CN111380910A - Device for testing critical explosion temperature of explosive substance solution - Google Patents

Device for testing critical explosion temperature of explosive substance solution Download PDF

Info

Publication number
CN111380910A
CN111380910A CN202010378147.XA CN202010378147A CN111380910A CN 111380910 A CN111380910 A CN 111380910A CN 202010378147 A CN202010378147 A CN 202010378147A CN 111380910 A CN111380910 A CN 111380910A
Authority
CN
China
Prior art keywords
temperature
hole
valve
explosion
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
CN202010378147.XA
Other languages
Chinese (zh)
Other versions
CN111380910B (en
Inventor
曹雄
曹小青
薛仲卿
胡立双
胡双启
张建忠
崔超
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.)
North University of China
Original Assignee
North University of China
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 North University of China filed Critical North University of China
Priority to CN202010378147.XA priority Critical patent/CN111380910B/en
Publication of CN111380910A publication Critical patent/CN111380910A/en
Application granted granted Critical
Publication of CN111380910B publication Critical patent/CN111380910B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N25/00Investigating or analyzing materials by the use of thermal means
    • G01N25/50Investigating or analyzing materials by the use of thermal means by investigating flash-point; by investigating explosibility
    • G01N25/54Investigating or analyzing materials by the use of thermal means by investigating flash-point; by investigating explosibility by determining explosibility

Landscapes

  • Physics & Mathematics (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • General Physics & Mathematics (AREA)
  • Immunology (AREA)
  • Pathology (AREA)
  • Investigating Strength Of Materials By Application Of Mechanical Stress (AREA)

Abstract

The invention belongs to the technical field of explosive safety, and provides a device for testing the critical explosion temperature of an explosive substance solution. The problem that the explosion limit moisture of the existing test water-containing liquid mixture has great influence on the result and the problem that the test result is meaningless because the components of steam and the components of a naturally volatile gas phase of the liquid mixture during production, storage, transportation and use are obviously different during the test are solved. The test result is accurate, and the method has practical guiding significance.

