CN106092813A - A kind of Thermal Properties of Coke determinator and method - Google Patents

A kind of Thermal Properties of Coke determinator and method Download PDF

Info

Publication number
CN106092813A
CN106092813A CN201610415711.4A CN201610415711A CN106092813A CN 106092813 A CN106092813 A CN 106092813A CN 201610415711 A CN201610415711 A CN 201610415711A CN 106092813 A CN106092813 A CN 106092813A
Authority
CN
China
Prior art keywords
coke
reactor
thermal properties
gas
determinator
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.)
Pending
Application number
CN201610415711.4A
Other languages
Chinese (zh)
Inventor
王炜
戴柏文
项恩广
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.)
Anshan Syd Science And Technology Co Ltd
Wuhan University of Science and Engineering WUSE
Wuhan University of Science and Technology WHUST
Original Assignee
Anshan Syd Science And Technology Co Ltd
Wuhan University of Science and Engineering WUSE
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 Anshan Syd Science And Technology Co Ltd, Wuhan University of Science and Engineering WUSE filed Critical Anshan Syd Science And Technology Co Ltd
Priority to CN201610415711.4A priority Critical patent/CN106092813A/en
Publication of CN106092813A publication Critical patent/CN106092813A/en
Pending legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N5/00Analysing materials by weighing, e.g. weighing small particles separated from a gas or liquid
    • G01N5/04Analysing materials by weighing, e.g. weighing small particles separated from a gas or liquid by removing a component, e.g. by evaporation, and weighing the remainder
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N1/00Sampling; Preparing specimens for investigation
    • G01N1/28Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q

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)
  • Coke Industry (AREA)

Abstract

The invention belongs to chemical metallurgy technical field, be specifically related to a kind of Thermal Properties of Coke determinator and method.This device includes distributing instrument, electric furnace, reactor, electronic weighing device and tails assay device, reactor by link coupled reaction device and is weighed by electronic weighing device, distributing instrument passes through air inlet pipe coupled reaction device, for providing coke reactivity gas to reactor, reactor connects tails assay device by escape pipe, for providing reaction end gas to tails assay device, coke reactivity gas controller connects nitrogen feeder, carbon dioxide feeder, carbon monoxide feeder and hydrogen feeder.By this device in addition to measuring coke reactivity with GB GB/T4000 2008 experimental standard with constant temperature, it is also possible to measure its reactivity worth in coke temperature-rise period, coke and pure CO both can be measured2Reactivity, can be again that coke is at blast furnace gas atmosphere i.e. CO, CO2、H2O、H2And N2Reactivity under the atmosphere combined by a certain percentage.

