16 results on '"LIU Jiong-tian"'
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2. Extended DLVO theory applied to coal slime-water suspensions
- Author
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Zhang, Ming-qing / 张明青, Liu, Qi / 刘颀, and Liu, Jiong-tian / 刘炯天
- Published
- 2012
- Full Text
- View/download PDF
3. Modification technology for separation of oily sludge
- Author
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Li, Xiao-bing, Liu, Jiong-tian, Xiao, Yun-qi, and Xiao, Xin
- Published
- 2011
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4. Effects of clay and calcium ions on coal flotation
- Author
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Zhang Zhi-jun, Ma Liqiang, Xu Zhiqiang, and Liu Jiong-tian
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lcsh:TN1-997 ,inorganic chemicals ,Scanning electron microscope ,Energy Engineering and Power Technology ,chemistry.chemical_element ,Mineralogy ,Calcium ,engineering.material ,complex mixtures ,Ion ,Coating ,Geochemistry and Petrology ,otorhinolaryngologic diseases ,Coal ,lcsh:Mining engineering. Metallurgy ,High concentration ,business.industry ,technology, industry, and agriculture ,respiratory system ,Geotechnical Engineering and Engineering Geology ,Chemical engineering ,chemistry ,engineering ,Spectrum analysis ,business ,Clay minerals ,Geology - Abstract
The microflotation of three single minerals, mixed coal–kaolinite and mixed coal–montmorillonite were examined to study the effects of clay and calcium ions on coal flotation. The results show that the ash content of flotation concentrate increases by 3% in the presence of clay minerals, and the ash content would further increase by 3% in co-presence of clay minerals and high concentration of Ca2+. Scanning electron microscope (SEM) images and elemental spectrum analysis indicate that fine clay particles that coat on the coal surface, which is called slime coating, can affect the coal flotation. The slime coating would be induced much more easily in the presence of Ca2+. Keywords: Microflotation, Clay, Calcium ions, Slime coating
- Published
- 2013
5. Experimental research on anionic reverse flotation of hematite with a flotation column
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Liu Jiong-tian, Li Lin, Cao Yi-jun, Wang Yong-tian, Yu He-sheng, and Zhang Hai-jun
- Subjects
Chromatography ,Materials science ,flotation column ,Earth and Planetary Sciences(all) ,General Medicine ,Hematite ,Flow sheet ,hematite ,Experimental research ,Chemical engineering ,visual_art ,visual_art.visual_art_medium ,anionic reverse flotation ,Reverse flotation - Abstract
An experimental research on magnetic concentrate of a hematite using the anionic reverse flotation technology in the flotation column was conducted. Through systematic studies in the lab, the optimal technological and operational conditions had been obtained as follows: the circulation pressure of 0.055 MPa, the feeding quantity of 160 g/min, the collector dosage of 800 g/t and the starch dosage of 900 g/t. The results show that the iron concentrate with grade of 67.37% can be achieved according to the flow sheet of one roughing and one scavenging under the optimal conditions, and also reflects the advantages of excellent selectivity and high recovery. The application of cyclonic static micro-bubble flotation column in hematite reverse flotation provides a new approach for hematite reverse flotation in China.
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- 2009
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- View/download PDF
6. Study of chlorite flotation and its influencing factors
- Author
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Liu Jiong-tian, Cao Yi-jun, Zheng Gui-shan, Liu Li-jun, and Wang Yong-tian
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fluoride ,Inorganic chemistry ,Cationic polymerization ,flotation ,Earth and Planetary Sciences(all) ,General Medicine ,activator ,depressor ,chemistry.chemical_compound ,Oleic acid ,chlorite ,chemistry ,Amine gas treating ,regulatory ,Neutral ph ,Fluoride ,Chlorite - Abstract
This paper made deep studies on chlorite flotation using anionic/cationic collector, and the following effect factors such as pH,Ca 2+ ,Na 2 S,NaF,Na 2 SiF 6 and (NaPO 3 ) 6 are investigated. In the process of chlorite flotation using oleic acid as anionic collector, pH value increases. The concentration increase of Na 2 S and NaF can activate the chlorite flotation. However, Ca 2+ , Na 2 SiF 6 and (NaPO 3 ) 6 can depress the chlorite flotation. In the process of chlorite flotation using lauryl amine as cationic collector, the maximum recovery of chlorite flotation happened in neutral pH condition, and the concentration increase of Ca 2+ can activate the chlorite flotation; however, NaF and Na 2 SiF 6 can depress the chlorite flotation.