Description

Device for testing critical explosion temperature of explosive substance solution
Technical Field
The invention belongs to the technical field of explosive safety, and particularly relates to a device for testing the thermal safety of an explosive substance, in particular to a device for testing the critical explosion temperature of an explosive mixed substance containing one or more impurities in different solvents with different concentrations under a high-temperature and high-pressure state, and particularly relates to a device for testing the critical explosion temperature of an explosive substance solution in a simulated actual production process.
Background
At present, research on explosive substances mainly focuses on processes of synthesis, refinement, production and the like based on thermal decomposition behaviors in a solid phase and a gas phase and mechanisms thereof, in the actual production process, the processes of synthesis, preparation, purification and the like of most explosive substances are carried out in solution, and the explosive substances have different thermal safety performances in different solvents, so that the thermal stability of the solution can be changed under different temperatures and pressures under the stimulation and influence of external factors, and the danger degrees are different.
Taking ammonium nitrate as an example, the ammonium nitrate is used as a common fertilizer and an industrial raw material and is also a main component of industrial energetic materials (such as explosives, solid propellants and the like). The ammonium nitrate chemical substances have thermal instability, and can be thermally decomposed to generate toxic nitrogen oxide smoke under different temperature environments and under the conditions of violent impact, friction, vibration and the like, and particularly form a strong oxidizing mixture when the ammonium nitrate chemical substances are subjected to an acidic environment or the synergistic action of substances such as chlorides, organic oils and the like, so that the ammonium nitrate chemical substances cause fire disasters and further induce the increase of explosion risks. Ammonium nitrate is a representative substance of the nitramine-type hazardous chemicals, and pure ammonium nitrate has relatively safe and stable performance compared with other hazardous chemicals.
At present, most of domestic and foreign safety standards only stipulate the danger of solid ammonium nitrate, but neglect the instability and the danger of ammonium nitrate solution. The explosion accidents of ammonium nitrate and ammonium nitrate explosives in recent years show that ammonium nitrate is a typical dangerous substance which has low accident probability in theory but frequently occurs in actual accidents.
Ammonium nitrate is stable at normal temperature, but with the increase of temperature and the action of certain impurities, the physical and chemical properties of the ammonium nitrate can be seriously influenced or changed, and even the instability or explosion of the system can be caused. The ammonium nitrate stored in a pile for a long time is a poor heat dissipation system, and if the heat generated by the slow self-decomposition reaction cannot be dissipated, the slow self-heating decomposition can be caused. Once a certain impurity is mixed therein, the local reaction is highly likely to further raise the temperature of the system, while promoting the progress of the existing self-decomposition reaction which is not perceived, and may induce thermal explosion of ammonium nitrate. As ammonium nitrate is used in the manufacture of industrial explosives, a number of varieties of ammonium nitrate explosives, "faviet" explosives, aluminum-containing ammonium nitrate explosives, ammonium nitrate fuel oil explosives, and the like have been developed. In many cases, ammonium nitrate is in a high-temperature and high-concentration aqueous solution state in industrial production, and the explosion accident of the ammonium nitrate is caused to a certain extent by the aqueous solution of the ammonium nitrate.
In fact, the research work on the thermal safety of the explosive material solution is less developed, and the condition and mechanism of explosion are not well known, and an important factor is that the vapor pressure of the solvent is very high at a high temperature, so that a proper testing device and a research means are not available, and further the development of the explosive material production and the related technical field is restricted.
Disclosure of Invention
The invention aims to provide a device for testing the critical explosion temperature of an explosive substance solution, in particular to a device for testing the critical explosion temperature of an explosive mixed substance containing one or more impurities in solvents with different concentrations.
In order to solve the problems, the technical scheme adopted by the invention is as follows: the utility model provides a critical explosion temperature testing arrangement of explosive substance solution, including heating system, be equipped with the explosion container in heating system, connect pressure sensor on the explosion container, the explosion container passes through the solenoid valve and connects superhigh pressure relief device, superhigh pressure relief device connects the relief pressure valve, little negative pressure reservoir is connected to the relief pressure valve, gas chromatograph is connected to little negative pressure reservoir, be equipped with temperature sensor and heating system temperature control sensor in the survey container in the explosion container, heating system temperature control sensor, temperature sensor connects the temperature controller in the survey container, heating system temperature control sensor, temperature sensor and pressure sensor connect the computer in the survey container.
The explosion container comprises a barrel body and a barrel cover, wherein an annular groove is formed in the upper surface of the barrel body, a circular truncated cone with the size consistent with that of the annular groove is arranged on the lower surface of the barrel cover, the barrel body is connected with the barrel cover through a bolt, and the circular truncated cone is inserted into the annular groove to form a closed space;
a temperature measuring hole of a temperature control sensor is arranged in the barrel of the explosion container; a first temperature measuring hole, a second temperature measuring hole and an exhaust hole are formed in the barrel cover, and a protective sleeve is arranged at the lower part of the second temperature measuring hole; after the cylinder body is connected with the cylinder cover, the temperature control sensor is communicated with the first temperature measuring hole and used for accommodating the temperature control sensor of the heating system, and a temperature sensor for measuring the temperature in the container is inserted in the second temperature measuring hole; the lower end of the exhaust hole is provided with a first exhaust valve, and the upper end of the exhaust hole is provided with a second exhaust valve;
the first exhaust valve comprises a central column body and a platform body, a first through hole is formed in the central column body of the first exhaust valve, a second through hole is formed in the platform body, and the first through hole is communicated with the second through hole; the central column body is provided with external threads, the lower end of the exhaust hole is provided with a clamping hole, the clamping hole is provided with internal threads, and the central column body is inserted into the clamping hole;
