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Rheological properties of coal gangue slurry

                demonstrated  significant  effectiveness  and  economic   mass  ratios  (e.g.,  7:3  and  3:7)  —were  systematically
                benefits in subsidence control across multiple mining   examined to analyze their effects on slurry properties.
                areas in China. 2                                   To improve viscosity, two types of superplasticizers –
                  The primary objectives of strata separation injection   polycarboxylate and sulfamic acid – were analyzed for
                are  to  mitigate  ground  subsidence,  prevent  water-  their role in reducing viscosity. Finally, the influence of
                related  hazards  in  separated  strata,  and  facilitate  the   injection pressure on the water bleeding rate of the slurry
                disposal  of  mining  solid  waste.  The  ideal  injection   was analyzed to simulate practical injection conditions.
                slurry  should  exhibit  low  viscosity  and  high  fluidity   This study provides valuable insights into the preparation
                to ensure effective diffusion to distant areas from the   and injection of fly ash–coal gangue mixed slurry.
                injection  station.   Moreover,  the  slurries  should  have
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                a  low  water  bleeding  rate  to  avoid  pipeline  clogging   2. Materials and methods
                during  prolonged  grouting  operations.  The  slurries
                must  be  environmentally  safe,  ensuring  non-toxicity   2.1. Raw materials
                and  minimal  environmental  impact  to  protect  both   The  chemical  compositions  and  component  contents
                geological formations and human health.             of  fly  ash  and  coal  gangue  used  in  this  study  were
                  The  key  performance  indicators  for  strata    analyzed  using  an  X-ray  fluorescence  spectrometer
                separation  injection  slurries  include  density,  water   (S8 Tiger, Bruker, Germany) and an X-ray diffraction
                bleeding  characteristics,  and  viscosity.   In  addition,   system  (D8,  Bruker,  Germany).  The  results  revealed
                                                    4
                the cost-effectiveness of materials must be taken into   that  coal  gangue  was  predominantly  composed  of
                consideration during the raw material selection process.   silicon dioxide, aluminum oxide, titanium dioxide, and

                Fly ash has been proven to be the dominant material in   ferric oxide, while fly ash primarily consists of silicon
                mining areas for strata separation injection due to its   dioxide and ferric oxide (Table 1 and Figure 2). Fly ash
                low cost and accessibility, while its increasing demand   is  typically  obtained  by  collecting  fine  residues  from
                –  driven  by  the  expanding  application  of  diverse   ground  coal  combustion  and  has  a  similar  geological
                technologies – has led to shortages in some regions.    origin  to  coal  gangue.  Apart  from  differences  in
                                                                5
                Consequently,  coal  gangue  –  a  prevalent  solid  waste   component  proportions,  the  two  raw  materials  share
                in coal mining areas – is being explored as a potential   similar  major  crystalline  phases,  including  quartz,
                alternative raw material for injection slurries.    hematite,  and  anhydrite.  Elemental  analysis  did  not
                  Critical  challenges  include  determining  the   detect high concentrations of heavy metals in fly ash or
                optimal  grinding  particle  size  for  coal  gangue  to   coal gangue, indicating their environmental safety for
                balance economic feasibility and slurry performance.    injection into the separated strata space.
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                Although extensive research and engineering practices   Figure 3 illustrates the results of thermogravimetric-
                have  focused  on  preparing  slurries  with  fly  ash,  the   differential  scanning  calorimetry  analysis  of  coal
                development  of  injection  slurries  using  coal  gangue   gangue and fly ash. The mass of coal gangue and fly
                without  cementitious  materials  remains  limited,  and   ash declined by 6 wt% and 4 wt%, respectively, after
                diffusion  modeling  for  such  suspensions  in  fractured   heating to 400℃. This mass loss is typically attributed
                strata  lacks  experimental  validation.   Specifically,   to the evaporation of water and the decomposition of
                                                   7,8
                studies  on  the  fluid  properties  of  slurries  prepared   organic  matter.  As  the  temperature  further  increased
                from fly ash and coal gangue under injection pressure   to  900℃,  the  mass  continued  to  decrease  due  to  the
                are  relatively  scarce.  This  gap  underscores  the  need   decomposition of carbonates and sulfates.
                for  systematic  research  to  evaluate  the  compatibility,
                rheology,  and  long-term  stability  of  such  complex   2.2. Orthogonal experimental design
                systems in practical injection applications.        A  mixed-level  L18  (3  × 5 )  orthogonal  array  was
                                                                                         2
                                                                                               1
                  This study investigates the rheological performance   adopted  to  systematically  evaluate  the  main  effects
                of  coal  gangue  and  fly  ash  mixed  slurry  as  a  filling   of  the  selected  factors  (factor  A:  solid  volume
                material  through  orthogonal  experiments.  The    concentration, factor B: coal gangue particle size, and
                evaluated  performance  parameters  include  water   factor C: fly ash-to-coal gangue mass ratio) on slurry
                bleeding  characteristics,  density,  and  viscosity.  Three   properties. While orthogonal designs inherently assume
                independent  factors  –  solid  volume  concentrations   minimal  interaction  effects  to  efficiently  screen  main
                (e.g., 50%, 60%, and 70%), coal gangue particle sizes   factors, potential interactions were statistically assessed
                (e.g., 50, 100, and 150 mesh), and fly ash-to-coal gangue   post-experiment  using  one-way  analysis  of  variance



                Volume 22 Issue 5 (2025)                       215                           doi: 10.36922/AJWEP025210162
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