Journal articles: 'Entrained flow reactor'

1

FLAXMAN, R., and W. HALLETT. "Flow and particle heating in an entrained flow reactor." Fuel 66, no. 5 (May 1987): 607–11. http://dx.doi.org/10.1016/0016-2361(87)90266-3.

Full text

APA, Harvard, Vancouver, ISO, and other styles

2

YIN, Xinyi, and Ping LU. "ICOPE-15-C138 Migration of AAEMs during biomass pyrolysis in an entrained flow reactor." Proceedings of the International Conference on Power Engineering (ICOPE) 2015.12 (2015): _ICOPE—15——_ICOPE—15—. http://dx.doi.org/10.1299/jsmeicope.2015.12._icope-15-_200.

Full text

APA, Harvard, Vancouver, ISO, and other styles

3

Mularski, Jakub, and Norbert Modliński. "Impact of Chemistry–Turbulence Interaction Modeling Approach on the CFD Simulations of Entrained Flow Coal Gasification." Energies 13, no. 23 (December 7, 2020): 6467. http://dx.doi.org/10.3390/en13236467.

Full text

Abstract:

This paper examines the impact of different chemistry–turbulence interaction approaches on the accuracy of simulations of coal gasification in entrained flow reactors. Infinitely fast chemistry is compared with the eddy dissipation concept considering the influence of turbulence on chemical reactions. Additionally, ideal plug flow reactor study and perfectly stirred reactor study are carried out to estimate the accuracy of chosen simplified chemical kinetic schemes in comparison with two detailed mechanisms. The most accurate global approach and the detailed one are further implemented in the computational fluid dynamics (CFD) code. Special attention is paid to the water–gas shift reaction, which is found to have the key impact on the final gas composition. Three different reactors are examined: a pilot-scale Mitsubishi Heavy Industries reactor, a laboratory-scale reactor at Brigham Young University and a Conoco-Philips E-gas reactor. The aim of this research was to assess the impact of gas phase reaction model accuracy on simulations of the entrained flow gasification process. The investigation covers the following issues: impact of the choice of gas phase kinetic reactions mechanism as well as influence of the turbulence–chemistry interaction model. The advanced turbulence–chemistry models with the complex kinetic mechanisms showed the best agreement with the experimental data.

APA, Harvard, Vancouver, ISO, and other styles

4

Plou, Jorge, Isabel Martínez, Gemma S. Grasa, and Ramón Murillo. "Experimental carbonation of CaO in an entrained flow reactor." Reaction Chemistry & Engineering 4, no. 5 (2019): 899–908. http://dx.doi.org/10.1039/c9re00015a.

Full text

APA, Harvard, Vancouver, ISO, and other styles

5

Kim, Hakduck, Kitae Jeon, Heechang Lim, and Juhun Song. "Parameter analysis of an entrained flow gasification process." Advances in Mechanical Engineering 10, no. 12 (December 2018): 168781401881525. http://dx.doi.org/10.1177/1687814018815255.

Full text

Abstract:

This work presents primary results of a parameter study for entrained flow gasification using a steady-flow reactor model. The influences of important parameters such as coal types, gasifier pressure, gas/coal feeding rate, and coal particle size were studied based on coal conversion and gas product species. The prediction results were compared and validated against those published previously. In particular, a relative importance of reaction stoichiometry, temperature, reaction time (kinetics), or residence time considered in this simulation work was evaluated to affect the gas composition produced from different coals. The optimal carbon monoxide concentration was observed at an oxygen-to-fuel ratio of 0.8, while a greatest carbon conversion was found at a steam-to-fuel ratio of 0.4. Coal particle size has a strong influence on carbon conversion. However, the coal feeding rate has no effect on carbon conversion despite differences in residence time.

APA, Harvard, Vancouver, ISO, and other styles

6

Laxminarayan, Yashasvi, Peter Arendt Jensen, Hao Wu, Flemming Jappe Frandsen, Bo Sander, and Peter Glarborg. "Biomass fly ash deposition in an entrained flow reactor." Proceedings of the Combustion Institute 37, no. 3 (2019): 2689–96. http://dx.doi.org/10.1016/j.proci.2018.06.039.

