Liquid-phase oxidative digestion method for radioactively contaminated carbon-containing material

Abstract

Disclosed is a liquid-phase oxidative decomposition method for radioactively contaminated carbonaceous material, providing a method of oxidizing carbon into a gas in liquid phase to treat radioactively contaminated carbonaceous material. The method comprises the following steps: ball milling a mixture of a molybdenum-containing substance and a carbonaceous material, thermally treating the ball milled mixture, and performing liquid-phase oxidation of the thermally treated mixture. The thermal treatment causes carbon to enter space between molybdenum atoms so as to reduce the particle size of carbon and improve the chemical reactivity of carbon, and an oxidant is then used to oxidize the carbon in the space between molybdenum atoms into a gas in liquid phase, while the molybdenum-containing moiety is converted into a water-soluble substance. The method of has technical effects of mild reaction conditions, low energy consumption, high operation safety, and facilitates the recovery of elements attached to carbonaceous material.

Claims

1. A method of oxidative digestion of a radioactively contaminated carbonaceous material in liquid phase, comprising steps of: a) milling a mixture of a molybdenum-containing substance and the radioactively contaminated the radioactively contaminated carbonaceous material by using a planetary ball mill at a fixed ball mill revolution speed to provide first-stage powders; b) placing the first-stage powders obtained in Step a) into a heating furnace, performing a thermal treatment to the first-stage powders under a flowing gas, and then naturally cooling the first-stage powders to provide second-stage powders; and c) adding the second-stage powders to water, and adding an oxidant, such that such that carbon contained therein is oxidized into a gas, and molybdenum-containing moiety is converted into a water-soluble substance, wherein a component ratio between the radioactively contaminated carbonaceous material and the molybdenum-containing substance in Step a) is, in parts by weight, 1 part of the radioactively contaminated carbonaceous material to 2-50 parts of the molybdenum-containing substance.

2. The method of oxidative digestion of a radioactively contaminated carbonaceous material in liquid phase according to claim 1, wherein a component ratio between the radioactively contaminated carbonaceous material and the molybdenum-containing substance in Step a) is, in parts by weight, 1 part of the radioactively contaminated carbonaceous material to 3.5-50 parts of the molybdenum-containing substance.

3. The method of oxidative digestion of a radioactively contaminated carbonaceous material in liquid phase according to claim 1, wherein a component ratio between the radioactively contaminated carbonaceous material and the molybdenum-containing substance in Step a) is, in parts by weight, 1 part of the radioactively contaminated carbonaceous material to 2 parts, 3 parts, 3.5 parts, 10 parts, 15 parts, 20 parts, 30 parts, 40 parts or 50 parts of the molybdenum-containing substance.

4. The method of oxidative digestion of a radioactively contaminated carbonaceous material in liquid phase according to claim 1, wherein the gas in Step b) is an inert gas or a gas mixture of hydrogen and an inert gas.

5. The method of oxidative digestion of a radioactively contaminated carbonaceous material in liquid phase according to claim 1, wherein the oxidant in Step c) is one of ozone, hydrogen peroxide, permanganates, and dichromates, or any combination thereof.

6. The method of oxidative digestion of a radioactively contaminated carbonaceous material in liquid phase according to claim 1, wherein the molybdenum-containing substance is one of molybdenum trioxide, molybdenum dioxide, hexaammonium molybdate, phosphomolybdic acid, silicomolybdic acid, and metallic molybdenum, or any combination thereof.

7. The method of oxidative digestion of a radioactively contaminated carbonaceous material in liquid phase according to claim 1, wherein the radioactively contaminated carbonaceous material is radioactively contaminated activated carbon, or radioactively contaminated carbon nanotubes, or radioactively contaminated graphite, or radioactively contaminated carbon fibers, or radioactively contaminated carbon black, or radioactively contaminated resin.

8. The method of oxidative digestion of a radioactively contaminated carbonaceous material in liquid phase according to claim 1, wherein the inert gas is argon or helium.

9. The method of oxidative digestion of a radioactively contaminated carbonaceous material in liquid phase according to claim 1, wherein the thermal treatment in Step b) is to heat at a temperature rise rate of 0.5-20 C./min to a temperature of 500-1100 C., with the temperature being maintained for 1-6 hours.

10. The method of oxidative digestion of a radioactively contaminated carbonaceous material in liquid phase according to claim 1, wherein the thermal treatment in Step b) is to heat at a temperature rise rate of 0.5-20 C./min to a temperature of 900-1100 C., with the temperature being maintained for 1-6 hours.

11. The method of oxidative digestion of a radioactively contaminated carbonaceous material in liquid phase according to claim 1, wherein the thermal treatment in Step b) is to heat at a temperature rise rate of 0.5 C./min, 1 C./min, 2 C./min, 5 C./min, 10 C./min or 20 C./min.