Description

A kind of Thermal Properties of Coke determinator and method
Technical field
The invention belongs to chemical metallurgy technical field, be specifically related to a kind of Thermal Properties of Coke determinator and method.
Background technology
Along with the development of ironmaking technology, in blast furnace process, the prescription of STRENGTH ON COKE is more and more higher, and Thermal Properties of Coke It is to affect the key factor that coke quality is good and bad.At present, Thermal Properties of Coke mainly measures according to GB GB/T4000-2008, But it is 1100 DEG C that this standard fixes reaction temperature, CO in reacting gas2It is 100%, it is impossible to complete to simulate coke in blast furnace Response situation.And the temperature measured is constant, it is impossible to draw the coke reactivity under different temperatures.Blast furnace gas contains There is N2、CO2、CO、H2And steam, therefore if able to adjust reacting gas proportioning, and adjusting reaction temperature, experiment obtains Thermal Properties of Coke more can react the truth of blast furnace.
Blast furnace all have employed the operation of big coal injection at present, owing to the hydrogen content in coal dust is higher, along with the increase of coal ratio, coal Hydrogen content in gas is consequently increased, so, the impact of the measurement hydrogen to be considered of coke reactivity.Current existing coke gasification reaction Property detection equipment all detect under the influence of steam not considering in coal gas, and for the gas componant in course of reaction Unclear.So the shortcoming of existing detection equipment be cannot coal gas environment in approximate simulation blast furnace, testing result can not generation completely Table coke practical situation in blast furnace, the detection of STRENGTH ON COKE hot property is the most comprehensive.
Summary of the invention
For solving the deficiencies in the prior art, the invention provides a kind of Thermal Properties of Coke determinator and method, in order to Preferably detect coke reactivity.
A kind of Thermal Properties of Coke determinator, including distributing instrument, electric furnace, the reactor being arranged in described electric furnace, electronics Weighing device and tails assay device, described electronic weighing device connects described reactor and to described reactor by link Weighing, described distributing instrument connects described reactor by air inlet pipe, for providing coke reactivity gas to described reactor Body, described reactor connects described tails assay device by escape pipe, for providing reaction tail to described tails assay device Gas, described distributing instrument is also associated with nitrogen feeder, carbon dioxide feeder, carbon monoxide feeder and hydrogen supply Device.
The link of reactor is connected by spring with reactor.
Further, described Thermal Properties of Coke determinator also includes gasify controller and gasification furnace, and described gasification furnace is even Connecing described gasification controller, for providing steam to described gasification controller, described gasification controller connects described reactor, For providing steam to described reactor.
Concrete, described gasification furnace include the distilled water storage device being sequentially connected in series, constant flow pump, water inlet pipe, add heat pipe and Steam discharges capillary tube, and described steam is discharged capillary tube and connected described gasification controller.Constant flow pump accurately controls distilled water flow And water is conveyed into continually and steadily adds in heat pipe.
Concrete, tetrafluoro sampling tube that described tails assay device includes being sequentially connected in series, the first dehumidifier, sampling pump, the Two dehumidifiers and infrared gas analysis meter.
Concrete, the described gasification that the air inlet pipe of described reactor connects described distributing instrument respectively by tee T controls Instrument.
Further, described Thermal Properties of Coke determinator also includes computer measurement and control device, described computer measurement and control Device electrically connects described distributing instrument, for controlling composition and the gas output of described coke reactivity gas;Described computer measurement and control Device electrically connects described gasification controller, for controlling the gas output of described gasification controller;Described computer measurement and control device electricity Connect described constant flow pump, for controlling the output of described constant flow pump;Heat pipe is added described in the electrical connection of described computer measurement and control device, Add the heating-up temperature of heat pipe described in control;Described computer measurement and control device electrically connects described electronic weighing device, is used for surveying Measure the weight change of described reactor;Described computer measurement and control device electrically connects described infrared gas analysis meter, is used for detecting tail Gas forms.
Computer measurement and control device can control heating rate and gas flow, and whole process is realized automatic measurement and control System.
Thermal Properties of Coke determinator provided by the present invention is equipped with gasification furnace, it is contemplated that blast furnace gas is aqueous, therefore Can input water, analog blast furnace includes nitrogen atmosphere.Heating rate, gas flow can be arranged according to blast furnace practical situation voluntarily, Simulation coke practical situation in blast furnace more really.Gas after coke gasification reaction can pass through tails assay device analysis Go out composition, tail gas and response situation more comprehensively can be analyzed detection.This device can measure the coke under different temperatures Reactivity, and coke reactivity can be measured in temperature-rise period, gas controller can realize the Ring of different ratio Border, more conforms to the complex situations in blast furnace.
