CN108680491A - Method for testing using dynamic electrochemical device - Google Patents

Method for testing using dynamic electrochemical device Download PDF

Info

Publication number
CN108680491A
CN108680491A CN201810204840.8A CN201810204840A CN108680491A CN 108680491 A CN108680491 A CN 108680491A CN 201810204840 A CN201810204840 A CN 201810204840A CN 108680491 A CN108680491 A CN 108680491A
Authority
CN
China
Prior art keywords
electrode
autoclave body
working electrode
hole
pressure
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.)
Granted
Application number
CN201810204840.8A
Other languages
Chinese (zh)
Other versions
CN108680491B (en
Inventor
徐连勇
路永新
韩永典
赵雷
荆洪阳
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tianjin University
Original Assignee
Tianjin University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Tianjin University filed Critical Tianjin University
Priority to CN201810204840.8A priority Critical patent/CN108680491B/en
Publication of CN108680491A publication Critical patent/CN108680491A/en
Application granted granted Critical
Publication of CN108680491B publication Critical patent/CN108680491B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N17/00Investigating resistance of materials to the weather, to corrosion, or to light
    • G01N17/02Electrochemical measuring systems for weathering, corrosion or corrosion-protection measurement
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N17/00Investigating resistance of materials to the weather, to corrosion, or to light
    • G01N17/006Investigating resistance of materials to the weather, to corrosion, or to light of metals

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Ecology (AREA)
  • Environmental & Geological Engineering (AREA)
  • Environmental Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • General Physics & Mathematics (AREA)
  • Immunology (AREA)
  • Pathology (AREA)
  • Testing Resistance To Weather, Investigating Materials By Mechanical Methods (AREA)

Abstract

The invention discloses a method for testing by utilizing a dynamic electrochemical device, which comprises the following steps of firstly, filling corrosive liquid into a high-pressure kettle body through a feeding auxiliary device and a feeding hole; introducing inert gas into the corrosive liquid in the high-pressure kettle body through the gas inlet pipe; introducing experimental gas into the corrosive liquid in the high-pressure kettle body through an air inlet pipe; starting a heating and heat-preserving device through an external control box, heating the corrosive liquid in the high-pressure kettle to a set experimental temperature and preserving heat, adjusting the control box, and changing the rotating speed of a rotating shaft to enable the rotating speed to reach a preset rotating speed; and the external electrochemical workstation is respectively connected with the working electrode, the auxiliary electrode and the reference electrode, receives signals and starts to perform experimental tests. The technical scheme of the invention is suitable for detecting the corrosion in-situ electrochemical signal of the metal material under the dynamic working condition of the high-temperature high-pressure corrosion medium so as to carry out high-temperature high-pressure dynamic corrosion behavior and mechanism research, and solves the problem that the electrochemical signal measurement of the simulation solution under the high-temperature high-pressure condition cannot be carried out in the past.