two discharge valve including the connection platform of disk seat and lower part, the disk seat with connect the platform middle part and be exhaust passage, connect the platform and be equipped with the external screw thread, be equipped with the card hole on the exhaust hole, the internal thread is established in the card hole, connect the platform and insert card downthehole, be connected with the pressure release pipe on the disk seat, be equipped with pressure sensor and solenoid valve on the pressure release pipe, ultrahigh pressure relief device is connected to the pressure release pipe.
The wall thickness of the cylinder body of the explosion container is not less than 30mm, the diameter of the outer wall of the explosion container is not more than 100mm, the diameter of the inner wall of the explosion container is not more than 40mm, and the depth of the inner cylinder of the explosion container is not less than 70 mm; the thickness of the cylinder cover is not less than 30 mm; one diameter of the temperature measuring hole is not more than 5mm, and the diameter of the second temperature measuring hole is not more than 5 mm; the wall thickness of the protective sleeve is not less than 3mm, and the length of the protective sleeve is 60 mm; the diameter of the vent hole is 1 mm.
Superhigh pressure relief device including pressure release section of thick bamboo and pressure release cover, pressure release bobbin base center is inlet channel, the inlet channel upper end is equipped with interior valve, interior valve upper end is equipped with movable valve gap, establish reset spring between interior valve and the movable valve gap, movable valve gap upper end is the taper, the awl top is globular, be equipped with the exhaust hole on the pressure release cover, the exhaust hole lower extreme is equipped with the inner tube, the lower mouth of a river and the contact of awl top spheroid of inner tube, be equipped with movable valve plate inside the pressure release section of thick bamboo, and the movable valve plate cover locates the inner tube outside, be equipped with the spring between movable valve plate and pressure release cover, be equipped with the locator card at pressure release section of thick bamboo inner wall, be equipped with relief valve (1.2 MPA) and pressure release valve (.
The testing device further comprises a protection device, and the heating system, the explosion container, the ultrahigh pressure relief device and the pressure reducing valve are all located in the protection device. The protection device is a steel shell. The explosion container is made of titanium alloy materials, is in a cylindrical shell shape, and has the capacity of 20ml and the pressure bearing capacity of 20 MPa.
A critical explosion temperature test method of an explosive substance solution adopts the test device of the critical explosion temperature of the explosive substance solution to test the critical explosion temperature of the explosive substance solution, and the test device mainly comprises an explosion container, a heating and temperature control device, a temperature measurement sensor, a safety protection box and a data acquisition system; the explosion container comprises an explosion tank body and a sealing cover, the explosion tank body and the sealing cover are connected through an interface bolt, and a temperature measurement sensor hole is formed in the side wall of the explosion tank body; the sealing cover is provided with a pressure relief hole, a temperature measuring sensor hole and a pressure sensor, and a protective shell is arranged at the lower side of the temperature measuring sensor hole; the heating and temperature control device comprises a heating furnace and a temperature controller, and the temperature controller is adjusted through a computer program to realize different heating rates of the heating furnace.
Adding an explosive substance solution sample into an explosion tank body of an explosion container of the testing device, placing a sealing cover and the explosion tank body into a heating furnace after the sealing cover is hermetically connected with the explosion tank body by using bolts and gaskets, placing the explosion container and the heating furnace on a platform in a safety protection box, closing an explosion door, installing a heating system temperature control sensor and a temperature sensor in a measuring container, and adjusting a temperature controller by a computer program to realize different heating rates of the heating furnace;
the temperature in the explosive tank body can be observed in real time by using the data acquisition system through the computer display, when the temperature rises to a certain critical value, the explosive substance solution generates violent reaction, and a singular point appears on the temperature curve of the data acquisition system, so that the critical explosion temperature of the explosive substance solution can be measured.
The invention well solves the problems that the explosion limit moisture of the aqueous liquid mixture tested by the existing testing instrument has great influence on the test result and the test result is meaningless because the steam component and the natural volatile gas-phase component of the liquid mixture in the processes of production, storage, transportation and use are obviously different during the test. The test result is accurate, and the method has more guiding significance for actual production and life.
Drawings
FIG. 1 is a schematic diagram of a critical explosion temperature testing device for an explosive material solution according to the present invention; FIG. 2 is a block diagram of the barrel of the explosive container; FIG. 3 is a schematic view of the structure of the cover of the explosion container; FIG. 4 is a partial view A of FIG. 3; FIG. 5 is a view of part B of FIG. 3; FIG. 6 is a schematic view of an ultra-high pressure relief device; FIG. 7 is a partial view A of FIG. 6; FIG. 8 is a temperature acquisition image; fig. 9 is a pressure acquisition image.
In the figure: 1-a heating system; 2-an explosive container; 3-measuring the temperature sensor in the container; 4-heating system temperature control sensor; 5-a pressure sensor; 6-electromagnetic valve; 7-an ultrahigh pressure relief device; 8-a pressure reducing valve; 9-a guard; 10-micro negative pressure air storage chamber; 11-gas chromatography; 12-a temperature controller; 13-a computer; 14-temperature measuring hole of temperature control sensor; 15-an annular groove; 16-upper bolt holes; 17-a first temperature measuring hole; 18-a vent hole; 19-a second temperature measuring hole; 20-lower bolt holes; 21-protective sleeve; 22-a circular truncated cone; 23-a clamping hole; 24-a central cylinder; 25-a second through hole; 26-a table body; 27-a first through hole; 28-pressure relief pipe; 29-valve seat; 30-a connection station; 31-an inner tube; 32-a locator card; 33-pressure relief cylinder cover; 34-a pressure relief cylinder; 35-upper pressure relief valve; 36-a compression spring; 37-a movable valve plate; 38-lower relief valve; 39-inner valve; 40-a movable valve cover; 41-an intake passage; 42-return spring.
Detailed Description