Full text

APA, Harvard, Vancouver, ISO, and other styles

7

Gorton, C. W., R. J. Kovac, J. A. Knight, and T. I. Nygaard. "Modeling pyrolysis oil production in an entrained-flow reactor." Biomass 21, no. 1 (January 1990): 1–10. http://dx.doi.org/10.1016/0144-4565(90)90043-j.

Full text

APA, Harvard, Vancouver, ISO, and other styles

8

BITOWFT, B., L. ANDERSSON, and I. BJERLE. "Fast pyrolysis of sawdust in an entrained flow reactor." Fuel 68, no. 5 (May 1989): 561–66. http://dx.doi.org/10.1016/0016-2361(89)90150-6.

Full text

APA, Harvard, Vancouver, ISO, and other styles

9

Morgan, Mark E., and Robert G. Jenkins. "Pyrolysis of a lignite in an entrained flow reactor." Fuel 65, no. 6 (June 1986): 757–63. http://dx.doi.org/10.1016/0016-2361(86)90064-5.

Full text

APA, Harvard, Vancouver, ISO, and other styles

10

Morgan, Mark E., and Robert G. Jenkins. "Pyrolysis of a lignite in an entrained flow reactor." Fuel 65, no. 6 (June 1986): 764–68. http://dx.doi.org/10.1016/0016-2361(86)90065-7.

Full text

APA, Harvard, Vancouver, ISO, and other styles

11

Jenkins, Robert G., and Mark E. Morgan. "Pyrolysis of a lignite in an entrained flow reactor." Fuel 65, no. 6 (June 1986): 769–71. http://dx.doi.org/10.1016/0016-2361(86)90066-9.

Full text

APA, Harvard, Vancouver, ISO, and other styles

12

Zarzycki, Robert. "Pulverized coal gasification with steam and flue gas." MATEC Web of Conferences 240 (2018): 05036. http://dx.doi.org/10.1051/matecconf/201824005036.

Full text

Abstract:

The study presents the concept and numerical calculations of the coal dust gasification in the entrained flow reactor with power of 16 MWt. The gasification process in the reactor can be performed in the atmosphere of O2, CO2 and H2O. The combustible gases obtained during gasification are composed mainly of CO and H2 and can be used to feed pulverized coal-fired boilers. Integration of the reactor (reactors) for coal dust gasification with the pulverized coal-fired boiler allows for improved flexibility, especially in the range of low loads if stabilization of coal dust combustion in pulverized-fuel burners or support for their work with ignition burners fed with gas or light fuel oil is necessary. The concept of the gasification reactor assumes strong eddy motion of the coal dust, which substantially allows for elongation of the time of fuel remaining in the reactor and obtaining a high reaction level. The concept of the entrained flow reactor presented in this study and the results of numerical calculations can be helpful for development of the devices with greater powers which in the nearest future should be integrated in the systems of pulverized coal-fired boilers in order to reduce their minimum load without using the ignition burners.

APA, Harvard, Vancouver, ISO, and other styles

13

OKUYAMA, Keiichi, Seiji KINOSHITA, Takeshi UCHIYAMA, Toshihiko IWASAKI, Yasuo SUZUKI, Takao USHIYAMA, and Hiroshi ONODA. "203 Rapid Pyrolysis of Woody Biomass in Entrained Flow Reactor." Proceedings of the Symposium on Environmental Engineering 2009.19 (2009): 137–38. http://dx.doi.org/10.1299/jsmeenv.2009.19.137.

Full text

APA, Harvard, Vancouver, ISO, and other styles

14

OKUYAMA, Keiichi, Takeshi UCHIYAMA, Toshihiko IWASAKI, Satoshi MATSUI, Yasuo SUZUKI, Takao USHIYAMA, and Hiroshi ONODA. "205 Development of Biomass Liquefaction Technology Using Entrained Flow Reactor." Proceedings of the Symposium on Environmental Engineering 2010.20 (2010): 104–5. http://dx.doi.org/10.1299/jsmeenv.2010.20.104.

Full text

APA, Harvard, Vancouver, ISO, and other styles

15

Erşahan, H., O. N. Şara, and R. Boncukcuoğlu. "Desulphurization of two Turkish lignites in an entrained flow reactor." Journal of Analytical and Applied Pyrolysis 44, no. 1 (November 1997): 65–74. http://dx.doi.org/10.1016/s0165-2370(97)00067-3.

