CN106290463A - The device of adiabatic calorimetry measurement is carried out under High Temperature High Pressure - Google Patents
The device of adiabatic calorimetry measurement is carried out under High Temperature High Pressure Download PDFInfo
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Abstract
The present invention relates to carry out under a kind of High Temperature High Pressure the device of adiabatic calorimetry measurement, mainly solve prior art there is no the problem carrying out adiabatic calorimetry measuring method under High Temperature High Pressure.The present invention carries out the device of adiabatic calorimetry measurement by using under a kind of High Temperature High Pressure, calorimetric test can be carried out with below 20MPa according to adiabatic model, isothermal pattern below 800 DEG C, course of reaction can be implemented precision control and can Real-time Collection and analytical data, described device includes that central control system, pressure control unit, temperature control unit, the technical scheme of reactor preferably solve the problems referred to above, can be used for carrying out in adiabatic calorimetry measurement under High Temperature High Pressure.
Description
Technical field
The present invention relates to carry out under a kind of High Temperature High Pressure the device of adiabatic calorimetry measurement.
Background technology
The hot blast danger of one concrete technology is evaluated, needs to obtain rate of heat release, thermal discharge, adiabatic temperature rise, thermal insulation
The parameters such as pressure liter, the acquisition of these parameters then must throughput Thermal test.The operational mode of calorimeter include isothermal, dynamically and
Adiabatic.Conventional calorimetry apparatus mainly includes reacting the adiabatic calorimetry instrument such as calorimeter (RC1), accelerating calorimeter (ARC)
(Accelerating Rate Calorimeter and Method of Operation, US4208907), differential scanning amount
Hot instrument (DSC) etc..
For testing by the calorimetric for the purpose of process heat risk assessment, generally require and meet following condition: 1)
Sample size is sufficiently large, to reduce the impact of enlarge-effect；2) because adiabatic model is closer to actual condition heat often and loses
Reaction pattern during control, the data therefore using adiabatic model to measure are more applicable for simulated condition；3) numerous reactions are at height
Carrying out under the operating mode of temperature high pressure, calorimeter is required to simulate this type of maximum conditions；4) technical process may relate to heterogeneous thing
Reaction between matter, it is desirable to have good stirring and sample-adding function；5) the phi factor (thermal inertia factor) of calorimeter should to the greatest extent may be used
Can be low, in order to avoid affect the process that system own temperature raises because of holder absorption heat.To sum up considering, sample size is at 10g level, energy
Enough tolerate a certain degree of High Temperature High Pressure extreme operating condition, have sample-adding agitating function, low phi value adiabatic calorimetry instrument for technique
Hot risk assessment has irreplaceable meaning.
The VSP2 equipment of FAI company of the U.S. can meet the demand to a great extent, therefore becomes hot blast danger and comments
The instrument that valency is important.(Fauske,H.K.,“Emergency Relef Systems(ERS)Design,”Chemical
Engineering Progress,1985,53-56；Fauske,H.K.and Leung,J.C.,”New Experimental
Technique for Characterizing Runaway Chemical Reactions,”Chemical Engineering
Progress,1985,81,39-46.；Askonas,C.F.,Burelbach,J,P.,and Leung,J.C,”The
Versatile VSP2:A Tool for Adiabatic Thermal Analysis and Vent Sizing
Applications,”2000,North American Thermal Analysis Society,28th Annual
Conference.；Advanced reactive system screening tool,US6157009.)