As shown in fig. 1, a critical explosion temperature testing device for an explosive material solution, which comprises a heating system 1, an explosion container 2 is arranged in the heating system 1, the explosion container 2 is connected with a pressure sensor 5, the explosion container 2 is connected with an ultrahigh pressure relief device 7 through an electromagnetic valve 6, the ultrahigh pressure relief device 7 is connected with a pressure reducing valve 8, the pressure reducing valve 8 is connected with a micro-negative pressure air storage chamber 10, the micro-negative pressure air storage chamber 10 is connected with a gas chromatograph 11, a temperature sensor 3 and a heating system temperature control sensor 4 are arranged in the explosion container 2, the heating system temperature control sensor 4, the temperature sensor 3 in the measurement container is connected with a temperature controller 12, the heating system temperature control sensor 4, the temperature sensor 3 in the measurement container and the pressure sensor 5 are connected.
The testing device further comprises a protection device 9, and the heating system 1, the explosion container 2, the ultrahigh pressure relief device 7 and the pressure reducing valve 8 are all located in the protection device 9. The protective device 9 protects the test person well in case of an explosion of one of the components. The guard 9 may be a steel housing.
As shown in fig. 2 and 3, the explosion container 2 includes a cylinder and a cylinder cover, an annular groove 15 is formed in the upper surface of the cylinder, a circular truncated cone 22 with the same size as the annular groove is formed in the lower surface of the cylinder cover, the cylinder and the cylinder cover are connected through a bolt, the circular truncated cone 22 and the annular groove 15 are inserted to form a closed space, and the diameter of the bolt is not less than 7 mm.
The wall thickness of the cylinder body of the explosion container 2 is not less than 30mm, the diameter of the outer wall is not more than 100mm, the diameter of the inner wall is not more than 40mm, the depth of the inner cylinder is not less than 70mm, a temperature measuring hole 14 of a temperature control sensor is arranged in the cylinder body, the thickness of the cylinder cover is not less than 30mm, a first temperature measuring hole 17, a second temperature measuring hole 19 and an exhaust hole 18 are arranged on the barrel cover, the diameter of the first temperature measuring hole 17 is not more than 5mm, the diameter of the second temperature measuring hole 19 is not more than 5mm, a protective sleeve 21 is arranged at the lower part of the second temperature measuring hole 19, the wall thickness of the protective sleeve 21 is not less than 3mm, the length of the protective sleeve 21 is 60mm, the diameter of the exhaust hole 18 is 1mm, after the cylinder body and the cylinder cover are connected, the temperature measuring hole 14 of the temperature control sensor is communicated with the first temperature measuring hole 17, used for accommodating a heating system temperature control sensor 4, a temperature sensor 3 in the measuring container is inserted in the second temperature measuring hole 19, the lower end of the exhaust hole 18 is provided with a first exhaust valve, and the upper end of the exhaust hole 18 is provided with a second exhaust valve.
As shown in FIG. 4, the first exhaust valve includes a central column 24 and a platform 26, a first through hole 27 is formed in the central column 24 of the first exhaust valve, a second through hole 25 is formed in the platform 26, and the first through hole 27 is communicated with the second through hole 25. The central column body 24 is provided with external threads, the lower end of the exhaust hole is provided with a clamping hole 23, the clamping hole 23 is provided with internal threads, and the central column body 24 is inserted into the clamping hole 23.
As shown in fig. 5, the two exhaust valves include a valve seat 29 and a lower connecting platform 30, the middle parts of the valve seat 29 and the connecting platform 30 are exhaust passages, the connecting platform 30 is provided with external threads, a clamping hole is formed in the upper end of the exhaust hole, an internal thread is formed in the clamping hole, the connecting platform 30 is inserted into the clamping hole, a pressure relief pipe 28 is connected to the upper end of the valve seat 29, a pressure sensor 5 and an electromagnetic valve 6 are arranged on the pressure relief pipe 28, and the pressure relief pipe 28 is connected with the ultrahigh pressure device.
As shown in fig. 6 and 7, the ultrahigh pressure relief device 7 includes a pressure relief cylinder 34 and a pressure relief cylinder cover 33, an air inlet channel 41 is arranged at the center of the bottom of the pressure relief cylinder, an inner valve 39 is arranged at the upper end of the air inlet channel 41, a movable valve cover 40 is arranged at the upper end of the inner valve 39, a return spring 42 is arranged between the inner valve 39 and the movable valve cover 40, the upper end of the movable valve cover 40 is tapered, the top of the tapered portion is spherical, an air outlet hole is arranged on the pressure relief cylinder cover 33, an inner tube 31 is arranged at the lower end of the air outlet hole, the lower pipe orifice of the inner tube 31 is in contact with the tapered spherical body, a movable valve plate 37 is arranged inside the pressure relief cylinder 34, the movable valve plate 37 is sleeved outside the inner tube 31, a compression spring 36 is arranged between the movable valve plate 37 and the pressure relief cylinder cover 33, a positioning clamp 32 is arranged on the inner wall of the.
The working process is as follows: after the tested substance in the explosion container explodes, high-pressure gas needs to enter the pressure relief tube 34, the electromagnetic valve on the pressure relief tube 28 is opened, the gas firstly enters the inner valve 39 to jack the movable valve cover 40, the upper end of the movable valve cover 40 blocks the opening of the inner tube 31, the high-pressure gas enters the pressure relief tube 34 from the gap between the inner valve 39 and the movable valve cover 40, then the gas expands to push the movable valve plate 37 to ascend, after the gas expands, the pressure is reduced, the movable valve cover 40 falls, the inner tube 31 is conducted, and the gas is discharged through the inner tube 31. At this time, the gas is still at a certain pressure, is further decompressed by the decompression valve 8, is introduced into the micro negative pressure gas storage chamber, and is finally introduced into the gas chromatograph.
The apparatus used in the present invention is a sealed explosive container designed according to 10g TNT equivalent:
1. calculating the thickness of the cylinder of the container, namely calculating the transient load generated by explosion in the container by a plurality of methods, taking the maximum loading of the container as 10g TNT equivalent and the maximum external dimension as phi 100 × 100mm as an example,
(1) determination of incident overpressure: calculated as TNT equivalent of 0.01 kg, takingR=0.05m, then:
Figure 40386DEST_PATH_IMAGE001
(ii) a When in use
Figure 645942DEST_PATH_IMAGE002
And when the voltage is 0.05-0.3, calculating the incident overpressure by adopting a Fesef-Henge formula:
Figure 425680DEST_PATH_IMAGE003
(2) reflection overpressure:
Figure 820889DEST_PATH_IMAGE004
(3) equivalent static load:
