CN107185400B - Material for absorbing VOCs - Google Patents

Material for absorbing VOCs Download PDF

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CN107185400B
CN107185400B CN201710375777.XA CN201710375777A CN107185400B CN 107185400 B CN107185400 B CN 107185400B CN 201710375777 A CN201710375777 A CN 201710375777A CN 107185400 B CN107185400 B CN 107185400B
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parts
vocs
zeolite
solution
absorbing
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CN107185400A (en
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莫招育
陈志明
毛敬英
李宏姣
黄炯丽
张达标
杨俊超
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Scientific Research Academy of Guangxi Environmental Protection
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86—Catalytic processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86—Catalytic processes
    • B01D53/8668—Removing organic compounds not provided for in B01D53/8603 - B01D53/8665
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2252/00—Absorbents, i.e. solvents and liquid materials for gas absorption
    • B01D2252/10—Inorganic absorbents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/708—Volatile organic compounds V.O.C.'s
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2259/00—Type of treatment
    • B01D2259/80—Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
    • B01D2259/816—Sonic or ultrasonic vibration
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Abstract

The invention discloses a material for absorbing VOCs, which comprises the following raw materials: peat soil, nano ceramic powder, diatomite, zeolite, a stabilizer A, a synthetic adsorbent and a catalyst. When the material for absorbing VOCs is used for treating waste gas containing VOCs, the treatment effect on VOCs is good, and VOCs can be effectively degraded.

Description

Material for absorbing VOCs
[ technical field ] A method for producing a semiconductor device
The invention belongs to the technical field of VOCs treatment, and particularly relates to a material for absorbing VOCs.
[ background of the invention ]
Volatile organic compounds, namely VOCs (volatile organic compounds) in English, have the name of more than 70Pa at normal temperature and have the boiling point of less than 260 ℃ at normal pressure, or all organic compounds with the corresponding volatility and the vapor pressure of more than or equal to 10Pa at 20 ℃. The most common VOCs are benzene, toluene, xylene, styrene, trichloroethylene, chloroform, trichloroethane, diisocyanates and the like.
VOCs belong to atmospheric pollutants, take air as a transmission medium, and generate toxic action on human bodies through a respiratory system and skin. At present, the main methods for treating VOCs include physical methods, chemical methods and biological methods. Wherein, the physical method is to shield and dilute the odor of the VOCs by a substance without changing the chemical properties of the VOCs, or to transfer the odor from a gas phase to a liquid phase or a solid phase, and the common treatment methods are a masking method, a dilution method and an absorption method; the chemical method is to change the chemical structure of VOCs into non-irritant or low-irritant substances through chemical reaction, and the common methods include combustion method, catalytic oxidation method and acid-alkali liquor washing method; the physical method and the chemical method have the defects of more used equipment, complex process, difficult regeneration after secondary pollution, complex subsequent treatment process, high energy consumption and the like. The biological method is to decompose and oxidize VOCs into CO by using the metabolism of microorganisms2、H2Inorganic substances such as O and the like achieve the purpose of purification. The biological treatment processes commonly used at present are biological filter tanks and biological trickling filter tanks.
The liquid absorption of the prior art has low efficiency, short work, quick replacement period and short time; the materials for absorbing VOCs also have short replacement period and low efficiency, and further improvement is still needed.
[ summary of the invention ]
The invention provides a material for absorbing VOCs (volatile organic compounds), which aims to solve the problems of liquid absorption, low efficiency, short work, quick replacement period and short time in the prior art; and the material for absorbing VOCs also has the problems of short replacement period and low efficiency.
In order to solve the technical problems, the invention provides the following technical scheme:
a material for absorbing VOCs, comprising the following raw materials: peat soil, nano ceramic powder, diatomite, zeolite, a stabilizer, a synthetic adsorbent and a catalyst.
Preferably, the material for absorbing VOCs comprises the following raw materials in parts by weight: 23-45 parts of peat soil, 15-25 parts of nano ceramic powder, 12-20 parts of diatomite, 8-14 parts of zeolite, 2-4 parts of stabilizer, 2-3 parts of synthetic adsorbent and 1-2 parts of catalyst.