The existing size bag VSP2 that releases is a kind of adiabatic calorimetry instrument based on temperature compensation principle.Its principle is to react
System is placed in adiabatic environment, by heating-wait-search or the operation of isothermal both of which, analogue measurement potential out of control instead
Should be with some chemicals of quantization and the heat of mixture, pressure hazard.VSP2 test is used for imitating multiple out-of-control condition, as lost
Go cooling, lose stirring, charging mistake, reactant pile up the pollution of out of control, material and pyrolytic etc..Test can be an envelope
Carry out under the test cell pattern closed or open, response system vapour pressure or substantial amounts of gas can be escaped and directly survey
Amount.Test data include that temperature and pressure changes, and these data may be directly applied to commercial plant, determines gas chi of releasing
Very little, the design of quenching groove and to other bleed-off system design parameters that management is relevant with process safety.Special owing to which employs
Thin-walled reaction tank, the phi value of equipment can as little as 1.05-1.09, its test result may be directly applied in commercial plant, from
And avoid uninteresting calculating, correct the radiating effect being associated with heavy wall test cell.But the heating efficiency of this instrument
Limited, only allow to be heated to 300 DEG C, the pressure limit upper limit is 1900psi (130bar), for the dangerous work of some High Temperature High Pressure
Condition is inapplicable.
The present invention provides a kind of adiabatic calorimetry method being applicable to high temperature and high pressure condition, makes it more be intended for industrialized unit
Operating environment, the design to elements such as its temperature control system, control pressurer system, reactor and relevant pipe valves adds it
Toleration to extreme operating condition.
Summary of the invention
The technical problem to be solved is to there is no in prior art to carry out adiabatic calorimetry measurement side under High Temperature High Pressure
The problem of method, it is provided that carry out the device of adiabatic calorimetry measurement under a kind of new High Temperature High Pressure.This device has and is capable of high temperature
To the observation of reaction and excellent with real-time sample introduction in advance that be capable of gas, liquid, solid various materials under the extreme condition of high pressure
Point.
For solving the problems referred to above, the technical solution used in the present invention is as follows: carry out adiabatic calorimetry survey under a kind of High Temperature High Pressure
The device of amount, described device includes central control system, pressure control unit, temperature control unit, reactor, described reactor
Built-in reaction tank, reaction tank is connected to air inlet and pipe box is placed in evacuation passageway, temperature sensor, pressure transducer probe is opened
Mouth, solid/liquid injection port, described reaction tank built-in strength magneton, reaction tank is provided around heating unit and heat-insulation unit, logical
Cross heat-insulation unit connecting line, heating power supply connecting line is connected with temperature control unit, and in described reactor, non-metal component is whole
For high temperature resistant material: reactor top uses the seal form of linear contact lay, rely on high accuracy and the fineness of contact surface, reach good
Sealing effectiveness, sealing ring uses metallic graphite carbon to be wound around silk, without plastic material wire in still；Reactor top be provided with rupture disk,
Compensating gas passage, compensate gas passage and be provided with pressure transducer probe, kettle cover is reached obturation effect by fixing bolt occlusion, occlusion
Pressure is higher than 20MPa；It is equipped with thermocouple outside reaction tank sidewall, insulation material and in heat-insulation unit；Outside is led in reactor
All circuits be equipped with sealing structure with still wall intersection；By pass to inside still outside in addition to temperature sensor scheme
All pipelines outside still, first connect cooling system；High-intensity magnetic agitator, pressure control unit it is provided with bottom reactor
Entrance is connected with high-pressure compressor, and pressure control unit outlet is connected with air inlet and the evacuation passageway of reactor, central authorities
Control system is connected with pressure control unit, temperature control unit.
In technique scheme, it is preferable that described device can below 800 DEG C and below 20MPa according to adiabatic model,
Isothermal pattern carries out calorimetric test, it is possible to control accurate to course of reaction enforcement also can Real-time Collection and analytical data；Reaction
Pool wall thickness is 0.2-0.5mm, and described reactor shell is setting of stainless steel 304 or 316L, shell and solder joint and cutting ferrule
Meter pressure is 40MPa, tests being resistant to 20MPa pressure through hydraulic pressure and air pressure.
In technique scheme, it is preferable that magneton has inert material external coating, for metal coating or Organic substance coating,
Selected internal magnetic material needs to avoid high temperature demagnetization.
In technique scheme, it is preferable that cooling system is dividing wall type heat exchanger.
In technique scheme, it is preferable that set on the pipeline that pressure control unit entrance is connected with high-pressure compressor
There is check valve.