Description

The method tested using dynamic electrochemical appliance
The present patent application is the division of parent application " high temperature and pressure dynamic electro-chemical test experimental provision and test method " The applying date of application, parent application is on May 16th, 2016, and application No. is 2016103221363.
Technical field
The present invention relates to electro-chemical test experimental provision, especially high temperature and pressure dynamic electro-chemical test experimental provisions and survey Method for testing.
Background technology
Occur to destroy or go bad caused by chemistry or electrochemical action between metal material and ambient enviroment (medium) to claim For corrosion, metal erosion spreads the every field of industrial and agricultural production and national defense construction, and harm is very serious.And high temperature pressure corrosion It is a kind of to lead to a kind of phenomenon of material failure because electrochemical corrosion acts on.Such as during oil and gas development, in associated gas Often contain H2S and CO2, various pipelines or structure is caused to fail in the form of high temperature pressure corrosion.Carry out high temperature pressure corrosion process Simulated experiment is defeated oil/gas material screening and evaluation, the screening of sustained release agent and evaluation and research material corrosion resistance and etching machine The important means of reason.But due under high-temperature and high-pressure conditions, to working electrode, reference electrode and the isostructural resistance to height of auxiliary electrode Mild high voltage performance has very high requirement, is not easy to realize the output of electrochemical signals.Meanwhile related forming currently on the market The price of product is all higher, affects the extensive research to high temperature pressure corrosion behavior and mechanism.
Invention content
The present invention overcomes the disadvantages of the prior art, provides high temperature and pressure dynamic electro-chemical test experimental provision and surveys Method for testing.The device is suitable for high temperature pressure corrosion medium under the conditions of dynamic operation condition, to metallic material corrosion electrochemical in-situ Signal is detected, and to carry out the behavior of high temperature and pressure Dynamic Corrosion and mechanism study, solving in the past cannot be to simulated solution The problem of electrochemical signals measurement is carried out under high-temperature and high-pressure conditions.
In order to solve the above-mentioned technical problem, the present invention is achieved by the following technical solutions:
High temperature and pressure dynamic electrochemical testing device, including high-temperature high-pressure reaction kettle, three-electrode system, external control cabinet, External air supply system, external electrochemical workstation and computer;
High-temperature high-pressure reaction kettle include autoclave body, high pressure kettle cover, air inlet pipe, escape pipe, rotation axis, pressure sensor, Pressure gauge, temperature sensor, heating device and heat preservation heat insulation layer, autoclave body is cylindrical container, in the outside of autoclave body Heating device is set, thermal insulating warm-keeping layer is set in the outside of heating device, high pressure kettle cover is set in the upper surface of autoclave body, tightly Fixing bolt passes through fixed mounting hole, is connected with autoclave body interconnecting piece, so that kettle cover is tightened to an entirety with autoclave body, and realizes It seals, is diametrically disposed on high pressure kettle cover circular surface:Air inlet pipe hole, temperature sensor hole, working electrode hole, Rotational axis hole, charging aperture, pressure sensor hole and outlet pore, wherein rotational axis hole are located at circle centre position, are arranged in rotational axis hole Rotation axis, rotation axis connection control motor, and rotation axis top half is located on high pressure kettle cover, and rotation axis lower half portion is located at height It presses in autoclave body, the lower end of rotation axis is provided with mixing component, is respectively arranged with above and below working electrode hole is adjacent Auxiliary electrode hole and reference electrode hole, are provided with working electrode column on working electrode hole, and auxiliary is arranged on auxiliary electrode hole Reference electrode is arranged on reference electrode hole, air inlet pipe is arranged in air inlet pipe hole, outlet is arranged in outlet pore for electrode column Pipe, setting charging auxiliary device, pressure sensor and pressure gauge are provided on pressure sensor hole on charging aperture;
In the above-mentioned technical solutions, the lower half portion length in autoclave body that is located at of the rotation axis accounts for autoclave body height , the mixing component is agitating paddle or stirring disk;
In the above-mentioned technical solutions, the air inlet pipe gos deep into the bottom of autoclave body, and escape pipe is located in autoclave body It is more than liquid surface;
In the above-mentioned technical solutions, temperature sensor is connected with temperature controller, and temperature controller is connected with heating device;
In above-mentioned technical proposal, when three electrodes is arranged in three electrode holes, electrode is with the structure at high pressure kettle cover sealing, Setting of casing, upper casing and plug are set gradually from bottom to top;
