WO2019111540A1 - Method for producing reformed coal - Google Patents
Method for producing reformed coal Download PDFInfo
- Publication number
- WO2019111540A1 WO2019111540A1 PCT/JP2018/038445 JP2018038445W WO2019111540A1 WO 2019111540 A1 WO2019111540 A1 WO 2019111540A1 JP 2018038445 W JP2018038445 W JP 2018038445W WO 2019111540 A1 WO2019111540 A1 WO 2019111540A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- coal
- dry
- oxidation treatment
- comparative example
- distilled
- Prior art date
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L9/00—Treating solid fuels to improve their combustion
- C10L9/02—Treating solid fuels to improve their combustion by chemical means
- C10L9/06—Treating solid fuels to improve their combustion by chemical means by oxidation
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L9/00—Treating solid fuels to improve their combustion
- C10L9/08—Treating solid fuels to improve their combustion by heat treatments, e.g. calcining
Definitions
- the present disclosure relates to a method of producing modified coal.
- an object of this invention is to provide the manufacturing method of the modification coal which can manufacture the modification coal in which the spontaneous ignition property was fully suppressed with high yield.
- the present invention comprises a dry distillation step of dry-distilling coal at 300 to 650 ° C. to obtain dry-distilled carbon, and an oxidation treatment step of oxidizing dry-distilled carbon at a temperature range of over 200 ° C. and 240 ° C. or less for 10 to 60 minutes. Providing a method of producing modified coal.
- oxidation treatment of raw material carbon is performed at a temperature range of over 200 ° C. and less than 240 ° C. for 10 to 60 minutes.
- the oxidation treatment is performed under such conditions, the surface component of the raw material carbon is oxidized to stabilize the surface state, and hence it is considered that the self-heating property is reduced and the spontaneous ignition property is suppressed.
- the loss due to self-combustion can be suppressed, and the yield can be increased.
- the above-mentioned manufacturing method has a dry distillation step of dry-distilling coal to obtain dry-distilled carbon prior to the oxidation treatment step.
- Dry distillation of coal is effective as a means of upgrading coal.
- the yield at the dry distillation tends to be high while the spontaneous ignition tends to be high.
- the self heating property can be reduced by the oxidation treatment step. For this reason, even if the dry distillation temperature in the dry distillation step is 650 ° C. or lower, the spontaneous ignition can be suppressed. Therefore, it is possible to produce a high grade, reformed coal with sufficiently suppressed spontaneous combustion property, with high yield.
- the above manufacturing method may have a drying step of drying coal at 150 ° C. or less before the oxidation treatment step. Since the moisture of coal is reduced by this, a higher quality modified coal can be obtained by an oxidation treatment process or a dry distillation process and an oxidation treatment process.
- the above-mentioned production method may have a combustion step of burning a gas containing volatile components generated by dry distillation of coal in a combustion furnace.
- the dry-distilled coal be oxidized by the exhaust gas containing oxygen from the combustion furnace.
- the present invention can provide a method for producing a modified coal capable of producing a modified coal with sufficiently suppressed spontaneous ignition property with high yield.
- FIG. 1 is a flowchart showing an example of a method for producing modified coal.
- FIG. 2 is a graph showing the results of the spontaneous ignition evaluation test of Examples 1 and 2 and Reference Examples 1 and 2 and Comparative Examples 1 to 4.
- FIG. 3 is a graph showing the time-dependent change of the calorific value of dry-distilled carbon of Comparative Examples 5 to 8 having different dry distillation degrees.
- FIG. 4 is a graph showing time-dependent changes in calorific value of the modified coals of Example 3 and Reference Example 4 and Comparative Examples 9 and 10 having different oxidation treatment temperatures and the dry-distilled carbon of Comparative Example 6.
- FIG. 1 is a flowchart showing an example of a method for producing modified coal.
- FIG. 2 is a graph showing the results of the spontaneous ignition evaluation test of Examples 1 and 2 and Reference Examples 1 and 2 and Comparative Examples 1 to 4.
- FIG. 3 is a graph showing the time-dependent change of the calorific value of dry-distilled carbon of Comparative Examples 5 to 8 having different dry distillation degrees.
- FIG. 5 is a graph showing the concentrations of carbon monoxide and carbon dioxide in the exhaust gas at the time of the oxidation treatment of Examples 5, 6 and Reference Example 7 and Comparative Examples 11-13.
- FIG. 6 is a diagram showing the results of infrared spectroscopic analysis of Comparative Example 6, Comparative Example 14 and Comparative Example 15.
- FIG. 7 is a graph showing the results of thermogravimetric analysis of Comparative Examples 16 to 19 and Examples 8, 9 and Reference Example 10 in which the oxidation treatment temperature is different.
- FIG. 8 is a graph showing the results of differential thermal analysis of Comparative Examples 16 to 19, and Examples 8 and 9, and Reference Example 10 having different oxidation treatment temperatures.
- FIG. 10 is a graph showing the results of the spontaneous firing evaluation test.
- the method for producing modified coal according to the present embodiment includes a dry distillation step of dry-distilling coal at 300 to 650 ° C. to obtain dry-distilled carbon, and an oxidation treatment of oxidizing dry-distilled carbon at a temperature range of 200 ° C. to 240 ° C. It has a process.
- dry-distilled coal tends to ignite spontaneously more than dry coal in coal.
- by performing an oxidation treatment step under predetermined conditions on dry-distilled coal having a surface condition different from that of coal and its dry coal reformed coal in which spontaneous ignition is sufficiently suppressed is obtained from dry-distilled carbon. be able to.
- the dry distillation step is a step of dry-distilling coal at 300 to 650 ° C. to obtain dry-distilled carbon.
- the water content of the coal is reduced at the beginning of the dry distillation process.
- the dry distillation step is preferably performed in a temperature range of 300 to 600.degree. This makes it possible to maintain a high yield while sufficiently promoting the carbonization of coal.
- the dry distillation step can be performed using a conventional dry distillation furnace such as a vertical shaft furnace, a coke oven, or a tunnel kiln furnace.
- the volatile matter (VM) of the dry-distilled carbon obtained in the dry distillation step is preferably 10 to 30% by mass.
- Such dry-distilled carbon usually has high spontaneous ignition properties, but in the present embodiment, it is possible to suppress the spontaneous ignition properties by performing an oxidation treatment step after the dry distillation step. Therefore, high yield can be realized.