Full text

APA, Harvard, Vancouver, ISO, and other styles

16

Chen, Caixia, Gang Chen, Jihua Qiu, Xuexin Sun, and Yuyi Ma. "VOLATILE EVOLUTION OF PULVERIZED COAL IN AN ENTRAINED FLOW REACTOR." Fuel Science and Technology International 12, no. 5 (January 1994): 785–93. http://dx.doi.org/10.1080/08843759408916206.

Full text

APA, Harvard, Vancouver, ISO, and other styles

17

Zhao, Yijun, Shaozeng Sun, Hongming Tian, Juan Qian, Fengming Su, and Feng Ling. "Characteristics of rice husk gasification in an entrained flow reactor." Bioresource Technology 100, no. 23 (December 2009): 6040–44. http://dx.doi.org/10.1016/j.biortech.2009.06.030.

Full text

APA, Harvard, Vancouver, ISO, and other styles

18

Sohn, Geun, Insoo Ye, Changkook Ryu, Ho Won Ra, and Sung Min Yoon. "Determination of Effective Reaction Conditions for Char Gasification in an Entrained Flow Reactor." Energy & Fuels 33, no. 1 (December 26, 2018): 148–58. http://dx.doi.org/10.1021/acs.energyfuels.8b03465.

Full text

APA, Harvard, Vancouver, ISO, and other styles

19

Zhao, Yijun, Shaozeng Sun, Hao Zhou, Rui Sun, Hongming Tian, Jiyi Luan, and Juan Qian. "Experimental study on sawdust air gasification in an entrained-flow reactor." Fuel Processing Technology 91, no. 8 (August 2010): 910–14. http://dx.doi.org/10.1016/j.fuproc.2010.01.012.

Full text

APA, Harvard, Vancouver, ISO, and other styles

20

Álvarez, L., M. Gharebaghi, M. Pourkashanian, A. Williams, J. Riaza, C. Pevida, J. J. Pis, and F. Rubiera. "CFD modelling of oxy-coal combustion in an entrained flow reactor." Fuel Processing Technology 92, no. 8 (August 2011): 1489–97. http://dx.doi.org/10.1016/j.fuproc.2011.03.010.

Full text

APA, Harvard, Vancouver, ISO, and other styles

21

Kirtania, Kawnish, and Sankar Bhattacharya. "CO2 gasification behavior of biomass chars in an entrained flow reactor." Biomass Conversion and Biorefinery 6, no. 1 (July 14, 2015): 49–59. http://dx.doi.org/10.1007/s13399-015-0174-6.

Full text

APA, Harvard, Vancouver, ISO, and other styles

22

Celik, Ismail, Thomas J. O'Brien, and Devendra B. Godbole. "A numerical study of coal devolatilization in an entrained-flow reactor." Chemical Engineering Science 45, no. 1 (1990): 65–77. http://dx.doi.org/10.1016/0009-2509(90)87081-3.

Full text

APA, Harvard, Vancouver, ISO, and other styles

23

Wang, Wuyin, Qin Zhong, Zhicheng Ye, and Ingemar Bjerle. "Simultaneous reduction of SO2 and NOx in an entrained-flow reactor." Fuel 74, no. 2 (February 1995): 267–72. http://dx.doi.org/10.1016/0016-2361(95)92664-r.

Full text

APA, Harvard, Vancouver, ISO, and other styles

24

Lee, Jae Goo, Jae Ho Kim, Hyo Jin Lee, Tae Jun Park, and Sang Done Kim. "Characteristics of entrained flow coal gasification in a drop tube reactor." Fuel 75, no. 9 (July 1996): 1035–42. http://dx.doi.org/10.1016/0016-2361(96)00084-1.

Full text

APA, Harvard, Vancouver, ISO, and other styles

25

Faúndez, J., A. Arenillas, F. Rubiera, X. García, A. L. Gordon, and J. J. Pis. "Ignition behaviour of different rank coals in an entrained flow reactor." Fuel 84, no. 17 (December 2005): 2172–77. http://dx.doi.org/10.1016/j.fuel.2005.03.028.

Full text

APA, Harvard, Vancouver, ISO, and other styles

26

Li, Zhi He, Wei Ming Yi, Qiao Chun Gao, Yong Jun Li, Xue Yuan Bai, and De Li Zhang. "Research on Pyrolysis Reactors for Bio-Oil Production from Agricultural Residues." Advanced Materials Research 512-515 (May 2012): 459–63. http://dx.doi.org/10.4028/www.scientific.net/amr.512-515.459.