In technique scheme, it is preferable that when the pressure reduction of reactor pressure transducer with reaction tank pressure transducer is higher than
After setting value, central control system controls pressure control unit in still by compensating gas passage topping up, indifferent gas
Body is nitrogen.
In technique scheme, it is preferable that central control system passes according to reaction tank temperature sensor, heating system temperature
The signal of sensor, makes system with certain temperature programming, keeps temperature or carry out temperature tracking.
In technique scheme, it is preferable that central control system is embedded on-off control, proportional action, integral action, micro-
Transfer makees the even single-chip microcomputer of pid algorithm, PLC, intelligence instrument, computer, it is possible to the signal gathered is carried out signal conversion, display
And it is controlled signal output according to feedback signal, it is possible to realize temperature, the collection of pressure signal, process and show, and
The behavior of temperature control unit and pressure control unit is adjusted in real time according to feedback signal.
The present invention relates to a kind of adiabatic calorimetry method based on temperature-compensating pattern, main purpose is to evaluate material heat
Stability and simulation reaction are released process.Technological difficulties to be solved by this invention are: 1) how to design heating system and pipe
Valve system, enables devices to be heated to target temperature (room temperature～800 DEG C) according to assigned rate and can tolerate this temperature for a long time；
How to follow the trail of principle by temperature and eliminate heat exchange to simulate adiabatic model；2) how whole system is made to meet 20MPa the highest
The requirement of pressure and how to utilize pressure compensation principle to ensure the thin-walled reaction tank tolerance level to pressure；3) how gas is met
The sample introduction requirement of the several samples such as liquid, liquid-solid, gas-solid, gas-liquid-solid；4) how to carry out real time data by central control system to adopt
Collection and analysis.The invention provides a kind of adiabatic calorimetry measuring method, compared with prior art, the method can be implemented in high temperature
Under the extreme condition of high pressure to reaction observation, it is possible to realize gas, liquid, solid various materials in advance with real-time sample introduction, achieve
Preferably technique effect.
Accompanying drawing explanation
Fig. 1 is the schematic flow sheet of device of the present invention.
In Fig. 1,1 high-pressure compressor；2 check valves；3 pressure control units；4 check valves；5 reactor pressure sensings
Device；6 inlet control valve；7 reaction tank pressure transducers；8 reactor rupture disks；9 reactors；10 high-intensity magnetic agitators；11 is anti-
Answer pond temperature sensor；12 heating system temperature sensors；13 temperature control units；14 central control systems；Solid line represents real
Border pipeline, dotted line represents electric appliance circuits.
Fig. 2 is reactor structural representation.
In Fig. 2,1 air inlet and evacuation passageway；The 2 sealing structures passing still wall；3 reaction tanks；Semi-finals power magneton；5 temperature pass
Sensor places pipe box；6 pressure transducer probes；7 solid/liquid injection ports；8 heat-insulation unit；9 heating units；10 heat-insulation unit
Connecting line；11 heating power supply connecting lines；12 thermocouples being placed on reaction tank sidewall；13 are placed on insulation material external thermal insulation unit
Within thermocouple；14 fix bolt；15 rupture disks；16 still inside thermal conservation materials；17 compensate gas passage；18 pressure transducers are visited
Head.
Fig. 3 is Temperature-time and pressure versus time change curve in residual hydrogenation course of reaction in embodiment 1.
Below by embodiment, the invention will be further elaborated, but is not limited only to the present embodiment.
Detailed description of the invention
[embodiment 1]
The present invention provides a kind of device that can carry out calorimetric test below 800 DEG C with below 20MPa, it is possible to according to absolutely
Heat pattern, isothermal pattern carry out calorimetric measurement, it is possible to control accurate to course of reaction enforcement also can Real-time Collection and analysis number
According to.
This device mainly comprises the following steps (as shown in Figure 1):
Central control system: be typically made up of the computer software of data acquisition card, digital to analog converter and preprogramming.