- the coal may contain low grade coal or may contain high grade coal. When low grade coal is contained, it is preferable to perform the drying process mentioned later before an oxidation treatment process. However, it is not always essential to carry out the drying step.
- the particle size of the raw material carbon may be, for example, 50 mm or less, 30 mm or less, or 10 mm or less.
- the oxidation treatment step by setting the temperature (oxidation treatment temperature) at which oxidation treatment of dry-distilled carbon is carried out in a range exceeding 200 ° C., the surface of dry-distilled carbon is sufficiently reformed to sufficiently suppress spontaneous ignition. Can be obtained.
- the oxidation treatment temperature By setting the oxidation treatment temperature to 240 ° C. or less, the reduction of the volatile component in the oxidation treatment process is suppressed, and the modified coal can be produced with a high yield.
- the oxidation treatment temperature is preferably 210 to 240 ° C., more preferably 220 to 240 ° C., from the viewpoint of achieving both suppression of spontaneous ignition and improvement of yield at a higher level.
- the oxidation treatment step may not be performed at a constant oxidation treatment temperature, and the oxidation treatment temperature may fluctuate within the above-mentioned range.
- the time of the oxidation treatment step is 10 to 60 minutes from the viewpoint of producing the modified coal with high yield. From the viewpoint of sufficiently suppressing the spontaneous ignition, the time of the oxidation treatment step may be 15 to 60 minutes.
- the atmosphere in the oxidation treatment step is not particularly limited as long as it is an atmosphere containing oxygen, and may be air or a mixed atmosphere of an inert gas such as nitrogen and oxygen. Moreover, it may be the exhaust gas of a combustion furnace.
- the oxygen concentration may be, for example, 2 to 13% by volume or 3 to 10% by volume from the viewpoint of safety and the efficiency of the oxidation treatment. This "volume%" is a volume ratio in the conditions of a standard state (25 degreeC, 100 kPa).
- the volatile content (VM) of the modified coal may be 5% by mass or more, or 10% by mass or more from the viewpoint of enhancing the usefulness as a fuel.
- the volatile content (VM) of the modified coal may be 30% by mass or less or 25% by mass or less from the viewpoint of further reducing the spontaneous ignition property.
- the volatile matter content in this specification is a value of the anhydrous basis measured based on the "square electric furnace method" of JISM 8812: 2006.
- the manufacturing method of the present embodiment it is possible to manufacture the modified coal in which the spontaneous combustion property is sufficiently suppressed at a high yield.
- Such reformed coal can also be used effectively as a fuel because it can contain a certain amount of volatile matter.
- it is highly useful as a fuel, and it is possible to safely carry out storage of coal in a yard, and on-shore / sea transportation from a coal-producing area.
- the method for producing modified coal according to another embodiment includes a drying step of drying coal at 150 ° C. or less before the above-mentioned dry distillation step.
- a drying step of drying coal at 150 ° C. or less before the above-mentioned dry distillation step.
- low-grade coal having a high water content for example, lignite and sub-bituminous coal having a water content of 50% by mass or more
- the coal is dried by heating, for example, to a temperature range of 40 to 150.degree.
- the drying step may be performed in air or in an inert gas atmosphere. Alternatively, it may be performed in the exhaust gas of a combustion furnace.
- the water content of coal is reduced to, for example, 20% by mass or less.
- the drying step may be performed using a common electric furnace or the like, or may be performed using an indirect heater or an air fluidized bed dryer.
- the time of the drying step is not particularly limited, and can be adjusted depending on the moisture content of coal, the particle size of coal, and the like.
- the particle size of the modified coal may be, for example, 50 mm or less, or 10 mm or less.
- the modified coal obtained by the above-mentioned production method may be classified to be divided into particles (for example, particles with a particle diameter of 3 mm or more) and powders (for example, particles with a particle diameter of less than 3 mm).
- the powdery modified carbon (powder) obtained by classification may be molded with or without a binder, and may be mixed with the particulate modified carbon (particles) obtained by classification as well.
- FIG. 1 is a view showing an example of an apparatus configuration for performing a method of manufacturing modified coal according to an embodiment.
- the drying process is performed in the drying apparatus 10
- the dry distillation process is performed in the dry distillation apparatus 20
- the oxidation treatment process is performed in the oxidation treatment apparatus 30.
- the gas containing volatile components generated from the dry distillation apparatus 20 is consumed as a fuel gas in the combustion furnace 40 (combustion process).
- the drying device 10 may be, for example, a conventional dryer.
- Examples of the oxidation treatment apparatus 30 include a conventional electric furnace.
- the exhaust gas generated by burning the fuel gas containing the volatile component in the combustion furnace 40 usually contains about 5 to 10% by volume of oxygen.
- the exhaust gas generated in the combustion furnace 40 may be used as a heating gas in the drying apparatus 10.
- Example 1 [Manufacturing of modified coal]
- Commercially available coal for boilers, sub-bituminous coal (Adaro coal from Indonesia), was dried in the air using a drier to obtain dried coal (drying step).
- the heating temperature in the drying step was 150 ° C., and the heating time was 30 minutes.
- the volatile matter (VM) of the obtained dried coal was 50% by mass, and the water content was 10% by mass or less.
- the obtained dried coal was subjected to dry distillation using a dry distillation furnace to obtain dry distilled carbon (dry distillation step).
- the heating temperature in the dry distillation step was 430 ° C., and the heating time was 40 minutes.
- the volatile matter (VM) of dry-distilled carbon was 25% by mass.
- the dry-distilled carbon obtained was oxidized using an electric furnace to produce granular modified carbon (particle size: about 1 to 3 mm) (oxidation treatment step).
- the conditions for the oxidation treatment were a mixed gas atmosphere of nitrogen gas and oxygen gas (oxygen concentration: 8% by volume), a heating temperature of 240 ° C., and a heating time of 40 minutes.
- Example 2 Modified coal was produced in the same manner as in Example 1 except that the heating temperature in the oxidation treatment step was 210 ° C. Then, in the same manner as in Example 1, a spontaneous ignition evaluation test was conducted. The results were as shown in curve A2 of FIG.
- Example 4 Dry carbon was obtained in the same manner as Example 1.
- the volatile matter (VM) of the dried charcoal was 50% by mass, and the water content was 10% by mass or less.