Three-electrode system includes reference electrode, working electrode column, auxiliary electrode column, working electrode stabilising arrangement and electrode Folder, wherein reference electrode are an integral structure Ag/AgCl electrodes, and working electrode column and auxiliary electrode column have identical structure, i.e., Cylindrical structure is arranged metallic channel directed downwardly in the lower section of cylinder, sheet metal is arranged in metallic channel, along cylindrical center's setting The bottom end of portion's conducting wire, inner lead is in contact with the sheet metal in metallic channel, the side setting fastening spiral shell button in the position that is in contact, Fasten the connection that spiral shell button is used for fixing internal conducting wire and sheet metal;In order to make working electrode and reference in autoclave body under stirring Stabilizing distance is kept, therefore working electrode auxiliary stabilizing device is set, which includes first clamping plate, second clamping plate and third clamping plate And telescopic device, telescopic device connect into an entirety across three pieces of clamping plates, first clamping plate and third clamping plate can be along telescopic devices It carries out, close to the activity with separate second clamping plate, secure component (not marking in figure) being arranged in first clamping plate and third clamping plate, For strap and telescopic device, electrode holder includes stable disk, conducting wire and sheet metal, and working electrode groove is arranged in stable disk, Working electrode sample is set in working electrode groove, and stable disk is connected by conducting wire with sheet metal, and reference electrode is fixed on the first folder Between plate and second clamping plate, the stable disk of electrode holder is fixed between second clamping plate and third clamping plate, keeps working electrode sample flat It is hollow structure between clamping plate facing towards reference electrode, makes to be full of experimental solutions between working electrode sample and reference electrode, gold Belong to piece and be connected with working electrode by being inserted into the metallic channel below working electrode column, is set in the lower-lying metal slot of auxiliary electrode column Set platinum plate electrode;
In the above-mentioned technical solutions, the working electrode is the test button of epoxy encapsulation,
In the above-mentioned technical solutions, the auxiliary electrode is the platinum plate electrode of 13 × 10 × 0.2mm, unilateral exposed surface Product is 10 × 10mm,
In the above-mentioned technical solutions, the working electrode surface is away from reference electrode 2-5mm;
In the above-mentioned technical solutions, the working electrode auxiliary stabilizing device and electrode holder are maximum temperature 260 DEG C, maximum pressure is the polytetrafluoroethylene (PTFE) of 10Mpa;
In the above-mentioned technical solutions, the reference electrode is 310 DEG C of maximum temperature, and maximum pressure is the high temperature of 10Mpa High pressure Ag/AgCl electrodes;
External control cabinet is connected with heating and heat-insulating device and rotation axis, and heating and thermal insulation dress can be adjusted by external control cabinet The rotating speed of the temperature and rotation axis set;
External air supply system is connected with the air inlet pipe of device, for providing corrosive gas;
External electrochemical workstation is connected with the terminals of auxiliary electrode, reference electrode and working electrode, auxiliary for acquiring The electrochemical signals of electrode, reference electrode and working electrode, computer are helped to be connected with external electrochemical workstation, for external The data of electrochemical workstation acquisition are recorded, analyzing processing and output.
The test method of high temperature and pressure dynamic electrochemical testing device is as follows:
Step 1, corrosive liquid is packed into autoclave body by charging auxiliary device and charging aperture, and covers high pressure kettle cover and gives With fixation;
Step 2, it is passed through inert gas in the corrosive liquid by air inlet pipe into autoclave body, to remove in autoclave body Oxygen;
In step 2, inert gas is nitrogen, helium or argon gas;
In step 2, the time for being passed through inert gas is 12-24 hours, preferably 15-20 hours;
Step 3, it is passed through experimental gas in the corrosive liquid by air inlet pipe into autoclave body, so that experimental gas is filled in Autoclave body inner space;
In step 3, the time for being passed through experimental gas is 22-24 hours, experimental gas CO2Or H2S gases;
Step 4, heating and heat-insulating device is started by external control cabinet, autoclave internal corrosion liquid is heated to setting experiment temperature It spends and keeps the temperature, adjusting control case changes rotation rotating speed, reaches preset rotation speed;
Step 5, external electrochemical workstation is connected with working electrode, auxiliary electrode and reference electrode respectively, and receives letter Number, proceed by experiment test.
In actual use, pressure setting, during excluding oxygen, high pressure are carried out by pressure sensor and pressure gauge When pressure reaches preset value in kettle, it can generally assert that oxygroup originally drains;Similarly, when pressure reaches preset value in autoclave, one As can assert that experimental gas has been filled with space in autoclave.
Compared with prior art, the beneficial effects of the invention are as follows:Using high temperature and pressure Ag/AgCl reference electrodes, reach The requirement of test environment leakproofness and heat-resisting quantity, while also ensuring the accuracy of test result, it is assisted using working electrode Stabilising arrangement makes working electrode keep relative distance to fix with reference electrode, and autoclave body meets the requirement of leakproofness and heat-resisting quantity, The device provides the test environments of high temperature and pressure can be used for dynamic high temperature high pressure corrosion behavior and mechanism study.
Description of the drawings
Fig. 1 is the autoclave superstructure schematic diagram of the present invention.
Fig. 2 is the whole kettle side structure schematic view of A-A sections in Fig. 1.
Fig. 3 is that autoclave covers component connection sealing means schematic diagram.
Fig. 4 is working electrode column/reference electrode rod structure schematic diagram.
Fig. 5 is electrode holder structural schematic diagram.
Fig. 6 is working electrode auxiliary stabilizing device overlooking structure diagram.
Fig. 7 is working electrode auxiliary stabilizing device side structure schematic view.
Fig. 8 is temperature 60 C, CO2Divide 0.03Mpa, under 0m/s and 0.3m/s rotating speeds, the electrochemical corrosion of carbon steel A106B Polarization curve.
Fig. 9 is 90 DEG C of temperature, CO2Divide 0.1Mpa, under 0m/s and 0.3m/s rotating speeds, the electrochemical corrosion of carbon steel A106B Polarization curve.