Present invention also offers a kind of Thermal Properties of Coke assay method, survey including with Thermal Properties of Coke provided by the present invention Determine the following steps that device is carried out:
1) by the sampling method of GB GB/T4000-2008, coke specimen is prepared, then by sample at 175~185 DEG C At a temperature of be dried 1.5~2.5h, be cooled to room temperature after taking-up standby.
2) put into flat sieve plate at reactor bottom, make coke be positioned at when putting into reactor at the some high aluminium balls in sieve plate upper berth In the flat-temperature zone of electric furnace, dried coke specimen is weighed 200 ± 0.5g, put into reactor and recorded the granule of coke Number.
3) controlling electricity in-furnace temperature to heat up, when being warming up to 400 DEG C, controlling distributing instrument provides nitrogen to protect to reactor Protect, control gasifier operation and heat.
4) control electricity in-furnace temperature to heat up, be warming up to less than preset temperature value 45~when 55 DEG C, control distributing instrument to dioxy Change carbon etc. to preheat.
5) control electricity in-furnace temperature to heat up, be warming up to preset temperature value, temperature stabilization 8~after 12 minutes, control distributing instrument Cut off nitrogen and also provide at carbon dioxide and steam to reactor, with specimen reaction 1.5~2.5 hours.
6), after reaction terminates, control distributing instrument and cut off carbon dioxide etc. and provide nitrogen to protect to reactor;Control Constant flow pump quits work.
Further, measure the weight change of described reactor after being warming up to preset temperature value, carry out coke under constant temperature The mensuration of hot property;Measure the weight change of described reactor before and after the temperature range of any one end before being warming up to preset temperature value Change, carry out the mensuration of Thermal Properties of Coke in temperature-rise period.
Concrete, described preset temperature value is the arbitrary temp value more than or equal to 900 DEG C and less than or equal to 1200 DEG C.
Concrete, step 5) in: carbon dioxide, carbon monoxide, hydrogen, nitrogen and steam are combined into according to any proportioning Reacting gas, reaction gas flow is the arbitrary value less than or equal to 5.0L/min.
Thermal Properties of Coke assay method provided by the present invention can measure coke difference to fixed temperature (900,1000, 1100 DEG C etc.) under reactivity, except measuring in addition to coke reactivity with constant temperature with GB GB/T4000-2008 experimental standard, Its reactivity worth can also be measured in coke temperature-rise period, owing to used device is furnished with gas controller, can prepare Different gaseous environments, therefore its reactivity worth is not only coke and pure CO2Reaction, and can also is that coke is at blast furnace gas Atmosphere i.e. CO, CO2、H2O、H2And N2Reactivity under the atmosphere combined by a certain percentage.
Accompanying drawing explanation
Fig. 1 is the overall structure schematic diagram of Thermal Properties of Coke determinator provided by the present invention.
Fig. 2 is the structural representation of the gasification furnace of Thermal Properties of Coke determinator provided by the present invention.
Fig. 3 is the structural representation of the tails assay device of Thermal Properties of Coke determinator provided by the present invention.
In accompanying drawing 1,2,3, the list of parts representated by each label is as follows:
1, electric furnace, 2, reactor, 3, electronic weighing device, 4, computer measurement and control device, 5, gasification furnace, 6, gasification controls Instrument, 7, distributing instrument, 8, air inlet pipe, 9, escape pipe, 10, tails assay device, 11, thermocouple, 12, nitrogen feeder, 13, two Carbonoxide feeder, 14, carbon monoxide feeder, 15, hydrogen feeder, 16, distilled water storage device, 17, constant current Pump, 18, water inlet pipe, 19, add heat pipe, 20, steam discharge capillary tube, 21, tetrafluoro sampling tube, the 22, first dehumidifier, 23, sampling Pump, 24, infrared gas analysis meter, the 25, second dehumidifier.
Detailed description of the invention
Principle and feature to the present invention are described below, and illustrated embodiment is served only for explaining the present invention, is not intended to Limit the scope of the present invention.
In a detailed description of the invention, as it is shown in figure 1, a kind of Thermal Properties of Coke determinator, including distributing instrument 7, gas Change controller 6, gasification furnace 5, electric furnace 1, the reactor 2 being arranged in electric furnace 1, electronic weighing device 3 and tails assay device 10, reactor 2 by link coupled reaction device 2 and is weighed by electronic weighing device 3, and the link of reactor leads to reactor Crossing spring to connect, reactor 2 is provided with thermocouple 11.
Distributing instrument 7, is used for providing coke reactivity gas to reactor 2 by air inlet pipe 8 coupled reaction device 2 via tee T Body.Gasification controller 6 also passes through air inlet pipe 8 coupled reaction device 2 via tee T, for providing steam to reactor 2.Gasification Stove 5 connects gasification controller 6, for providing steam to gasification controller 6.