- the pyrophoricity evaluation test of the obtained dried coal was conducted. The results were as shown in curve D1 of FIG.
- the dry-distilled carbon (curve E1) of Comparative Example 1 in which the oxidation treatment step was not performed generated heat to 250 ° C. or more in about one hour. That is, the modified coal was the highest in spontaneous ignition.
- the dry charcoal (curve D1) of Comparative Example 4 was lower in pyrophoric property than the dry-distilled charcoal (curve E1) of Comparative Example 1.
- the spontaneous ignition property of the modified coal of Example 2 was lower than that of the commercially available subbituminous coal, and the spontaneous ignition property of the modified coal of Example 1 was lower than that of the commercially available bituminous coal. Thus, it was confirmed that the pyrophoric properties of the modified coals of Example 1 and Example 2 were sufficiently suppressed despite being carbonized.
- Differential scanning calorimetry (DSC measurement) of the prepared dried charcoal was performed using a commercially available measuring device. Specifically, in a nitrogen atmosphere, the dried charcoal and the reference substance were each heated by a heater and heated to 107 ° C. Thereafter, the nitrogen atmosphere was switched to air, and the calorific value when air oxidation was performed at a constant temperature (107 ° C.) was measured. The results are as shown in curve D2 of FIG.
- the dried carbon (curve D2) of Comparative Example 5 has a lower calorific value than the dried carbon (E2) of Comparative Example 6. Also in FIG. 2, it is shown that dry charcoal (curve D1) is lower in self-ignitability than dry carbon (E1). From these tendencies, it can be said that, even when dry coal is subjected to oxidation treatment, it is possible to suppress spontaneous ignition as in dry-distilled coal. That is, the oxidation treatment is effective for dry coal as well as dry-distilled coal.
- FIG. 4 also shows the result of Comparative Example 6 in order to facilitate the comparison.
- the modified coals (curves A3 and A4) of Example 3 and Reference Example 4 were able to significantly reduce the calorific value compared to the dried carbon (curve E2) of Comparative Example 6.
- the calorific value of the modified coals of Example 3 and Reference Example 4 was lower than the calorific value of the modified coals of Comparative Example 9 and Comparative Example 10. From this, it was confirmed that the modified coals of Example 3 and Reference Example 4 can reduce the self-heating property more than Comparative Examples 6, 9, 10.
- Example 6 Modified coal was produced in the same manner as in Comparative Example 11 except that the oxidation treatment temperature in the oxidation treatment step was 240 ° C. The concentration of CO 2 and CO in the exhaust gas during the oxidation treatment step was analyzed in the same manner as in Comparative Example 11.
- FIG. 5 is a graph in which the concentrations of CO 2 and CO in the exhaust gas determined in Examples 5 and 6 and Reference Example 7 and Comparative Examples 11 to 13 are plotted. As shown in FIG. 5, it was confirmed that when the oxidation treatment temperature exceeded 200 ° C., the generation amount of CO 2 and CO increased. From this, it can be said that the surface of the modified coal can be sufficiently reformed by setting the oxidation treatment temperature in a range exceeding 200 ° C.
- FIG. 6 shows, on an enlarged scale, a portion at 2800 to 3000 cm -1 at which a peak derived from an aliphatic hydrocarbon group is observed in the measurement charts of infrared spectroscopic analysis of Comparative Example 14 and Comparative Example 15. Further, for comparison, FIG. 6 also shows the results of infrared spectroscopy of the dry-distilled carbon prepared in Comparative Example 6 (curve E2). As shown in FIG. 6, it was confirmed that the surface composition of dry-distilled carbon was changed by oxidizing dry-distilled carbon. In addition, it was confirmed that when the oxidation treatment temperature is changed within the temperature range of 200 to 300 ° C., the surface composition of the resulting modified coal changes significantly.
- thermogravimetric / differential thermal analysis in the oxidation process (FIGS. 7 and 8)] (Comparative example 16)
- the oxidation treatment process was performed using the dry-distilled carbon of Comparative Example 6.
- the weight and differential heat at the time of the oxidation treatment step were measured using a commercially available thermogravimetric / differential thermal simultaneous analyzer. Specifically, dry-distilled coal was placed in an analyzer, and the temperature was raised to 140 ° C. at a rate of 10 ° C./minute in a nitrogen atmosphere. Thereafter, the atmosphere was switched to a mixed atmosphere of nitrogen and oxygen (oxygen concentration: 10% by volume) to start the oxidation treatment.
- Thermogravimetric / differential thermal simultaneous analysis was performed based on this switching time.
- the results of thermogravimetric analysis were as shown in curve B7 in FIG. 7, and the results of differential thermal analysis were as shown in curve B7 in FIG.
- thermogravimetric / differential thermal simultaneous analysis was performed in the same manner as in Comparative Example 16 except that the oxidation treatment temperature (the temperature at which the mixed atmosphere was switched) in the oxidation treatment step was 220 ° C.
- the results of thermogravimetric analysis were as shown in curve A5 in FIG. 7, and the results of differential thermal analysis were as shown in curve A5 in FIG.
- Example 9 Thermal weight and differential thermal simultaneous analysis were performed in the same manner as in Comparative Example 16 except that the oxidation treatment temperature (the temperature at which the mixed atmosphere was switched) in the oxidation treatment step was 240 ° C.
- the results of thermogravimetric analysis were as shown by curve A6 in FIG. 7, and the results of differential thermal analysis were as shown by curve A6 in FIG.
- FIG. 9 is a graph showing the relationship between the height of the maximum peak (peak top) in the DTA analysis results (differential thermal analysis results) of each example and each comparative example shown in FIG. 8 and the oxidation treatment temperature.
- the oxidation treatment temperature is 200 ° C. or lower (Comparative Examples 16, 17, 18)
- the oxidation reaction does not progress so actively.
- the oxidation treatment temperature exceeds 200 ° C., the oxidation reaction proceeds rapidly. Therefore, in order to advance the oxidation of the surface of the modified coal to a certain extent, it can be said that the oxidation treatment temperature needs to be in the range exceeding 200.degree.