Pressure control unit: be connected with compensating gas (usually nitrogen) source of the gas, controlled in still by the folding of electromagnetic valve
Compensate pressure；
Temperature control unit: control heating and the start-stop of heat-insulation unit and power so that actual temperature meets setting value；
Reactor (for the intermediate portions of the present invention): inclusive reaction pond, temperature/pressure sensor, heating and heat-insulation unit.
Annexation (numbering described in numbered Fig. 1 of this part) between each unit:
Central control system 14 is connected with pressure control unit 3, temperature control unit 13 respectively, is responsible for receiving each sensor
Signal, after calculation process, adjust pressure control unit 3 and the action of temperature control unit 13.
Pressure control unit 3 is connected with high-pressure compressor 1 by check valve 2, by check valve 4 and reactor 9
Portion is connected, and is regulated and controled by central control system 14, when reactor pressure transducer 5, reaction tank pressure transducer 7 pressure reduction are higher than one
During definite value, central control system 14 controls pressure control unit make-up gas in still.
Temperature control unit 13 is positioned at the heating of reactor 9 and the work of muff heater by changing size of current change
The rate of doing work, under the regulation and control of central control system 14, according to answering pond temperature sensor 11, the letter of heating system temperature sensor 12
Number, make system with certain temperature programming, keep temperature or carry out temperature tracking.
Arranging rupture disk 8 on reactor 9, in still, pressure is detected by reactor pressure transducer 5, and in reaction tank, pressure is by pressing
Force transducer 7 detects, and in pond, temperature is detected by temperature sensor 11, and near the external heat device of pond, temperature is sensed by heating system temperature
Device 12 detects.
1) central control system:
On-off control, proportional action (P), integral action (I), differential action (D) the even list of pid algorithm can be embedded into
Sheet machine, PLC (programmable logic controller (PLC)), intelligence instrument, computer, it is possible to gather signal carry out signal conversion, display with
And it is controlled signal output according to feedback signal.The function being capable of is: to temperature, the collection of pressure signal, process and
Display, and the behavior of temperature control unit and pressure control unit is adjusted in real time according to feedback signal.
2) pressure control unit:
In order to avoid built-in reaction tank changes, due to reaction tank internal pressure, the deformation caused in test process, need dynamic
State reactor inside is carried out pressure compensation, make reaction tank inside and outside differential pressure remain within the specific limits, thus accurately
Test reaction puts thermogenetic pressure.Pressure control unit is made up of some electromagnetic valve for adjustings, with the pressure in central control system
Power control module collectively constitutes control pressurer system.In test process, when reaction tank internal pressure is higher than reaction tank external pressure
During certain value (such as 0.3MPa), control pressurer system automatically turns on pressure compensation electromagnetic valve, control pressurer system controls high pressure
Gas compressor compensates noble gas in reactor, and noble gas isNitrogen or other noble gas；When reaction tank external pressure
Higher than in reaction tank during pressure certain value (such as 0.1MPa), control pressurer system automatically turns on pressure releasing electromagnetic valve, will reaction
Pressure unnecessary in still is laid down, and makes reaction tank inside and outside differential pressure be in all the time in certain limit (such as 0.2-0.3MPa).
3) temperature control unit:
In order to ensure that test is carried out under adiabatic environment, need dynamically to ensure ambient temperature and temperature of reaction system one
Causing, therebetween without heat exchange, system heat does not lose.Therefore, temperature controls common by heating unit and heat-insulation unit
Realize.The function of heating unit is that temperature is rapidly increased to setting value, and this heater power is relatively big, and environment is to body in the process
It it is heat supply.After entering heating-wait-search pattern, once occurring temperature rise in system, environment is heated by heat-insulation system immediately,
Making its temperature keep consistent with system temperature, this heater power is relatively small.Heating and heat-insulation unit constitute temperature and control single
Unit, it collectively forms temperature control system with the temperature control modules in central control system.
4) reactor (as in figure 2 it is shown, numbering described in numbered Fig. 2 of this part):
(1) described reactor shell is stainless steel 304 or 316L, and the design pressure of shell (and solder joint, cutting ferrule) is
40MPa, tests through hydraulic pressure and air pressure and can tolerate 20MPa pressure.