Reactor 2 connects tails assay device 10 by escape pipe 9, for providing reaction tail to tails assay device 10 Gas.
Coke reactivity gas controller connects nitrogen feeder 12, carbon dioxide feeder 13, carbon monoxide Feeder 14 and hydrogen feeder 15.
Such as Fig. 2, gasification furnace 5 includes the distilled water storage device 16 being sequentially connected in series, constant flow pump 17, water inlet pipe 18, adds heat pipe 19 and steam discharge capillary tube 20, steam discharge capillary tube 20 connect gasification controller 6.
As it is shown on figure 3, tails assay device 10 includes tetrafluoro sampling tube the 21, first dehumidifier 22, the sampling being sequentially connected in series Pump the 23, second dehumidifier 25 and infrared gas analysis meter 24.
Thermal Properties of Coke determinator also includes computer measurement and control device 4, and the control carried out is as follows:
Computer measurement and control device 4 electrically connects distributing instrument 7, for controlling composition and the gas output of coke reactivity gas;Meter Calculation machine measure and control device 4 electrical connection gasification controller 6, for controlling the gas output of gasification controller 6;Computer measurement and control device 4 electricity Connect constant flow pump 17, for controlling the output of constant flow pump 17;Computer measurement and control device 4 electrical connection adds heat pipe 19, is used for controlling Add the heating-up temperature of heat pipe 19;Computer measurement and control device 4 electrically connects electronic weighing device 3, becomes for measuring the weight of reactor 2 Change;Computer measurement and control device 4 electrically connects infrared gas analysis meter 24, is used for detecting tail gas composition.
Thermal Properties of Coke measures
Utilizing said apparatus to be measured, coke sample is that certain steel plant's blast furnace is burnt.
By the sampling method of GB 1997 regulation, take in proportion the coke 20kg of 25mm, discard that bubble is burnt and burner is burnt.Use jaw Formula crusher in crushing, mixing, division go out 10kg, then use φ 25mm, φ 21mm round-hole mesh to sieve, and the coke button more than φ 25mm breaks again Broken, screening, takes φ 21mm oversize, removes lamellar burnt burnt with strip, and division obtains coke button 2kg, and (each lkg) is placed in I at twice In type rotary drum, with the rotating speed of 20r/min, turn 50r, sieve with φ 21mm round-hole mesh again after taking-up, oversize division is gone out 900g As sample, by quartering, sample being divided into four parts, every part is no less than 220g.The coke of testing coke oven can use 40mm-60mm grain The coke of level carries out sample preparation.Take respectively and pound into spherical shape not less than 25mm coke.Then sample is put into drying baker, at 180 DEG C At a temperature of be dried 2h, be cooled to room temperature after taking-up, then sieve with the round-hole mesh of a diameter of 23mm, weigh 200g ± 0.5g Sample.
Flat sieve plate, 45, sieve plate upper berth high aluminium ball is put into, it is ensured that energy position when coke puts into reactor at reactor bottom In the flat-temperature zone of stove.
Dried material is weighed 200 ± 0.5g, puts into reactor and recorded the granule number of coke.
System has set parameter, only needs every PV value that monitoring control system shows, SP value, PV-SP value, each stage gas Body is passed through whether situation meets regulation parameter, and temperature is the most in upward status, as temperature reaches the reaction rank of 1100 DEG C Its fluctuation range of section should be within ± 5 DEG C.(it is passed through CO2Although after reaction, temperature has larger fluctuation, but should be at 10min Inside it is maintained at 1100 ± 5 DEG C).
When control temperature rises to 400 DEG C, system can switch to N2(0.8L/min) protection sample, it is necessary to confirm this operation (furnace temperature must could load sample below 400 DEG C and react), gasifier control system runs, begins to warm up.
Control temperature and rise to 1050 DEG C (850 DEG C or 950 DEG C) left and right, automatically turn on CO2Preheating device, is carried out really it Recognize.
Control temperature to rise to after 1100 DEG C (1000 DEG C, 900 DEG C) stablize 10 minutes, automatically cut off N2, and switch CO2 (5.0L/min, 4.875L/min, 4.75L/min) and steam (0L/min, 0.125L/min, 0.25L/min), anti-with sample Answer 2 hours, it is confirmed.
After reaction terminates, intensification will be automatically stopped and be automatically switched off CO2And constant flow pump, and switch N2(3.0L/min) protection, people Work takes out reactor, and (if arranging automatic tapping mode, reactor will propose outside burner hearth automatically, and be positioned over reactor frame overhead Sample is gone out after being as cold as less than 100 DEG C.(after reaction terminates, carefully do not scalded by high temperature during artificial taking-up reactor, the most do not roll over Disconnected thermocouple, gas piping does not wants contact reactor surface).
After reaction experiment terminates, weigh and record coke granule number.
It can be seen that the experiment of coke rich water is truly feasible from above example, the detection of STRENGTH ON COKE reactivity provides A kind of new approaches.The reactivity of coke can be detected more accurately, carry for understanding coke operation reactive state in blast furnace For more accurate data-guiding.
The foregoing is only presently preferred embodiments of the present invention, not in order to limit the present invention, all spirit in the present invention and Within principle, any modification, equivalent substitution and improvement etc. made, should be included within the scope of the present invention.