- the oxidation treatment of dry-distilled coal at 200 to 300 ° C. increased the oxygen concentration. That is, the oxidation treatment step has the function of oxidizing the functional group to increase the oxygen content. It is considered that the spontaneous firing property is suppressed by such an action.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
Description
[改質炭の製造]
市販のボイラ用の石炭である亜瀝青炭(インドネシア産のアダロ炭)を、乾燥器を用いて空気中で乾燥して乾燥炭を得た(乾燥工程)。乾燥工程における加熱温度は150℃、加熱時間は30分間とした。得られた乾燥炭の揮発分(VM)は50質量%であり、水分量は10質量%以下であった。得られた乾燥炭を、乾留炉を用いて乾留して乾留炭を得た(乾留工程)。乾留工程における加熱温度は430℃、加熱時間は40分間とした。乾留炭の揮発分(VM)は25質量%であった。 Example 1
[Manufacturing of modified coal]
Commercially available coal for boilers, sub-bituminous coal (Adaro coal from Indonesia), was dried in the air using a drier to obtain dried coal (drying step). The heating temperature in the drying step was 150 ° C., and the heating time was 30 minutes. The volatile matter (VM) of the obtained dried coal was 50% by mass, and the water content was 10% by mass or less. The obtained dried coal was subjected to dry distillation using a dry distillation furnace to obtain dry distilled carbon (dry distillation step). The heating temperature in the dry distillation step was 430 ° C., and the heating time was 40 minutes. The volatile matter (VM) of dry-distilled carbon was 25% by mass.
国際連合危険物輸送勧告試験[クラス4、区分4.2(自然発火性物質・自己発熱性物質)]に準じた手法によって、得られた改質炭の自然発火性評価試験を行った。具体的には、金網で形成された、一辺が10cmの立方体形状を有する容器の中に改質炭を入れ、140℃の空気中に保管して発熱温度の経時変化を調べた。結果は、図2の曲線A1(改質炭)に示すとおりであった。 [Evaluation of spontaneous ignition (Fig. 2)]
The pyrophoricity evaluation test of the obtained modified coal was conducted by the method according to the United Nations Recommendations on the Transport of Hazardous Substances [
酸化処理工程における加熱温度を210℃にしたこと以外は、実施例1と同様にして改質炭を製造した。そして、実施例1と同様にして自然発火性評価試験を行った。結果は、図2の曲線A2に示すとおりであった。 (Example 2)
Modified coal was produced in the same manner as in Example 1 except that the heating temperature in the oxidation treatment step was 210 ° C. Then, in the same manner as in Example 1, a spontaneous ignition evaluation test was conducted. The results were as shown in curve A2 of FIG.
実施例1で用いた亜瀝青炭(インドネシア産のアダロ炭)の自然発火性評価試験を実施例1と同様にして行った。結果は、図2の曲線C1に示すとおりであった。 (Reference Example 1)
The spontaneous ignition evaluation test of the sub bituminous coal (Adaro coal from Indonesia) used in Example 1 was conducted in the same manner as in Example 1. The results were as shown in curve C1 of FIG.
市販のボイラ用の石炭である瀝青炭(オーストラリア産のマウントアーサ炭)の自然発火性評価試験を実施例1と同様にして行った。結果は、図2の曲線C2に示すとおりであった。 (Reference Example 2)
The pyrophoricity evaluation test of bituminous coal (mount isa charcoal of Australian origin) which is coal for commercial boilers was conducted in the same manner as in Example 1. The results are as shown in curve C2 of FIG.
酸化処理工程を行わなかったこと以外は、実施例1と同様とした。すなわち、乾留工程で得られた乾留炭の自然発火性評価試験を行った。結果は、図2の曲線E1に示すとおりであった。 (Comparative example 1)
The process was the same as Example 1 except that the oxidation treatment step was not performed. That is, the pyrophoricity evaluation test of the dry-distilled carbon obtained in the dry distillation process was conducted. The results were as shown in curve E1 of FIG.
酸化処理工程における加熱温度を200℃にしたこと以外は、実施例1と同様にして改質炭を製造した。そして、実施例1と同様にして自然発火性評価試験を行った。結果は、図2の曲線B1に示すとおりであった。 (Comparative example 2)
Modified coal was manufactured in the same manner as in Example 1 except that the heating temperature in the oxidation treatment step was set to 200 ° C. Then, in the same manner as in Example 1, a spontaneous ignition evaluation test was conducted. The results were as shown in curve B1 of FIG.
酸化処理工程における加熱温度を290℃にしたこと以外は、実施例1と同様にして改質炭を製造した。そして、実施例1と同様にして自然発火性評価試験を行った。結果は、図2の曲線B2に示すとおりであった。 (Comparative example 3)
Modified coal was produced in the same manner as in Example 1 except that the heating temperature in the oxidation treatment step was set to 290 ° C. Then, in the same manner as in Example 1, a spontaneous ignition evaluation test was conducted. The results are as shown in curve B2 of FIG.
実施例1と同様にして乾燥炭を得た。乾燥炭の揮発分(VM)は50質量%、水分量は10質量%以下であった。得られた乾燥炭の自然発火性評価試験を行った。結果は、図2の曲線D1に示すとおりであった。 (Comparative example 4)
Dry carbon was obtained in the same manner as Example 1. The volatile matter (VM) of the dried charcoal was 50% by mass, and the water content was 10% by mass or less. The pyrophoricity evaluation test of the obtained dried coal was conducted. The results were as shown in curve D1 of FIG.
(比較例5)
市販のボイラ用の石炭である亜瀝青炭(インドネシア産のアダロ炭)を、乾燥器を用いて空気中で乾燥して粒状の乾燥炭(粒径:0.5mm以下)を得た(乾燥工程)。乾燥工程における加熱温度は150℃、加熱時間は30分間とした。乾燥炭の揮発分(VM)は50質量%、水分量は10質量%以下であった。 [Influence of calorific value on calorific value (Fig. 3)]
(Comparative example 5)
Commercially available coal for boilers, sub-bituminous coal (Adaro coal from Indonesia), was dried in the air using a drier to obtain granular dry coal (particle size: 0.5 mm or less) (drying step) . The heating temperature in the drying step was 150 ° C., and the heating time was 30 minutes. The volatile matter (VM) of the dried charcoal was 50% by mass, and the water content was 10% by mass or less.
