Patent Grant
10434501
The present invention belongs to the field of flue gas desulfuration. Specifically, the present invention relates to a supported solid-phase catalyst for oxidizing the by-product magnesium sulfite in a magnesium desulfuration process, and to preparation method and use thereof.
The magnesium desulfuration process is a flue gas treatment process commonly used in the medium-sized and small-sized industrial boilers in China, and the rationale of the process is that using an aqueous solution of magnesium oxide as an absorbing agent, thereby sulfur dioxide in a flue gas is absorbed to produce magnesium sulfite, which is oxidized to produce a magnesium sulfate solution. This process is featured by high desulfuration efficiency, low investment, low land occupation, stable operation and so on, and hence develops very fast in China recently.
In practical operation, since the oxidation reaction rate of magnesium sulfite (the by-product of the magnesium desulfuration process) is relatively low, and insufficient oxidation of magnesium sulfite tends to bring about issues of system scaling, blocking, low product quality, secondary pollution of effluents and so on, causing a relatively high investment and high energy consumption of the recovery process of desulfuration by-product. At the present time, the above problem is solved by adding transitional metal catalyst, and this can significantly improve the oxidation capacity of the system without changing the blow rate of the oxidizing gas and hence has good application prospect. However, since the catalyst is added in a solution form into the desulfuration slurry, operation cost of the application process is high; meanwhile, the catalyst being difficult to be recovered will inevitably cause secondary pollution of heavy metal(s) in the desulfuration by-product and effluents. Therefore, the application and popularization of the catalyst is greatly limited.
An object of the present invention is to provide a supported solid-phase catalyst, preparation method and use thereof.
Specifically, a supported solid-phase catalyst, characterized in that the catalyst uses an activated carbon particle as a support, and cobalt nitrate, manganese nitrate, copper nitrate and ferrous nitrate as catalytically active components, and the molar ratio of cobalt nitrate, manganese nitrate, copper nitrate and ferrous nitrate is (2-7):(1-4):(1-4):(1-4).
The total amount of metal ions in the catalytically active components is 0.01-0.2 percent by mass of the catalyst.
The activated carbon particle is one or more particles of coal-based spheral activated carbon, coconut shell-based activated carbon, nutshell-based activated carbon, wood-based activated carbon, bamboo-based activated carbon and coal-based columnar activated carbon.
The activated carbon particle has a particle size in the range of 0.1 mm to 10 mm, and has an average pore size in the range of 1 nm to 100 nm. The activated carbon particle has good stability and mechanical strength and is easy to achieve catalyst recovery.
The method for preparing the catalyst described above has the steps of:
In step (2), the specific operations are: immersing the obtained activated carbon support in a mixed solution of cobalt nitrate, manganese nitrate, copper nitrate and ferrous nitrate, dynamically immersing at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtrating, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
Application of the above mentioned catalyst is to add the catalyst into the by-product oxidation system of the magnesium desulfuration process and catalyze the oxidation of magnesium sulfite.
In the by-product oxidation system of the magnesium desulfuration process, concentration of magnesium sulfite is in the range of 10 g/L to 160 g/L.
Compared with the prior art, the present invention has beneficial effects of simple preparation process and easy operation, and also has the following advantages:
The present invention relates to a supported solid-phase catalyst, preparation method and use thereof, which are described as below in detail by way of exemplified examples.
Activated carbon support used in the following examples was pre-treated as follows: activated carbon was heated and refluxed in a concentrated nitric acid of 50% concentration for 1 h, then ultrasonically oscillated at 40 Hz for 40 min, stood, filtrated, washed to neutral, dried at 120° C. for 5 h, so as to obtain the activated support for use.
Method for determining the reaction rate of magnesium sulfite under catalytic condition was as follows: an amount of the catalyst was added into the oxidation reaction system of magnesium sulfite, the reaction conditions were: reaction solution volume: 200 ml, reaction temperature: 45° C., initial concentration of magnesium sulfite: 20 g/L, pH: 8.0, forced air flow rate: 60 L/h. The concentration of sulfate ion in the reactor was tested at intervals, production amount of sulfate ion in a unit time representing the oxidation reaction rate of magnesium sulfite; the reaction rate of magnesium sulfite under catalytic condition was thus obtained.