Preferably, the preparation method of the synthetic adsorbent comprises the following steps:
(a) analyzing the element content in the blast furnace slag by adopting an X-ray fluorescence spectrum analysis method, and calculating that the ratio of Mg/(Mn + Si) is 0.05-0.09 and the ratio of Mn/(Mn + Si) is 0.187-0.213 according to the element content;
(b) regulating the Mg/(Mn + Si) ratio and the Mn/(Mn + Si) ratio of the blast furnace slag, and adding MgO and SiO into 1g of the blast furnace slag2Adjusting the Mg/(Mn + Si) ratio and the Mn/(Mn + Si) ratio to 0.83-0.85 and 0.142-0.148 respectively to prepare a mixture A;
(c) adding 32-35mL of deionized water into the mixture A prepared in the step B, and stirring for 12-15min at the microwave power of 100-150W, the temperature of 30-35 ℃ and the rotating speed of 200-300r/min to prepare a mixture B;
(d) and c, placing the mixture B prepared in the step c into a reaction kettle, reacting for 4-6h at the temperature of 400-500 ℃ to obtain a reaction product, washing the reaction product with deionized water, and drying at the temperature of 75-82 ℃ until the water content is less than or equal to 0.6% to obtain the synthetic adsorbent.
Preferably, the preparation method of the catalyst comprises the following steps:
(1) soaking zeolite with particle size of 0.03-0.2cm in deionized water for 0.7-1h, taking out, adding into 6-10% sulfuric acid solution, heating and boiling for 0.4-0.8h, washing with deionized water until pH is 6.8-7.2, drying in oven at 85-88 deg.C for 1.5-1.8h, and cooling;
(2) dripping 18-30mL of tin tetrabromide solution into 3-3.5 times of anhydrous ethanol at the speed of 1 drop/s, and stirring at the rotating speed of 300-; dropwise adding 2-4mL of palladium salt solution with the mass concentration of 0.2-0.6% into 5-12mL of absolute ethyl alcohol at the speed of 1-2 drops/s to prepare solution B, and adjusting the pH value of the solution to 1.2-2.4; slowly dripping the solution B into the solution A at the speed of 1 drop/2-4 seconds under the conditions that the rotating speed is 350-450r/min and the temperature is 42-46 ℃, controlling the temperature to be 42-46 ℃, continuously stirring for 6-8 hours at the rotating speed of 200-300r/min in the dark, standing in the air until the viscosity of the solution is 4.2-5.8mPa & s, and preparing sol;
(3) loading the sol prepared in step 2 into a spray gun at 4-10Kg/cm2The zeolite is uniformly sprayed on the surface of the zeolite at a moving speed of 2-4mm/s under the drive of compressed air, and the distance between a spray gun and the zeolite is 18-22 cm; standing at 38-42 deg.C for 3-5 hr to form a uniform gel film; drying in an oven at 55-62 deg.C for 1.2-1.8h, cooling to room temperature, and calcining in a muffle furnace at 520-550 deg.C for 2-2.5h to obtain the catalyst.
The principle is as follows: the material integrates physical and chemical absorption methods, the working period is long, the absorption efficiency is greatly improved, the material is similar to an absorption film, is not a film but is similar to a wormhole structure, so that a channel through which waste gas passes is bent, the absorption time and the reaction efficiency are increased, the channel is long but the retention time is short, and the wormhole structure has a super-structure similar to a black hole; meanwhile, under the action of ultrasonic waves, absorption liquid in the wormhole structure can react violently under the action of the ultrasonic waves;
when strong ultrasound is transmitted in liquid, a special physical phenomenon is caused, and the physical process of the rapid and repeated motion of the hollow cavity of the liquid, such as generation, growth, compression, closure and rebound is also caused. When the cavitation bubbles collapse and close, local high pressure and high temperature are generated, and due to the influence of frequency and sound intensity in a sound field, surface tension and viscosity of liquid, temperature and pressure of surrounding environment and the like, tiny gas nuclei in the liquid are generated in time and time in a strong and slow way under the action of the sound field. The acoustic cavitation causes the exhaust gas to have both steady-state and transient cavitation types.
Stable cavitation refers primarily to the dynamic behavior of cavitation bubbles containing gases and vapors, a long-lived vibration of the bubbles. The cavitation process is generally generated at an acoustic intensity of less than 1W/cm2, and the cavitation bubbles vibrate for a long time and last for several acoustic cycles. In the acoustic field, the surface area of the vibrating bubble is larger during expansion than during compression, so that the gas diffusing into the bubble during expansion is larger than the gas diffusing out of the bubble during compression, and the bubble is enlarged during vibration. When the vibration amplitude is large enough, the bubble is converted from steady state to transient cavitation, and then collapses.
The invention has the following effects:
when the material for absorbing VOCs is used for treating waste gas containing VOCs, the treatment effect on VOCs is good, VOCs can be effectively degraded, and the material for absorbing VOCs simultaneously comprises the following raw materials: when the peat soil, the nano ceramic powder, the diatomite, the zeolite, the stabilizer, the synthetic adsorbent and the catalyst generate a synergistic effect, and the degradation of VOC is promoted.
[ description of the drawings ]
Figure 1 is a schematic diagram of an apparatus for absorbing VOCs,
figure 2 is a schematic diagram of the wormhole structure of a material that absorbs VOCs,
in the figure, 1 is an ultrasonic generating device, 2 is an absorbing device, 21 is a wormhole structure material channel, 22 is an air inlet and 23 is an air outlet.
