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This post was last edited by penghh1985 on 2016-2-22 08:16. Multiple-choice question (fill in the correct option in the brackets). Continuing from series 1891: 91. (B-A-008) The initial reduction temperature of the B204 catalyst at an inlet H2 concentration of 1% is ( )°C. (A) 120 (B) 130 (C) 140 (D) 150 92. (B-A-009) The characteristic of the rapid heating and reduction method for ammonia synthesis catalysts is the full utilization of the heat generated by the synthesis reaction to accelerate the reaction ( ). (A) Temperature (B) Velocity (C) Pressure (D) Equilibrium 93. (B-A-009) For synthesis towers with a diameter of φ1,000 or more, synthesis catalysts with a size of ( ) mm are generally used. (A) 1.5~4.7 (B) 4.7~6.3 (C) 9.4~13 (D) 6.3~9.4 94. (B-A-009) The catalyst particle size generally suitable for radial and axial-radial combined reactors is ( ). (A) 1.5~3.0 (B) 3.0~4.5 (C) 4.5~6.0 (D) 6.0~7.5 95. (B-A-010) The reduction of ammonia synthesis catalysts in industry can be divided into ( ) phases. (A) 4 (B) 3 (C) 5 (D) 2 DBCAC Scoring criteria: 3 points for participation, 8 points for a completely correct answer.
91. (B-A-008) The B204 catalyst exhibits an initial reduction temperature of (D) °C at an inlet H2 concentration of 1%. (A) 120 (B) 130 (C) 140 (D) 150 92. (B-A-009) The characteristic of the rapid heating and reduction method for ammonia synthesis catalysts is the full utilization of the heat generated by the synthesis reaction to accelerate the reaction (B). (A) Temperature (B) Velocity (C) Pressure (D) Equilibrium 93. (B-A-009) For shaft synthesis towers with a diameter of φ1,000 or more, synthesis catalysts with a size of (C) mm are generally used. (A) 1.5~4.7 (B) 4.7~6.3 (C) 9.4~13 (D) 6.3~9.4 94. (B-A-009) The catalyst particle size generally suitable for radial and axial-radial combined reactors is (A). (A) 1.5~3.0 (B) 3.0~4.5 (C) 4.5~6.0 (D) 6.0~7.5 95. (B-A-010) The reduction of ammonia synthesis catalysts in industry can be divided into (C) phases. (A) 4 (B) 3 (C) 5 (D) 2