Figure 10 is 90 DEG C of temperature, CO2Divide 0.2Mpa, under 0m/s and 0.5m/s rotating speeds, the electrochemical corrosion of carbon steel A106B Polarization curve.
Figure 11 is 90 DEG C of temperature, CO2Divide 0.5Mpa, under 0m/s and 1m/s rotating speeds, the electrochemical corrosion pole of carbon steel A106B Change curve.
In 1-7:1 is autoclave body, and 2 be heating device, and 3 be heat preservation heat insulation layer, and 4 be nut, and 5 be mixing component, and 6 are Escape pipe, 7 be pressure sensor, and 8 be pressure gauge, and 9 be charge door, and 10 be rotation axis, and 11 be auxiliary electrode column, and 12 be reference electricity Pole, 13 be working electrode column, and 14 be temperature sensor, and 15 be air inlet pipe, and 16 be fastening bolt, and 17 be high pressure kettle cover, and 18 be work Make electrode, 19 be auxiliary electrode, and 20 be autoclave outer wall, and 21 be outlet pore, and 22 be pressure sensor hole, and 23 be charging aperture, 24 be rotational axis hole, and 25 be auxiliary electrode hole, and 26 be working electrode hole, and 27 be temperature sensor hole, and 28 be air inlet pipe hole, 29 It is inner lead for reference electrode hole, 30,31 be plug, and 32 be upper casing, and 33 be setting of casing, and 34 be fastening spiral shell button, and 35 be gold Belong to slot, 36 be stable disk, and 37 be working electrode groove, and 38 be conducting wire, and 39 be sheet metal, and 40 be first clamping plate, and 41 be the second folder Plate, 42 be third clamping plate, and 43 be telescopic device, and 44 be fixed mounting hole, and 45 motors in order to control, 46 be autoclave body interconnecting piece.
In 8-11,1 is static lower test, and 2 indicate the lower test of dynamic.
Specific implementation mode
Present invention is further described in detail with specific embodiment below in conjunction with the accompanying drawings:
High temperature and pressure dynamic electrochemical testing device, including high-temperature high-pressure reaction kettle, three-electrode system, external control cabinet, External air supply system, external electrochemical workstation and computer;
High-temperature high-pressure reaction kettle include autoclave body, high pressure kettle cover, air inlet pipe, escape pipe, rotation axis, pressure sensor, Pressure gauge, temperature sensor, heating device and heat preservation heat insulation layer, autoclave body is cylindrical container, in the outside of autoclave body Heating device is set, thermal insulating warm-keeping layer is set in the outside of heating device, high pressure kettle cover is set in the upper surface of autoclave body, tightly Fixing bolt passes through fixed mounting hole, is connected with autoclave body interconnecting piece, so that kettle cover is tightened to an entirety with autoclave body, and realizes It seals, is diametrically disposed on high pressure kettle cover circular surface:Air inlet pipe hole, temperature sensor hole, working electrode hole, Rotational axis hole, charging aperture, pressure sensor hole and outlet pore, wherein rotational axis hole are located at circle centre position, are arranged in rotational axis hole Rotation axis, rotation axis connection control motor, and rotation axis top half is located on high pressure kettle cover, and rotation axis lower half portion is located at height It presses in autoclave body, the lower end of rotation axis is provided with mixing component, is respectively arranged with above and below working electrode hole is adjacent Auxiliary electrode hole and reference electrode hole, are provided with working electrode column on working electrode hole, and auxiliary is arranged on auxiliary electrode hole Reference electrode is arranged on reference electrode hole, air inlet pipe is arranged in air inlet pipe hole, outlet is arranged in outlet pore for electrode column Pipe, setting charging auxiliary device, pressure sensor and pressure gauge are provided on pressure sensor hole on charging aperture;
In the above-mentioned technical solutions, the lower half portion length in autoclave body that is located at of the rotation axis accounts for autoclave body height , the mixing component is agitating paddle or stirring disk;
In the above-mentioned technical solutions, the air inlet pipe gos deep into the bottom of autoclave body, and escape pipe is located in autoclave body It is more than liquid surface;
In the above-mentioned technical solutions, temperature sensor is connected with temperature controller, and temperature controller is connected with heating device;
In above-mentioned technical proposal, when three electrodes is arranged in three electrode holes, electrode is with the structure at high pressure kettle cover sealing, Setting of casing, upper casing and plug are set gradually from bottom to top;
Three-electrode system includes reference electrode, working electrode column, auxiliary electrode column, working electrode stabilising arrangement and electrode Folder, wherein reference electrode are an integral structure Ag/AgCl electrodes, and working electrode column and auxiliary electrode column have identical structure, i.e., Cylindrical structure is arranged metallic channel directed downwardly in the lower section of cylinder, sheet metal is arranged in metallic channel, along cylindrical center's setting The bottom end of portion's conducting wire, inner lead is in contact with the sheet metal in metallic channel, the side setting fastening spiral shell button in the position that is in contact, Fasten the connection that spiral shell button is used for fixing internal conducting wire and sheet metal;In order to make working electrode and reference in autoclave body under stirring Stabilizing distance is kept, therefore working electrode auxiliary stabilizing device is set, which includes first clamping plate, second clamping plate and third clamping plate And telescopic device, telescopic device connect into an entirety across three pieces of clamping plates, first clamping plate and third clamping plate can be along telescopic devices It carries out, close to the activity with separate second clamping plate, secure component (not marking in figure) being arranged in first clamping plate and third clamping plate, For strap and telescopic device, electrode holder includes stable disk, conducting wire and sheet metal, and working electrode groove is arranged in stable disk, Working electrode sample is set in working electrode groove, and stable disk is connected by conducting wire with sheet metal, and reference electrode is fixed on the first folder Between plate and second clamping plate, the stable disk of electrode holder is fixed between second clamping plate and third clamping plate, keeps working electrode sample flat It is hollow structure between clamping plate facing towards reference electrode, makes to be full of experimental solutions between working electrode sample and reference electrode, gold Belong to piece and be connected with working electrode by being inserted into the metallic channel below working electrode column, is set in the lower-lying metal slot of auxiliary electrode column Set platinum plate electrode;