Full text

Abstract:

This paper provides an updated review on fast biomass pyrolysis reactors for bio-oil production in Shandong University of Technology. The technologies that were developed include horizontal entrained bed (HEB), fluidized bed (FB), down flow tuber reactor (DFTR), double concentric cylinder rotary reactor (DCCRR) and new type down flow tube reactor (N-DFTR). The patented DFTR, DCCRR and N-DFTR in China were developed based on the technology of direct heat exchange between hot solid heat carriers and biomass particles during both of the particles flowing in a mixed condition. The process and characteristics of each reactor were discussed in this topic. Contrasting to conventional reactors, the DFTR, DCCRR and N-DFTR are promising technologies due to their characteristics of high solid-liquid conversion rate, energy self-sufficient, easy operation and scaling up.

APA, Harvard, Vancouver, ISO, and other styles

27

Katalambula, H. "Modelling of Coal Slag flow and Layer Thickness in a High Temperature Entrained Flow Gasifier." Tanzania Journal of Engineering and Technology 32, no. 1 (June 30, 2009): 9–17. http://dx.doi.org/10.52339/tjet.v32i1.541.

Full text

Abstract:

A 2-D model for the slag flow simulation in an entrained flow gasifier has been developed. In addition tomass, momentum and energy conservation equations, volume of fluid (VOF) equation was solved to track theliquid-gas interface. Liquid phase consists of melted coal ash particles which deposits on the wall and movedownward. The gasification reaction is not considered here but it is postulated to have a mass flow throughthe interface towards the mass of the liquid phase. The reactor walls are usually kept cold so a temperaturegradient and then a solid layer form within the slag layer. The solidification and its effect on the slag layerthickness are also considered here. Results show that, depending on the ash composition which determines thefluid’s rheological properties, the solid phase constitutes a large part of the slag layer

APA, Harvard, Vancouver, ISO, and other styles

28

Tsai, Ching Yi, and Alan W. Scaroni. "Pyrolysis and combustion of bituminous coal fractions in an entrained-flow reactor." Energy & Fuels 1, no. 3 (May 1987): 263–69. http://dx.doi.org/10.1021/ef00003a007.

Full text

APA, Harvard, Vancouver, ISO, and other styles

29

Nelson, Peter F., Peter C. Nancarrow, John Bus, and Antoni Prokopiuk. "Fractional conversion of char N to no in an entrained flow reactor." Proceedings of the Combustion Institute 29, no. 2 (January 2002): 2267–74. http://dx.doi.org/10.1016/s1540-7489(02)80276-0.

Full text

APA, Harvard, Vancouver, ISO, and other styles

30

Ku, Xiaoke, Jin Wang, Hanhui Jin, and Jianzhong Lin. "Effects of operating conditions and reactor structure on biomass entrained-flow gasification." Renewable Energy 139 (August 2019): 781–95. http://dx.doi.org/10.1016/j.renene.2019.02.113.

Full text

APA, Harvard, Vancouver, ISO, and other styles

31

Gullett, Brian K., John A. Blom, and George R. Gillis. "Design and characterization of a 1200 °C entrained flow, gas/solid reactor." Review of Scientific Instruments 59, no. 9 (September 1988): 1980–84. http://dx.doi.org/10.1063/1.1140062.

Full text

APA, Harvard, Vancouver, ISO, and other styles

32

Lu, Ping, Sheng-Rong Xu, and Xiu-Ming Zhu. "Study on NO heterogeneous reduction with coal in an entrained flow reactor." Fuel 88, no. 1 (January 2009): 110–15. http://dx.doi.org/10.1016/j.fuel.2008.08.001.

Full text

APA, Harvard, Vancouver, ISO, and other styles

33

Hu, Lishun, Xinjun Wang, Guangsuo Yu, Fuchen Wang, and Zunhong Yu. "Study on gas–liquid phase mass transfer coefficient of entrained flow reactor." Chemical Engineering Journal 141, no. 1-3 (July 2008): 278–83. http://dx.doi.org/10.1016/j.cej.2007.12.032.

