546.56.4:542.947:314 . , . . 5% Cu/ -Al2O3 – 100 % -11- , , . , . , 0,5 -1- –9- -1- 5% - , . 11. -1- 9,6 16 , 9- 11- -1- 0,5 11- -1- ( 5% 1). , - 100% . 7%, -1- 99% 1% -11- 12% . 10% -11- -1- . 9,6 1. 5% Cu/ -Al2O3 0,5% Y , 1% Y – 12 11- -1, . ,% ., .Y % , Cu/ -Al2O3 393 , 6,2 0,0 0,5 1 3 5 7 10 0,0 0,5 1 3 5 7 10 100 % , - 8 , ( . 11- 10 10 10 10 10 10 10 5 5 5 5 5 5 5 11,2 3% Y – 15, 5% Y – 16, 7% Y – 20, 10% – 24 ( 1). 7 10% . , 5% Cu/ -Al2 O3 , 5% Y 10% Cu/ -Al2O3 3% Y , 10% Cu/ -Al2O3, , 100% -11-1, 5% Cu/ -Al2O3 . 25 , 0,5% Y, 15 5% Y. , 11-1- 5% Cu/ , -Al2O3, -1- 135 8 10 12 23 25 30 240 25 20 16 15 12 10 14 -1100 100 100 100 92 91 91 100 100 100 100 100 99 88 ), % - 11- -18 9 9 1 12 . 2007. 10% Cu/ -Al2O3, [1]. 5% Cu/ -Al2O3 Al2O3 ( -1(0,5-10% Y) 5% Cu/ -Al2O311-1- . 5% Cu/ -Al2O3 0,5-5% Y 9-1-9- -1- , 100% 2). . 7 10% -9-1- . 0,5% Y 6,2 , 1% Y – 8 , 3% Y – 9,3, 5% Y – 11,2, 7% Y – 14, 10% Y – 17,5 . 7 10% Y , 11-1- . 5% Cu/ -Al2O3 3% Y 10% Cu/ -Al2O3 (3% Y) . 9-, 11-110% Cu/ -Al2O3 – , (0,5-10% Y), [2] . ) , 9- -1- ,% . ,% , . 10% Cu / -Al2O3 , 2000- , , 3000A, 40-60Å. 5% Cu / -Al2O3 , - 5% Cu / -Al2O3, Y 2O3, Cu/ -Al2O3 , , 8 – ( . ), % 9- 10 10 10 10 10 10 10 5 5 5 5 5 5 5 , - . 393 Y - , - 2. - , , , 10% Cu/ . 9- 5 0,0 0,5 1,0 3,0 5,0 7,0 10 0,0 0,5 1,0 3,0 5,0 7,0 10 160 20 25 30 33 42 47 280 45 35 30 25 20 16 15 -1- 100 100 100 100 100 96 94 100 100 100 100 100 98 89 9- -14 6 2 11 3. Y 2O3 S, 10% Cu/ -Al2O 3 10% Cu+ Y2O3 (1% Y) / 10% Cu+ Y2O3 (5% Y) / 10% Cu+ Y2O3 (7% Y) / 10% Cu+ Y2O3 (10% Y)/ 2 / S, 90 75 74 70 38 -Al2O3 -Al2O3 -Al2O3 -Al2O3 5% 5% 5% 5% 5% 10% Cu / -Al2O3 [3]. Cu/ -Al2O 3 Cu+ Y 2O3 (1% Y) / Cu+ Y 2O3 (5% Y) / Cu+ Y 2O3 (7% Y) / Cu+ Y2O3 (10% Y) / 1. [4,5]. [6], . - . 5% Cu / -Al2O3 . - [7]. - , [8]. -1- -9- . , - -11- -1- .« – i – -1- - , , . « ., 21 ., ., ., . // . ». ( . . , 2001, . 0,55 %5% Cu / -Al2O3 . , , . ), . , 59-72. 3. Marino F., Laborde M., Jobbady M. Characterization and Performance of Cu-Ni Supported Catalysts // 4 th European Congress on Catalysts. Rimini, Italy. Book of Abstracts. 1999. p. /1/307. 4. Gallaher G.R., Godwin I.G., Chen-Shi Huang. XPS and Reaction Investigation of Alkali Promotion. // J. Catal. 1993. v.140, 2, p. 453-456. 5. Bachiller-Baeza B., Gurrero-Ruiz A., Rodriguez-Ramos V. Role of CeO 2 in the gas phase to krotonaldehyde hydrogenation over promoted Ru/C and Ru/Al2O3 catalysts. // 4th European Congress on Catalysis. Rimini, Italy. Sept. 5-10. 1999. Book of Abstracts. 1999, p. /1/040. p. 240. 6. ., ., . . // , 1993, .34, 5, . 909-912. 7. . VIII . : . 1983. 304 . 8. Yefremenko I.G., Zilberberg I.L., Zhidomirov G.M., Pak A.M. Hydrogen Activation on Copper Catalytic Sites in Stereoselective Alkyne Hydrogenation. // React. Kinet. Catal. Lett., 1995, 56, 1., p.77-86. , , // 2(15), . 25-30. ., ., . / 95 85 67 58 45 -Al2O3 -Al2O3 -Al2O3 -Al2O3 . », 2006, 2. 2 -11100%- . - . . 16 - -1- - -9i. , 07.11.2007 .