CN113304727A - Preparation method of formaldehyde purification activated carbon with low cost and high activity - Google Patents

Preparation method of formaldehyde purification activated carbon with low cost and high activity Download PDF

Info

Publication number
CN113304727A
CN113304727A CN202110670185.7A CN202110670185A CN113304727A CN 113304727 A CN113304727 A CN 113304727A CN 202110670185 A CN202110670185 A CN 202110670185A CN 113304727 A CN113304727 A CN 113304727A
Authority
CN
China
Prior art keywords
activated carbon
weighing
formaldehyde
acid
low cost
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN202110670185.7A
Other languages
Chinese (zh)
Other versions
CN113304727B (en
Inventor
刘小军
于晓琳
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Suzhou Lanlu New Material Technology Co ltd
Original Assignee
Suzhou Lanlu New Material Technology Co ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Suzhou Lanlu New Material Technology Co ltd filed Critical Suzhou Lanlu New Material Technology Co ltd
Priority to CN202110670185.7A priority Critical patent/CN113304727B/en
Publication of CN113304727A publication Critical patent/CN113304727A/en
Application granted granted Critical
Publication of CN113304727B publication Critical patent/CN113304727B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/20Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/72Organic compounds not provided for in groups B01D53/48 - B01D53/70, e.g. hydrocarbons
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77Liquid phase processes
    • B01D53/78Liquid phase processes with gas-liquid contact
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F8/00Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
    • F24F8/10Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering
    • F24F8/15Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering by chemical means
    • F24F8/158Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering by chemical means using active carbon
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/80Organic bases or salts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Biomedical Technology (AREA)
  • Health & Medical Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Inorganic Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)

Abstract

The invention discloses a preparation method of formaldehyde purification activated carbon with low cost and high activity, which comprises the following steps: s1: preparing an impregnation liquid containing high-boiling-point acid and organic amine; s2: soaking the soaking solution obtained in the step S1 and activated carbon in equal volume to obtain soaked activated carbon; s3: and (4) flatly laying the impregnated activated carbon obtained in the step S2, ventilating and air-drying to obtain the formaldehyde purification activated carbon. In step S1, the high boiling acid includes one or two of sulfuric acid and phosphoric acid. Compared with the prior art, the method adopts the active carbon nano-pore liquid phase to form the film, and the introduction of the high-boiling-point acid greatly strengthens and accelerates the mass transfer process of formaldehyde molecules to the water phase liquid film, so that the formaldehyde and the organic amine are quickly reacted in the liquid phase, and the purification efficiency of the formaldehyde is greatly improved; meanwhile, the whole process is simple and convenient to operate, a high-temperature drying process is avoided, and the production cost is greatly reduced.