12. The method of oxidative digestion of a radioactively contaminated carbonaceous material in liquid phase according to claim 1, wherein the thermal treatment in Step b) is to heat to a temperature of 500 C., 600 C., 700 C., 750 C., 800 C., 900 C., 1000 C. or 1100 C.

13. The method of oxidative digestion of a radioactively contaminated carbonaceous material in liquid phase according to claim 1, wherein a duration for temperature maintenance of a high temperature condition in the thermal treatment in Step b) is 1 hour, 2 hours, 4 hours, 5 hours or 6 hours.

Description

DETAILED DESCRIPTION OF THE EMBODIMENTS

(1) Except for mutually exclusive features and/or steps, all the features or all the steps in the method or the process disclosed in the present specification may be combined with each other in any manner.

(2) Unless expressly stated otherwise, any feature disclosed in the specification (including any appended claims, the abstract or the drawings) can be replaced by any other alternative feature that is equivalent or has a similar object. That is to say, unless expressly stated otherwise, each feature is only one example of a series of equivalent or similar features.

(3) A method of oxidative digestion of a radioactively contaminated carbonaceous material in liquid phase, comprising the following steps:

(4) (1) milling a mixture of a molybdenum-containing substance and a carbonaceous material by using a planetary ball mill at a fixed ball mill revolution speed, to provide first-stage powders;

(5) (2) placing the first-stage powders obtained in Step (1) into a heating furnace, performing thermal treatment to the first-stage powders under a flowing gas, and then naturally cooling the same to provide second-stage powders;

(6) (3) adding the second-stage powders to water, and adding an oxidant, such that carbon contained therein is oxidized into a gas, and molybdenum-containing moiety is converted into a water-soluble substance.

Example 1

(7) (1) Graphite and molybdenum trioxide were mixed in a weight ratio of 1:20, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(8) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 900 C. at a temperature rise rate of 2 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 4 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(9) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 100% after 1 hour.

Example 2

(10) (1) Graphite and molybdenum trioxide were mixed in a weight ratio of 1:20, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(11) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 900 C. at a temperature rise rate of 2 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 4 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(12) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 100% after 1 hour.

Example 3

(13) (1) Activated carbon and molybdenum trioxide were mixed in a weight ratio of 1:15, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(14) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 700 C. at a temperature rise rate of 5 C./min in a helium-hydrogen mixture with the helium having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 2 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(15) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % potassium permanganate water solution, and the digestion rate of the activated carbon was determined as 60% after 1 hour.

Example 4

(16) (1) Graphite and molybdenum trioxide were mixed in a weight ratio of 1:10, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(17) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 900 C. at a temperature rise rate of 2 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 4 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(18) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 100% after 1 hour.

Example 5

(19) (1) Graphite and hexaammonium molybdate were mixed in a weight ratio of 1:40, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(20) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 900 C. at a temperature rise rate of 2 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 4 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(21) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 100% after 1 hour.

Example 6

(22) (1) Graphite and molybdenum trioxide were mixed in a weight ratio of 1:30, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(23) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 600 C. at a temperature rise rate of 2 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 5 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(24) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 48% after 1 hour.

Example 7

(25) (1) Graphite and phosphomolybdic acid were mixed in a weight ratio of 1:30, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(26) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 900 C. at a temperature rise rate of 2 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 4 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(27) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 100% after 1 hour.

Example 8

(28) (1) Graphite and molybdenum dioxide were mixed in a weight ratio of 1:20, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(29) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 900 C. at a temperature rise rate of 2 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 5 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(30) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 100% after 1 hour.

Example 9

(31) (1) Graphite and silicomolybdic acid were mixed in a weight ratio of 1:50, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(32) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 900 C. at a temperature rise rate of 20 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 1 hour, then the gas was turned off, and powders were obtained after natural cooling; and

(33) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 100% after 1 hour.

Example 10

(34) (1) Graphite and molybdenum trioxide were mixed in a weight ratio of 1:5, and then placed in a ball mill pot and milled for 1 hour by using a planetary ball mill at a revolution speed of 300 r/min;

(35) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 500 C. at a temperature rise rate of 1 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 5 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(36) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 22% after 1 hour.

Example 11

(37) (1) D152 macroporous weak acid cation exchange resin and molybdenum trioxide were mixed in a weight ratio of 1:30, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(38) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 1000 C. at a temperature rise rate of 2 C./min in a helium-hydrogen mixture with the helium having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 5 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(39) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the D152 macroporous weak acid cation exchange resin was determined as 100% after 1 hour.