In the above-mentioned technical solutions, the working electrode is the test button of epoxy encapsulation,
In the above-mentioned technical solutions, the auxiliary electrode is the platinum plate electrode of 13 × 10 × 0.2mm, unilateral exposed surface Product is 10 × 10mm,
In the above-mentioned technical solutions, the working electrode surface is away from reference electrode 2-5mm;
In the above-mentioned technical solutions, the working electrode auxiliary stabilizing device and electrode holder are maximum temperature 260 DEG C, maximum pressure is the polytetrafluoroethylene (PTFE) of 10Mpa;
In the above-mentioned technical solutions, the reference electrode is 310 DEG C of maximum temperature, and maximum pressure is the high temperature of 10Mpa High pressure Ag/AgCl electrodes;
External control cabinet is connected with heating and heat-insulating device and rotation axis, and heating and thermal insulation dress can be adjusted by external control cabinet The rotating speed of the temperature and rotation axis set;
External air supply system is connected with the air inlet pipe of device, for providing corrosive gas;
External electrochemical workstation is connected with the terminals of auxiliary electrode, reference electrode and working electrode, auxiliary for acquiring The electrochemical signals of electrode, reference electrode and working electrode, computer are helped to be connected with external electrochemical workstation, for external The data of electrochemical workstation acquisition are recorded, analyzing processing and output.
The test method of high temperature and pressure dynamic electrochemical testing device is as follows:
Step 1, corrosive liquid is packed into autoclave body by charging auxiliary device and charging aperture, and covers high pressure kettle cover and gives With fixation;
Step 2, it is passed through inert gas in the corrosive liquid by air inlet pipe into autoclave body, to remove in autoclave body Oxygen;
In step 2, inert gas is nitrogen, helium or argon gas;
In step 2, the time for being passed through inert gas is 12-24 hours, preferably 15-20 hours;
Step 3, it is passed through experimental gas in the corrosive liquid by air inlet pipe into autoclave body, so that experimental gas is filled in Autoclave body inner space;
In step 3, the time for being passed through experimental gas is 22-24 hours, experimental gas CO2Or H2S gases;
Step 4, heating and heat-insulating device is started by external control cabinet, autoclave internal corrosion liquid is heated to setting experiment temperature It spends and keeps the temperature, adjusting control case changes rotation rotating speed, reaches preset rotation speed;
Step 5, external electrochemical workstation is connected with working electrode, auxiliary electrode and reference electrode respectively, and receives letter Number, proceed by experiment test.
In actual use, pressure setting, during excluding oxygen, high pressure are carried out by pressure sensor and pressure gauge When pressure reaches preset value in kettle, it can generally assert that oxygroup originally drains;Similarly, when pressure reaches preset value in autoclave, one As can assert that experimental gas has been filled with space in autoclave.
With the present apparatus under different rotating speeds, temperature and air pressure conditions to the electrochemical corrosion polarization curve of carbon steel A106B into Row test, sample impregnates before testing continues 1 hour in the solution, until specimen surface system reaches dynamic stability, test result As shown below.1 indicates static lower test in figure, and 2 indicate the lower test of dynamic.Fig. 8 is temperature 60 C, CO20.03Mpa is divided, Polarization curve under 0m/s and 0.3m/s rotating speeds.Due to CO2Relatively low and Acclimation temperature is divided, the anode of polarization curve is propped up with activity Based on dissolving.Meanwhile rotating speed reduces polarization curve cathode in such a way that diffusion polarization controls.Fig. 9 is 90 DEG C of temperature, CO2Point Press 0.1Mpa, the polarization curve under 0m/s and 0.3m/s rotating speeds.Due to CO2The raising of partial pressure, the anode branch and Fig. 8 of polarization curve It compares, slight deactivation phenomenon occurs, this is because raising and the CO of temperature2The raising of partial pressure accelerates specimen surface corrosive film Formation, it can be seen that the passivation phenomenon of the lower specimen surface of static state becomes apparent from.The raising and dynamic test of temperature are so that polarization is bent Line cathode is no longer carried out with polarization curve cathode.Figure 10 is 90 DEG C of temperature, and CO2 divides 0.2Mpa, under 0m/s and 0.5m/s rotating speeds Polarization curve.Test result and Fig. 9 are close under this condition, are that anode surface slight deactivation occurs, cathode turns to electrochemistry Polarizing control.Figure 11 is 90 DEG C of temperature, CO2Divide 0.5Mpa, the polarization curve under 0m/s and 1m/s rotating speeds.Due to CO2Partial pressure carries Height, anode branch passivation phenomenon is apparent, and cathode is carried out with activation polarization control mode.
It describes the invention in detail, but content is only the preferred embodiment of the present invention, cannot be recognized above For the practical range for limiting the present invention.Any changes and modifications in accordance with the scope of the present application should all still return Belong within the patent covering scope of the present invention.