[ detailed description ] embodiments
In order to facilitate a better understanding of the invention, the following examples are given to illustrate, but not to limit the scope of the invention.
As shown in fig. 1, in the embodiment, the material for absorbing VOCs comprises the following raw materials: peat soil, nano ceramic powder, diatomite, zeolite, a stabilizer A, a synthetic adsorbent and a catalyst.
The material for absorbing VOCs comprises the following raw materials in parts by weight: 23-45 parts of peat soil, 15-25 parts of nano ceramic powder, 12-20 parts of diatomite, 8-14 parts of zeolite, 2-3 parts of a stabilizer A2-4 parts of a synthetic adsorbent and 1-2 parts of a catalyst.
The preparation method of the synthetic adsorbent comprises the following steps:
(a) analyzing the element content in the blast furnace slag by adopting an X-ray fluorescence spectrum analysis method, and calculating that the ratio of Mg/(Mn + Si) is 0.05-0.09 and the ratio of Mn/(Mn + Si) is 0.187-0.213 according to the element content;
(b) regulating the Mg/(Mn + Si) ratio and the Mn/(Mn + Si) ratio of the blast furnace slag, and adding MgO and SiO into 1g of the blast furnace slag2Adjusting the Mg/(Mn + Si) ratio and the Mn/(Mn + Si) ratio to 0.83-0.85 and 0.142-0.148 respectively to prepare a mixture A;
(c) adding 32-35mL of deionized water into the mixture A prepared in the step B, and stirring for 12-15min at the microwave power of 100-150W, the temperature of 30-35 ℃ and the rotating speed of 200-300r/min to prepare a mixture B;
(d) and c, placing the mixture B prepared in the step c into a reaction kettle, reacting for 4-6h at the temperature of 400-500 ℃ to obtain a reaction product, washing the reaction product with deionized water, and drying at the temperature of 75-82 ℃ until the water content is less than or equal to 0.6% to obtain the synthetic adsorbent.
The preparation method of the catalyst comprises the following steps:
(1) soaking zeolite with particle size of 0.03-0.2cm in deionized water for 0.7-1h, taking out, adding into 6-10% sulfuric acid solution, heating and boiling for 0.4-0.8h, washing with deionized water until pH is 6.8-7.2, drying in oven at 85-88 deg.C for 1.5-1.8h, and cooling;
(2) dripping 18-30mL of tin tetrabromide solution into 3-3.5 times of anhydrous ethanol at the speed of 1 drop/s, and stirring at the rotating speed of 300-; dropwise adding 2-4mL of palladium salt solution with the mass concentration of 0.2-0.6% into 5-12mL of absolute ethyl alcohol at the speed of 1-2 drops/s to prepare solution B, and adjusting the pH value of the solution to 1.2-2.4; slowly dripping the solution B into the solution A at the speed of 1 drop/2-4 seconds under the conditions that the rotating speed is 350-450r/min and the temperature is 42-46 ℃, controlling the temperature to be 42-46 ℃, continuously stirring for 6-8 hours at the rotating speed of 200-300r/min in the dark, standing in the air until the viscosity of the solution is 4.2-5.8mPa & s, and preparing sol;
(3) loading the sol prepared in step 2 into a spray gun at 4-10Kg/cm2The zeolite is uniformly sprayed on the surface of the zeolite at a moving speed of 2-4mm/s under the drive of compressed air, and the distance between a spray gun and the zeolite is 18-22 cm; standing at 38-42 deg.C for 3-5 hr to form a uniform gel film; drying in an oven at 55-62 deg.C for 1.2-1.8h, cooling to room temperature, and calcining in a muffle furnace at 520-550 deg.C for 2-2.5h to obtain the catalyst.
The preparation method of the material for absorbing VOCs comprises the following steps:
s1: weighing peat soil, nano ceramic powder, diatomite, zeolite, a stabilizer A, a synthetic adsorbent and a catalyst, and uniformly mixing to obtain a mixture;
s2: and (5) printing the mixture prepared in the step (S1) layer by using a laser powder sintering three-dimensional printing technology to form a icosahedron wormhole structure, wherein each hole is mutually connected and communicated to prepare the material for absorbing the VOCs.
As shown in fig. 1: the utility model provides an equipment of absorption VOCs, includes ultrasonic generator 1, absorbing device 2, ultrasonic generator 1 links to each other with receiving device 2, the interior middle part of absorbing device 2 is provided with wormhole structure material passageway 21, the bottom and the top of absorbing device 2 are provided with air inlet 22 and gas outlet 23 respectively, there is mixed absorption liquid at the top and the bottom of wormhole structure material passageway 21.