Full text

APA, Harvard, Vancouver, ISO, and other styles

34

Goldberger, Lexie A., Lydia G. Jahl, Joel A. Thornton, and Ryan C. Sullivan. "N2O5 reactive uptake kinetics and chlorine activation on authentic biomass-burning aerosol." Environmental Science: Processes & Impacts 21, no. 10 (2019): 1684–98. http://dx.doi.org/10.1039/c9em00330d.

Full text

Abstract:

The reactive uptake kinetics of nitrogen pentoxide (N₂O₅) to authentic biomass-burning aerosol and the production of nitryl chloride (ClNO₂) was determined using an entrained aerosol flow tube reactor.

APA, Harvard, Vancouver, ISO, and other styles

35

Mularski, Jakub, and Norbert Modliński. "Entrained-Flow Coal Gasification Process Simulation with the Emphasis on Empirical Char Conversion Models Optimization Procedure." Energies 14, no. 6 (March 20, 2021): 1729. http://dx.doi.org/10.3390/en14061729.

Full text

Abstract:

Computational fluid dynamics (CFD) modeling of an entrained-flow reactor is demonstrated and compared with experimental data. The study is focused on char conversion modeling and its impact on gasification simulation results. An innovative procedure of optimizing input data to empirical char conversion kinetic-diffusion model is investigated, based on the complex carbon burnout kinetic model for oxidation (CBK/E) and gasification (CBK/G). The kinetics of the CBK/G model is determined using the data from char gasification experiments in a drop tube reactor. CFD simulations are performed for the laboratory-scale entrained-flow reactor at Brigham Young University for the bituminous coal. A substantial impact of applied kinetic parameters on the in-reactor gas composition and char conversion factor was observed. The effect was most considerable for the reduction zone, where gasification reactions dominate, although a non-negligible impact could also be observed in the flame zone. Based on the quantitative assessment of the incorporated optimization procedure, its application allowed to obtain one of the lowest errors of CO, H2, CO2, and H2O axial distribution with respect to the experimental data. The maximum errors for these species were equal to 18.48, 7.95, 10.15, and 20.22%, respectively, whereas the average errors were equal to 4.82, 5.47, 4.72, and 9.58%, respectively.

APA, Harvard, Vancouver, ISO, and other styles

36

Freihaut, J. D., W. M. Proscia, and D. J. Seery. "Chemical characteristics of tars produced in a novel low-severity, entrained-flow reactor." Energy & Fuels 3, no. 6 (November 1989): 692–703. http://dx.doi.org/10.1021/ef00018a006.

Full text

APA, Harvard, Vancouver, ISO, and other styles

37

Sun, Shaozeng, Hongming Tian, Yijun Zhao, Rui Sun, and Hao Zhou. "Experimental and numerical study of biomass flash pyrolysis in an entrained flow reactor." Bioresource Technology 101, no. 10 (May 2010): 3678–84. http://dx.doi.org/10.1016/j.biortech.2009.12.092.

Full text

APA, Harvard, Vancouver, ISO, and other styles

38

Peterson, Braden, Chaiwat Engtrakul, Tabitha J. Evans, Kristiina Iisa, Michael J. Watson, Mark W. Jarvis, David J. Robichaud, Calvin Mukarakate, and Mark R. Nimlos. "Optimization of Biomass Pyrolysis Vapor Upgrading Using a Laminar Entrained-Flow Reactor System." Energy & Fuels 34, no. 5 (April 24, 2020): 6030–40. http://dx.doi.org/10.1021/acs.energyfuels.0c00649.

Full text

APA, Harvard, Vancouver, ISO, and other styles

39

Galletti, Chiara, Gianluca Caposciutti, and Leonardo Tognotti. "Evaluation of Scenario Uncertainties in Entrained Flow Reactor Tests through CFD Modeling: Devolatilization." Energy & Fuels 30, no. 9 (September 2016): 7511–23. http://dx.doi.org/10.1021/acs.energyfuels.6b01000.

Full text

APA, Harvard, Vancouver, ISO, and other styles

40

Fjellerup, Jan, Erik Gjernes, and Lars K. Hansen. "Pyrolysis and Combustion of Pulverized Wheat Straw in a Pressurized Entrained Flow Reactor†." Energy & Fuels 10, no. 3 (January 1996): 649–51. http://dx.doi.org/10.1021/ef950204e.

