Disclosure of Invention
In order to overcome the technical problems mentioned in the background technology, the invention provides a method for industrially treating a sulfur-containing and arsenic-containing material by microwaves.
The purpose of the invention can be realized by the following technical scheme:
a method for industrially treating a sulfur-containing and arsenic-containing material by microwaves specifically comprises the following steps:
step S1: pretreatment of waste materials: detecting the content of sulfur and arsenic in the material, adding the material into a crusher for crushing, and then adding the crushed material into a grinder to prepare a powder material;
step S2: mixing materials: adding the powder material and potassium ferrate into a stirrer, uniformly stirring to prepare mixed powder, then adding a prepared salt solution into the stirrer, and continuously stirring to prepare a mixed wet material;
step S3: spreading materials: adding the mixed wet material into a bin of microwave equipment, spreading the mixed wet material on a material containing plate through a material spreading plate, and conveying the mixed wet material into the microwave equipment by a conveyor;
step S4: microwave oxidation: conveying the material containing plate to an oxidation area, introducing oxygen into the mixed wet material by an aeration rake, and simultaneously carrying out microwave heating;
step S5: microwave detoxification: conveying the material containing plate to a high-heat area, and performing microwave heating again to remove oxides containing sulfur and arsenic;
step S6: and (3) cooling: the material containing plate is conveyed to a cooling area and cooled through a coil heat exchanger, and the material subjected to microwave detoxification is cooled to be lower than 60 ℃.
Furthermore, exhaust fans are arranged at the tops of the oxidation zone, the high heating zone and the cooling zone, and exhaust gas is pumped out to the treatment liquid for sedimentation.
Further, in step S1, the particle size of the powder material is controlled to be 40-300 mesh.
Further, in step S2, the amount of potassium ferrate added is 1.1-1.5 times the total mass of sulfur and arsenic in the powdered material.
Further, in step S2, the salt solution includes one or more of soluble sodium salt, soluble ammonium salt and soluble nitrate, which are mixed in any proportion, and the mass fraction of the salt solution is 1.0% to 10.0%, and the addition amount of the salt solution is 10.0% to 20.0% of the mass of the powder material.
Further, the soluble sodium salt is one or a mixture of more of sodium chloride, sodium carbonate, sodium bicarbonate, sodium bisulfate, sodium sulfate and sodium sulfite.
Further, the soluble ammonium salt is one or a mixture of more of ammonium chloride, ammonium sulfate, ammonium nitrate and the like;
further, the nitrate is one or a mixture of several of sodium nitrate, potassium nitrate, ammonium nitrate and calcium nitrate.
Further, in step S3, the spreading thickness of the mixed wet material in the material containing plate is 1-20 cm.
Further, in step S4, the amount of oxygen and the mixed wet material is 2-5L/100 kg.
Further, in step S4, the microwave heating temperature in the oxidation zone is 80-105 ℃, and the treatment time of the mixed wet material in the oxidation zone is 0.5-3 h.
Further, in step S4, the microwave heating temperature in the high-heat zone is 105-500 ℃, and the processing time of the mixed wet material in the high-heat zone is 0.5-7 h.
Further, in step S4, the processing liquid is a mixture of ferric trichloride, calcium hydroxide and water, and the mass fraction of the ferric trichloride is 10.0-20.0%, and the mass fraction of the calcium hydroxide is 5.5-8%.
Furthermore, microwave equipment is adopted in the treatment process of the mixed wet materials, the microwave equipment comprises a conveyor and a protective cover arranged on the outer side of the conveyor, the protective cover is sequentially divided into an oxidation area, a high-heat area and a cooling area through partition plates, and a plurality of material containing plates are conveyed on the conveyor.