比較例5の乾燥炭を用いて乾留工程を行い、乾留炭を調製した。乾留工程における加熱温度は430℃、加熱時間は40分間とした。乾留炭の揮発分(VM)は25質量%であった。この乾留炭のDSC測定を比較例5と同様にして行った。結果は、図3の曲線E2に示すとおりであった。 (Comparative example 6)
A dry distillation step was carried out using the dried charcoal of Comparative Example 5 to prepare dry distilled charcoal. The heating temperature in the dry distillation step was 430 ° C., and the heating time was 40 minutes. The volatile matter (VM) of dry-distilled carbon was 25% by mass. The DSC measurement of this dry-distilled coal was performed in the same manner as in Comparative Example 5. The results are as shown in curve E2 of FIG.
乾留工程における加熱温度を550℃としたこと以外は、比較例6と同様にして乾留炭を調製した。乾留炭の揮発分(VM)は12質量%であった。この乾留炭のDSC測定を比較例5と同様にして行った。結果は、図3の曲線E3に示すとおりであった。 (Comparative example 7)
Dry-distilled carbon was prepared in the same manner as in Comparative Example 6 except that the heating temperature in the dry distillation step was 550 ° C. The volatile matter (VM) of dry-distilled carbon was 12% by mass. The DSC measurement of this dry-distilled coal was performed in the same manner as in Comparative Example 5. The results are as shown in curve E3 of FIG.
乾留工程における加熱温度を1000℃としたこと以外は、比較例6と同様にして乾留炭を調製した。乾留炭の揮発分(VM)は0質量%であった。この乾留炭のDSC測定を比較例5と同様にして行った。結果は、図3の曲線E4に示すとおりであった。 (Comparative example 8)
Dry-distilled carbon was prepared in the same manner as in Comparative Example 6 except that the heating temperature in the dry distillation step was set to 1000 ° C. The volatile matter (VM) of dry-distilled carbon was 0% by mass. The DSC measurement of this dry-distilled coal was performed in the same manner as in Comparative Example 5. The results are as shown in curve E4 of FIG.
(実施例3)
比較例6の乾留炭を用いて酸化処理工程を行い、改質炭を製造した。酸化処理の条件は、窒素ガスと酸素ガスの混合ガス雰囲気中(酸素濃度:10体積%)、加熱温度240℃、加熱時間40分間とした。製造した改質炭のDSC測定を比較例5と同様にして行った。結果は、図4の曲線A3に示すとおりであった。 [Influence of oxidation treatment temperature (Figure 4)]
(Example 3)
An oxidation treatment step was performed using the dry-distilled carbon of Comparative Example 6, to produce a modified coal. The conditions for the oxidation treatment were a mixed gas atmosphere of nitrogen gas and oxygen gas (oxygen concentration: 10% by volume), a heating temperature of 240 ° C., and a heating time of 40 minutes. DSC measurement of the produced modified coal was performed in the same manner as Comparative Example 5. The results were as shown in curve A3 of FIG.
比較例6の乾留炭を用いて酸化処理工程を行い、改質炭を製造した。酸化処理の条件は、窒素ガスと酸素ガスの混合ガス雰囲気中(酸素濃度:10体積%)、加熱温度260℃、加熱時間40分間とした。製造した改質炭のDSC測定を比較例5と同様にして行った。結果は、図4の曲線A4に示すとおりであった。 (Reference Example 4)
An oxidation treatment step was performed using the dry-distilled carbon of Comparative Example 6, to produce a modified coal. The conditions for the oxidation treatment were a mixed gas atmosphere of nitrogen gas and oxygen gas (oxygen concentration: 10% by volume), a heating temperature of 260 ° C., and a heating time of 40 minutes. DSC measurement of the produced modified coal was performed in the same manner as Comparative Example 5. The results were as shown in curve A4 of FIG.
比較例6の乾留炭を用いて酸化処理工程を行い、改質炭を製造した。酸化処理の条件は、窒素ガスと酸素ガスの混合ガス雰囲気中(酸素濃度:10体積%)、加熱温度200℃、加熱時間40分間とした。製造した改質炭のDSC測定を比較例5と同様にして行った。結果は、図4の曲線B3に示すとおりであった。 (Comparative example 9)
An oxidation treatment step was performed using the dry-distilled carbon of Comparative Example 6, to produce a modified coal. The conditions for the oxidation treatment were a mixed gas atmosphere of nitrogen gas and oxygen gas (oxygen concentration: 10% by volume), a heating temperature of 200 ° C., and a heating time of 40 minutes. DSC measurement of the produced modified coal was performed in the same manner as Comparative Example 5. The results are as shown in curve B3 of FIG.
比較例6の乾留炭を用いて酸化処理工程を行い、改質炭を製造した。酸化処理の条件は、窒素ガスと酸素ガスの混合ガス雰囲気中(酸素濃度:10体積%)、加熱温度300℃、加熱時間40分間とした。製造した改質炭のDSC測定を比較例5と同様にして行った。結果は、図4の曲線B4に示すとおりであった。 (Comparative example 10)
An oxidation treatment step was performed using the dry-distilled carbon of Comparative Example 6, to produce a modified coal. The conditions for the oxidation treatment were a mixed gas atmosphere of nitrogen gas and oxygen gas (oxygen concentration: 10% by volume), a heating temperature of 300 ° C., and a heating time of 40 minutes. DSC measurement of the produced modified coal was performed in the same manner as Comparative Example 5. The results were as shown in curve B4 of FIG.
(比較例11)
比較例6の乾留炭を、電気炉を用いて、窒素ガス雰囲気中、140℃に昇温した。昇温後、酸化処理工程を行って改質炭を製造した。酸化処理条件は、窒素ガスと酸素ガスの混合ガス雰囲気中(酸素濃度:10体積%)、酸化処理温度140℃、酸化処理時間20分間とした。酸化処理工程時の排ガスを全てサンプリングして平均化し、平均化したガス中のCO2及びCOの濃度を、ガスクロマトグラフ法を用いて測定した。 [Change of gas generation amount by oxidation treatment temperature (Fig. 5)]
(Comparative example 11)
The dry-distilled coal of Comparative Example 6 was heated to 140 ° C. in a nitrogen gas atmosphere using an electric furnace. After the temperature rise, an oxidation treatment step was carried out to produce modified coal. The oxidation treatment conditions were a mixed gas atmosphere of nitrogen gas and oxygen gas (oxygen concentration: 10% by volume), an oxidation treatment temperature of 140 ° C., and an oxidation treatment time of 20 minutes. All exhaust gases from the oxidation treatment step were sampled and averaged, and the concentration of CO 2 and CO in the averaged gas was measured using a gas chromatography method.