Claims (10)

1. a Thermal Properties of Coke determinator, including distributing instrument (7), electric furnace (1), the reaction that is arranged in described electric furnace (1) Device (2), electronic weighing device (3) and tails assay device (10), described electronic weighing device (3) connects described by link Described reactor (2) is also weighed by reactor (2), and described distributing instrument (7) connects described reactor by air inlet pipe (8) (2), for providing coke reactivity gas to described reactor (2), described reactor (2) connects described by escape pipe (9) Tails assay device (10), for providing reaction end gas to described tails assay device (10), it is characterised in that: described distributing instrument (7) it is also associated with nitrogen feeder (12), carbon dioxide feeder (13), carbon monoxide feeder (14) and hydrogen to supply Device of air (15).
Thermal Properties of Coke determinator the most according to claim 1, it is characterised in that: described Thermal Properties of Coke determinator Also including gasify controller (6) and gasification furnace (5), described gasification furnace (5) connects described gasification controller (6), for described Gasification controller (6) provides steam, and described gasification controller (6) connects described reactor (2), for described reactor (2) steam is provided.
Thermal Properties of Coke determinator the most according to claim 2, it is characterised in that: described gasification furnace (5) includes successively Series connection distilled water storage device (16), constant flow pump (17), water inlet pipe (18), add heat pipe (19) and steam discharge capillary tube (20), described steam discharge capillary tube (20) connects described gasification controller (6).
Thermal Properties of Coke determinator the most according to claim 3, it is characterised in that: described tails assay device (10) is wrapped Include tetrafluoro sampling tube (21), the first dehumidifier (22), sampling pump (23), the second dehumidifier (25) and the infrared coal gas being sequentially connected in series Analyser (24).
Thermal Properties of Coke determinator the most according to claim 2, it is characterised in that: the air inlet pipe of described reactor (2) (8) the described gasification controller (6) of described distributing instrument (7) is connected respectively by tee T.
Thermal Properties of Coke determinator the most according to claim 4, it is characterised in that: described Thermal Properties of Coke determinator Also include that computer measurement and control device (4), described computer measurement and control device (4) electrically connect described distributing instrument (7), be used for controlling described The composition of coke reactivity gas and gas output;Described computer measurement and control device (4) electrically connects described gasification controller (6), uses In the gas output controlling described gasification controller (6);Described computer measurement and control device (4) electrically connects described constant flow pump (17), uses In the output controlling described constant flow pump (17);Add heat pipe (19) described in the electrical connection of described computer measurement and control device (4), be used for controlling The heating-up temperature of heat pipe (19) is added described in system;Described computer measurement and control device (4) electrically connects described electronic weighing device (3), uses In the weight change measuring described reactor (2);Described computer measurement and control device (4) electrically connects described infrared gas analysis meter (24), it is used for detecting tail gas composition.
7. a Thermal Properties of Coke assay method, it is characterised in that enter with the Thermal Properties of Coke determinator described in claim 6 Row Thermal Properties of Coke measures, and comprises the following steps:
1) by the sampling method of GB GB/T4000-2008, coke specimen is prepared, then by sample the temperature of 175~185 DEG C Under be dried 1.5~2.5h, be cooled to room temperature after taking-up standby;
2) flat sieve plate is put in reactor (2) bottom, the position when the some high aluminium balls in sieve plate upper berth make coke put into reactor (2) In the flat-temperature zone of electric furnace (1), dried coke specimen is weighed 200 ± 0.5g, put into reactor (2) and recorded coke Granule number;
3) controlling electric furnace (1) interior temperature to heat up, when being warming up to 400 DEG C, controlling distributing instrument (7) provides nitrogen to enter to reactor (2) Row protection, controls gasification furnace (5) operation and heats;
4) control electric furnace (1) interior temperature to heat up, be warming up to less than preset temperature value 45~when 55 DEG C, control distributing instrument (7) to two Carbonoxide preheats;
5) control electric furnace (1) interior temperature to heat up, be warming up to preset temperature value, temperature stabilization 8~after 12 minutes, control distributing instrument (7) nitrogen provide at carbon dioxide and steam to reactor (2) is cut off, with specimen reaction 1.5~2.5 hours;
6), after reaction terminates, control distributing instrument (7) and cut off carbon dioxide and provide nitrogen to protect to reactor (2);Control Constant flow pump (17) quits work.
Thermal Properties of Coke assay method the most according to claim 7, it is characterised in that: measure be warming up to preset temperature value it The weight change of rear described reactor (2), carries out the mensuration of Thermal Properties of Coke under constant temperature;Before measurement is warming up to preset temperature value The arbitrarily weight change of described reactor (2) before and after the temperature range of one end, carries out the mensuration of Thermal Properties of Coke in temperature-rise period.
Thermal Properties of Coke assay method the most according to claim 7, it is characterised in that: described preset temperature value is for being more than In 900 DEG C and less than or equal to the arbitrary temp value of 1200 DEG C.
Thermal Properties of Coke assay method the most according to claim 7, it is characterised in that step 5) in: carbon dioxide, Carbonoxide, hydrogen, nitrogen and steam are combined into reacting gas according to any proportioning, and reaction gas flow is for being less than or equal to The arbitrary value of 5.0L/min.
CN201610415711.4A 2016-06-14 2016-06-14 A kind of Thermal Properties of Coke determinator and method Pending CN106092813A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610415711.4A CN106092813A (en) 2016-06-14 2016-06-14 A kind of Thermal Properties of Coke determinator and method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610415711.4A CN106092813A (en) 2016-06-14 2016-06-14 A kind of Thermal Properties of Coke determinator and method