The mixed absorption liquid comprises the following raw materials in parts by weight: 32-50 parts of nano iron powder, 2-4 parts of non-ionic surfactant, 1-3 parts of anionic surfactant, 2-3 parts of emulsifier, 1-2 parts of carbon surfactant, 0.6-1.5 parts of silicon ion surfactant, 0.3-0.8 part of fluorocarbon surfactant and 1-2 parts of stabilizer B.
Example 1
A material for absorbing VOCs, comprising the following raw materials: peat soil, nano ceramic powder, diatomite, zeolite, a stabilizer A, a synthetic adsorbent and a catalyst.
The material for absorbing VOCs comprises the following raw materials in parts by weight: 40 parts of peat, 20 parts of nano ceramic powder, 16 parts of diatomite, 12 parts of zeolite, 3 parts of a stabilizer A, 2.6 parts of a synthetic adsorbent and 1.3 parts of a catalyst.
The preparation method of the synthetic adsorbent comprises the following steps:
(a) analyzing the element content in the blast furnace slag by adopting an X-ray fluorescence spectrum analysis method, and calculating that the ratio of Mg/(Mn + Si) is 0.08 and the ratio of Mn/(Mn + Si) is 0.201 according to the element content;
(b) regulating the Mg/(Mn + Si) ratio and the Mn/(Mn + Si) ratio of the blast furnace slag, and adding MgO and SiO into 1g of the blast furnace slag2Adjusting the Mg/(Mn + Si) ratio and the Mn/(Mn + Si) ratio to 0.84 and 0.146 respectively to prepare a mixture A;
(c) adding 34mL of deionized water into the mixture A prepared in the step B, and stirring for 14min at the microwave power of 130W, the temperature of 33 ℃ and the rotating speed of 200r/min to prepare a mixture B;
(d) and c, placing the mixture B prepared in the step c into a reaction kettle, reacting for 5 hours at 450 ℃ to obtain a reaction product, washing the reaction product with deionized water, and drying at 78 ℃ until the water content is 0.6% to obtain the synthetic adsorbent.
The preparation method of the catalyst comprises the following steps:
(1) soaking zeolite with particle size of 0.12cm in deionized water for 0.9h, taking out, adding into 8% sulfuric acid solution, heating and boiling for 0.6h, washing with deionized water until pH is 7, drying in oven at 86 deg.C for 1.7h, and cooling;
(2) dripping 25mL of tin tetrabromide solution into 3.3 times of absolute ethyl alcohol at the speed of 1 drop/s, and stirring at the rotating speed of 400r/min in the dripping process to prepare solution A; dropwise adding 3mL of palladium salt solution with the mass concentration of 0.4% into 8mL of absolute ethyl alcohol at the speed of 1 drop/s to prepare solution B, and adjusting the pH value of the solution to 1.8; slowly dripping the solution B into the solution A at the speed of 1 drop/3 seconds at the rotation speed of 400r/min and the temperature of 45 ℃, controlling the temperature to be 45 ℃, continuously stirring for 7 hours at the rotation speed of 200r/min in the dark, standing in the air until the viscosity of the solution is 5mPa & s, and preparing sol;
(3) loading the sol prepared in the step 2 into a spray gun at 7Kg/cm2The zeolite is uniformly sprayed on the surface of the zeolite at a moving speed of 3mm/s under the driving of compressed air, and the distance between a spray gun and the zeolite is 20 cm; standing at 40 deg.C for 4 hr to form a uniform gel film; drying at 58 deg.C for 1.5 hr, cooling to room temperature, and calcining at 540 deg.C for 2.3 hr in muffle furnace to obtain the catalyst.
The preparation method of the material for absorbing VOCs comprises the following steps:
s1: weighing peat soil, nano ceramic powder, diatomite, zeolite, a stabilizer, a synthetic adsorbent and a catalyst, and uniformly mixing to obtain a mixture;
s2: and (5) printing the mixture prepared in the step (S1) layer by using a laser powder sintering three-dimensional printing technology to form a icosahedron wormhole structure, wherein each hole is mutually connected and communicated to prepare the material for absorbing the VOCs.
The utility model provides an equipment of absorption VOCs, includes ultrasonic generator 1, absorbing device 2, ultrasonic generator 1 links to each other with receiving device 2, the interior middle part of absorbing device 2 is provided with wormhole structure material passageway 21, the bottom and the top of absorbing device 2 are provided with air inlet 22 and gas outlet 23 respectively, there is mixed absorption liquid at the top and the bottom of wormhole structure material passageway 21.