A. determination of the power coefficient: required power coefficientC d The action time of the reflected overpressure must be calculatedt 1And the self-oscillation period T of the container:
Figure 572944DEST_PATH_IMAGE005
will be provided withRSubstitution of =0.02 can result:t 1=4.536×10-6s; in the formula:Ris the vessel shell radius (m);Q 0detonation heat per unit mass (J/Kg), η is an empirical coefficient, η =0.5 for column symmetry, for TNTQ 0=4860874.8 J/Kg。
Figure 395407DEST_PATH_IMAGE006
(ii) a When will beRSubstitution of =0.02m gives:T=2.445×10-5(ii) a In the formula (I), the compound is shown in the specification,Eis Young's modulus;ρis the density (Kg/m) of the shell material3);RA vessel shell radius (m); when the material of the container is 16MnR,E=206GPa,ρ=7.8×103Kg/ m3t 1/T=0.186 < 3/8=0.375, willω=2π/T=2.57×105ωt 1=1.165 substitutes the following equation:
Figure 662440DEST_PATH_IMAGE007
B. equivalent static load:
Figure 48291DEST_PATH_IMAGE008
(ii) a And in the structural design process, taking the equivalent static load of 60 MPa to calculate the subject structure.
(4) Calculating the wall thickness of the container body: according to JB4732-1995 design Standard of stress analysis method for Steel pressure vessel
Figure 654853DEST_PATH_IMAGE009
The method comprises the following steps:
Figure 648216DEST_PATH_IMAGE010
(ii) a In the formula (I), the compound is shown in the specification,
Figure 402546DEST_PATH_IMAGE011
is the inner diameter of the container;
Figure 816254DEST_PATH_IMAGE012
is the equivalent static load;
Figure 339640DEST_PATH_IMAGE013
designing the stress intensity;for the load combination coefficient, 1.0 was taken.
For 16MnR steel fullThe minimum thickness required by sufficient rigidity is 7.5-25 mm, and the minimum thickness is takenδ minIs 25 mm. Negative biasC 1=1.0mm, corrosion marginC 2=2.0mm, the additional amount of wall thicknessCC=C 1+C 2=3 mm。
Designed thicknessδ d δ d =δ+C 2=11.2+2= 13.2mm。
Determining the wall thickness of the cylinderδ e δ e =δ min+C=25+3=28mm>δ d =13.2 mm; finally, the wall thickness of the cylinder body is taken to be 30 mm.
(5) Maximum allowable working pressure and wall thickness verification:
a. calculation of the stress of the cylinder at the design temperature:
Figure 769484DEST_PATH_IMAGE014
b. maximum allowable working pressure:
Figure 948793DEST_PATH_IMAGE015
(ii) a In the formula (I), the compound is shown in the specification,D i is the inner diameter of the container; [σ]tThe allowable stress of the cylinder material at the design temperature is obtained;φtaking 1.0 as welding joint coefficient;δ e for processing the wall thickness of the cylinder.
2. Design of the end socket (cylinder cover): a flat plate end socket is adopted, and the calculation method is as follows:
Figure 223916DEST_PATH_IMAGE016
(ii) a In the formula:p edesigned pressure, MPa;φtaking the value of 1 as a welding coefficient;D eis the effective diameter of the end socket, 100 mm; [σ]tThe yield limit of the 16Mn R steel at 300 ℃ is 135 MPa;Kthe flat cover coefficient is 0.25;δ pis the thickness of the end socket, mm. Based on the above calculation results, the circular flat plate designed hereinThe thickness of the seal head is 35 mm.
3. A pressure pipeline:
Figure 867387DEST_PATH_IMAGE017
in the formula (I), the compound is shown in the specification,D 0is the outer diameter of the pipeline;δthe wall thickness of the pipeline;σ staking 16MnR as 350MPa for yield limit;σ btaking the 16MnR as 520MPa for tensile strength; wherein the content of the first and second substances,
Figure 389504DEST_PATH_IMAGE018
in the above technical solution, preferably, the entire explosion container is made of a titanium alloy material or a high-temperature-resistant and corrosion-resistant material embedded in an inner wall thereof.
In the above technical solution, preferably, a proper amount of the test mixture is taken before ignition to analyze the concentration of the mixture.
A method for testing the critical explosion temperature of the solution of explosive substance includes such steps as putting the substance to be tested and the solution in the cylinder of explosion container, sealing the cylinder by cover, putting it in heating furnace, installing the temp-control sensor of heating system and the temp-sensor in container, and regulating temp-controller by computer program to realize different temp-raising rates of heating furnace. Place explosion container and heating furnace on safety protection box inner platform and close the explosion vent, the rate of rise of temperature of the adjustable heating furnace of utilization temperature controller, but use data acquisition system to pass through computer display real-time observation explosion tank internal temperature and pressure, when the temperature rises to certain critical value, explosive material solution takes place violent reaction, the singular point appears in data acquisition system temperature curve, can survey the critical explosion temperature of this explosive material solution, then start the solenoid valve, make high-pressure gas pass through superhigh pressure relief device pressure reduction, the rethread relief valve makes gas pressure further reduce, at last leading-in little negative pressure reservoir, reentrant gas chromatograph carries out composition analysis. Furthermore, the explosion container is made of titanium alloy materials, is in a cylindrical shell shape, and has the capacity of 20ml and the pressure bearing capacity of 20 MPa.
Experimental example: initial parameters: the sample to be tested was selected to be a 5% solution of HNS (hexanitrostilbene) -acetone containing 0.5g of HNS and 9.5g of acetone. The design requirement is as follows: the designed explosion container has the advantages that after a measured object is gradually heated to explode, the sealing cover and the pressure-bearing tank are free of deformation and cracks, and the sensor is free of damage.
The testing steps are as follows: adding a sample into an explosion container under normal pressure; connecting all parts of the device, setting initial temperature and heating rate, and recording the internal temperature of different moments in real time by an acquisition system; starting heating; the acquisition system records the internal temperature at different moments in real time; and observing whether flame propagates.
The measurement process comprises the following steps: HNS and acetone are put into a closed pressure device, a 2mm asbestos gasket is put between a sealing cover and a cylinder body, and the sealing cover and the cylinder body are connected and fixed through bolts, so that the tightness of the cylinder body is good; the pressure sensor is connected with a pressure sensor threaded interface on the top of the sealing cover, and a raw adhesive tape is wound between threads to keep good tightness; and then putting the closed pressure gauge into a heating furnace, inserting the two temperature sensors into the sensor holes on the top of the sealing cover, and finishing the preparation work. The power supply is turned on, the heating rate is adjusted to 3 ℃/min, the initial temperature is set to be 20 ℃, and the maximum heating temperature is set to be 400 ℃. The temperature recording software was then turned on to record the temperature data. The critical explosion temperature of the HNS-acetone solution obtained by the experiment is 299.7 ℃, the critical explosion pressure is 8MPa, and the experimental data acquisition is shown as the temperature acquisition image in figure 8 and the pressure acquisition image in figure 9.