酸化処理工程における酸化処理温度を200℃にしたこと以外は、比較例11と同様にして改質炭を製造した。比較例11と同様にして酸化処理工程時の排ガス中のCO2及びCOの濃度を分析した。 (Comparative example 12)
Modified coal was produced in the same manner as in Comparative Example 11 except that the oxidation treatment temperature in the oxidation treatment step was set to 200 ° C. The concentration of CO 2 and CO in the exhaust gas during the oxidation treatment step was analyzed in the same manner as in Comparative Example 11.
酸化処理工程における酸化処理温度を220℃にしたこと以外は、比較例11と同様にして改質炭を製造した。比較例11と同様にして酸化処理工程時の排ガス中のCO2及びCOの濃度を分析した。 (Example 5)
Modified coal was produced in the same manner as in Comparative Example 11 except that the oxidation treatment temperature in the oxidation treatment step was set to 220 ° C. The concentration of CO 2 and CO in the exhaust gas during the oxidation treatment step was analyzed in the same manner as in Comparative Example 11.
酸化処理工程における酸化処理温度を240℃にしたこと以外は、比較例11と同様にして改質炭を製造した。比較例11と同様にして酸化処理工程時の排ガス中のCO2及びCOの濃度を分析した。 (Example 6)
Modified coal was produced in the same manner as in Comparative Example 11 except that the oxidation treatment temperature in the oxidation treatment step was 240 ° C. The concentration of CO 2 and CO in the exhaust gas during the oxidation treatment step was analyzed in the same manner as in Comparative Example 11.
酸化処理工程における酸化処理温度を260℃にしたこと以外は、比較例11と同様にして改質炭を製造した。比較例11と同様にして酸化処理工程時の排ガス中のCO2及びCOの濃度を分析した。 (Reference Example 7)
Modified coal was produced in the same manner as in Comparative Example 11 except that the oxidation treatment temperature in the oxidation treatment step was 260 ° C. The concentration of CO 2 and CO in the exhaust gas during the oxidation treatment step was analyzed in the same manner as in Comparative Example 11.
酸化処理工程における酸化処理温度を300℃にしたこと以外は、比較例11と同様にして改質炭を製造した。比較例11と同様にして酸化処理工程時の排ガス中のCO2及びCOの濃度を分析した。 (Comparative example 13)
Modified coal was produced in the same manner as in Comparative Example 11 except that the oxidation treatment temperature in the oxidation treatment step was set to 300 ° C. The concentration of CO 2 and CO in the exhaust gas during the oxidation treatment step was analyzed in the same manner as in Comparative Example 11.
(比較例14)
酸化処理工程における混合ガス雰囲気の酸素濃度を8体積%にしたこと以外は、比較例12と同様にして改質炭(酸化処理温度:200℃)を製造した。市販の赤外線分光分析計を用いて、製造した改質炭の赤外線分光分析(IR分析)を行った。分析結果は、図6の曲線B5に示すとおりであった。 [Analysis of surface condition of dry-distilled coal and modified coal (Fig. 6)]
(Comparative example 14)
Modified coal (oxidation treatment temperature: 200 ° C.) was produced in the same manner as in Comparative Example 12 except that the oxygen concentration in the mixed gas atmosphere in the oxidation treatment step was changed to 8% by volume. Infrared spectroscopy (IR analysis) of the produced modified coal was performed using a commercially available infrared spectrometer. The analysis results were as shown in curve B5 of FIG.
酸化処理工程における混合ガス雰囲気の酸素濃度を8体積%にしたこと以外は、比較例13と同様にして改質炭(酸化処理温度:300℃)を製造した。そして、比較例14と同様にして製造した改質炭の赤外線分光分析を行った。分析結果は、図6の曲線B6に示すとおりであった。 (Comparative example 15)
Modified coal (oxidation treatment temperature: 300 ° C.) was produced in the same manner as in Comparative Example 13 except that the oxygen concentration in the mixed gas atmosphere in the oxidation treatment step was changed to 8% by volume. Then, infrared spectroscopy analysis of the modified coal produced in the same manner as Comparative Example 14 was performed. The analysis results were as shown in curve B6 of FIG.
(比較例16)
比較例6の乾留炭を用いて酸化処理工程を行った。市販の熱重量・示差熱同時分析装置を用いて、酸化処理工程時における重量及び示差熱を測定した。具体的には、乾留炭を分析装置の中に設置して、窒素雰囲気中、140℃まで10℃/分の速度で昇温した。その後、雰囲気を窒素と酸素の混合雰囲気(酸素濃度:10体積%)に切り替えて、酸化処理を開始した。この切り替え時を基準として、熱重量・示差熱同時分析を行った。熱重量分析の結果は図7の曲線B7に、示差熱分析の結果は図8の曲線B7に示すとおりであった。 [Thermogravimetric / differential thermal analysis in the oxidation process (FIGS. 7 and 8)]
(Comparative example 16)
The oxidation treatment process was performed using the dry-distilled carbon of Comparative Example 6. The weight and differential heat at the time of the oxidation treatment step were measured using a commercially available thermogravimetric / differential thermal simultaneous analyzer. Specifically, dry-distilled coal was placed in an analyzer, and the temperature was raised to 140 ° C. at a rate of 10 ° C./minute in a nitrogen atmosphere. Thereafter, the atmosphere was switched to a mixed atmosphere of nitrogen and oxygen (oxygen concentration: 10% by volume) to start the oxidation treatment. Thermogravimetric / differential thermal simultaneous analysis was performed based on this switching time. The results of thermogravimetric analysis were as shown in curve B7 in FIG. 7, and the results of differential thermal analysis were as shown in curve B7 in FIG.
酸化処理工程における酸化処理温度(混合雰囲気への切り替え温度)を180℃にしたこと以外は、比較例16と同様にして熱重量・示差熱同時分析を行った。熱重量分析の結果は図7の曲線B8に、示差熱分析の結果は図8の曲線B8に示すとおりであった。 (Comparative example 17)
Simultaneous thermal weight and differential thermal analysis were performed in the same manner as in Comparative Example 16 except that the oxidation treatment temperature (the temperature at which the mixed atmosphere was switched) in the oxidation treatment step was set to 180 ° C. The results of thermogravimetric analysis were as shown by curve B8 in FIG. 7, and the results of differential thermal analysis were as shown by curve B8 in FIG.