The mixed absorption liquid comprises the following raw materials in parts by weight: 42 parts of nano iron powder, 3 parts of non-ionic surfactant, 2 parts of anionic surfactant, 2.5 parts of emulsifier, 1.6 parts of carbon surfactant, 1 part of silicon ion surfactant, 0.6 part of fluorocarbon surfactant and 1.2 parts of stabilizer.
Example 2
A material for absorbing VOCs, comprising the following raw materials: peat soil, nano ceramic powder, diatomite, zeolite, a stabilizer A, a synthetic adsorbent and a catalyst.
The material for absorbing VOCs comprises the following raw materials in parts by weight: 24 parts of peat soil, 15 parts of nano ceramic powder, 12 parts of diatomite, 8 parts of zeolite, 2 parts of stabilizer A, 2 parts of synthetic adsorbent and 1-2 parts of catalyst.
The preparation method of the synthetic adsorbent comprises the following steps:
(a) analyzing the element content in the blast furnace slag by adopting an X-ray fluorescence spectrum analysis method, and calculating that the ratio of Mg/(Mn + Si) is 0.05 and the ratio of Mn/(Mn + Si) is 0.187 according to the element content;
(b) regulating the Mg/(Mn + Si) ratio and the Mn/(Mn + Si) ratio of the blast furnace slag, and adding MgO and SiO into 1g of the blast furnace slag2Adjusting the Mg/(Mn + Si) ratio and the Mn/(Mn + Si) ratio to 0.83 and 0.142 respectively to prepare a mixture A;
(c) adding 32mL of deionized water into the mixture A prepared in the step B, and stirring for 15min at the microwave power of 100W, the temperature of 30 ℃ and the rotating speed of 200r/min to prepare a mixture B;
(d) and c, placing the mixture B prepared in the step c into a reaction kettle, reacting for 6 hours at 400 ℃ to obtain a reaction product, washing the reaction product with deionized water, and drying at 75 ℃ until the water content is 0.5% to obtain the synthetic adsorbent.
The preparation method of the catalyst comprises the following steps:
(1) soaking zeolite with particle size of 0.03cm in deionized water for 1 hr, taking out, adding into 6% sulfuric acid solution, heating and boiling for 0.8 hr, washing with deionized water until pH is 6.8, drying in oven at 85 deg.C for 1.8 hr, and cooling;
(2) dripping 18mL of tin tetrabromide solution into 3 times of absolute ethyl alcohol at the speed of 1 drop/s, and stirring at the rotating speed of 300r/min in the dripping process to prepare solution A; dropwise adding 2mL of 0.2% palladium salt solution into 5mL of absolute ethanol at a speed of 1 drop/s to prepare solution B, and adjusting the pH value of the solution to 1.2; slowly dripping the solution B into the solution A at the speed of 1 drop/2 seconds at the rotation speed of 350r/min and the temperature of 42 ℃, controlling the temperature to be 42 ℃, continuously stirring for 8 hours at the rotation speed of 200r/min in the dark, standing in the air until the viscosity of the solution is 4.2mPa & s, and preparing sol;
(3) loading the sol prepared in the step 2 into a spray gun at 4Kg/cm2The zeolite is uniformly sprayed on the surface of the zeolite at a moving speed of 2mm/s under the driving of compressed air, and the distance between a spray gun and the zeolite is 18 cm; standing at 38 deg.C for 5 hr to form a uniform gel film; drying in an oven at 55 deg.C for 1.8 hr, cooling to room temperature, and calcining in a muffle furnace at 520 deg.C for 2.5 hr to obtain the catalyst.
The preparation method of the material for absorbing VOCs comprises the following steps:
s1: weighing peat soil, nano ceramic powder, diatomite, zeolite, a stabilizer A, a synthetic adsorbent and a catalyst, and uniformly mixing to obtain a mixture;
s2: and (5) printing the mixture prepared in the step (S1) layer by using a laser powder sintering three-dimensional printing technology to form a icosahedron wormhole structure, wherein each hole is mutually connected and communicated to prepare the material for absorbing the VOCs.
As shown in fig. 1: the utility model provides an equipment of absorption VOCs, includes ultrasonic generator 1, absorbing device 2, ultrasonic generator 1 links to each other with receiving device 2, the interior middle part of absorbing device 2 is provided with wormhole structure material passageway 21, the bottom and the top of absorbing device 2 are provided with air inlet 22 and gas outlet 23 respectively, there is mixed absorption liquid at the top and the bottom of wormhole structure material passageway 21.
The mixed absorption liquid comprises the following raw materials in parts by weight: 32 parts of nano iron powder, 2 parts of non-ionic surfactant, 1 part of anionic surfactant, 2 parts of emulsifier, 1 part of carbon surfactant, 0.6 part of silicon ion surfactant, 0.3 part of fluorocarbon surfactant and 1 part of stabilizer B.