- Published
- 2009
- Full Text
- View/download PDF
7. Technologic optimization for separation of scarce coal sludge
- Author
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Zheng Gui-shan, Wang Yong-tian, Liu Li-jun, and Liu Jiong-tian
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Grinding process ,Waste management ,business.industry ,Earth and Planetary Sciences(all) ,General Medicine ,Coke ,Production efficiency ,grinding ,Grinding ,difficult-to-float coal slime ,condition optimization ,Environmental science ,Coal ,business ,flotation process - Abstract
Qianjiaying coke coal slime is extremely difficult to float. Conventional flotation process leads to a massive waste of high quality coal. In this paper, raw coal slime and rough separation concentrate are grinded to improve separation effect. Coal slime grinded directly through rough-cleaning process can get concentrate rate of 52.87% and concentrate ash of 11.27%. In the rough concentrate grinding process, concentrate ash drops to 10.74%, when the concentrate accumulation rate reaches up to 55.53%. Compared with the coal slime direct floatation, the concentrate rate was enhanced by 4.66%, and the ash was decreased by 1.02%. Besides, in the regrinding of middlings flotation, the concentrate rate reaches as high as 68.35% and ash rate is only 11.51%, the production efficiency is greatly improved.
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- 2009
8. Settling characteristics analysis of coal slime water based on original hardness.
- Author
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ZHANG Zhi-jun and LIU Jiong-tian
- Abstract
A new conception of original hardness was proposed to evaluate the settling characteristics of coal slime water. The mineralogical and water quality analysis of four coal preparation plants shows the original hardness is determined by the basic hardness of washing water and the minerals composition of coal ores, and the mathematical iteration model of original hardness was developed, and the model has high reliability which is verified by laboratory simulation tests of coal slime water cycle. The settling tests indicate that the higher water hardness, the higher settling rate, and the clearer supernatant when the water hardness under 5 mmol/L. Some examples of coal preparation plants show that coal slime water is hard to settle at low original hardness, and it is easy to clarify at high original hardness. As a result, the original hardness is key influence factor of settling characteristics of coal slime water. [ABSTRACT FROM AUTHOR]
- Published
- 2014
- Full Text
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9. Application and affect mechanism of high turbulence in pipe unit enhancing coal column flotation.
- Author
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LIAO Yin-fei, LIU Jiong-tian, and LI Shu-lei
- Abstract
In order to enhance the coal column flotation and fine size fraction recovery, the pipe unit length of cyclonicstatic micro bubble flotation bed was adjusted. The variation of flotation performance, product features and carrying capacity at different length was analyzed with the affect mechanism also investigated combining hydrodynamics and flotation kinetics theory. It is shown that when the length is extended from 1. 5 m to 3. 0 m, the combustible recovery increases by 6. 46% in the case of equivalent ash and the fine size fraction recovery of 0. 074-0. 045 mm and <0. 045 mm is also increased by 7. 96% and 8. 41% respectively at the same time carrying capacity raising 0. 09 t/ ( h ⋅ m²). All of these increase rates increase with the mass flow rate of solids in the feed. The pipe unit length extended improves the turbulent kinetic energy and collision rate between mineral particles and bubbles, which can promote the improvement of the overall flotation index. [ABSTRACT FROM AUTHOR]
- Published
- 2014
- Full Text
- View/download PDF
10. Carrying capacity and axial distribution of gas holdup in coal column flotation.
- Author
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LIAO Yin-fei, LIU Jiong-tian, and LI Shu-lei
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GASES , *FLUIDS , *COAL , *CAUSTOBIOLITHS , *FLOTATION - Abstract
In order to optimize the capacity and separation performance of column flotation equipment, pressure difference method was used to monitor gas holdup in flotation column. By adjusting the feed rate and feed concentration, the variation of carrying capacity and gas holdup profile in the axial was analyzed, with their internal relations and effect on separation performance also investigated. It is shown that the axial gas holdup increases from the bottom to the top when the feed rate is less than critical velocity. But it is opposite when more than or equal to critical velocity, which decreases with the increase of feed concentration. Increasing feed rate, the carrying capacity fist increases and then decreases, whose inflection point just is the critical velocity. The feed concentration increase can help improve the carrying capacity and the combustible recovery within a certain range. The carrying capacity prediction model is proposed with the squared correlation coefficient R² = 0. 873, which achieves a relatively high fitting precision. [ABSTRACT FROM AUTHOR]