The upper and lower both sides in oxidation zone, high hot district all are provided with the polar plate, and the polar plate distributes in the upper and lower of flourishing flitch, and the protection casing is close to the one side that the high hot district was kept away from in the oxidation zone and is provided with the feed bin, and the top that the protection casing is close to the one end of feed bin is provided with the cylinder, and the output of cylinder runs through the polar plate fixedly connected with aeration harrow above the conveyer, and the inlet end intercommunication oxygen pipeline of aeration harrow through the aeration height of cylinder regulation aeration harrow, adapts to different stone thickness aerations.
The side wall of the protective cover where the cooling area is located is fixed with a coil heat exchanger, so that the treated material is quickly cooled, and sulfur and arsenic oxides are prevented from entering air.
Exhaust fans are arranged at the tops of the protective covers of the oxidation zone, the high heat zone and the cooling zone, and are used for extracting steam containing sulfur and arsenic oxides generated in the process.
The invention has the beneficial effects that:
1. according to the method provided by the invention, potassium ferrate and a salt solution are mixed with a waste material to prepare a mixed wet material, the mixed wet material contains ions with higher concentration, trivalent arsenic is oxidized into pentavalent arsenic by the potassium ferrate, the toxicity of the arsenic is reduced, the divalent sulfur is converted into trivalent sulfur, and oxygen is introduced in an aeration mode, so that on one hand, the oxidation is promoted, on the other hand, pentavalent arsenic oxide and trivalent sulfur oxide are generated, the pentavalent arsenic oxide is easily soluble in water and can be removed along with steam heated by microwave, the trivalent sulfur oxide reacts with water to release heat and promote the oxidation, the trivalent sulfur oxide is easily soluble in water and can be removed along with the steam, thereby realizing desulfurization and dearsenification, and through experimental detection, the waste material with the sulfur content of 5.27 percent and the arsenic content of 18.58 percent has the arsenic removal rate of 96.0 percent and the sulfur removal rate of 96.9 percent, and realizing the effective separation of sulfur, arsenic and the material.
2. In the treatment process, arsenic is converted into pentavalent arsenic which has higher removal rate at the pH value of 5-10, and trivalent arsenic in the material has higher removal rate only at the pH value of 8-10, so that the pH value requirement in the post-treatment process is widened, and the subsequent treatment is facilitated.
3. The invention fully combines the advantages of the microwave heating effect and the traditional industrial treatment, provides simple microwave equipment which is suitable for the invention, has simple operation and is suitable for the industrial treatment of the sulfur-containing arsenic material.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
In the embodiment, industrial smoke dust, flue dust, copper arsenic filter cake, acid sludge or a mixed material of raw arsenic-containing ores is selected as a processing object, and the sulfur content and the arsenic content of the processing object are detected to be 5.27% and 18.58%, respectively.
Example 1
The embodiment of the present invention is to process the mixture as shown in fig. 1-2, and the specific process is as follows:
step S1: pretreatment of waste materials: adding 100kg of materials into a crusher for crushing, then adding the materials into a grinder for grinding, sieving the powder materials through a 40-mesh sieve, returning and grinding the materials on the sieve until the granularity of all the powder materials is less than 40 meshes, and preparing the powder materials;
step S2: mixing materials: adding the powder material prepared in the step S1 and 1.65kg of potassium ferrate into a stirrer, controlling the rotating speed to be 180r/min, stirring for 20min to prepare mixed powder, and simultaneously taking sodium chloride, sodium carbonate, ammonium chloride and sodium nitrate according to the mass ratio of 1.5: 1: 0.5:1.3, adding tap water, stirring and completely dissolving to prepare a salt solution, wherein the mass fraction of the salt solution is 1.0%, adding 10kg of the salt solution into the mixed powder under the stirring state, and continuously stirring for 10min to prepare a mixed wet material;
step S3: spreading materials: adding the mixed wet material into a bin 12 of microwave equipment, spreading the mixed wet material on a material containing plate 16 through a material spreading plate, setting the thickness of the spread material to be 1cm, and then conveying the spread material into the microwave equipment by a conveyor 11;
step S4: microwave oxidation: conveying the material containing plate 16 to an oxidation area 19, introducing 2L of oxygen into the mixed wet material by using the aeration rake, simultaneously controlling the output power and the microwave frequency of the microwave source, controlling the microwave heating temperature to be 80 ℃, controlling the conveying speed of the conveyor 11, and conveying the mixed wet material in the oxidation area 19 for 0.5 h;
step S5: microwave detoxification: the material containing plate 16 is conveyed to the high heat area 18, the output power and the microwave frequency of the microwave source are controlled at the same time, the microwave heating temperature is controlled to be 105 ℃, the conveying speed of the conveyor 11 is controlled, and the conveying time of the mixed wet material in the high heat area 18 is 0.5 h;
step S6: and (3) cooling: the material containing plate 16 is conveyed to the cooling area 17, cold air is blown into the cooling area 17 through the cooling device, the material subjected to microwave detoxification is cooled to 60 ℃, and the material is taken out for detection again.