Example 3
A material for absorbing VOCs, comprising the following raw materials: peat soil, nano ceramic powder, diatomite, zeolite, a stabilizer A, a synthetic adsorbent and a catalyst.
The material for absorbing VOCs comprises the following raw materials in parts by weight: 44 parts of peat soil, 25 parts of nano ceramic powder, 20 parts of diatomite, 14 parts of zeolite, 4 parts of stabilizer A, 3 parts of synthetic adsorbent and 2 parts of catalyst.
The preparation method of the synthetic adsorbent comprises the following steps:
(a) analyzing the element content in the blast furnace slag by adopting an X-ray fluorescence spectrum analysis method, and calculating that the ratio of Mg/(Mn + Si) is 0.09 and the ratio of Mn/(Mn + Si) is 0.213 according to the element content;
(b) regulating the Mg/(Mn + Si) ratio and the Mn/(Mn + Si) ratio of the blast furnace slag, and adding MgO and SiO into 1g of the blast furnace slag2Adjusting the Mg/(Mn + Si) ratio and the Mn/(Mn + Si) ratio to 0.85 and 0.148 respectively to prepare a mixture A;
(c) adding 35mL of deionized water into the mixture A prepared in the step B, and stirring for 12min at the microwave power of 150W, the temperature of 30-35 ℃ and the rotating speed of 300r/min to prepare a mixture B;
(d) and c, placing the mixture B prepared in the step c into a reaction kettle, reacting for 4 hours at 500 ℃ to obtain a reaction product, washing the reaction product with deionized water, and drying at 82 ℃ until the water content is 0.5% to obtain the synthetic adsorbent.
The preparation method of the catalyst comprises the following steps:
(1) soaking zeolite with particle size of 0.2cm in deionized water for 0.7h, taking out, adding into 10% sulfuric acid solution, heating and boiling for 0.8h, washing with deionized water until pH is 6.8, drying in oven at 88 deg.C for 1.5h, and cooling;
(2) dripping 30mL of tin tetrabromide solution into 3.5 times of absolute ethyl alcohol at the speed of 1 drop/s, and stirring at the rotating speed of 500r/min in the dripping process to prepare solution A; 4mL of palladium salt solution with the mass concentration of 0.6% is dropwise added into 12mL of absolute ethyl alcohol at the speed of 2 drops/s to prepare solution B, and the pH value of the solution is adjusted to 2.4; slowly dripping the solution B into the solution A at the speed of 1 drop/4 seconds under the conditions that the rotating speed is 3500r/min and the temperature is 46 ℃, controlling the temperature to be 46 ℃, continuously stirring for 6 hours at the rotating speed of 300r/min in the dark, standing in the air until the viscosity of the solution is 5.8mPa & s, and preparing sol;
(3) will be provided withLoading the sol prepared in the step 2 into a spray gun at 10Kg/cm2The zeolite is uniformly sprayed on the surface of the zeolite at a moving speed of 4mm/s under the driving of compressed air, and the distance between a spray gun and the zeolite is 22 cm; standing at 42 deg.C for 3 hr to form a uniform gel film; drying at 62 deg.C for 1.2 hr, cooling to room temperature, and calcining at 550 deg.C for 2 hr in muffle furnace to obtain the catalyst.
The preparation method of the material for absorbing VOCs comprises the following steps:
s1: weighing peat soil, nano ceramic powder, diatomite, zeolite, a stabilizer A, a synthetic adsorbent and a catalyst, and uniformly mixing to obtain a mixture;
s2: and (5) printing the mixture prepared in the step (S1) layer by using a laser powder sintering three-dimensional printing technology to form a icosahedron wormhole structure, wherein each hole is mutually connected and communicated to prepare the material for absorbing the VOCs.
As shown in fig. 1: the utility model provides an equipment of absorption VOCs, includes ultrasonic generator 1, absorbing device 2, ultrasonic generator 1 links to each other with receiving device 2, the interior middle part of absorbing device 2 is provided with wormhole structure material passageway 21, the bottom and the top of absorbing device 2 are provided with air inlet 22 and gas outlet 23 respectively, there is mixed absorption liquid at the top and the bottom of wormhole structure material passageway 21.
The mixed absorption liquid comprises the following raw materials in parts by weight: 50 parts of nano iron powder, 4 parts of non-ionic surfactant, 3 parts of anionic surfactant, 3 parts of emulsifier B, 2 parts of carbon surfactant, 5 parts of silicon ion surfactant, 0.8 part of fluorocarbon surfactant and 2 parts of stabilizer.
Comparative example 1
The process is essentially the same as in example 3, except that the material for absorbing VOCs comprises the following raw materials: peat soil, nano ceramic powder, diatomite, zeolite and a stabilizer, but do not compose an adsorbent and a catalyst.