Claims (7)

1. A critical explosion temperature testing device for explosive substance solution is characterized in that: including heating system (1), be equipped with explosion container (2) in heating system (1), connect pressure sensor (5) on explosion container (2), explosion container (2) are through solenoid valve (6) connection superhigh pressure relief device (7), superhigh pressure relief device (7) are connected relief pressure valve (8), little negative pressure reservoir (10) are connected in relief pressure valve (8), gas chromatograph (11) are connected in little negative pressure reservoir (10), be equipped with in explosion container (2) survey container temperature sensor (3) and heating system temperature control sensor (4), survey container temperature sensor (3) and connect temperature controller (12), heating system temperature control sensor (4), survey container temperature sensor (3) and pressure sensor (5) and connect computer (13).
2. The device for testing the critical explosion temperature of an explosive material solution according to claim 1, wherein: the explosion container (2) comprises a cylinder body and a cylinder cover, wherein an annular groove (15) is formed in the upper surface of the cylinder body, a circular truncated cone (22) with the size consistent with that of the annular groove is arranged on the lower surface of the cylinder cover, the cylinder body and the cylinder cover are connected through bolts, and the circular truncated cone (22) and the annular groove (15) are spliced to form a closed space;
a temperature measuring hole (14) of a temperature control sensor is arranged in the barrel of the explosion container (2);
a first temperature measuring hole (17), a second temperature measuring hole (19) and an exhaust hole (18) are arranged on the barrel cover, and a protective sleeve (21) is arranged at the lower part of the second temperature measuring hole (19);
after the barrel body is connected with the barrel cover, the temperature control sensor (14) is communicated with the first temperature measuring hole (17) and used for accommodating the heating system temperature control sensor (4), and the temperature sensor (3) in the measuring container is inserted into the second temperature measuring hole (19);
a first exhaust valve is arranged at the lower end of the exhaust hole (18), and a second exhaust valve is arranged at the upper end of the exhaust hole (18);
the first exhaust valve comprises a central cylinder (24) and a platform body (26), a first through hole (27) is formed in the central cylinder (24) of the first exhaust valve, a second through hole (25) is formed in the platform body (26), and the first through hole (27) is communicated with the second through hole (25);
the central column body (24) is provided with external threads, the lower end of the exhaust hole (18) is provided with a clamping hole (23), the clamping hole (23) is provided with internal threads, and the central column body (24) is inserted into the clamping hole (23);
discharge valve two include disk seat (29) and lower part connect platform (30), disk seat (29) and connect platform (30) middle part for exhaust passage, it is equipped with the external screw thread to connect platform (30), be equipped with the card hole on exhaust hole (18), the internal thread is established in the card hole, it is downthehole to connect platform (30) to insert the card, be connected with pressure release pipe (28) on disk seat (29), be equipped with pressure sensor (5) and solenoid valve (6) on pressure release pipe (28), superhigh pressure relief device (7) is connected in pressure release pipe (28).
3. The device for testing the critical explosion temperature of an explosive material solution according to claim 1, wherein: the ultrahigh pressure relief device (7) comprises a pressure relief cylinder (34) and a pressure relief cylinder cover (33), the center of the bottom of the pressure relief cylinder (34) is provided with an air inlet channel (41), the upper end of the air inlet channel (41) is provided with an inner valve (39), the upper end of the inner valve (39) is provided with a movable valve cover (40), a return spring (42) is arranged between the inner valve (39) and the movable valve cover (40), the upper end of the movable valve cover (40) is conical, the top of the cone is spherical, the pressure relief cylinder cover (33) is provided with an exhaust hole, the lower end of the exhaust hole is provided with an inner pipe (31), the lower pipe orifice of the inner pipe (31) is contacted with the cone-top spherical body, a movable valve plate (37) is arranged inside the pressure relief cylinder (34), the movable valve plate (37) is sleeved outside the inner pipe (31), a spring (36) is arranged between the movable valve plate (37) and, an upper pressure relief valve (35) and a lower pressure relief valve (38) are arranged on the wall of the pressure relief cylinder (34).
4. The device for testing the critical explosion temperature of an explosive material solution according to claim 1, wherein: the testing device further comprises a protection device (9), and the heating system (1), the explosion container (2), the ultrahigh pressure relief device (7) and the pressure reducing valve (8) are all located in the protection device (9).
5. The device for testing the critical explosion temperature of an explosive material solution according to claim 4, wherein: the protection device (9) is a steel shell.
6. The device for testing the critical explosion temperature of an explosive material solution according to claim 2, wherein: the wall thickness of the cylinder body of the explosion container (2) is not less than 30mm, the diameter of the outer wall is not more than 100mm, the diameter of the inner wall is not more than 40mm, and the depth of the inner cylinder is not less than 70 mm; the thickness of the cylinder cover is not less than 30 mm; the diameter of the first temperature measuring hole (17) is not more than 5mm, and the diameter of the second temperature measuring hole (19) is not more than 5 mm; the wall thickness of the protective sleeve (21) is not less than 3mm, and the length of the protective sleeve (21) is 60 mm; the diameter of the exhaust hole (18) is 1 mm.
7. The device for testing the critical explosion temperature of an explosive material solution according to claim 2, wherein: the explosion container (2) is made of titanium alloy materials, is in a cylindrical shell shape, and has the capacity of 20ml and the pressure bearing capacity of 20 MPa.
CN202010378147.XA 2020-05-07 2020-05-07 Device for testing critical explosion temperature of explosive substance solution Active CN111380910B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010378147.XA CN111380910B (en) 2020-05-07 2020-05-07 Device for testing critical explosion temperature of explosive substance solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202010378147.XA CN111380910B (en) 2020-05-07 2020-05-07 Device for testing critical explosion temperature of explosive substance solution