(2) the described built-in reaction tank of reactor still 3, reaction tank size can be adjusted according to sample size, usually
About 100mL cylinder.In order to ensure low phi value, reaction tank wall thickness is at about 0.2mm, and material can be Stainless steel 316 L.
Different number of opening can be welded on reaction tank as required, in order to meet the sample introduction demand of multiclass material, typically at least contain
There is 1 bottom opening in reaction tank upper gaseous phase space for pressure transducer probe 6 insertion, at least contain a bottom
Opening in reaction tank upper gaseous phase space, for being evacuated to vacuum and gas phase sample introduction in experimentation, at least contains one
Opening, for charging before reaction, also should insert for temperature sensor containing a concave inward structure goed deep into bottom reaction tank, this
Can also expand according to demand or reduce number of openings outward.
(3) a preset strength magneton 4 in described reaction tank, magneton has inert material external coating (metal coating or have
Machine thing coating), selected internal magnetic material needs to avoid high temperature demagnetization.
(4) heating unit 9 and heat-insulation unit 8 are placed around reaction tank.
(5) all high temperature resistant materials of non-metal component in described reactor: reactor top uses the sealing shape of linear contact lay
Formula, relies on high accuracy and the fineness of contact surface, reaches good sealing effectiveness.Sealing ring uses metallic graphite carbon to be wound around silk, still
Interior wire without plastic material.
(6) passed to outside all pipelines (except temperature sensor scheme) by inside outside still, first connect cooling system
System, in case high-temperature material is hurted sb.'s feelings.Cooling system is generally dividing wall type heat exchanger, and visual response temperature selects different model, usual feelings
Under condition, jacketed type exchanger can meet requirement.Or, can select and be resistant to the pressure transducer of high temperature and outer connecting portion
Part.
(7) temperature sensor degree and pressure transducer produce analogue signal or digital signal, deliver to carry out outside still signals collecting,
Signal processing and data analysis.
(8) kettle cover by fix bolt 14 occlusion reach obturation effect, on rupture disk 15 is set.
The using method of device is:
Solid and liquid reactants join inside reaction tank by the opening on reaction tank, and this opening is in course of reaction
Remain turned-off.If desired for adding solid or liquid reactants in course of reaction, need this opening by reactor outer wall
Passage be connected with outside material source.
External air source is directly communicated to inside reaction tank by conduit, or passes through in reaction process to control before starting the reaction
On pipeline, the folding of valve adds gas reactant (external air source pressure need to be more than reaction tank internal pressure).
Place reaction tank with after each pipeline that is connected, close reactor top cover.Fix by screw means between two-layer top cover,
Ensure that biting pressure is higher than 20MPa.Top cover is provided with and the pressure transducer come round in still and pipeline, connects and compensates gas source of the gas.
Top cover is provided with rupture disk (or relief valve), and vent pressure can select voluntarily.
Open condenser after screwing top cover, open pressure compensating system, open stirring, start to add by control system
Heat, records data simultaneously.
Utilize this device to carry out residual hydrogenation reaction temperature pressure to investigate
Experimental procedure:
(1) preheating residual oil, makes it flowing, adds in reaction tank；According to oil preparation than weighing the amount of catalyst and adding anti-
Ying Chizhong；The sample size of experiment test is 30g residual oil, the catalyst 4.60g (oil preparation volume ratio 4:1) activated；
(2) heater is installed, reaction tank is put in autoclave, connect feeding line, heater and temperature sensor and lead
Line, reaction tank ground connection, to get rid of signal noise；Glass cotton is filled up in space between reaction tank and autoclave, covers kettle cover, close
Envelope autoclave；
(3) by table test lead connection state and insulating properties, set heating schedule parameter, start VSP system and to temperature
Degree, piezometry system are corrected；
(4) open the electromagnetic valve on vacuum pipeline, start vacuum pump, pressure in autoclave is evacuated to-0.09MPa (g) with
Keep ten minutes after Xia, the air-tightness of trial inspection system；
(5) open gas cylinder valve, it is ensured that air supply system can provide the gas that pressure is more than 10MPa, open pressure automatic
Tracking system；Feeding line accesses hydrogen cylinder, squeezes into hydrogen in reaction tank；Keep ten minutes, check that system is airtight further
Property；
(6) start heating system, start to heat up by setup program.Heating schedule is set to ladder-elevating temperature to 320 DEG C, stable
Start after 15 minutes to test according to " heating-wait-search " pattern.Adiabatic model, heating is entered after heat release being detected
If can't detect heat release, then temperature raises 10 DEG C, enters next one circulation.Start cooling system to protect pressure transducer.Temperature
When degree reaches 150 DEG C, start super magnetic stirring apparatus；
(7) observation experiment pressure, variations in temperature, record experimental phenomena is until experiment terminates；
(8) open autoclave, take out reactor, it is carried out, purges；
(9) derive experimental data, analyze experimental result.