In an oxidation reaction system of magnesium sulfite, no additive was added, the reaction solution volume was 200 ml, the reaction temperature was 45° C., the initial concentration of magnesium sulfite was 20 g/L, pH was 8.0, the forced air flow rate was 60 L/h, under such conditions, the reaction rate was 0.0087 mmol/(L·s), as shown by case 0 in
After pre-treatment, 10.000 g of coal-based columnar activated carbon (CYC) having a diameter of 0.5 mm was added into a mixed solution of 1.4797 g of Co(NO3)2·6H2O, 0.4932 g of Mn(NO3)2·4H2O, 0.6840 g of Fe(NO3)2·9H2O, and 0.4840 g of Cu(NO3)2·3H2O, then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
1 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0207 mmol/(L·s), as shown by case 1 in
After pre-treatment, 10.000 g of wood-based activated carbon (WC) having a diameter of 2-4 mm was added into a mixed solution of 1.4797 g of Co(NO3)2·6H2O, 0.4932 g of Mn(NO3)2·4H2O, 0.6840 g of Fe(NO3)2·9H2O, and 0.4840 g of Cu(NO3)2·3H2O, then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
1 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0260 mmol/(L·s), as shown by case 2 in
After pre-treatment, 10.000 g of bamboo-based activated carbon (BC) having a diameter of 2-4 mm was added into a mixed solution of 1.4797 g of Co(NO3)2·6H2O, 0.4932 g of Mn(NO3)2·4H2O, 0.6840 g of Fe(NO3)2·9H2O, and 0.4840 g of Cu(NO3)2·3H2O, then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
1 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0238 mmol/(L·s), as shown by case 3 in
After pre-treatment, 10.000 g of coconut shell-based activated carbon (CC) having a diameter of 2-4 mm was added into a mixed solution of 1.4797 g of Co(NO3)2·6H2O, 0.4932 g of Mn(NO3)2·4H2O, 0.6840 g of Fe(NO3)2·9H2O, and 0.4840 g of Cu(NO3)2·3H2O, then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
1 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0282 mmol/(L·s), as shown by case 4 in
After pre-treatment, 10.000 g of nutshell-based activated carbon (FC) having a diameter of 2-4 mm was added into a mixed solution of 1.4797 g of Co(NO3)2·6H2O, 0.4932 g of Mn(NO3)2·4H2O, 0.6840 g of Fe(NO3)2·9H2O, and 0.4840 g of Cu(NO3)2·3H2O, then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst 1 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0392 mmol/(L·s), as shown by case 5 in
After pre-treatment, 10.000 g of nutshell-based activated carbon (FC) having a diameter of 2-4 mm was added into a mixed solution of 0.2910 g of Co(NO3)2·6H2O, 0.2510 g of Mn(NO3)2·4H2O, 0.3420 g of Fe(NO3)2·9H2O, and 0.2420 g of Cu(NO3)2·3H2O (in a molar ratio of 1:1:1:1), then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
1 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0181 mmol/(L·s), as shown by case 1 in
After pre-treatment, 10.000 g of nutshell-based activated carbon (FC) having a diameter of 2-4 mm was added into a mixed solution of 0.873 g of Co(NO3)2·6H2O, 0.7530 g of Mn(NO3)2·4H2O, 0.6840 g of Fe(NO3)2·9H2O, and 0.4840 g of Cu(NO3)2·3H2O (in a molar ratio of 3:3:2:2), then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
1 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0210 mmol/(L·s), as shown by case 2 in
After pre-treatment, 10.000 g of nutshell-based activated carbon (FC) having a diameter of 2-4 mm was added into a mixed solution of 1.1640 g of Co(NO3)2·6H2O, 0.5020 g of Mn(NO3)2·4H2O, 0.6840 g of Fe(NO3)2·9H2O, and 0.4840 g of Cu(NO3)2·3H2O (in a molar ratio of 4:2:2:2), then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
1 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0280 mmol/(L·s), as shown by case 3 in
After pre-treatment, 10.000 g of nutshell-based activated carbon (FC) having a diameter of 2-4 mm was added into a mixed solution of 1.4550 g of Co(NO3)2·6H2O, 0.4932 g of Mn(NO3)2·4H2O, 0.6840 g of Fe(NO3)2·9H2O, and 0.4840 g of Cu(NO3)2·3H2O (in a molar ratio of 5:2:2:1), then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
1 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0332 mmol/(L·s), as shown by case 1 in
After pre-treatment, 10.000 g of nutshell-based activated carbon (FC) having a diameter of 2-4 mm was added into a mixed solution of 2.0370 g of Co(NO3)2·6H2O, 0.2510 g of Mn(NO3)2·4H2O, 0.3420 g of Fe(NO3)2·9H2O, and 0.2420 g of Cu(NO3)2·3H2O (in a molar ratio of 7:1:1:1), then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
1 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0391 mmol/(L·s), as shown by case 1 in