Example 2
The embodiment of the present invention is to process the mixture as shown in fig. 1-2, and the specific process is as follows:
step S1: pretreatment of waste materials: adding 100kg of materials into a crusher for crushing, then adding the materials into a grinder for grinding, sieving the powder materials through a sieve with 150 meshes, returning and grinding the materials on the sieve until the granularity of all the powder materials is less than 150 meshes, and preparing the powder materials;
step S2: mixing materials: adding the powder material prepared in the step S1 and 1.95kg of potassium ferrate into a stirrer, controlling the rotating speed to be 180r/min, stirring for 20min to prepare mixed powder, and simultaneously taking sodium bicarbonate, sodium bisulfate, ammonium sulfate, potassium nitrate and ammonium nitrate according to the mass ratio of 1.1: 1.3: 0.7:0.9:0.6, adding tap water, stirring and completely dissolving to prepare a salt solution, wherein the mass fraction of the salt solution is 5.0%, adding 10kg of the salt solution into the mixed powder under the stirring state, and continuously stirring for 10min to prepare a mixed wet material;
step S3: spreading materials: adding the mixed wet material into a bin 12 of microwave equipment, spreading the mixed wet material on a material containing plate 16 through a material spreading plate, setting the thickness of the spread material to be 10cm, and then conveying the spread material into the microwave equipment by a conveyor 11;
step S4: microwave oxidation: the material containing plate 16 is conveyed to an oxidation area 19, 4L of oxygen is introduced into the mixed wet material by the aeration rake, the output power and the microwave frequency of the microwave source are controlled at the same time, the microwave heating temperature is controlled to be 90 ℃, the conveying speed of the conveyor 11 is controlled, and the conveying time of the mixed wet material in the oxidation area 19 is 1.5 hours;
step S5: microwave detoxification: the material containing plate 16 is conveyed to the high heat area 18, the output power and the microwave frequency of the microwave source are controlled at the same time, the microwave heating temperature is controlled to be 220 ℃, the conveying speed of the conveyor 11 is controlled, and the conveying time of the mixed wet material in the high heat area 18 is 4 hours;
step S6: and (3) cooling: the material containing plate 16 is conveyed to the cooling area 17, cold air is blown into the cooling area 17 through the cooling device, the material subjected to microwave detoxification is cooled to 60 ℃, and the material is taken out for detection again.