酸化処理工程における酸化処理温度(混合雰囲気への切り替え温度)を200℃にしたこと以外は、比較例16と同様にして熱重量・示差熱同時分析を行った。熱重量分析の結果は図7の曲線B9に、示差熱分析の結果は図8の曲線B9に示すとおりであった。 (Comparative example 18)
Simultaneous thermal weight and differential thermal analysis were performed in the same manner as in Comparative Example 16 except that the oxidation treatment temperature (the switching temperature to the mixed atmosphere) in the oxidation treatment step was set to 200 ° C. The results of thermogravimetric analysis were as shown by curve B9 in FIG. 7, and the results of differential thermal analysis were as shown by curve B9 in FIG.
酸化処理工程における酸化処理温度(混合雰囲気への切り替え温度)を220℃にしたこと以外は、比較例16と同様にして熱重量・示差熱同時分析を行った。熱重量分析の結果は図7の曲線A5に、示差熱分析の結果は図8の曲線A5に示すとおりであった。 (Example 8)
The thermogravimetric / differential thermal simultaneous analysis was performed in the same manner as in Comparative Example 16 except that the oxidation treatment temperature (the temperature at which the mixed atmosphere was switched) in the oxidation treatment step was 220 ° C. The results of thermogravimetric analysis were as shown in curve A5 in FIG. 7, and the results of differential thermal analysis were as shown in curve A5 in FIG.
酸化処理工程における酸化処理温度(混合雰囲気への切り替え温度)を240℃にしたこと以外は、比較例16と同様にして熱重量・示差熱同時分析を行った。熱重量分析の結果は図7の曲線A6に、示差熱分析の結果は図8の曲線A6に示すとおりであった。 (Example 9)
Thermal weight and differential thermal simultaneous analysis were performed in the same manner as in Comparative Example 16 except that the oxidation treatment temperature (the temperature at which the mixed atmosphere was switched) in the oxidation treatment step was 240 ° C. The results of thermogravimetric analysis were as shown by curve A6 in FIG. 7, and the results of differential thermal analysis were as shown by curve A6 in FIG.
酸化処理工程における酸化処理温度(混合雰囲気への切り替え温度)を260℃にしたこと以外は、比較例16と同様にして熱重量・示差熱同時分析を行った。熱重量分析の結果は図7の曲線A7に、示差熱分析の結果は図8の曲線A7に示すとおりであった。 (Reference Example 10)
Simultaneous thermal weight and differential thermal analysis were performed in the same manner as in Comparative Example 16 except that the oxidation treatment temperature (the temperature at which the mixed atmosphere was switched) in the oxidation treatment step was 260 ° C. The results of thermogravimetric analysis were as shown in curve A7 in FIG. 7, and the results of differential thermal analysis were as shown in curve A7 in FIG.
酸化処理工程における酸化処理温度(混合雰囲気への切り替え温度)を300℃にしたこと以外は、比較例16と同様にして熱重量・示差熱同時分析を行った。熱重量分析の結果は図7の曲線B10に、示差熱分析の結果は図8の曲線B10に示すとおりであった。 (Comparative example 19)
Thermal weight and differential thermal simultaneous analysis were performed in the same manner as in Comparative Example 16 except that the oxidation treatment temperature (the temperature at which the mixed atmosphere was switched) in the oxidation treatment step was set to 300 ° C. The results of thermogravimetric analysis were as shown in curve B10 of FIG. 7 and the results of differential thermal analysis were as shown in curve B10 of FIG.
上述の比較例6の乾留炭と、比較例9、実施例3及び比較例10の改質炭の元素分析を行った。その結果を表1に示す。 <Mechanism to suppress spontaneous firing property>
The elemental analysis of the dry-distilled carbon of the above-mentioned comparative example 6 and the modified coal of comparative example 9, example 3 and comparative example 10 was conducted. The results are shown in Table 1.
実施例1の乾燥工程を行って得られた乾燥炭を、660℃で40分間加熱して乾留炭を調製した。実施例1と同じ自然発火性評価試験を行って、調整した乾留炭の自然発火性の評価を行った。その結果を図10の曲線F1に示す。また、図10には、図2に示されている曲線E1(乾留炭、乾留温度:430℃)も比較のため示す。 <Comparison of spontaneous firing ability>
The dried charcoal obtained by performing the drying step of Example 1 was heated at 660 ° C. for 40 minutes to prepare dry distilled charcoal. The same pyrophoricity evaluation test as in Example 1 was carried out to evaluate the pyrophoric nature of the adjusted dried carbon. The result is shown by curve F1 in FIG. Further, FIG. 10 also shows a curve E1 (dry carbon, dry distillation temperature: 430 ° C.) shown in FIG. 2 for comparison.
Claims (6)
- 石炭を300~650℃で乾留して乾留炭を得る乾留工程と、
前記乾留炭を、200℃を超え且つ240℃以下の温度範囲で10~60分間酸化処理する酸化処理工程と、を有する、改質炭の製造方法。 Dry distillation at 300 to 650 ° C. to obtain dry carbon;
And oxidizing the dried carbon in a temperature range of more than 200 ° C. and not more than 240 ° C. for 10 to 60 minutes. - 前記乾留工程の前に、150℃以下で石炭を乾燥する乾燥工程を有し、
前記乾留工程では、前記乾燥工程で乾燥された石炭を乾留する、請求項1に記載の改質炭の製造方法。 Before the said dry distillation process, it has a drying process which dries coal below 150 ° C,
The method for producing modified coal according to claim 1, wherein in the dry distillation step, the coal dried in the drying step is dry distilled. - 前記石炭は水分が50質量%以上である、請求項1又は2に記載の改質炭の製造方法。 The method for producing modified coal according to claim 1, wherein the coal has a water content of 50% by mass or more.
- 前記乾留工程で得られる前記乾留炭の揮発分は10~30質量%である、請求項1~3のいずれか一項に記載の改質炭の製造方法。 The method for producing modified coal according to any one of claims 1 to 3, wherein the volatile matter content of the dry distilled carbon obtained in the dry distillation step is 10 to 30% by mass.
- 前記酸化処理工程で得られる改質炭の揮発分は5~30質量%である、請求項1~4のいずれか一項に記載の改質炭の製造方法。 The method for producing modified coal according to any one of claims 1 to 4, wherein the volatile content of the modified coal obtained in the oxidation treatment step is 5 to 30% by mass.