Residual oil adiabatic reaction temperature and pressure test result in a hydrogen atmosphere is carried out as shown in Figure 3 with said apparatus:
Detecting that system starts heat release when 370 DEG C, now system pressure is 4.48Mpa.After entering adiabatic model, the spontaneous intensification of system
To 397 DEG C, pressure rises to 4.93MPa.When temperature is less than 384 DEG C, pressure rises speed and raises with temperature and be increased slightly, and change is not
Greatly, pressure following temperature raises near-linear increase.After 384 DEG C, pressure change is substantially, and pressure raising speed increases with temperature and increases, and presents
Curve uptrending.
The present invention's it is a technical advantage that the adiabatic calorimetry that can carry out under high temperature, high pressure is measured.Compared with VSP, this dress
The resistance to pressure put has been brought up to 20MPa by 5MPa, and thermostability has also brought up to 800 DEG C, and can carry out adiabatic model, isothermal mould
Calorimetric under formula, constant temperature mode and test of releasing.Residual hydrogenation reaction in upper example, is to cannot be carried out in common calorimetry apparatus
Measure.
Claims (8)
1. carrying out a device for adiabatic calorimetry measurement under High Temperature High Pressure, described device includes central control system, Stress control
Unit, temperature control unit, reactor, the built-in reaction tank of described reactor, reaction tank is connected to air inlet and evacuation passageway, temperature
Pipe box placed by degree sensor, pressure transducer pops one's head in opening, solid/liquid injection port, described reaction tank built-in strength magneton, instead
Ying Chi is provided around heating unit and heat-insulation unit, controls single by heat-insulation unit connecting line, heating power supply connecting line with temperature
Unit is connected, all high temperature resistant materials of non-metal component in described reactor: reactor top uses the seal form of linear contact lay, depends on
Being abutted against high accuracy and the fineness of contacting surface, reach good sealing effectiveness, in sealing ring uses metallic graphite carbon to be wound around silk, still, nothing is moulded
Material material wire；Reactor top is provided with rupture disk, compensates gas passage, compensates gas passage and is provided with pressure transducer probe, still
Covering and reached obturation effect by the occlusion of fixing bolt, biting pressure is higher than 20MPa；Reaction tank sidewall, insulation material be outer and Warm keeping sheet
Thermocouple it is equipped with in unit；The all circuits leading to outside in reactor are being equipped with sealing structure with still wall intersection；By still
Inside passes to all pipelines in addition to temperature sensor scheme of outside and first connects cooling system outside still；Polycondensation Reactor and Esterification Reactor
Portion is provided with high-intensity magnetic agitator, and pressure control unit entrance is connected with high-pressure compressor, pressure control unit outlet with
The air inlet of reactor is connected with evacuation passageway, and central control system is connected with pressure control unit, temperature control unit.
The device of adiabatic calorimetry measurement is carried out the most according to claim 1, it is characterised in that described device energy under High Temperature High Pressure
Enough below 800 DEG C, carry out calorimetric test with below 20MPa according to adiabatic model, isothermal pattern, it is possible to course of reaction is implemented
Accurate control also can Real-time Collection and analytical data；Reaction tank wall thickness is 0.2-0.5mm, and described reactor shell is stainless
Steel matter 304 or 316L, the design pressure of shell and solder joint and cutting ferrule is 40MPa, tests being resistant to through hydraulic pressure and air pressure
20MPa pressure.