- Published
- 2013
11. Experimental study on removal of unburned carbon from coal fly ash using flotation column.
- Author
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LI Guo-sheng, LIU Jiong-tian, CAO Yi-jun, and REN Lin-zhu
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X-ray diffraction , *CARBON , *CONTACT angle measurement , *X-ray fluorescence , *FLY ash - Abstract
The fly ash sample was characterized by size fraction, X-ray diffraction, contact angle measurements and X-ray fluorescence. The function of a new type of frother (KD) which can produce more stable foam than conventional frothers was studied. The effect of the column flotation operating variables on the removal of unburned carbon from the fly ash was also systematically examined. Within the range studied, the optimum frother dosage is 400 g/t, superficial gas velocity is 1. 8 cm/s, froth thickness is about 150-200 mm and circulating pressure is 0. 22 MPa. The results indicate that Cyclonic-Static Micro-bubble Flotation Column (FCSMC ) technique is effective in removing the unburned carbon from coal fly ash. Under the optimized conditions, a cleaning ash with 3. 15% LOI (Loss on Ignition) and 91. 88% RUC(Removal Rate of Unburned Carbon) is obtained. [ABSTRACT FROM AUTHOR]
- Published
- 2013
12. Separation index prediction of cyclonic-static micro-bubble flotation column based on BP neural network.
- Author
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Liao Yin-Fei and Liu Jiong-Tian
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MICROBUBBLES , *BUBBLES , *FLOTATION , *COAL ash , *ARTIFICIAL neural networks - Abstract
BP neural network model was used to predict the cleaned coal ash and combustible recovery in different operational conditions. Taking the circulation pressure, air flow, dosage of collector and frother as input set, the BP neural networkas prediction model was proposed to estimate the cleaned coal ash and combustible recovery as outputs. It is shown that BP neural network model can estimate the separation index quite satisfactorily in which the relative errors between the predicted values and experimental values are both less than 5% for the cleaned coal ash and combustible recovery. [ABSTRACT FROM AUTHOR]
- Published
- 2012
13. Two-phase numerical simulation on the pipe flow unit of cyclonicstatic micro bubble flotation column.
- Author
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Yan Xiao-Kang, Liu Jiong-Tian, and Zhou Chang-Chun
- Subjects
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NUMERICAL analysis , *PIPE flow , *GAS flow , *BAUXITE , *FLOTATION - Abstract
Two-phase, three-dimensional (3D) numerical simulation was performed to predict the mineralization efficiency of the pipe flow unit of a micro-bubble floatation column. Based on the numerical model, the length parameter of pipe flow unit was optimized, and get a coherent result with industrial test. The results show that eulerian multiphase model can be used to calculate the gas-fluid flow in pipe unit accurately. For pipe unit, the mineralization effect of different pipe lengths can be qualitatively evaluated by the value of k (turbulent kinetic energy). The volume integral value of k grows logarithmically with the increase of L(pipe length). Namely, the increment speed of k is fast at the beginning, and then not obvious when L is increasing. Pipe length has no effect on the maximal value of k. 2. 5 m is a proper length for the research object. Bauxite recovery increases 2.79% when L is extended from 0. 3 m to 2.5 m in industrial test. [ABSTRACT FROM AUTHOR]
