Large scale experimental simulations of underground coal gasification (UCG) process with selected European lignites

Transcription

1 8 th International Freiberg Conference on IGCC & XtL Technologies Large scale experimental simulations of underground coal gasification (UCG) process with selected European lignites Krzysztof Kapusta 1, Krzysztof Stańczyk 1, Alexandru Solschi 2, Simon Zavšek 3, Sorin Balacescu 4 1 Central Mining Institute (GIG), Poland 2 Institutul de Studii si Proiectari Energetice (ISPE), Romania 3 Premogovnik Velenje DD, Slovenia 4 Complexul Energetic Oltenia (CEO), Romania Cologne, 14 th June

2 UCG of low-grade lignites: Perspectives and challenges Lignites, the recoverable reserves of which are estimated at 18 percent of the total global coal reserves, remain a crucial contributor to the energy supply in many countries They are characterised by high moisture contents, reaching up to 60 wt%, poor calorific values and high susceptibility to spontaneous ignition (must be used in close proximity to their mining sites) The issue of the suitability of high-moisture lignites for UCG is still questionable due to many technological difficulties to be solved, e.g. poor gas quality, low thermal efficiency and water management Regarding the UCG of lignites, most of the global research activities were focused on hard lignite (meta-lignite). 2

3 Project Coal2Gas: In brief Enhanced Coal Exploitation through Underground Coal Gasification in European Lignite Mines Objectives The overall objective of the COAL2GAS Project is to evaluate the feasibility of UCG in shallow lignite seams, geologically, technically and environmentally and to illustrate this for a selected deposit in Romania. A future pilot will be prepared focusing on environmental protection. Chances will be assessed for other similar European deposits. Project Consortium Project co-funded by the European Commission under the Research Fund for Coal and Steel (RFCS) 3

4 Lignite bulk samples for ex-situ UCG tests : Origin Premogovnik Velenje (Slovenia) Pesteana Open Pit Mine CEO Oltenia (Romania) 4

5 Lignite bulk samples for ex-situ UCG tests : Origin Pesteana Open Pit Mine CEO Oltenia (Romania) Premogovnik Velenje (Slovenia) 5

6 Lignite bulk samples for ex-situ UCG tests : Delivery Pesteana Open Pit CEO Oltenia (Romania) Premogovnik Velenje (Slovenia) 6

7 Lignite characteristics: Proximate and ultimate analysis No. As received Parameter Velenje Coal sample Oltenia 1 Total moisture W tr, % Ash A t r, % Volatiles V r, % Total sulphur S tr, % Calorific value Q ir, kj/kg Analytical 6 Total moisture, % Ash A a, % Volatiles V a, % Heat of combustion Q sa, kj/kg Calorific value Q ia, kj/kg Total sulfur S a, % Carbon C ta, % Hydrogen H ta, % Nitrogen N a, % Oxygen O da, %

8 Product yield, % Lignites characteristics: Fischer assay Semi-char Tar Water Gas Valenje (SLO) Oltenia (RO) 8

9 Lignites characteristics: Sulphur speciation Total sulphur [%] Pyritic sulphur [%] Sulphate sulphur [%] Ash sulphur [%] Combustible sulphur [%] Valenje (SLO) Oltenia (RO) 9

10 Ex-situ UCG tests: Laboratory Installation to thermal combustor F O 2 H 2 O p,t Coal seam p,t Air N 2 (1) 7.4 m (2) (3) (4) (5) (6) GC (1) reagents supply system, (2) gasification chamber, (3) water scrubber, (4) gas cooler, (5) separator, (6) filters 10

11 Ex-situ UCG experimental installation: Characteristics Technical parameters: coal type: lignite, hard coal coal seam length: 7 m gasification pressure: max 0.5 bar temperature: max C coal seam inclination: 0, 15, 30, 45 0 a) b) c) 11

12 UCG experimental simulations: Coal seam preparation 12

13 Artificial coal seam: Geometry and thermocouples 0.25 m 1.25 m 2.25 m 3.25 m 4.25 m 5.25 m 6.25 m m Inlet Gasification channel Wylot Outlet 6.0 m Coal seam 0.70m Gasification channel 0.70 m 13

14 UCG experimental simulations: Artificial seam of lignite 14

15 UCG experimental simulations: Installation of thermocouples 13

16 UCG experimental simulations: Reactor closure 13

17 Flow rate, Nm 3 /h Flow rate, Nm 3 /h UCG experiments: Oxidants supply and gas production rates Premogovnik Velenje (Slovenia) CEO Oltenia (Romania) Gas production Oxygen supply rate Gas production Oxygen supply rate Steam/O 2 Steam Time,h Time,h 17

18 Results: Changes in gas composition Premogovnik Velenje (Slovenia) CEO Oltenia (Romania) Concentration, % vol CO2 H2 N2 CH4 CO Concentration, % vol CO2 H2 N2 CH4 CO Steam/O 2 Steam Time, h Time, h 18

19 Results: Average gas composition Coal Composition, % vol. CO 2 C 2 H 6 H 2 O 2 N 2 CH 4 CO H 2 S CV, MJ/Nm 3 Velenje Oltenia

20 Results: Changes in gas calorific value Premogovnik Velenje (Slovenia) CEO Oltenia (Romania) Average: 6.4 MJ/Nm 3 Average: 4.8 MJ/Nm 3 8 Calorific value, MJ/Nm Calorific value, MJ/Nm Time, h Time, h 20

21 Temperature [ o C] Results: Temperature distribution Premogovnik Velenje (Slovenia) CEO Oltenia (Romania) T8 T9 T10 T11 T Time [h] 0.25 m 1.25 m 2.25 m 3.25 m 4.25 m 5.25 m 6.25 m m Inlet Gasification channel Wylot Outlet 6.0 m 21

22 Results: Material and energy balance data Parameter Velenje Oltenia Estimated total coal consumption (kg) Average coal consumption rate (kg/h) Average gas production rate (Nm 3 /h) Average reactor power (kw) Gross energy efficiency (%)

23 Post experimental studies: Solid residues Dried lignite Char Ash 23

24 Analysis of UCG residues: Scope Gasification char Gas and water transport properties Mechanical properties Mineralogical studies Molten mineral matter (slag) Leaching tests (organic and inorganic contaminants) 24

25 Conclusions 1. The UCG experiments demonstrated that the physicochemical properties of the feed lignite considerably affect the in-seam gasification process 2. Because the excessive water leads to the substantial decrease in the gasification efficiency, the coal moisture content is one of the crucial parameters 3. Nevertheless, the results obtained indicate that UCG may be a feasible option for exploitation of lignite deposits, especially in the case of moderately wet lignites, such as Velenje lignite 4. Recovery of the physical heat of gas on the surface is one of the options that can be considered for the improvement of the overall process performance 25

26 Thank you for your kind attention! Contacts: Dr Krzysztof Kapusta Główny Instytut Górnictwa Podleska 72, Mikołów, Poland Prof. Krzysztof Stańczyk Główny Instytut Górnictwa Plac Gwarków 1, Katowice, Poland