Publications (2)

Publication Number Publication Date
CN111380910A true CN111380910A (en) 2020-07-07
CN111380910B CN111380910B (en) 2022-09-16

Family

ID=71214447

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202010378147.XA Active CN111380910B (en) 2020-05-07 2020-05-07 Device for testing critical explosion temperature of explosive substance solution

Country Status (1)

Country Link
CN (1) CN111380910B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112557442A (en) * 2020-12-14 2021-03-26 西安近代化学研究所 Post-combustion effect judgment test method
CN113125490A (en) * 2021-04-08 2021-07-16 北京理工大学 Multi-component liquid energetic material thermal safety parameter measuring device

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4108204A (en) * 1976-05-13 1978-08-22 C. J. Hendry Company Pressure relief valve
US5632297A (en) * 1995-09-26 1997-05-27 Amcast Industrial Corporation Piston-type thermally or pressure activated relief device
JP2002005319A (en) * 2000-06-16 2002-01-09 Bosch Automotive Systems Corp Pressure relief valve
US6354137B1 (en) * 2001-02-09 2002-03-12 The United States Of America As Represented By The Secretary Of The Navy Inertial confinement cylinder for explosive characterization
CN102937603A (en) * 2012-10-19 2013-02-20 中国石油化工股份有限公司 High-temperature high-pressure explosion limit tester, method for determining explosion limit, and application thereof
CN103011243A (en) * 2012-12-01 2013-04-03 中北大学 Preparation method of nano metal oxide and reaction device for preparing nano metal oxide
JP2014190704A (en) * 2013-03-26 2014-10-06 Taiyo Nippon Sanso Corp Combustion/explosion test device
CN104280421A (en) * 2014-10-20 2015-01-14 中国人民解放军总后勤部油料研究所 Fuel explosive performance testing system and fuel explosive performance testing method
CN104749218A (en) * 2015-03-27 2015-07-01 中国石油大学(华东) Device and method for testing explosion properties of flammable gases at ultralow temperature
US20150330631A1 (en) * 2014-05-15 2015-11-19 Tokyo Electron Limited Method for preventing explosion of exhaust gas in decompression processing apparatus
CN208634454U (en) * 2018-07-27 2019-03-22 上海皮尔萨管业有限公司 A kind of pipeline explosion-proof relief valve
CN109975354A (en) * 2019-04-11 2019-07-05 中国矿业大学(北京) Visualize combustible explosion chemical looping reaction process test device and method
CN110940698A (en) * 2018-09-06 2020-03-31 中国石油化工股份有限公司 Explosion limit testing device for difficult-to-volatilize liquid and application thereof