The device of adiabatic calorimetry measurement is carried out the most according to claim 1, it is characterised in that magneton has lazy under High Temperature High Pressure
Property material overcoat, for metal coating or Organic substance coating, selected internal magnetic material needs to avoid high temperature demagnetization.
The device of adiabatic calorimetry measurement is carried out the most according to claim 1, it is characterised in that cooling system is under High Temperature High Pressure
Dividing wall type heat exchanger.
The device of adiabatic calorimetry measurement is carried out the most according to claim 1, it is characterised in that Stress control list under High Temperature High Pressure
The pipeline that unit's entrance is connected with high-pressure compressor is provided with check valve.
The device of adiabatic calorimetry measurement is carried out the most according to claim 1, it is characterised in that when reactor pressure under High Temperature High Pressure
The pressure reduction of force transducer and reaction tank pressure transducer is higher than after setting value, and central control system controls pressure control unit to still
Interior by compensating gas passage topping up, noble gas is nitrogen.
The device of adiabatic calorimetry measurement is carried out the most according to claim 1, it is characterised in that central authorities control system under High Temperature High Pressure
System, according to reaction tank temperature sensor, the signal of heating system temperature sensor, makes system with certain temperature programming, keeps temperature
Spend or carry out temperature tracking.
The device of adiabatic calorimetry measurement is carried out the most according to claim 1, it is characterised in that central authorities control system under High Temperature High Pressure
System for embedded on-off control, proportional action, integral action, the differential action even single-chip microcomputer of pid algorithm, PLC, intelligence instrument,
Computer, it is possible to the signal gathered is carried out signal conversion, display and is controlled signal output according to feedback signal, it is possible to be real
Now to temperature, the collection of pressure signal, process and show, and adjusting temperature control unit and pressure control according to feedback signal in real time
The behavior of unit processed.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107884435A (en) * | 2017-10-20 | 2018-04-06 | 中国科学院工程热物理研究所 | The device of material thermal conductivity is measured under a kind of high pressure gas environment |
| CN109270119A (en) * | 2018-11-08 | 2019-01-25 | 浙江大学 | A kind of open on-line measurement system of coal dust calorific value and measurement method |
| CN110297011A (en) * | 2019-08-12 | 2019-10-01 | 杭州仰仪科技有限公司 | Calorimetric method is quickly screened in a kind of quasi-adiabatic |
| CN113358685A (en) * | 2020-08-24 | 2021-09-07 | 中海油能源发展股份有限公司 | Temperature compensation system for low-temperature oxidation intelligent detection |
| CN114225971A (en) * | 2021-12-27 | 2022-03-25 | 广东蓝玖新能源科技有限公司 | Automatic activation system and activation process of methanol hydrogen production catalyst |
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| CN107884435A (en) * | 2017-10-20 | 2018-04-06 | 中国科学院工程热物理研究所 | The device of material thermal conductivity is measured under a kind of high pressure gas environment |
| CN107884435B (en) * | 2017-10-20 | 2020-12-01 | 中国科学院工程热物理研究所 | Device for measuring heat conductivity coefficient of material under high-pressure gas environment |
| CN109270119A (en) * | 2018-11-08 | 2019-01-25 | 浙江大学 | A kind of open on-line measurement system of coal dust calorific value and measurement method |
| CN109270119B (en) * | 2018-11-08 | 2023-09-22 | 浙江大学 | Open type online measurement system and measurement method for calorific value of pulverized coal |
| CN110297011A (en) * | 2019-08-12 | 2019-10-01 | 杭州仰仪科技有限公司 | Calorimetric method is quickly screened in a kind of quasi-adiabatic |
| CN113358685A (en) * | 2020-08-24 | 2021-09-07 | 中海油能源发展股份有限公司 | Temperature compensation system for low-temperature oxidation intelligent detection |
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