Description

Preparation method of formaldehyde purification activated carbon with low cost and high activity
Technical Field
The invention relates to a preparation method of formaldehyde purification activated carbon with low cost and high activity, belonging to the field of air purification.
Background
Formaldehyde is a highly toxic gas and has been identified as a class 1 carcinogen by the International agency for research on cancer, IARC, the world health organization. China 'indoor air quality Standard' GB/T18883-2002 stipulates that the limit value of formaldehyde in indoor air of the second type of civil construction engineering is 0.10 mg/m for cultivation, and the limit value of formaldehyde in indoor air of the first type of civil construction engineering is 0.08 mg/m for cultivation. The main harm of formaldehyde is represented by stimulation to skin mucosa, and when the formaldehyde reaches a certain concentration indoors, people feel uncomfortable. A formaldehyde concentration higher than 0.08 mg/m can cause redness of the eye, itching of the eye, discomfort or pain in the throat, hoarseness, sneezing, chest distress, asthma, dermatitis and the like in a short period; and the long-term exposure of human body to low-concentration formaldehyde can easily cause nervous system disorder, memory decline, nasopharyngeal carcinoma, colon cancer and the like.
For the treatment of indoor formaldehyde pollution, people develop different purification methods and purification materials, mainly comprising: the active carbon adsorption method physically adsorbs formaldehyde in the air by utilizing a porous structure rich in active carbon, and has the defects of low adsorption capacity, easiness in saturation, secondary pollution caused by formaldehyde release after long-term use and the like; the spraying method is characterized in that nano titanium dioxide or a formaldehyde catching agent is dissolved in a water phase system and sprayed in the air to achieve the purpose of purifying formaldehyde, and the defect is that the formaldehyde gas continuously released in a room can not be continuously purified; a catalytic method, in which active metals such as Mn, Pd, Pt and the like are loaded on a porous material, and formaldehyde is effectively decomposed into water and carbon dioxide by utilizing the catalytic activity of the active metals; the absorption method is to load formaldehyde scavenger in porous material and utilize the chemical reaction between formaldehyde and scavenger to eliminate formaldehyde. Among the many methods, the absorption method is one of the more effective means for purifying formaldehyde in a room.
The national standard GB/T18801-. The existing absorption method material is difficult to consider the purification efficiency and the accumulative purification capacity of formaldehyde under the specified test condition, and the complex preparation process greatly increases the material cost.
Disclosure of Invention
In view of the above-mentioned shortcomings of the prior art, the present invention aims to provide a method for preparing formaldehyde purification activated carbon with low cost and high activity.
The purpose of the invention is realized by the following technical scheme: a preparation method of formaldehyde purification activated carbon with low cost and high activity comprises the following steps:
s1: preparing an impregnation liquid containing high-boiling-point acid and organic amine;
s2: soaking the soaking solution obtained in the step S1 and activated carbon in equal volume to obtain soaked activated carbon;
s3: and (4) flatly laying the impregnated activated carbon obtained in the step S2, ventilating and air-drying to obtain the formaldehyde purification activated carbon.
Preferably, in the S1 step, the high-boiling acid includes one or a mixture of two of sulfuric acid and phosphoric acid.
Preferably, in the step S1, the organic amine includes one or more of ethylene urea, diethylamine, diethylenetriamine, triethylenetetramine and amino acids; wherein, the amino acid substances comprise: glycine, aspartic acid, glutamic acid, cysteine, lysine, histidine and arginine.
Preferably, in the step S2, the mass ratio of the high-boiling-point acid to the activated carbon is 0.1-1.0: 10; the mass ratio of the organic amine to the active carbon is 0.1-1.0:15, and the soaking time is 6-24 hours; in the step S2, the equal volume of the impregnation solution is calculated according to the saturated water absorption of the required activated carbon.
Preferably, in the step S3, the activated carbon is spread flat and ventilated for air drying, in order to spread the impregnated activated carbon evenly and flat at room temperature, natural ventilation is performed to volatilize part of the moisture absorbed by the activated carbon, and the air drying time is determined according to the temperature at room temperature, and the sample is weighed until the moisture content in the material is 20-40%, so as to prepare the formaldehyde purification activated carbon.