Full text

APA, Harvard, Vancouver, ISO, and other styles

41

Bösenhofer, Markus, Ethan Hecht, Christopher R. Shaddix, Bernhard König, Johannes Rieger, and Michael Harasek. "Computational fluid dynamics analysis of char conversion in Sandia’s pressurized entrained flow reactor." Review of Scientific Instruments 91, no. 7 (July 1, 2020): 074103. http://dx.doi.org/10.1063/5.0005733.

Full text

APA, Harvard, Vancouver, ISO, and other styles

42

Li, Yan, Xuebin Wang, Houzhang Tan, Shengjie Bai, Hrvoje Mikulčić, and Fuxin Yang. "Evolution of PM2.5 from biomass high-temperature pyrolysis in an entrained flow reactor." Journal of the Energy Institute 92, no. 5 (October 2019): 1548–56. http://dx.doi.org/10.1016/j.joei.2018.07.019.

Full text

APA, Harvard, Vancouver, ISO, and other styles

43

Umeki, Kentaro, Kawnish Kirtania, Luguang Chen, and Sankar Bhattacharya. "Fuel Particle Conversion of Pulverized Biomass during Pyrolysis in an Entrained Flow Reactor." Industrial & Engineering Chemistry Research 51, no. 43 (October 22, 2012): 13973–79. http://dx.doi.org/10.1021/ie301530j.

Full text

APA, Harvard, Vancouver, ISO, and other styles

44

OGI, Tomoko, Masakazu NAKANISHI, and Yoshio FUKUDA. "Gasification of Empty Fruit Bunch and Bagasse Using an Entrained-flow Mode Reactor." Journal of the Japan Institute of Energy 90, no. 9 (2011): 886–94. http://dx.doi.org/10.3775/jie.90.886.

Full text

APA, Harvard, Vancouver, ISO, and other styles

45

STEENE, L. VAN DE, S. SALVADOR, and G. CHARNAY. "Controlling Powdered Fuel Combustion at Low Temperature in a New Entrained Flow Reactor." Combustion Science and Technology 159, no. 1 (October 2000): 255–79. http://dx.doi.org/10.1080/00102200008935786.

Full text

APA, Harvard, Vancouver, ISO, and other styles

46

Dupont, Capucine, Jean-Michel Commandré, Paola Gauthier, Guillaume Boissonnet, Sylvain Salvador, and Daniel Schweich. "Biomass pyrolysis experiments in an analytical entrained flow reactor between 1073K and 1273K." Fuel 87, no. 7 (June 2008): 1155–64. http://dx.doi.org/10.1016/j.fuel.2007.06.028.

Full text

APA, Harvard, Vancouver, ISO, and other styles

47

Zhang, Yongsheng, Lilin Zhao, Ruitao Guo, Na Song, Jiawei Wang, Yan Cao, William Orndorff, and Wei-ping Pan. "Mercury adsorption characteristics of HBr-modified fly ash in an entrained-flow reactor." Journal of Environmental Sciences 33 (July 2015): 156–62. http://dx.doi.org/10.1016/j.jes.2015.01.011.

Full text

APA, Harvard, Vancouver, ISO, and other styles

48

Lu, Ping, Shengrong Xu, and Xiuming Zhu. "Pyrolysis property of pulverized coal in an entrained flow reactor during coal reburning." Chemical Engineering and Processing: Process Intensification 48, no. 1 (January 2009): 333–38. http://dx.doi.org/10.1016/j.cep.2008.04.010.

Full text

APA, Harvard, Vancouver, ISO, and other styles

49

Shuangning, Xiu, Yi Weiming, and Baoming Li. "Flash pyrolysis of agricultural residues using a plasma heated laminar entrained flow reactor." Biomass and Bioenergy 29, no. 2 (August 2005): 135–41. http://dx.doi.org/10.1016/j.biombioe.2005.03.002.

Full text

APA, Harvard, Vancouver, ISO, and other styles

50

Göktepe, Burak, Ammar Hazim Saber, Rikard Gebart, and T. Staffan Lundström. "Cold flow experiments in an entrained flow gasification reactor with a swirl-stabilized pulverized biofuel burner." International Journal of Multiphase Flow 85 (October 2016): 267–77. http://dx.doi.org/10.1016/j.ijmultiphaseflow.2016.06.016.

Full text

APA, Harvard, Vancouver, ISO, and other styles

Journal articles on the topic 'Entrained flow reactor'

Create a spot-on reference in APA, MLA, Chicago, Harvard, and other styles