Claims (8)

1. the method tested using dynamic electrochemical appliance, which is characterized in that dynamic electrochemical appliance includes high temperature and pressure Reaction kettle, three-electrode system, external control cabinet, external air supply system, external electrochemical workstation and computer;High temperature high pressure reverse Answer kettle include autoclave body, high pressure kettle cover, air inlet pipe, escape pipe, rotation axis, pressure sensor, pressure gauge, temperature sensor, Heating device and heat preservation heat insulation layer, autoclave body is cylindrical container, and heating device is arranged in the outside of autoclave body, is heating Thermal insulating warm-keeping layer is arranged in the outside of device, high pressure kettle cover is arranged in the upper surface of autoclave body, fastening bolt, which passes through, to be fixedly mounted Hole is connected with autoclave body interconnecting piece, so that kettle cover is tightened to an entirety with autoclave body, and realizes sealing, and high pressure kettle cover is round It is diametrically disposed on surface:Air inlet pipe hole, temperature sensor hole, working electrode hole, rotational axis hole, charging aperture, Pressure sensor hole and outlet pore, wherein rotational axis hole are located at circle centre position, and rotation axis is arranged in rotational axis hole, rotates axis connection Motor is controlled, rotation axis top half is located on high pressure kettle cover, and rotation axis lower half portion is located in autoclave body, in rotation axis Lower end be provided with mixing component, be respectively arranged with above and below working electrode hole is adjacent auxiliary electrode hole and reference electricity Pole hole is provided with working electrode column on working electrode hole, auxiliary electrode column is arranged on auxiliary electrode hole, in reference electrode hole Upper setting reference electrode, air inlet pipe hole is interior to be arranged air inlet pipe, escape pipe is arranged in outlet pore, tracheae gos deep into autoclave body Bottom, escape pipe are located in autoclave body more than liquid surface, the setting charging auxiliary device on charging aperture, in pressure sensor Pressure sensor and pressure gauge are provided on hole, temperature sensor is connected with temperature controller, temperature controller and heating device It is connected;
Three-electrode system includes reference electrode, working electrode column, auxiliary electrode column, working electrode stabilising arrangement and electrode holder, Middle reference electrode is an integral structure Ag/AgCl electrodes, and working electrode column and auxiliary electrode column have identical structure, i.e. cylinder Structure is arranged metallic channel directed downwardly in the lower section of cylinder, sheet metal is arranged in metallic channel, is led along cylindrical center's setting inside The bottom end of line, inner lead is in contact with the sheet metal in metallic channel, the side setting fastening spiral shell button in the position that is in contact, fastening Spiral shell button is used for the connection of fixing internal conducting wire and sheet metal;In order to make working electrode be kept under stirring in autoclave body with reference Stabilizing distance, therefore working electrode auxiliary stabilizing device is set, which includes first clamping plate, second clamping plate and third clamping plate and stretches Compression apparatus, telescopic device connect into an entirety across three pieces of clamping plates, and first clamping plate and third clamping plate can be carried out along telescopic device Close to far from second clamping plate activity, secure component is set in first clamping plate and third clamping plate, for strap with stretch Compression apparatus, electrode holder include stable disk, conducting wire and sheet metal, and working electrode groove is arranged in stable disk, is arranged in working electrode groove Working electrode sample, stable disk are connected by conducting wire with sheet metal, and reference electrode is fixed between first clamping plate and second clamping plate, The stable disk of electrode holder is fixed between second clamping plate and third clamping plate, makes working electrode sample plane towards reference electrode, folder It is hollow structure between plate, makes to be full of experimental solutions between working electrode sample and reference electrode, sheet metal is by being inserted into work Metallic channel below electrode column is connected with working electrode, and platinum plate electrode is arranged in the lower-lying metal slot of auxiliary electrode column;
External control cabinet is connected with heating and heat-insulating device and rotation axis, and heating and heat-insulating device can be adjusted by external control cabinet The rotating speed of temperature and rotation axis;
External air supply system is connected with the air inlet pipe of device, for providing corrosive gas;
External electrochemical workstation is connected with the terminals of auxiliary electrode, reference electrode and working electrode, for acquiring auxiliary electricity Pole, reference electrode and working electrode electrochemical signals, computer is connected with external electrochemical workstation, for external electrification The data for learning workstation collection are recorded, analyzing processing and output;It is being tested, is being carried out as steps described below:
Step 1, corrosive liquid is packed into autoclave body by charging auxiliary device and charging aperture, and covers high pressure kettle cover and is consolidated It is fixed;
Step 2, it is passed through inert gas in the corrosive liquid by air inlet pipe into autoclave body, to remove the oxygen in autoclave body;
Step 3, it is passed through experimental gas in the corrosive liquid by air inlet pipe into autoclave body, so that experimental gas is filled in high pressure Autoclave body inner space;
Step 4, heating and heat-insulating device is started by external control cabinet, autoclave internal corrosion liquid is heated to setting experimental temperature simultaneously Heat preservation, adjusting control case change rotation rotating speed, reach preset rotation speed;
Step 5, external electrochemical workstation is connected with working electrode, auxiliary electrode and reference electrode respectively, and receives signal, opens Begin to carry out experiment test.
2. the method according to claim 1 tested using dynamic electrochemical appliance, which is characterized in that in step 2 In, the inert gas is nitrogen, helium or argon gas, and the time for being passed through inert gas is 12-24 hours, preferably 15-20 Hour.
3. the method according to claim 1 tested using dynamic electrochemical appliance, which is characterized in that in step 3 In, the experimental gas is CO2Or H2S gases, the time for being passed through experimental gas are 22-24 hours.
4. the method according to claim 1 tested using dynamic electrochemical appliance, which is characterized in that described turns The lower half portion length in autoclave body that is located at of moving axis accounts for the 1/3-1/2 of autoclave body height, the mixing component be agitating paddle or Stir disk.
5. the method according to claim 1 tested using dynamic electrochemical appliance, which is characterized in that the work Make electrode surface away from reference electrode 2-5mm.
6. the method according to claim 1 tested using dynamic electrochemical appliance, which is characterized in that described is auxiliary It is the platinum plate electrode of 13 × 10 × 0.2mm to help electrode, and unilateral bare area is 10 × 10mm.
7. the method according to claim 1 tested using dynamic electrochemical appliance, which is characterized in that the ginseng It is 310 DEG C of maximum temperature than electrode, maximum pressure is the high temperature and pressure Ag/AgCl electrodes of 10Mpa.
8. the method according to claim 1 tested using dynamic electrochemical appliance, which is characterized in that the work It is 260 DEG C of maximum temperature to make electrode auxiliary stabilizing device and electrode holder, and maximum pressure is the polytetrafluoroethylene (PTFE) of 10Mpa.
CN201810204840.8A 2016-05-16 2016-05-16 Method for testing using dynamic electrochemical device Active CN108680491B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810204840.8A CN108680491B (en) 2016-05-16 2016-05-16 Method for testing using dynamic electrochemical device