- 前記石炭の乾留によって発生する揮発成分を含むガスを燃焼炉で燃焼する燃焼工程を有し、
前記酸化処理工程では、前記燃焼炉からの酸素を含む排ガスによって前記乾留炭を酸化処理する、請求項1~5のいずれか一項に記載の改質炭の製造方法。 The combustion step of burning the gas containing the volatile component generated by the carbonization of the coal in the combustion furnace,
The method for producing reformed coal according to any one of claims 1 to 5, wherein in the oxidation treatment step, the dry-distilled coal is oxidized by an exhaust gas containing oxygen from the combustion furnace.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2018378746A AU2018378746B2 (en) | 2017-12-08 | 2018-10-16 | Method for producing reformed coal |
CN201880077972.7A CN111433330A (en) | 2017-12-08 | 2018-10-16 | Method for producing modified coal |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2017235840A JP6402235B1 (en) | 2017-12-08 | 2017-12-08 | Method for producing modified coal |
JP2017-235840 | 2017-12-08 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2019111540A1 true WO2019111540A1 (en) | 2019-06-13 |
Family
ID=63788039
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2018/038445 WO2019111540A1 (en) | 2017-12-08 | 2018-10-16 | Method for producing reformed coal |
Country Status (4)
Country | Link |
---|---|
JP (1) | JP6402235B1 (en) |
CN (1) | CN111433330A (en) |
AU (1) | AU2018378746B2 (en) |
WO (1) | WO2019111540A1 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP6972418B1 (en) * | 2021-06-24 | 2021-11-24 | 日鉄エンジニアリング株式会社 | Oxidation treatment equipment and oxidation treatment method, and method for manufacturing reformed fuel |
JP7091530B1 (en) * | 2021-08-04 | 2022-06-27 | 日鉄エンジニアリング株式会社 | Carbon material and its manufacturing method |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH10279969A (en) * | 1997-03-31 | 1998-10-20 | Mitsubishi Heavy Ind Ltd | Aging of improved coal and aged improved coal |
JPH10332134A (en) * | 1997-03-31 | 1998-12-15 | Mitsubishi Heavy Ind Ltd | Production of reformed coal and equipment therefor |
JP2013139537A (en) * | 2012-01-06 | 2013-07-18 | Mitsubishi Heavy Ind Ltd | Method for deactivating coal |
JP2014031462A (en) * | 2012-08-06 | 2014-02-20 | Mitsubishi Heavy Ind Ltd | Coal carbonization apparatus and facility for producing modified coal by utilizing the same |
-
2017
- 2017-12-08 JP JP2017235840A patent/JP6402235B1/en active Active
-
2018
- 2018-10-16 WO PCT/JP2018/038445 patent/WO2019111540A1/en active Application Filing
- 2018-10-16 CN CN201880077972.7A patent/CN111433330A/en active Pending
- 2018-10-16 AU AU2018378746A patent/AU2018378746B2/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH10279969A (en) * | 1997-03-31 | 1998-10-20 | Mitsubishi Heavy Ind Ltd | Aging of improved coal and aged improved coal |
JPH10332134A (en) * | 1997-03-31 | 1998-12-15 | Mitsubishi Heavy Ind Ltd | Production of reformed coal and equipment therefor |
JP2013139537A (en) * | 2012-01-06 | 2013-07-18 | Mitsubishi Heavy Ind Ltd | Method for deactivating coal |
JP2014031462A (en) * | 2012-08-06 | 2014-02-20 | Mitsubishi Heavy Ind Ltd | Coal carbonization apparatus and facility for producing modified coal by utilizing the same |
Also Published As
Publication number | Publication date |
---|---|
CN111433330A (en) | 2020-07-17 |
JP6402235B1 (en) | 2018-10-10 |
AU2018378746A1 (en) | 2020-06-18 |
JP2019099777A (en) | 2019-06-24 |
AU2018378746B2 (en) | 2021-02-25 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP5511855B2 (en) | Coal deactivation treatment method | |
WO2019111540A1 (en) | Method for producing reformed coal | |
JP5412418B2 (en) | Coal inactivation processing equipment | |
KR101769627B1 (en) | Self-ignition resistant thermally-activated carbon | |
JPH09157671A (en) | Method for forming passivated charr by treating noncaking coal | |
WO2012166606A2 (en) | Coal processing to upgrade low rank coal having low oil content | |
JPS6367518B2 (en) | ||
JP6910546B2 (en) | Molded fuel and its manufacturing method | |
WO2011115262A1 (en) | Process for production of solid fuel for use in sintering, solid fuel for use in sintering, and process for manufacturing sintered ore using same | |
KR20150024913A (en) | Blast-furnace-blow-in charcoal and method for producing same | |
JP6988622B2 (en) | How to determine the spontaneous combustion of char and how to determine the spontaneous combustion of coal | |
JPS6362559B2 (en) | ||
WO2023012773A1 (en) | Carbon material and production method therefor | |
JPS6332839B2 (en) | ||
JP5967649B2 (en) | Method for producing carbonized coal, method for operating a blast furnace, and method for operating a boiler | |
KR20180120718A (en) | How to operate blast furnace | |
JP7397303B2 (en) | Method for producing sintered ore | |
JP6219185B2 (en) | Method for producing modified coal and modified coal | |
Cornea | Influence of the degree of carbonization and granulation of fuel on combustion process | |
JP2015218271A (en) | Method for producing modified coal and modified coal | |
JP6295791B2 (en) | Sinter ore production method and evaluation method of coal char or anthracite or semi-anthracite | |
KR100448727B1 (en) | Method of discriminating weathered coal using oxidation heat | |
JP6348250B2 (en) | Method for producing solid fuel and solid fuel | |
JP5729259B2 (en) | How to handle brown coal | |
SECARA | EVALUATION OF COMBUSTION BEHAVIOUR FOR INDONESIAN LOW-RANK COALS TREATED HYDROTHERMALLY |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 18885697 Country of ref document: EP Kind code of ref document: A1 |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
ENP | Entry into the national phase |
Ref document number: 2018378746 Country of ref document: AU Date of ref document: 20181016 Kind code of ref document: A |
|
122 | Ep: pct application non-entry in european phase |
Ref document number: 18885697 Country of ref document: EP Kind code of ref document: A1 |