Preferably, 100 g of coal columnar activated carbon is weighed, and the saturated water absorption rate of the coal columnar activated carbon is 76% of the mass of the coal columnar activated carbon; weighing 76 ml of deionized water in a beaker, weighing 5 g of sulfuric acid and 5 g of ethylene urea, and dissolving to prepare a dipping solution; mixing the impregnation liquid with the activated carbon, uniformly stirring, and standing for 12 h; the activated carbon was spread on a screen and air dried naturally at an indoor temperature of 28 ℃ for 6 hours, and the mass of the activated carbon was 159 g, at which time the water content of the material was 31%.
Preferably, 100 g of coal columnar activated carbon is weighed, and the saturated water absorption rate of the coal columnar activated carbon is 76% of the mass of the coal columnar activated carbon; weighing 76 ml of deionized water in a beaker, weighing 3 g of phosphoric acid and 6 g of glycine, and dissolving to prepare a steeping fluid; mixing the impregnation liquid with the active carbon, uniformly stirring, and standing for 10 h; the activated carbon is laid on a screen mesh and naturally dried at the indoor temperature of 30 ℃ for 6 hours, and the weight of the activated carbon is 145 g, and the water content of the material is 25%.
Preferably, 100 g of coconut shell activated carbon is weighed, and the saturated water absorption rate of the coconut shell activated carbon is 70% of the mass of the coconut shell activated carbon; weighing 70 ml of deionized water in a beaker, weighing 3 g of phosphoric acid, 3 g of sulfuric acid and 8 g of diethylamine, and dissolving to prepare a dipping solution; mixing the impregnation liquid with the active carbon, uniformly stirring, and standing for 8 hours; the activated carbon was spread on a screen and air dried naturally at an indoor temperature of 28 ℃ for 6 hours, and the mass of the activated carbon was 158 g, at which time the water content of the material was 28%.
Preferably, 100 g of coconut shell activated carbon is weighed, and the saturated water absorption rate of the coconut shell activated carbon is 70% of the mass of the coconut shell activated carbon; weighing 70 ml of deionized water in a beaker, and weighing 8 g of sulfuric acid and 10 g of glutamic acid to dissolve to prepare a steeping fluid; mixing the impregnation liquid with the activated carbon, uniformly stirring, and standing for 24 hours; the activated carbon was spread on a screen and air dried naturally at 25 ℃ in room temperature for 6 hours, and the mass of the activated carbon was 176 g, at which time the water content of the material was 33%.
Preferably, 100 g of coconut shell activated carbon is weighed, and the saturated water absorption rate of the coconut shell activated carbon is 70% of the mass of the coconut shell activated carbon; weighing 70 ml of deionized water in a beaker, weighing 7 g of sulfuric acid, 5 g of ethylene urea and 4 g of glycine, and dissolving to prepare a dipping solution; mixing the impregnation liquid with the activated carbon, uniformly stirring, and standing for 18 h; the activated carbon is laid on a screen mesh and naturally dried at the indoor temperature of 26 ℃ for 10 hours, and the weight of the activated carbon is 145 g, and the water content of the material is 20%.
The technical scheme of the invention has the advantages that: the method overcomes the defects of low adsorption capacity and easy saturation of the active carbon and low reaction efficiency of gas (formaldehyde) -solid (formaldehyde scavenger) after the active carbon loaded formaldehyde scavenger is subjected to high-temperature drying treatment in the prior art, and prepares the high-activity formaldehyde purification active carbon at lower cost by utilizing the processes of liquid-phase film formation of the active carbon, rapid adsorption of residual pore channels of the active carbon on the formaldehyde gas, and mass transfer strengthening of a formaldehyde-liquid film in an acidic environment so as to rapidly dissolve the formaldehyde in the liquid film and high-efficiency reaction of the liquid (formaldehyde) -liquid (organic amine formaldehyde scavenger).
Compared with the prior art, the method adopts the active carbon nano-pore liquid phase to form the film, and the introduction of the high-boiling-point acid greatly strengthens and accelerates the mass transfer process of formaldehyde molecules to the water phase liquid film, so that the formaldehyde and the organic amine are quickly reacted in the liquid phase, and the purification efficiency of the formaldehyde is greatly improved; meanwhile, the whole process is simple and convenient to operate, a high-temperature drying process is avoided, and the production cost is greatly reduced.
