating rope is wound outside a stainless steel pipe for heating, the pipe pass is designed to be 1 meter, the tail end adopts a thermocouple for measuring the temperature, and the outlet temperature of the second stage at the tail end is controlled to reach 120 ℃ in cooperation with a temperature relay; and thirdly, heating by binding high-power heating pipes outside the stainless steel pipes in parallel, designing a pipe pass to be 1 m, measuring the temperature at the tail end by adopting a thermocouple, and controlling the outlet temperature of the third stage at the tail end to reach 160 ℃ by matching with a temperature relay.
The utility model discloses the working process is as follows:
installing a working electrode 18 (sample) and connecting a three-electrode system for electrochemical measurement; adjusting the attack angle and the spray distance according to the working parameters, and starting a cooling system (a cooling water pipe 22, a reflux cooler 27 and an overflow cooler 28) and a three-stage heating system 26; starting a stirring and discharging pump 5 to enable the medium to be in a uniform state; starting the cam pump 4, and adjusting the rotating speed of the motor by using the frequency converter 2 so as to achieve the designed flow; the level of the spray chamber 9 is controlled by adjusting the drain ball valve III 8 and the overflow pipe 20. Adopt the utility model discloses can control the velocity of flow, attack angle, medium temperature under the higher temperature, erode the corrosion experiment, can realize experimental apparatus's long-time safety and stability operation under the higher temperature.
The result shows, the utility model discloses experimental apparatus is except having the driving pump, the nozzle, the spray chamber, electrochemistry test system, adopt the motor drive's that is equipped with the converter cam pump as the driving pump, be equipped with the angle of attack caliber of adjusting the sample angle of attack in the spray chamber, the pipeline at nozzle place even has jet distance adjusting device outside, through the position that rational design heating and cooling were located, part hot-fluid and driving pump ingeniously, thereby can solve the problem that equipment service cycle is short under the higher temperature among the prior art, make the jet type erode and corrode experimental apparatus realization phase and stabilize the service.
Claims (5)
1. A long-life high-temperature injection type liquid-solid two-phase flow erosion corrosion experimental device is characterized in that an input end of a motor is connected with a frequency converter, an output end of the motor is provided with a cam pump, an outlet of the cam pump is connected with an inlet of a three-stage heating system through a pipeline, an outlet of the three-stage heating system extends into an injection chamber through a pipeline, the pipeline is provided with an electromagnetic flowmeter, one end of the pipeline extending into the injection chamber is provided with a nozzle, and one side of a pipeline part positioned at an inlet at the top of the injection chamber is connected with a lifting screw rod; the bottom outlet of the spray chamber is connected with one end of a reflux cooler through a pipeline, the other end of the reflux cooler arranged in the slurry tank extends to the lower part in the slurry tank, and the slurry tank is communicated with the inlet of the cam pump through a pipeline.
2. The long-life high-temperature injection type liquid-solid two-phase flow erosion corrosion experimental device as claimed in claim 1, wherein a cooling water pipe is installed at the lower part of the side surface of the slurry tank, the upper part of the side surface of the slurry tank is connected with the inlet of the overflow cooler through a pipeline, and the outlet of the overflow cooler is communicated with the lower part of the side surface of the injection chamber through an overflow pipe.
3. The long-life high-temperature jet type liquid-solid two-phase flow erosion corrosion experiment device as claimed in claim 1, wherein the thermocouple I is inserted into the jet chamber, an attack angle measurer, a nozzle, a reference electrode, an auxiliary electrode, a working electrode and an acidimeter probe are arranged in the jet chamber, the attack angle measurer corresponds to the working electrode, the reference electrode, the auxiliary electrode and the working electrode are connected to an electrochemical workstation through leads, the electrochemical workstation is connected with a computer, and the acidimeter probe is connected to an acidimeter through leads.
4. The long-life high-temperature jet type liquid-solid two-phase flow erosion corrosion experimental device as claimed in claim 1, wherein a thermocouple II is inserted into a slurry tank, the slurry tank is communicated with an inlet of a stirring and discharging pump through a pipeline, an outlet of the stirring and discharging pump is divided into two branches, one branch is communicated with the slurry tank, a ball valve II is arranged on the branch, and a ball valve I is arranged on the other branch.
5. The long-life high-temperature jet type liquid-solid two-phase flow erosion corrosion experimental device as claimed in claim 1, wherein a ball valve III is arranged on a pipeline connecting an outlet at the bottom of the jet chamber with the reflux cooler.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922081498.XU CN211528168U (en) | 2019-11-27 | 2019-11-27 | Long-life high-temperature jet type liquid-solid dual-phase flow erosion corrosion experimental device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922081498.XU CN211528168U (en) | 2019-11-27 | 2019-11-27 | Long-life high-temperature jet type liquid-solid dual-phase flow erosion corrosion experimental device |
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| Publication Number | Publication Date |
|---|---|
| CN211528168U true CN211528168U (en) | 2020-09-18 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201922081498.XU Active CN211528168U (en) | 2019-11-27 | 2019-11-27 | Long-life high-temperature jet type liquid-solid dual-phase flow erosion corrosion experimental device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN211528168U (en) |
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- 2019-11-27 CN CN201922081498.XU patent/CN211528168U/en active Active
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