Publications (1)

Publication Number Publication Date
CN106092813A true CN106092813A (en) 2016-11-09

Family

ID=57845828

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610415711.4A Pending CN106092813A (en) 2016-06-14 2016-06-14 A kind of Thermal Properties of Coke determinator and method

Country Status (1)

Country Link
CN (1) CN106092813A (en)

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106885739A (en) * 2017-03-31 2017-06-23 武汉科技大学 A kind of hot compression strength online testing device of coke
CN107957486A (en) * 2017-12-25 2018-04-24 安徽工业大学 A kind of experimental system for being used to detect coke water vapor reaction
CN108131654A (en) * 2017-12-25 2018-06-08 安徽工业大学 A kind of vapor method for generation of coke reactivity measurement device
CN108181121A (en) * 2018-01-10 2018-06-19 西安建筑科技大学 A kind of internal heat type low-temperature dry distillation thermal simulation detection device and method
CN108507839A (en) * 2018-05-25 2018-09-07 安徽工业大学 sedimentation furnace constant temperature sampling method
CN108918330A (en) * 2018-05-15 2018-11-30 内蒙古科技大学 For studying the device and method that alkali metal STRENGTH ON COKE reactivity influences under vapor and carbon dioxide conditions
CN109099709A (en) * 2018-09-20 2018-12-28 攀钢集团攀枝花钢铁研究院有限公司 A kind of reduction experiment furnace
CN110286053A (en) * 2019-06-17 2019-09-27 包头钢铁(集团)有限责任公司 A method of detection lead oxide STRENGTH ON COKE Effect of Thermal Performance
CN110411852A (en) * 2019-07-30 2019-11-05 重庆大学 The measuring method of coke property alternation in a kind of blast furnace
CN110672661A (en) * 2019-08-27 2020-01-10 武汉科技大学 Multifunctional blast furnace harmful element adsorption experiment method and device thereof
CN110793880A (en) * 2019-09-30 2020-02-14 鞍钢股份有限公司 Device and method for simulating metallurgical reduction mineral aggregate process
CN112816361A (en) * 2021-01-05 2021-05-18 神华神东煤炭集团有限责任公司 System and method for evaluating thermal conversion of organic matter-containing solid
CN112903513A (en) * 2021-01-13 2021-06-04 东北大学 Method for measuring high-temperature pulverization performance of iron coke
CN112903512A (en) * 2021-01-13 2021-06-04 东北大学 Method for measuring high-temperature reactivity and post-reaction strength of iron coke
CN113970501A (en) * 2020-07-23 2022-01-25 宝山钢铁股份有限公司 Method for evaluating reaction performance of carbon-iron composite furnace charge
CN114167029A (en) * 2017-03-31 2022-03-11 华北理工大学 Detection device and detection method for reaction of water vapor, carbon dioxide and coke
CN114486794A (en) * 2022-01-25 2022-05-13 华北理工大学 Coke, steam and carbon dioxide co-gasification reaction detection device and method