Detailed Description
The objects, advantages and features of the present invention will be illustrated by the following non-limiting description of preferred embodiments. The embodiments are merely exemplary for applying the technical solutions of the present invention, and any technical solution formed by replacing or equivalently transforming the embodiments is within the scope of the present invention as claimed.
The invention discloses a preparation method of formaldehyde purification activated carbon with low cost and high activity, and the high activity is embodied in that the prepared material can quickly, efficiently and durably eliminate indoor formaldehyde. Dissolving high-boiling-point acid and organic amine substances into a water phase, impregnating and loading the materials with active carbon in an equal volume, naturally drying the materials until the water content of the materials is 20-40%, allowing part of water vapor to escape in the air drying process of the materials to enable the materials to still have a developed pore structure, spreading impregnation liquid in a micro pore channel of the active carbon to form a uniform liquid film, quickly adsorbing formaldehyde molecules in the air by using the porous structure of the materials, strengthening the mass transfer absorption process of the formaldehyde molecules to the liquid film by using an acidic environment, and finally performing liquid-liquid reaction of organic amine and formaldehyde to achieve the aim of quickly, efficiently and durably eliminating the formaldehyde.
A preparation method of formaldehyde purification activated carbon with low cost and high activity comprises the following steps:
s1: preparing an impregnation liquid containing high-boiling-point acid and organic amine;
s2: soaking the soaking solution obtained in the step S1 and activated carbon in equal volume to obtain soaked activated carbon;
s3: and (4) flatly laying the impregnated activated carbon obtained in the step S2, ventilating and air-drying to obtain the formaldehyde purification activated carbon.
In the technical scheme, the concentration of the high-boiling-point acid is not particularly specified, and because different activated carbons require different water amounts when equal-volume impregnation is carried out, only the use amount of the high-boiling-point acid and the water amount required by equal-volume impregnation are mentioned. In addition, the molar ratios are not mentioned here, but are used only in mass ratios. Wherein, the high boiling point acid refers to one or a mixture of sulfuric acid and sulfuric acid; the organic amine comprises one or more of diethylamine, diethylenetriamine, triethylene tetramine and amino acid substances. Wherein, the amino acid substances comprise: glycine, aspartic acid, glutamic acid, cysteine, lysine, histidine and arginine.
Preparing a high-boiling-point acid and organic amine mixed impregnation liquid according to the volume of a solution required by equal volume impregnation according to the difference of saturated water absorption of the activated carbon, wherein the mass ratio of the high-boiling-point acid to the activated carbon is 0.1-1.0: 10; the mass ratio of the organic amine to the activated carbon is 0.1-1.0:10, and the impregnation time is generally 6-24 hours.
After the impregnation is finished, uniformly and flatly spreading the impregnated activated carbon at room temperature, naturally ventilating to volatilize part of water absorbed by the activated carbon, sampling and weighing until the water content in the material is 20-40% according to the room temperature, and thus obtaining the formaldehyde purification activated carbon.
Example 1
100 g of coal columnar activated carbon is weighed, in the technical scheme, no special requirement is generally made on activated carbon particles, as long as the activated carbon particles are not powdery, and the saturated water absorption of the activated carbon particles is 76 mass percent of the activated carbon particlesPercent; weighing 76 ml of deionized water in a beaker, weighing 5 g of sulfuric acid and 5 g of ethylene urea, and dissolving to prepare a dipping solution; mixing the impregnation liquid with the activated carbon, uniformly stirring, and standing for 12 h; spreading activated carbon on a screen, air drying, and indoor temperature 28oC, after air-drying for 6 hours, the mass of the activated carbon was 159 g, and the water content of the material at this time was 31%.