Comparative example 2
The process was essentially the same as in example 3, except that: the material for absorbing VOCs comprises the following raw materials: peat soil, nano ceramic powder, diatomite, zeolite and a stabilizer, but does not synthesize an adsorbent. .
Comparative example 3
The process is essentially the same as in example 3, except that the material for absorbing VOCs comprises the following raw materials: peat soil, nano ceramic powder, diatomite, zeolite, a stabilizer and a synthetic adsorbent, but does not contain a catalyst. .
Comparative example 4
The process is essentially the same as in example 3, except that the mixed absorption solution comprises the following raw materials: nano iron powder, non-ionic surfactant, anionic surfactant, carbon surfactant, silicon ion surfactant and fluorocarbon surfactant, but do not contain emulsifier and stabilizer.
Comparative example 5
The process is essentially the same as in example 3, except that the mixed absorption solution comprises the following raw materials: nano iron powder, non-ionic surfactant, anionic surfactant, carbon surfactant, silicon ion surfactant, fluorocarbon surfactant and stabilizer, but do not contain emulsifier.
Comparative example 6
The process is essentially the same as in example 3, except that the mixed absorption solution comprises the following raw materials: nano iron powder, non-ionic surfactant, anionic surfactant, carbon surfactant, silicon ion surfactant, fluorocarbon surfactant and emulsifier, but no stabilizer.
Example 4
The apparatus for absorbing VOCs of examples 1 to 3 and comparative examples 1 to 6 were used to treat exhaust gas containing VOCs. The waste gas containing VOCs mainly contains benzene, toluene, xylene and styrene, the concentration of VOCs in inlet gas is 600ppm, the concentration of VOCs in outlet gas of the mobile phase chamber is detected after 20s treatment, and the result is shown in the following table.
Figure GDA0001364632080000101
Figure GDA0001364632080000111
As can be seen from the table: when the equipment for absorbing VOCs is used for treating the waste gas containing VOCs, the treatment effect on VOCs is good, and the degradation efficiency can reach more than 98.87%; from the analysis of the degradation efficiency data of example 3 and comparative examples 1-3, it can be seen that the material absorbing VOCs comprises both the following raw materials: when the peat soil, the nano ceramic powder, the diatomite, the zeolite, the stabilizer, the synthetic adsorbent and the catalyst generate a synergistic effect, the degradation of VOCs is promoted; from the analysis of the degradation efficiency data of example 3 and comparative examples 4 to 6, it can be seen that the mixed absorbent solution simultaneously contains the following raw materials: nanometer iron powder, non-ionic surfactant, anionic surfactant, carbon surfactant, silicon ion surfactant, fluorocarbon surfactant, emulsifier and stabilizer to produce synergistic effect and promote the degradation of VOCs.
The foregoing is a more detailed description of the present invention and is not to be construed as limiting the invention. To those skilled in the art to which the invention relates, numerous changes, substitutions and alterations can be made without departing from the spirit of the invention, and these changes are deemed to be within the scope of the invention as defined by the appended claims.

Claims (3)

1. The treatment equipment for absorbing the VOCS is characterized by comprising an ultrasonic wave generation device and an absorption device, wherein the ultrasonic wave generation device is connected with the absorption device, a wormhole structure material channel made of a material for absorbing the VOCS is arranged in the middle of the inner part of the absorption device, an air inlet and an air outlet are respectively arranged at the bottom and the top of the absorption device, and mixed absorption liquid is arranged at the top and the bottom of the wormhole structure material channel; the preparation method of the wormhole structure material channel comprises the following steps:
s1: weighing peat soil, nano ceramic powder, diatomite, zeolite, a stabilizer A, a synthetic adsorbent and a catalyst, and uniformly mixing to obtain a mixture;
s2: printing the mixture prepared in the step S1 layer by using a laser powder sintering three-dimensional printing technology to form a wormhole structure, wherein each hole is mutually connected and communicated to prepare a wormhole structure material channel for absorbing VOCS;
the wormhole structure material channel enables the channel through which the waste gas passes to be bent, the absorption time and the reaction efficiency are increased, and the channel is long but the retention time is short;