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201810204840.8A CN108680491B (en) 2016-05-16 2016-05-16 Method for testing using dynamic electrochemical device
CN201610322136.3A CN105806774B (en) 2016-05-16 2016-05-16 High-temperature high-pressure dynamic electrochemical test experimental device and test method

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
CN201610322136.3A Division CN105806774B (en) 2016-05-16 2016-05-16 High-temperature high-pressure dynamic electrochemical test experimental device and test method

Publications (2)

Publication Number Publication Date
CN108680491A true CN108680491A (en) 2018-10-19
CN108680491B CN108680491B (en) 2020-05-08

Family

ID=56451197

Family Applications (3)

Application Number Title Priority Date Filing Date
CN201810204839.5A Active CN108519324B (en) 2016-05-16 2016-05-16 Three-electrode system and application thereof
CN201810204840.8A Active CN108680491B (en) 2016-05-16 2016-05-16 Method for testing using dynamic electrochemical device
CN201610322136.3A Active CN105806774B (en) 2016-05-16 2016-05-16 High-temperature high-pressure dynamic electrochemical test experimental device and test method

Family Applications Before (1)

Application Number Title Priority Date Filing Date
CN201810204839.5A Active CN108519324B (en) 2016-05-16 2016-05-16 Three-electrode system and application thereof

Family Applications After (1)

Application Number Title Priority Date Filing Date
CN201610322136.3A Active CN105806774B (en) 2016-05-16 2016-05-16 High-temperature high-pressure dynamic electrochemical test experimental device and test method

Country Status (1)

Country Link
CN (3) CN108519324B (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111024604A (en) * 2019-12-19 2020-04-17 韦正楠 Corrosion and scaling experiment detection system and method for geothermal water heat exchange process
CN112213256A (en) * 2020-10-09 2021-01-12 西南石油大学 Testing arrangement of bacterium to steel corrosion influence under oil gas pipeline cathodic polarization
CN112986111A (en) * 2019-12-13 2021-06-18 中国科学院大连化学物理研究所 Catalytic wet oxidation corrosion experiment device
CN113834765A (en) * 2020-06-08 2021-12-24 中国石油化工股份有限公司 Device and method for testing corrosion resistance of material

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106198192A (en) * 2016-08-18 2016-12-07 河南理工大学 The sample angle of attack of a kind of rotary erosion abrasion test device adjusts assembly and method
CN109100298A (en) * 2018-09-10 2018-12-28 遵义师范学院 Autoclave reactor and electrochemical appliance for measuring pollutant hydrothermal oxidization system
CN110044991B (en) * 2019-04-08 2021-11-02 山东瑞光生物科技有限公司 Glucose sensing device with sealing and temperature control functions
CN110243755B (en) * 2019-07-10 2023-12-22 北京科技大学 Top corrosion test system and test method for variable wind field regulation in autoclave
CN110501395A (en) * 2019-09-29 2019-11-26 中国石油大学(华东) A kind of precision electrode holder
CN111537588B (en) * 2020-04-23 2022-12-02 中国石油天然气集团有限公司 Electrochemical testing device and testing method for simulating oil field environment
CN111912777B (en) * 2020-07-15 2022-03-01 中国核动力研究设计院 Sample fixing device for high-temperature and high-pressure electrochemical experiment and mounting method thereof

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08102402A (en) * 1994-09-30 1996-04-16 Matsushita Electric Ind Co Ltd Resistor and manufacture method thereof
CN2475033Y (en) * 2001-02-26 2002-01-30 中国科学院海洋研究所 Electrolytic cell
CN101074487A (en) * 2007-03-29 2007-11-21 上海交通大学 Electrochemical experimental device
CN101349672A (en) * 2008-09-12 2009-01-21 福州大学 Microflow control chip electrochemical detection device capable of accurately controlling electrode distance
CN102944593A (en) * 2012-11-05 2013-02-27 上海大学 Miniature regulated electrolysis device
CN202814909U (en) * 2012-10-29 2013-03-20 黑龙江八一农垦大学 Inter-electrode distance adjustable electrolytic bath
CN204536262U (en) * 2015-03-09 2015-08-05 扬州工业职业技术学院 A kind of electrolytic cell three-electrode system position adjustable spiral clamp device
CN205139078U (en) * 2015-11-20 2016-04-06 山西大同大学 Three electrode system fixing device with adjustable

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1304834C (en) * 2005-03-25 2007-03-14 北京科技大学 Dynamic high-temperature and pressure electro-chemical measurement experimental device
RU2346267C1 (en) * 2007-05-07 2009-02-10 Инновационный технический центр Общество с ограниченной ответственностью "СИТИС" Method of determining electronic work function in vacuum (versions)
CN101865816A (en) * 2010-05-28 2010-10-20 北京科技大学 Experimental apparatus for high-temperature high-pressure loop spray corrosion simulation and electrochemical testing
CN202471565U (en) * 2012-03-14 2012-10-03 东北石油大学 High temperature and high pressure H2S/CO2 corrosion reaction device capable of realizing dynamic electrochemical test
CN103411879B (en) * 2013-07-18 2015-04-29 北京科技大学 High temperature and high pressure dynamic electrochemical test and pH in situ monitoring experimental device
CN204086201U (en) * 2014-07-04 2015-01-07 中国检验检疫科学研究院 A kind of clipping three electrode assemblies for micro-example Electrochemical Detection
CN104075987A (en) * 2014-07-22 2014-10-01 华北电力大学(保定) Electrochemistry test probe
CN105115887B (en) * 2015-09-08 2017-12-26 中国科学院海洋研究所 Metallic material corrosion test device and method under a kind of high-pressure solid bentonite environment
CN205679515U (en) * 2016-05-16 2016-11-09 天津大学 HTHP dynamic electric test chemical experimental provision