Example 12

(40) (1) 717-type strong base anion exchange resin and molybdenum trioxide were mixed in a weight ratio of 1:30, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(41) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 1000 C. at a temperature rise rate of 2 C./min in a helium-hydrogen mixture with the helium having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 5 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(42) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the 717-type strong base anion exchange resin was determined as 100% after 1 hour.

Example 13

(43) (1) Graphite and phosphomolybdic acid were mixed in a weight ratio of 1:40, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(44) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 900 C. at a temperature rise rate of 0.5 C./min in a helium-hydrogen mixture with the helium having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 4 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(45) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 100% after 1 hour.

Example 14

(46) (1) Natural flake graphite and metallic molybdenum were mixed in a weight ratio of 1:20, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(47) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 1100 C. at a temperature rise rate of 1 C./min in a helium-hydrogen mixture with the helium having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 5 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(48) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 100% after 1 hour.

Example 15

(49) (1) Graphite and molybdenum trioxide were mixed in a weight ratio of 1:5, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(50) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 900 C. at a temperature rise rate of 2 C./min in argon with a flowing rate of 100 ml/min, wherein the temperature was maintained for 6 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(51) (3) 1 g of the obtained powders was added to 200 ml of water acidized by nitric acid, and after blowing ozone therein at a velocity of 10 g/h for 5 hours, the digestion rate of the graphite was determined as 98%.

Example 16

(52) (1) Graphite and molybdenum trioxide were mixed in a weight ratio of 1:4, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(53) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 900 C. at a temperature rise rate of 2 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 5 ml/min and the hydrogen having a flowing rate of 95 ml/min, wherein the temperature was maintained for 6 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(54) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 100% after 0.5 hour.

Example 17

(55) (1) Activated carbon and molybdenum trioxide were mixed in a weight ratio of 1:10, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(56) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 700 C. at a temperature rise rate of 5 C./min in a helium-hydrogen mixture with the helium having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 4 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(57) (3) 1 g of the obtained powders was added to 100 ml of 30 wt % potassium permanganate water solution, and the digestion rate of the activated carbon was determined as 40% after 1 hour.

Example 18

(58) (1) D152 macroporous weak acid cation exchange resin and molybdenum trioxide were mixed in a weight ratio of 1:6, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(59) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 1100 C. at a temperature rise rate of 0.5 C./min in argon with a flowing rate of 100 ml/min, wherein the temperature was maintained for 6 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(60) (3) 1 g of the obtained powders was added to 200 ml of water alkalized by sodium hydroxide, and after blowing ozone therein at a velocity of 10 g/h for 5 hours, the digestion rate of the resin was determined as 98%.

Example 19

(61) (1) Graphite and hexaammonium molybdate were mixed in a weight ratio of 1:50, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(62) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 1000 C. at a temperature rise rate of 5 C./min in argon with a flowing rate of 100 ml/min, wherein the temperature was maintained for 6 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(63) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 96% after 1 hour.

Example 20

(64) (1) Graphite and molybdenum trioxide were mixed in a weight ratio of 1:2, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(65) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 900 C. at a temperature rise rate of 20 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 1 hour, then the gas was turned off, and powders were obtained after natural cooling; and

(66) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 62% after 1 hour.

Example 21

(67) (1) Graphite and phosphomolybdic acid were mixed in a weight ratio of 1:30, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(68) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 900 C. at a temperature rise rate of 5 C./min in a nitrogen-hydrogen mixture with the nitrogen having a flowing rate of 5 ml/min and the hydrogen having a flowing rate of 95 ml/min, wherein the temperature was maintained for 6 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(69) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 90% after 1 hour.

Example 22

(70) (1) Graphite and molybdenum dioxide were mixed in a weight ratio of 1:10, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(71) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 900 C. at a temperature rise rate of 2 C./min in nitrogen with a flowing rate of 100 ml/min, wherein the temperature was maintained for 5 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(72) (3) 1 g of the obtained powders was added to 200 ml of water acidized by nitric acid, and after blowing ozone therein at a velocity of 10 g/h for 5 hours, the digestion rate of the graphite was determined as 85%.

Example 23

(73) (1) Graphite and silicomolybdic acid were mixed in a weight ratio of 1:50, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(74) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 700 C. at a temperature rise rate of 20 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 4 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(75) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 39% after 1 hour.

Example 24

(76) (1) 717-type strong base anion exchange resin and molybdenum trioxide were mixed in a weight ratio of 1:10, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(77) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 900 C. at a temperature rise rate of 2 C./min in a helium-hydrogen mixture with the helium having a flowing rate of 5 ml/min and the hydrogen having a flowing rate of 95 ml/min, wherein the temperature was maintained for 6 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(78) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the 717-type strong base anion exchange resin was determined as 100% after 1 hour.