After pre-treatment, 10.000 g of nutshell-based activated carbon (FC) having a diameter of 2-4 mm was added into a mixed solution of 2.0370 g of Co(NO3)2·6H2O, 0.2510 g of Mn(NO3)2·4H2O, 0.3420 g of Fe(NO3)2·9H2O, and 0.2420 g of Cu(NO3)2·3H2O (in a molar ratio of 7:1:1:1), then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
0.5 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0299 mmol/(L·s), as shown by case 1 in
After pre-treatment, 10.000 g of nutshell-based activated carbon (FC) having a diameter of 2-4 mm was added into a mixed solution of 2.0370 g of Co(NO3)2·6H2O, 0.2510 g of Mn(NO3)2·4H2O, 0.3420 g of Fe(NO3)2·9H2O, and 0.2420 g of Cu(NO3)2·3H2O (in a molar ratio of 7:1:1:1), then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
1 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0342 mmol/(L·s), as shown by case 2 in
After pre-treatment, 10.000 g of nutshell-based activated carbon (FC) having a diameter of 2-4 mm was added into a mixed solution of 2.0370 g of Co(NO3)2·6H2O, 0.2510 g of Mn(NO3)2·4H2O, 0.3420 g of Fe(NO3)2·9H2O, and 0.2420 g of Cu(NO3)2·3H2O (in a molar ratio of 7:1:1:1), then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
2 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0457 mmol/(L·s), as shown by case 3 in
After pre-treatment, 10.000 g of nutshell-based activated carbon (FC) having a diameter of 2-4 mm was added into a mixed solution of 2.0370 g of Co(NO3)2·6H2O, 0.2510 g of Mn(NO3)2·4H2O, 0.3420 g of Fe(NO3)2·9H2O, and 0.2420 g of Cu(NO3)2·3H2O (in a molar ratio of 7:1:1:1), then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
4 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0558 mmol/(L·s), as shown by case 4 in
After pre-treatment, 10.000 g of nutshell-based activated carbon (FC) having a diameter of 2-4 mm was added into a mixed solution of 2.0370 g of Co(NO3)2·6H2O, 0.2510 g of Mn(NO3)2·4H2O, 0.3420 g of Fe(NO3)2·9H2O, and 0.2420 g of Cu(NO3)2·3H2O (in a molar ratio of 7:1:1:1), then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
8 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0781 mmol/(L·s), as shown by case 5 in
After pre-treatment, 10.000 g of nutshell-based activated carbon (FC) having a diameter of 0.5-1 mm was added into a mixed solution of 2.0370 g of Co(NO3)2·6H2O, 0.2510 g of Mn(NO3)2·4H2O, 0.3420 g of Fe(NO3)2·9H2O, and 0.2420 g of Cu(NO3)2·3H2O (in a molar ratio of 7:1:1:1), then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
1 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0349 mmol/(L·s), as shown in
After pre-treatment, 10.000 g of nutshell-based activated carbon (FC) having a diameter of 1-2 mm was added into a mixed solution of 2.0370 g of Co(NO3)2·6H2O, 0.2510 g of Mn(NO3)2·4H2O, 0.3420 g of Fe(NO3)2·9H2O, and 0.2420 g of Cu(NO3)2·3H2O (in a molar ratio of 7:1:1:1), then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
1 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0306 mmol/(L·s), as shown in
After pre-treatment, 10.000 g of nutshell-based activated carbon (FC) having a diameter of 2-4 mm was added into a mixed solution of 2.0370 g of Co(NO3)2·6H2O, 0.2510 g of Mn(NO3)2·4H2O, 0.3420 g of Fe(NO3)2·9H2O, and 0.2420 g of Cu(NO3)2·3H2O (in a molar ratio of 7:1:1:1), then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
1 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0217 mmol/(L·s), as shown in
After pre-treatment, 10.000 g of nutshell-based activated carbon (FC) having a diameter of 4-6 mm was added into a mixed solution of 2.0370 g of Co(NO3)2·6H2O, 0.2510 g of Mn(NO3)2·4H2O, 0.3420 g of Fe(NO3)2·9H2O, and 0.2420 g of Cu(NO3)2·3H2O (in a molar ratio of 7:1:1:1), then went through dynamical immersion at 2000 r/min in a thermostatic oscillator for 5 h, standing for 12 h under microwave irradiation, filtration, drying at 120° C. for 6 h, one-time calcining at 250° C. for 2 h, baking at 400° C. for 3 h, so as to obtain the supported solid-phase catalyst.
1 g of the obtained catalyst was added into the oxidation reaction system of magnesium sulfite having a reaction solution volume of 200 ml. Here, the catalytic reaction rate was 0.0206 mmol/(L·s), as shown in
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/CN2015/000585 | 8/12/2015 | WO | 00 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2017/024420 | 2/16/2017 | WO | A |
| Number | Name | Date | Kind |
|---|---|---|---|
| 4255400 | Hasebe | Mar 1981 | A |
| 5547648 | Buchanan | Aug 1996 | A |
| 20150126362 | Despen | May 2015 | A1 |
| Number | Date | Country |
|---|---|---|
| 101618331 | Jan 2010 | CN |
| 103285875 | Sep 2013 | CN |
| 103977832 | Aug 2014 | CN |
| S5148795 | Apr 1976 | JP |
| Number | Date | Country | |
|---|---|---|---|
| 20180029020 A1 | Feb 2018 | US |