the mixed absorption liquid comprises the following raw materials in parts by weight: 32-50 parts of nano iron powder, 2-4 parts of non-ionic surfactant, 1-3 parts of anionic surfactant, 2-3 parts of emulsifier, 1-2 parts of carbon surfactant, 0.6-1.5 parts of silicon ion surfactant, 0.3-0.8 part of fluorocarbon surfactant and 0.3-2 parts of stabilizer B1;
the waste gas containing VOCs mainly contains benzene, toluene, xylene and styrene;
in the step S1 of the preparation method of the wormhole structure material channel, the mass ratio of the peat soil, the nano ceramic powder, the diatomite, the zeolite, the stabilizer A, the synthetic adsorbent and the catalyst is 23-45:15-25:12-20:8-14:2-4:2-3: 1-2;
the preparation method of the synthetic adsorbent in the step S1 of the preparation method of the wormhole structure material channel comprises the following steps:
(a) analyzing the element content in the blast furnace slag by adopting an X-ray fluorescence spectrum analysis method, and calculating that the ratio of Mg/(Mn + Si) is 0.05-0.09 and the ratio of Mn/(Mn + Si) is 0.187-0.213 according to the element content;
(b) regulating the Mg/(Mn + Si) ratio and the Mn/(Mn + Si) ratio of the blast furnace slag, and adding MgO and SiO into 1g of the blast furnace slag2Adjusting the Mg/(Mn + Si) ratio and the Mn/(Mn + Si) ratio to 0.83-0.85 and 0.142-0.148 respectively to prepare a mixture A;
(c) adding 32-35mL of deionized water into the mixture A prepared in the step B, and stirring for 12-15min at the microwave power of 100-150W, the temperature of 30-35 ℃ and the rotating speed of 200-300r/min to prepare a mixture B;
(d) and c, placing the mixture B prepared in the step c into a reaction kettle, reacting for 4-6h at the temperature of 400-500 ℃ to obtain a reaction product, washing the reaction product with deionized water, and drying at the temperature of 75-82 ℃ until the water content is less than or equal to 0.6% to obtain the synthetic adsorbent.
2. A VOCS absorbing device as claimed in claim 1, wherein: the preparation method of the catalyst in the step S1 of the preparation method of the wormhole structure material channel comprises the following steps:
(1) soaking zeolite with particle size of 0.03-0.2cm in deionized water for 0.7-1h, taking out, adding into 6-10% sulfuric acid solution, heating and boiling for 0.4-0.8h, washing with deionized water until pH is 6.8-7.2, drying in oven at 85-88 deg.C for 1.5-1.8h, and cooling;
(2) dripping 18-30mL of tin tetrabromide solution into 3-3.5 times of anhydrous ethanol at the speed of 1 drop/s, and stirring at the rotating speed of 300-; dropwise adding 2-4mL of palladium salt solution with the mass concentration of 0.2-0.6% into 5-12mL of absolute ethyl alcohol at the speed of 1-2 drops/s to prepare solution B, and adjusting the pH value of the solution to 1.2-2.4; slowly dripping the solution B into the solution A at the speed of 1 drop/2-4 seconds under the conditions that the rotating speed is 350-450r/min and the temperature is 42-46 ℃, controlling the temperature to be 42-46 ℃, continuously stirring for 6-8 hours at the rotating speed of 200-300r/min in the dark, standing in the air until the viscosity of the solution is 4.2-5.8mPa & s, and preparing sol;
(3) loading the sol prepared in step 2 into a spray gun at 4-10Kg/cm2The zeolite is uniformly sprayed on the surface of the zeolite at a moving speed of 2-4mm/s under the drive of compressed air, and the distance between a spray gun and the zeolite is 18-22 cm; standing at 38-42 deg.C for 3-5 hr to form a uniform gel film; drying in an oven at 55-62 deg.C for 1.2-1.8h, cooling to room temperature, and calcining in a muffle furnace at 520-550 deg.C for 2-2.5h to obtain the catalyst.
3. A device for absorbing a VOCS as in claim 1, wherein the wormhole structure of said wormhole structure material channels is a icosahedron wormhole structure.
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103100386A (en) * 2013-01-15 2013-05-15 汕头大学 Preparation method of monolithic catalyst for degrading VOCS (Volatile Organic Compounds)
CN103252210A (en) * 2013-05-22 2013-08-21 武汉红金龙印务股份有限公司 Method for preparing adsorbent for volatile organic compounds (VOCs) in air
CN104096535A (en) * 2014-07-09 2014-10-15 西安交通大学 High-adsorbability powdered material forming technology based on 3D printing technology
CN205586752U (en) * 2016-03-31 2016-09-21 陈聪 High -efficient desulfurization machine of ultrasonic wave

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103100386A (en) * 2013-01-15 2013-05-15 汕头大学 Preparation method of monolithic catalyst for degrading VOCS (Volatile Organic Compounds)
CN103252210A (en) * 2013-05-22 2013-08-21 武汉红金龙印务股份有限公司 Method for preparing adsorbent for volatile organic compounds (VOCs) in air
CN104096535A (en) * 2014-07-09 2014-10-15 西安交通大学 High-adsorbability powdered material forming technology based on 3D printing technology
CN205586752U (en) * 2016-03-31 2016-09-21 陈聪 High -efficient desulfurization machine of ultrasonic wave

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