A sample without the addition of the high-boiling acid was prepared in the same manner, and the remaining preparation processes were the same. The following examples were also prepared under the same process conditions as those of the above examples without adding a high boiling acid.
Example 2
Weighing 100 g of coal columnar activated carbon, wherein the saturated water absorption of the coal columnar activated carbon is 76% of the mass of the coal columnar activated carbon; weighing 76 ml of deionized water in a beaker, weighing 3 g of phosphoric acid and 6 g of glycine, and dissolving to prepare a steeping fluid; mixing the impregnation liquid with the active carbon, uniformly stirring, and standing for 10 h; spreading activated carbon on a screen, naturally drying at an indoor temperature of 30 deg.CoC, after air-drying for 6 hours, the mass of the activated carbon was 145 g, and the water content of the material at this time was 25%.
Example 3
Weighing 100 g of coconut shell activated carbon, wherein the saturated water absorption rate of the coconut shell activated carbon is 70% of the mass of the coconut shell activated carbon; weighing 70 ml of deionized water in a beaker, weighing 3 g of phosphoric acid, 3 g of sulfuric acid and 8 g of diethylamine, and dissolving to prepare a dipping solution; mixing the impregnation liquid with the active carbon, uniformly stirring, and standing for 8 hours; spreading activated carbon on a screen, air drying, and indoor temperature 28oC, after air-drying for 6 hours, the mass of the activated carbon was 158 g, and the water content of the material at this time was 28%.
Example 4
Weighing 100 g of coconut shell activated carbon, wherein the saturated water absorption rate of the coconut shell activated carbon is 70% of the mass of the coconut shell activated carbon; weighing 70 ml of deionized water in a beaker, and weighing 8 g of sulfuric acid and 10 g of glutamic acid to dissolve to prepare a steeping fluid; mixing the impregnation liquid with the activated carbon, uniformly stirring, and standing for 24 hours; spreading activated carbon on a screen, naturally drying at an indoor temperature of 25 deg.CoC, after air-drying for 6 hours, the mass of the activated carbon was 176 g, and the water content of the material at this time was 33%.
Example 5
Weighing 100 g of coconut shellActivated carbon, the saturated water absorption of which is 70% of its mass; weighing 70 ml of deionized water in a beaker, weighing 7 g of sulfuric acid, 5 g of ethylene urea and 4 g of glycine, and dissolving to prepare a dipping solution; mixing the impregnation liquid with the activated carbon, uniformly stirring, and standing for 18 h; spreading the activated carbon on a screen, air drying naturally, and keeping the indoor temperature at 26 deg.CoC, after air-drying for 10 hours, the mass of the activated carbon was 145 g, and the water content of the material at this time was 20%.
In order to verify the feasibility of applying the formaldehyde purification activated carbon prepared by the invention to indoor air treatment, the air quantity is 15 m3The self-made small purifier for purifying formaldehyde is filled with about 50 g of activated carbon and placed at 1M3In the experiment cabin; dropwise adding formaldehyde into the experimental cabin to ensure that the formaldehyde in the cabin is balanced at 1.0 +/-0.2 mg/m for carrying out heavy planting (the initial concentration is 10 +/-2 times of the concentration limit specified in GB/T18883); and (3) starting a power switch of the purifier, starting the purifier to work, sampling and testing the concentration of the formaldehyde in the cabin after timing for 1 hour, and calculating the formaldehyde purification efficiency.
Figure DEST_PATH_IMAGE002
Note: the concentration of formaldehyde was measured using a chemical absorption method.
The formaldehyde purification activated carbon prepared by the invention has the following advantages: 1) the operation is simple and convenient, and the acid and alkali pretreatment of the activated carbon is not needed; 2) the method has no high-temperature operation flow, and the activated carbon is naturally dried at room temperature after being impregnated and loaded with high-boiling-point acid and organic amine; 3) the preparation cost of the formaldehyde purification activated carbon is greatly reduced; 4) the active carbon rapid adsorption-acidic environment reinforced formaldehyde-liquid membrane mass transfer-formaldehyde and organic amine liquid-liquid reaction technology is coupled, and the formaldehyde purification active carbon with higher activity is prepared
In addition to the above embodiments, the present invention may have other embodiments, and any technical solutions formed by equivalent substitutions or equivalent transformations are within the scope of the present invention as claimed.