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08102402A (en) * 1994-09-30 1996-04-16 Matsushita Electric Ind Co Ltd Resistor and manufacture method thereof
CN2475033Y (en) * 2001-02-26 2002-01-30 中国科学院海洋研究所 Electrolytic cell
CN101074487A (en) * 2007-03-29 2007-11-21 上海交通大学 Electrochemical experimental device
CN101349672A (en) * 2008-09-12 2009-01-21 福州大学 Microflow control chip electrochemical detection device capable of accurately controlling electrode distance
CN202814909U (en) * 2012-10-29 2013-03-20 黑龙江八一农垦大学 Inter-electrode distance adjustable electrolytic bath
CN102944593A (en) * 2012-11-05 2013-02-27 上海大学 Miniature regulated electrolysis device
CN204536262U (en) * 2015-03-09 2015-08-05 扬州工业职业技术学院 A kind of electrolytic cell three-electrode system position adjustable spiral clamp device
CN205139078U (en) * 2015-11-20 2016-04-06 山西大同大学 Three electrode system fixing device with adjustable

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112986111A (en) * 2019-12-13 2021-06-18 中国科学院大连化学物理研究所 Catalytic wet oxidation corrosion experiment device
CN111024604A (en) * 2019-12-19 2020-04-17 韦正楠 Corrosion and scaling experiment detection system and method for geothermal water heat exchange process
CN113834765A (en) * 2020-06-08 2021-12-24 中国石油化工股份有限公司 Device and method for testing corrosion resistance of material
CN112213256A (en) * 2020-10-09 2021-01-12 西南石油大学 Testing arrangement of bacterium to steel corrosion influence under oil gas pipeline cathodic polarization

Also Published As

Publication number Publication date
CN105806774B (en) 2018-07-03
CN105806774A (en) 2016-07-27
CN108519324B (en) 2020-05-08
CN108680491B (en) 2020-05-08
CN108519324A (en) 2018-09-11

Similar Documents

Publication Publication Date Title
CN105806774B (en) High-temperature high-pressure dynamic electrochemical test experimental device and test method
CN104515730B (en) HTHP monitors dissolved oxygen, pH buffering agent evaluation apparatus and detection method in real time
CN104515732B (en) A kind of test metal material device of hydrogen penetrating quality under liquid high pressure
CN104897490B (en) High Pressure Hydrogen penetration kinetics test device and method of testing
CN103424313B (en) In-situ tensile and hydrogen content monitoring device, and method for monitoring content of hydrogen by using same
CN207764151U (en) A kind of explosive parameters test device
CN205679515U (en) HTHP dynamic electric test chemical experimental provision
CN105954186A (en) Metal welded joint position couple corrosion determination apparatus and determination method thereof
CN102519833A (en) Complete immersion type online vacuum stability tester
CN201425578Y (en) Electrochemical behavior in dynamic liquid media test device
CN105136845B (en) The transient state Hot-strip Method measurement apparatus and method of solid powder thermal conductivity factor
CN103926299B (en) Gas sensor
CN107677593B (en) Corrosion test device and test method under heat insulation layer
CN106124565B (en) A kind of sealing fixation measuring device for measuring tight rock impedance characteristic
CN104931561B (en) It is a kind of to realize the electrochemical test experiment device of acoustic emission monitor(ing) under HTHP water environment
CN103822962B (en) A kind of solid-state proton conductor measures the device and method of material PCT curve
CN109443996B (en) Device and method for sensitively detecting membrane permeation pressure value in membrane distillation process
CN206804575U (en) The online moisture measurement apparatus of polyurethane
CN109612919A (en) A method of for detecting galvanic couple type atmospheric corrosion sensor
RU2326374C1 (en) Cell for measuring electrochemical properties of quick and flexible water saturated media
CN203365579U (en) Apparatus for measuring electrical parameters of natural gas hydrate in deposit
CN115468904B (en) High pressure dense phase CO 2 In-situ electrochemical and corrosion testing device and method in wet gas environment
CN110376121A (en) The thin liquid film system corrosion electrochemical test system and method for controllable temperature pressure-bearing
CN112540109A (en) Method and device for synchronously calculating hydrogen evolution amount during electrochemical test
CN206497017U (en) A kind of corrosion electrochemical test system

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CP02 Change in the address of a patent holder
CP02 Change in the address of a patent holder

Address after: 300452 Binhai Industrial Research Institute Campus of Tianjin University, No. 48 Jialingjiang Road, Binhai New Area, Tianjin

Patentee after: Tianjin University

Address before: 300072 Tianjin City, Nankai District Wei Jin Road No. 92

Patentee before: Tianjin University