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4108204A (en) * 1976-05-13 1978-08-22 C. J. Hendry Company Pressure relief valve
US5632297A (en) * 1995-09-26 1997-05-27 Amcast Industrial Corporation Piston-type thermally or pressure activated relief device
JP2002005319A (en) * 2000-06-16 2002-01-09 Bosch Automotive Systems Corp Pressure relief valve
US6354137B1 (en) * 2001-02-09 2002-03-12 The United States Of America As Represented By The Secretary Of The Navy Inertial confinement cylinder for explosive characterization
CN102937603A (en) * 2012-10-19 2013-02-20 中国石油化工股份有限公司 High-temperature high-pressure explosion limit tester, method for determining explosion limit, and application thereof
CN103011243A (en) * 2012-12-01 2013-04-03 中北大学 Preparation method of nano metal oxide and reaction device for preparing nano metal oxide
JP2014190704A (en) * 2013-03-26 2014-10-06 Taiyo Nippon Sanso Corp Combustion/explosion test device
US20150330631A1 (en) * 2014-05-15 2015-11-19 Tokyo Electron Limited Method for preventing explosion of exhaust gas in decompression processing apparatus
CN104280421A (en) * 2014-10-20 2015-01-14 中国人民解放军总后勤部油料研究所 Fuel explosive performance testing system and fuel explosive performance testing method
CN104749218A (en) * 2015-03-27 2015-07-01 中国石油大学(华东) Device and method for testing explosion properties of flammable gases at ultralow temperature
CN208634454U (en) * 2018-07-27 2019-03-22 上海皮尔萨管业有限公司 A kind of pipeline explosion-proof relief valve
CN110940698A (en) * 2018-09-06 2020-03-31 中国石油化工股份有限公司 Explosion limit testing device for difficult-to-volatilize liquid and application thereof
CN109975354A (en) * 2019-04-11 2019-07-05 中国矿业大学(北京) Visualize combustible explosion chemical looping reaction process test device and method

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
YUN ZHANG: "Dynamic hazard evaluation of explosion severity for premixed hydrogen–air mixtures in a spherical pressure vessel", 《FUEL》 *
侯秀婷: "硝酸化肥水溶液的临界爆炸温度的测试研究", 《中国优秀博硕士学位论文全文数据库(硕士)工程科技Ⅰ辑》 *
张凯: "有效磷含量对硝酸铵溶液临界爆温的影响规律研究", 《浙江化工》 *
罗帅: "HMX丙酮溶液在不同升温速率下的热爆炸研究", 《爆破》 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112557442A (en) * 2020-12-14 2021-03-26 西安近代化学研究所 Post-combustion effect judgment test method
CN112557442B (en) * 2020-12-14 2023-02-14 西安近代化学研究所 Afterburning effect judgment test method
CN113125490A (en) * 2021-04-08 2021-07-16 北京理工大学 Multi-component liquid energetic material thermal safety parameter measuring device

Also Published As

Publication number Publication date
CN111380910B (en) 2022-09-16

Similar Documents

Publication Publication Date Title
CN111380910B (en) Device for testing critical explosion temperature of explosive substance solution
Schröder et al. Explosion characteristics of hydrogen-air and hydrogen-oxygen mixtures at elevated pressures
CN106198849B (en) It is a kind of for solid propellant combustion rate/combustion temperature test device and its test method
US6354137B1 (en) Inertial confinement cylinder for explosive characterization
CN111380909B (en) Critical explosion temperature testing container for explosive material solution
CN104749218A (en) Device and method for testing explosion properties of flammable gases at ultralow temperature
CN104931531A (en) Method for testing pressure during heating process of explosive and propellant columns
CN109085271B (en) Small-dose thermal explosion gas collecting device and gas analysis method
CN104075948A (en) Test method of tensile and compression strength of explosive under temperature condition higher than 100 DEG C
Prodan et al. Correlation of explosion parameters and explosion type events for preventing environmental pollution
CN106290020B (en) Storage tank implosion multi- scenarios method experiment test device
CN107656031A (en) Gases at high pressure Impulsive load Testing Method of Safety for energetic material
CN107702601A (en) Gel state solid-liquid high-energy fuel bodies of charges dilatancy characterizing method
CN111380911B (en) Device and method for testing critical explosion temperature of explosive substance solution
CN209432674U (en) A kind of test device of packing element
CN110006949A (en) Gas burst experimental provision and method based on product analysis
CN112858386B (en) Critical explosion temperature test container for explosive substance solution
CN106338443B (en) Performance testing device and method for blasting equipment in simulated underwater environment
KR101754081B1 (en) Jig for Explosion &amp; Ignitability Test
CN110660496A (en) Real-time monitoring system for rupture and failure of cladding for high-temperature mandrel test
CN112858386A (en) Critical explosion temperature testing container for explosive material solution
CN206114443U (en) Storage tank implosion multi -field coupling tests testing arrangement
CN111208008A (en) Safety protection method for hydrogen storage cylinder fire test
US4505993A (en) Battery housing
CN112730515A (en) Experimental device and method for coal seam roof rupture and electric explosion

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