Claims (10)

1. A preparation method of formaldehyde purification activated carbon with low cost and high activity is characterized in that: the method comprises the following steps:
s1: preparing an impregnation liquid containing high-boiling-point acid and organic amine;
s2: soaking the soaking solution obtained in the step S1 and activated carbon in equal volume to obtain soaked activated carbon;
s3: and (4) flatly laying the impregnated activated carbon obtained in the step S2, ventilating and air-drying to obtain the formaldehyde purification activated carbon.
2. The method for preparing the formaldehyde purification activated carbon with low cost and high activity as claimed in claim 1, wherein the method comprises the following steps: in the step S1, the high-boiling acid includes one or two of sulfuric acid and phosphoric acid.
3. The method for preparing the formaldehyde purification activated carbon with low cost and high activity as claimed in claim 1, wherein the method comprises the following steps: in the step S1, the organic amine includes one or more of ethylene urea, diethylamine, diethylenetriamine, triethylenetetramine and amino acids; wherein, the amino acid substances comprise: glycine, aspartic acid, glutamic acid, cysteine, lysine, histidine and arginine.
4. The method for preparing the formaldehyde purification activated carbon with low cost and high activity as claimed in claim 1, wherein the method comprises the following steps: in the step S2, the mass ratio of the high-boiling-point acid to the activated carbon is 0.1-1.0: 10; the mass ratio of the organic amine to the active carbon is 0.1-1.0:15, and the soaking time is 6-24 hours; in the step S2, the equal volume of the impregnation solution is calculated according to the saturated water absorption of the required activated carbon.
5. The method for preparing the formaldehyde purification activated carbon with low cost and high activity as claimed in claim 1, wherein the method comprises the following steps: in the step S3, the activated carbon is spread flatly, ventilated and air-dried, in order to uniformly spread the impregnated activated carbon at room temperature, natural ventilation is carried out to volatilize part of moisture absorbed by the activated carbon, the air-drying time is determined according to the temperature at room temperature, and sampling and weighing are carried out until the moisture content in the material is 20-40%, thus obtaining the formaldehyde purification activated carbon.
6. The method for preparing the formaldehyde purification activated carbon with low cost and high activity as claimed in claim 1, wherein the method comprises the following steps: weighing 100 g of coal columnar activated carbon, wherein the saturated water absorption of the coal columnar activated carbon is 76% of the mass of the coal columnar activated carbon; weighing 76 ml of deionized water in a beaker, weighing 5 g of sulfuric acid and 5 g of ethylene urea, and dissolving to prepare a dipping solution; mixing the impregnation liquid with the activated carbon, uniformly stirring, and standing for 12 h; the activated carbon was spread on a screen and air dried naturally at an indoor temperature of 28 ℃ for 6 hours, and the mass of the activated carbon was 159 g, at which time the water content of the material was 31%.
7. The method for preparing the formaldehyde purification activated carbon with low cost and high activity as claimed in claim 1, wherein the method comprises the following steps: weighing 100 g of coal columnar activated carbon, wherein the saturated water absorption of the coal columnar activated carbon is 76% of the mass of the coal columnar activated carbon; weighing 76 ml of deionized water in a beaker, weighing 3 g of phosphoric acid and 6 g of glycine, and dissolving to prepare a steeping fluid; mixing the impregnation liquid with the active carbon, uniformly stirring, and standing for 10 h; the activated carbon is laid on a screen mesh and naturally dried at the indoor temperature of 30 ℃ for 6 hours, and the weight of the activated carbon is 145 g, and the water content of the material is 25%.
8. The method for preparing the formaldehyde purification activated carbon with low cost and high activity as claimed in claim 1, wherein the method comprises the following steps: weighing 100 g of coconut shell activated carbon, wherein the saturated water absorption rate of the coconut shell activated carbon is 70% of the mass of the coconut shell activated carbon; weighing 70 ml of deionized water in a beaker, weighing 3 g of phosphoric acid, 3 g of sulfuric acid and 8 g of diethylamine, and dissolving to prepare a dipping solution; mixing the impregnation liquid with the active carbon, uniformly stirring, and standing for 8 hours; the activated carbon was spread on a screen and air dried naturally at an indoor temperature of 28 ℃ for 6 hours, and the mass of the activated carbon was 158 g, at which time the water content of the material was 28%.
9. The method for preparing the formaldehyde purification activated carbon with low cost and high activity as claimed in claim 1, wherein the method comprises the following steps: weighing 100 g of coconut shell activated carbon, wherein the saturated water absorption rate of the coconut shell activated carbon is 70% of the mass of the coconut shell activated carbon; weighing 70 ml of deionized water in a beaker, and weighing 8 g of sulfuric acid and 10 g of glutamic acid to dissolve to prepare a steeping fluid; mixing the impregnation liquid with the activated carbon, uniformly stirring, and standing for 24 hours; the activated carbon was spread on a screen and air dried naturally at 25 ℃ in room temperature for 6 hours, and the mass of the activated carbon was 176 g, at which time the water content of the material was 33%.
10. The method for preparing the formaldehyde purification activated carbon with low cost and high activity as claimed in claim 1, wherein the method comprises the following steps: weighing 100 g of coconut shell activated carbon, wherein the saturated water absorption rate of the coconut shell activated carbon is 70% of the mass of the coconut shell activated carbon; weighing 70 ml of deionized water in a beaker, weighing 7 g of sulfuric acid, 5 g of ethylene urea and 4 g of glycine, and dissolving to prepare a dipping solution; mixing the impregnation liquid with the activated carbon, uniformly stirring, and standing for 18 h; the activated carbon is laid on a screen mesh and naturally dried at the indoor temperature of 26 ℃ for 10 hours, and the weight of the activated carbon is 145 g, and the water content of the material is 20%.
CN202110670185.7A 2021-06-17 2021-06-17 Preparation method of formaldehyde purification activated carbon with low cost and high activity Active CN113304727B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202110670185.7A CN113304727B (en) 2021-06-17 2021-06-17 Preparation method of formaldehyde purification activated carbon with low cost and high activity