Example 25

(79) (1) Natural flake graphite and metallic molybdenum were mixed in a weight ratio of 1:50, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(80) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 900 C. at a temperature rise rate of 1 C./min in helium with a flowing rate of 100 ml/min, wherein the temperature was maintained for 6 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(81) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 78% after 1 hour.

Example 26

(82) (1) Graphite and molybdenum trioxide were mixed in a weight ratio of 1:3.5, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(83) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 900 C. at a temperature rise rate of 20 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 1 hour, then the gas was turned off, and powders were obtained after natural cooling; and

(84) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 100% after 1 hour.

Example 27

(85) (1) Graphite and silicomolybdic acid were mixed in a weight ratio of 1:50, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(86) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 900 C. at a temperature rise rate of 20 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 4 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(87) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 100% after 1 hour.

Comparative Example 1

(88) (1) Graphite and molybdenum trioxide were mixed in a weight ratio of 1:1.5, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(89) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 600 C. at a temperature rise rate of 2 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 5 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(90) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 11% after 1 hour.

Comparative Example 2

(91) (1) Graphite and molybdenum trioxide were mixed in a weight ratio of 1:10, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(92) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 400 C. at a temperature rise rate of 2 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 4 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(93) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 5% after 1 hour.

Comparative Example 3

(94) (1) Graphite and molybdenum trioxide were mixed in a weight ratio of 1:10, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(95) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 600 C. at a temperature rise rate of 2 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 30 minutes, then the gas was turned off, and powders were obtained after natural cooling; and

(96) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 18% after 1 hour.

Comparative Example 4

(97) (1) Graphite and molybdenum trioxide were mixed in a weight ratio of 1:10, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(98) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 600 C. at a temperature rise rate of 25 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 4 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(99) (3) 1 g of the obtained powders was added to 200 ml of water alkalized by sodium hydroxide, and after blowing ozone therein at a velocity of 10 g/h for 5 hours, the digestion rate of the graphite was determined as 16%.

Comparative Example 5

(100) (1) Graphite and palladium oxide were mixed in a weight ratio of 1:1, and then placed in a ball mill pot and milled for 5 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(101) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 600 C. at a temperature rise rate of 2 C./min in an argon-hydrogen mixture with the argon having a flowing rate of 30 ml/min and the hydrogen having a flowing rate of 50 ml/min, wherein the temperature was maintained for 5 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(102) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the loss rate of the graphite was determined after 1 hour as 53%.

Comparative Example 6

(103) (1) Graphite and molybdenum trioxide were mixed in a weight ratio of 1:1, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(104) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 500 C. at a temperature rise rate of 2 C./min in argon with a flowing rate of 100 ml/min, wherein the temperature was maintained for 6 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(105) (3) 1 g of the obtained powders was added to 200 ml of water acidized by nitric acid, and after blowing ozone therein at a velocity of 10 g/h for 5 hours, the digestion rate of the graphite was determined as 10%.

Comparative Example 7

(106) (1) Graphite and molybdenum trioxide were mixed in a weight ratio of 1:10, and then placed in a ball mill pot and milled for 3 hours by using a planetary ball mill at a revolution speed of 300 r/min;

(107) (2) 2 g of the obtained powders was placed in a tube furnace and heated to 400 C. at a temperature rise rate of 2 C./min in argon with a flowing rate of 100 ml/min, wherein the temperature was maintained for 4 hours, then the gas was turned off, and powders were obtained after natural cooling; and

(108) (3) 1 g of the obtained powders was added to 20 ml of 30 wt % hydrogen peroxide, and the digestion rate of the graphite was determined as 8% after 1 hour.

(109) Compared with the above comparative examples conducted under non-preferred conditions, it can be determined that the digestion rate of carbon materials is significantly improved and the treatment efficiency is significantly increased, when the amount of a molybdenum oxide group-containing substances, the ball mill revolution speed of the planetary ball mill, the milling duration of the planetary ball mill, the temperature maintained under the high temperature condition during the thermal treatment and the duration of temperature maintenance under the high temperature condition during the thermal treatment fall within the preferred condition ranges according to the present disclosure, hereby achieving the technical effects of mild reaction conditions, low energy consumption, high operational safety and conduciveness to recovery of elements attached to the carbonaceous material.

(110) The present disclosure is not limited to the foregoing detailed description of the embodiments. The present disclosure extends to any novel feature disclosed in this specification or any novel combination thereof, as well as any step in a novel method or process disclosed or any novel combination thereof.

INDUSTRIAL APPLICABILITY

(111) The present disclosure discloses a method of oxidative digestion of a radioactively contaminated carbonaceous material in liquid phase, wherein the method achieves mild reaction conditions, low energy consumption, and high operational safety, and significantly improves the efficiency of the digestive disposal of a carbonaceous material, which is conducive to recovery of elements attached to the carbonaceous material.