Example 3
The embodiment of the present invention is to process the mixture as shown in fig. 1-2, and the specific process is as follows:
step S1: pretreatment of waste materials: adding 100kg of materials into a crusher for crushing, then adding the materials into a grinder for grinding, sieving the powder materials through a 300-mesh sieve, returning and grinding the sieved materials until the particle size of all the powder materials is smaller than 300 meshes, and preparing the powder materials;
step S2: mixing materials: adding the powder material prepared in the step S1 and 2.25kg of potassium ferrate into a stirrer, controlling the rotating speed to be 180r/min, stirring for 20min to prepare mixed powder, and simultaneously taking sodium sulfate, sodium sulfite, ammonium nitrate and calcium nitrate according to the mass ratio of 0.2: 0.7: 1.1:0.9, adding tap water, stirring and completely dissolving to prepare a salt solution, wherein the mass fraction of the salt solution is 10.0%, adding 10kg of the salt solution into the mixed powder under the stirring state, and continuously stirring for 10min to prepare a mixed wet material;
step S3: spreading materials: adding the mixed wet material into a bin 12 of microwave equipment, spreading the mixed wet material on a material containing plate 16 through a material spreading plate, setting the thickness of the spread material to be 20cm, and then conveying the spread material into the microwave equipment by a conveyor 11;
step S4: microwave oxidation: conveying the material containing plate 16 to an oxidation area 19, introducing 5L of oxygen into the mixed wet material by using the aeration rake, simultaneously controlling the output power and the microwave frequency of the microwave source, controlling the microwave heating temperature to be 105 ℃, controlling the conveying speed of the conveyor 11, and conveying the mixed wet material in the oxidation area 19 for 3 hours;
step S5: microwave detoxification: the material containing plate 16 is conveyed to the high heat area 18, the output power and the microwave frequency of the microwave source are controlled at the same time, the microwave heating temperature is controlled to be 500 ℃, the conveying speed of the conveyor 11 is controlled, and the conveying time of the mixed wet material in the high heat area 18 is 7 hours;
step S6: and (3) cooling: the material containing plate 16 is conveyed to the cooling area 17, cold air is blown into the cooling area 17 through the cooling device, the material subjected to microwave detoxification is cooled to 60 ℃, and the material is taken out for detection again.
Specific assay data for examples 1-3 are shown in Table 1:
TABLE 1
As is clear from table 1, in example 2, the arsenic removal rate of the scrap having a sulfur content of 5.27% and an arsenic content of 18.58% was 96.0%, and the sulfur removal rate was 96.9%, which showed excellent desulfurization and dearsenification effects.
Example 4
The top of the oxidation zone 19, the high heat zone 18 and the cooling zone 17 in the embodiment 1-3 are all provided with exhaust fans 14, exhaust gases are respectively pumped to the sample 1 treatment liquid containing 10.0% of ferric trichloride and 5.5% of calcium hydroxide, the sample 2 treatment liquid containing 15.0% of ferric trichloride and 7% of calcium hydroxide, and the sample 3 treatment liquid containing 20.0% of ferric trichloride and 8% of calcium hydroxide, aeration is carried out, the arsenic and sulfur content in the detected gas all reach the national standard, and finally floc in the treatment liquid is removed by coagulation.
Example 5
Referring to fig. 2, in the treatment process of the mixed wet material, microwave equipment is adopted, the microwave equipment comprises a conveyor 11 and a protective cover arranged outside the conveyor 11, the protective cover is sequentially divided into an oxidation area 19, a high heat area 18 and a cooling area 17 through partition plates, and a plurality of material containing plates 16 are conveyed on the conveyor 11.
The upper side and the lower side of the oxidation zone 19 and the high heat zone 18 are both provided with polar plates 15, the polar plates 15 are distributed above and below the conveyor, one side of the protective cover, which is close to the oxidation zone 19 and is far away from the high heat zone 18, is provided with a stock bin 12, the top of one end of the protective cover, which is close to the stock bin 12, is provided with an air cylinder 13, the output end of the air cylinder 13 penetrates through the polar plate 15 fixedly connected with an aeration rake above the conveyor 11, the air inlet end of the aeration rake is communicated with an oxygen pipeline, the aeration height of the aeration rake is adjusted through the air cylinder 13, and the aeration rake is suitable for aeration with different paving thicknesses.
In the description herein, references to the description of "one embodiment," "an example," "a specific example" or the like are intended to mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the invention. In this specification, the schematic representations of the terms used above do not necessarily refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.
The foregoing is merely exemplary and illustrative of the principles of the present invention and various modifications, additions and substitutions of the specific embodiments described herein may be made by those skilled in the art without departing from the principles of the present invention or exceeding the scope of the claims set forth herein.