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101936979A (en) * 2009-06-30 2011-01-05 宝山钢铁股份有限公司 Strength determination method and device for reacted blast furnace coke
CN102109446A (en) * 2009-12-25 2011-06-29 中国科学院过程工程研究所 Method for controlling reaction gas channeling of thermobalance analyzer, and pressurized thermobalance analyzer
CN102768161A (en) * 2012-08-15 2012-11-07 重庆大学 Experimental device and method for performing on-line monitoring on lump coal splitting decomposition
CN102928455A (en) * 2012-10-26 2013-02-13 武钢集团昆明钢铁股份有限公司 Method for detecting high-temperature metallurgical performance of coke
CN104101554A (en) * 2014-07-16 2014-10-15 首钢总公司 Determining device and detecting method for reactivity and hot strength of coke
CN104297282A (en) * 2014-10-27 2015-01-21 武汉钢铁(集团)公司 Coke thermal property analyzing method and device for realizing method
CN104614272A (en) * 2015-02-06 2015-05-13 中国科学院山西煤炭化学研究所 High-temperature pressuring thermobalance and application method thereof
CN105136601A (en) * 2015-08-14 2015-12-09 中南大学 High-temperature thermal field and complex atmosphere environment static coupling device

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101936979A (en) * 2009-06-30 2011-01-05 宝山钢铁股份有限公司 Strength determination method and device for reacted blast furnace coke
CN102109446A (en) * 2009-12-25 2011-06-29 中国科学院过程工程研究所 Method for controlling reaction gas channeling of thermobalance analyzer, and pressurized thermobalance analyzer
CN102768161A (en) * 2012-08-15 2012-11-07 重庆大学 Experimental device and method for performing on-line monitoring on lump coal splitting decomposition
CN102928455A (en) * 2012-10-26 2013-02-13 武钢集团昆明钢铁股份有限公司 Method for detecting high-temperature metallurgical performance of coke
CN104101554A (en) * 2014-07-16 2014-10-15 首钢总公司 Determining device and detecting method for reactivity and hot strength of coke
CN104297282A (en) * 2014-10-27 2015-01-21 武汉钢铁(集团)公司 Coke thermal property analyzing method and device for realizing method
CN104614272A (en) * 2015-02-06 2015-05-13 中国科学院山西煤炭化学研究所 High-temperature pressuring thermobalance and application method thereof
CN105136601A (en) * 2015-08-14 2015-12-09 中南大学 High-temperature thermal field and complex atmosphere environment static coupling device

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
李家新 等: "H2O-CO2混合气体对焦炭劣化反应的影响", 《安徽工业大学学报》 *
王平 等: "CO2与水蒸汽对焦炭溶损反应的影响", 《过程工程学报》 *
赵晴晴 等: "H2O和CO2对焦炭溶损反应动力学的研究", 《过程工程学报》 *
郭文涛 等: "焦炭与CO2和水蒸气气化后孔隙结构和高温抗压强度研究", 《燃料化学学报》 *