- Published
- 2012
14. Surface thermodynamic characterization of fine coal by Washburn dynamic method.
- Author
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ZOU Wen-jie, CAO Yi-jun, and LIU Jiong-tian
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COAL ash , *THERMODYNAMICS research , *KAOLINITE , *COAL research , *BROMINE compounds - Abstract
The poor selectivity and high ash content of clean coal are the prominent issues in fine coal flotation. Wettability is one of the important interface properties affecting the fine coal flotation. Thermodynamic characterization of fine coal and main impurity mineral kaolinite was investigated in this study. Washburn dynamic method was used to study the wetting process of different density level coal samples and kaolinite wetted by n-hexane, 1-bromine naphthalene, formamide and water as liquid molecular probe. Wetting rate and lipophilic hydrophilic ratio (LHR) was calculated by linear regression analysis method. Washburn equation and van Oss-Chaudhury-Good theory were used to estimate the surface free energy components of samples. The results show that n-hexane wetting rate of coal samples decreases with the increase of density level which is slight, but deionized water wetting rate of coal samples increases. The wetting rates of kaolinite wetted by n-hexane and water are 0. 010 1 and 0. 020 6 g²/s respectively, however, they are higher than that of coal samples. The LHR of kaolinite is 1.44 and kaolinite is hydrophilic; the LHR of coal samples increases with the increase of density level. The middle density level coal sample of 1.5-1.6 g/cm³ and 1.6-1.8 g/cm³ with similar wetting rates and LHR values are hydrophobic. Surface free energy polar component γsLW of each density level of coal samples reduces slightly and is all lower than γsLW of kaolinite. Furthermore, the alkaline force of the sample surface free energy polar components, which is of hydrogen bonding interaction, is correlated to LHR value. The results of regressive release flotation test coincides well with the coal sample surface properties. [ABSTRACT FROM AUTHOR]
- Published
- 2013
15. Process characteristics of heterogeneous fine mud in the coal flotation.
- Author
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Gui Xia-Hui, Cheng Gan, Liu Jiong-Tian, Li Shu-Lei, Wang Yong-Tian, and Cao Yi-Jun
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COAL , *CAUSTOBIOLITHS , *FLOTATION , *ORE-dressing , *CLAY - Abstract
Processing objects is a kind of hard-to-float and high-ash fine coal which collected in Kailuan mining. Flotation rate experiment was designed for investigating the process characteristics of fine coal. Size analysis and density analysis of five cleans and fine-grained of the flotation rate experiment were studied. The mineral morphology of flotation rate experiment cleans was observed by scanning electron microscopy(SEM). The results show that fine mud contamination exists throughout the flotation process. The fine mud content in J1, J2, J3, J4 and J5 is similar, but gradually increases in its product. With the conduct of flotation, the flotation rate of high-ash fine mud (ash content> 50% ) reduces, and the operation recovery of fine mud per unit time also reduce. Flotation rate and cumulative yield of heterogeneity fine mud increase with its size and density reducing. The way of high-ash fine mud into clean coal products is mechanical entrainment and covering the surface of coarse-grained coal by SEM and Stokes number(St) analysis. [ABSTRACT FROM AUTHOR]
- Published
- 2012
16. Selective flocculation of coal and kaolinite.
- Author
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ZOU Wen-jie, CAO Yi-jun, LI Wei-na, LIU Jiong-tian, and WANG Yong-tian
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FLOCCULATION , *CLUSTERING of particles , *COAL , *CAUSTOBIOLITHS , *KAOLINITE - Abstract
In order to study the selectivity of flocculant between coal and kaolinite in selective flocculation floatation, the adsorption isotherm and adsorbance difference of polyacrylamide onto kaolinite and coal was investigated. The laser particle size analyzer was used to measure the floes size distribution of coal and kaolinite in different polyacrylamide solution. Hydrodynamic radius and adsorption radius of polyacrylamide molecular were calculated to discuss its adsorption conformation. The adsorbance of anionic polyacrylamide onto coal is higher than that of kaolinite. The adsorbance difference between coal and kaolinite decreases with the increase of polyacrylamide molecular weight. The adsorbance of cationic polyacrylamide onto kaolinite is higher than that of coal, and the adsorbance difference is lower. Selectivity of anionic polyacrylamide with molecular weight 3x106 is the best. Adsorption process of coal and kaolinite is more accord with Langmuir adsorption model. The coal adsorbance of this polyacrylamide is 2.15 times larger than that of kaolinite. The indicators of particle size distribution, d10, d50 and d90 of coal floes are 8.42, 2.60 and 2.75 times of kaolinite floes, respectively. The calculated adsorption radius of polyacrylamide molecular is lower than its hydrodynamic radius. When different polyacrylamide is absorbed onto different mineral surfaces, the effect of compression or penetration with different intensity of polyacrylamide occurres. [ABSTRACT FROM AUTHOR]
- Published
- 2013
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