Cited By (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114167029A (en) * 2017-03-31 2022-03-11 华北理工大学 Detection device and detection method for reaction of water vapor, carbon dioxide and coke
CN106885739A (en) * 2017-03-31 2017-06-23 武汉科技大学 A kind of hot compression strength online testing device of coke
CN107957486B (en) * 2017-12-25 2024-05-14 安徽工业大学 Experimental system for detecting coke steam reactivity
CN107957486A (en) * 2017-12-25 2018-04-24 安徽工业大学 A kind of experimental system for being used to detect coke water vapor reaction
CN108131654A (en) * 2017-12-25 2018-06-08 安徽工业大学 A kind of vapor method for generation of coke reactivity measurement device
CN108131654B (en) * 2017-12-25 2019-07-30 安徽工业大学 A kind of vapor method for generation of coke reactivity measurement device
CN108181121A (en) * 2018-01-10 2018-06-19 西安建筑科技大学 A kind of internal heat type low-temperature dry distillation thermal simulation detection device and method
CN108918330A (en) * 2018-05-15 2018-11-30 内蒙古科技大学 For studying the device and method that alkali metal STRENGTH ON COKE reactivity influences under vapor and carbon dioxide conditions
CN108918330B (en) * 2018-05-15 2021-02-09 内蒙古科技大学 Device and method for researching influence of alkali metal on coke reactivity under conditions of water vapor and carbon dioxide
CN108507839A (en) * 2018-05-25 2018-09-07 安徽工业大学 sedimentation furnace constant temperature sampling method
CN108507839B (en) * 2018-05-25 2020-07-24 安徽工业大学 Constant-temperature sampling method for settling furnace
CN109099709A (en) * 2018-09-20 2018-12-28 攀钢集团攀枝花钢铁研究院有限公司 A kind of reduction experiment furnace
CN110286053A (en) * 2019-06-17 2019-09-27 包头钢铁(集团)有限责任公司 A method of detection lead oxide STRENGTH ON COKE Effect of Thermal Performance
CN110411852A (en) * 2019-07-30 2019-11-05 重庆大学 The measuring method of coke property alternation in a kind of blast furnace
CN110672661A (en) * 2019-08-27 2020-01-10 武汉科技大学 Multifunctional blast furnace harmful element adsorption experiment method and device thereof
CN110793880A (en) * 2019-09-30 2020-02-14 鞍钢股份有限公司 Device and method for simulating metallurgical reduction mineral aggregate process
CN113970501A (en) * 2020-07-23 2022-01-25 宝山钢铁股份有限公司 Method for evaluating reaction performance of carbon-iron composite furnace charge
CN112816361A (en) * 2021-01-05 2021-05-18 神华神东煤炭集团有限责任公司 System and method for evaluating thermal conversion of organic matter-containing solid
CN112816361B (en) * 2021-01-05 2023-03-14 神华神东煤炭集团有限责任公司 System and method for evaluating thermal conversion of organic matter-containing solid
CN112903513A (en) * 2021-01-13 2021-06-04 东北大学 Method for measuring high-temperature pulverization performance of iron coke
CN112903512A (en) * 2021-01-13 2021-06-04 东北大学 Method for measuring high-temperature reactivity and post-reaction strength of iron coke
CN114486794A (en) * 2022-01-25 2022-05-13 华北理工大学 Coke, steam and carbon dioxide co-gasification reaction detection device and method
CN114486794B (en) * 2022-01-25 2024-01-26 华北理工大学 Cogasification reaction detection device and method for coke, water vapor and carbon dioxide

Similar Documents

Publication Publication Date Title
CN106092813A (en) A kind of Thermal Properties of Coke determinator and method
CN108120795B (en) Self-feeding type heating coal pile low-temperature oxidation induction accelerating spontaneous combustion test simulation device
CN104212924B (en) A kind of detection method of blast furnace gas flow distribution
CN103940697B (en) A kind of blast-furnace coke reactivity method of testing
CN106124357A (en) A kind of multi-functional coal sample heating and oxidation rule test platform of automatic sampling
CN201425419Y (en) High-temperature reduction-reaction experimental electric stove
CN105842111B (en) The detection method of smelter coke gasification activity and post reaction strength
CN108918330A (en) For studying the device and method that alkali metal STRENGTH ON COKE reactivity influences under vapor and carbon dioxide conditions
JP6107382B2 (en) Evaluation method of solid fuel
CN103398918B (en) Method and device for testing thermal property of semicokes generated by cracking of block coal
CN101710054A (en) Measurement method and measurement device of coke reactivity
CN109342498A (en) A kind of Coal Self-ignition Process phase judgement method
CN103293177B (en) Quick heating and gasifying test device and application thereof
CN108593700A (en) It is a kind of simulation coke blast furnace melting with soft deterioration process test method and simulator
JP5455813B2 (en) Method for evaluating reduced powder properties of sintered ore
JP2016057149A (en) High-temperature property evaluation test device for ore
CN101308105A (en) Rare-earth magnesium alloy solidification process thermal analysis device
CN105842065B (en) The evaluation method of smelter coke post reaction strength
CN105823863A (en) Coal quality on-line industrial analysis and measurement method based on constant temperature thermogravimetric analysis
KR101848183B1 (en) Method for predicting of gas using ratio in blast furnace
CN207581847U (en) The analoging detecting device that a kind of burden distribution system influences blast furnace melting with soft
CN104931376B (en) High-temp solid powder adheres to the test device and method of testing of wall built-up characteristic
CN110793880A (en) Device and method for simulating metallurgical reduction mineral aggregate process
CN207850859U (en) A kind of device of detection iron-containing charge integral high temperature metallurgical performance
CN106680135B (en) Device and method for measuring high-temperature metallurgical property of coke

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20161109