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202110670185.7A CN113304727B (en) 2021-06-17 2021-06-17 Preparation method of formaldehyde purification activated carbon with low cost and high activity

Publications (2)

Publication Number Publication Date
CN113304727A true CN113304727A (en) 2021-08-27
CN113304727B CN113304727B (en) 2023-09-15

Family

ID=77379196

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202110670185.7A Active CN113304727B (en) 2021-06-17 2021-06-17 Preparation method of formaldehyde purification activated carbon with low cost and high activity

Country Status (1)

Country Link
CN (1) CN113304727B (en)

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0252043A (en) * 1988-03-31 1990-02-21 Matsushita Electric Ind Co Ltd Air purifying agent
CN101306345A (en) * 2008-06-06 2008-11-19 烟台宝源净化有限公司 Impregnated activated carbon and its preparation method
CN101468305A (en) * 2007-12-29 2009-07-01 中国船舶重工集团公司第七一八研究所 Methyl aldehyde adsorbing substance and preparation method thereof
US20160263549A1 (en) * 2015-03-12 2016-09-15 Marmon Water (Singapore) Pte. Ltd. Surface Modified Carbon for Filtration Applications and Process for Making the Same
CN107854981A (en) * 2017-11-08 2018-03-30 山西新华化工有限责任公司 Purifying formaldehyde material and preparation method thereof
CN107930666A (en) * 2017-11-10 2018-04-20 山东格蓝云天环境科技有限公司 Nano cerium Mn oxide/absorbent charcoal composite material of Oxidation at room temperature formaldehyde and preparation method thereof
CN107983152A (en) * 2017-12-14 2018-05-04 天津市联合环保工程设计有限公司 A kind of purifying ball to eliminate the unusual smell except aldehyde and preparation method and application
CN108295816A (en) * 2018-01-19 2018-07-20 深圳中纺滤材科技有限公司 A kind of normal-temperature efficient is except modified formaldehyde charcoal and preparation method thereof
JP2019051508A (en) * 2017-09-15 2019-04-04 フタムラ化学株式会社 Aldehyde adsorbent and filter body using the same

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0252043A (en) * 1988-03-31 1990-02-21 Matsushita Electric Ind Co Ltd Air purifying agent
CN101468305A (en) * 2007-12-29 2009-07-01 中国船舶重工集团公司第七一八研究所 Methyl aldehyde adsorbing substance and preparation method thereof
CN101306345A (en) * 2008-06-06 2008-11-19 烟台宝源净化有限公司 Impregnated activated carbon and its preparation method
US20160263549A1 (en) * 2015-03-12 2016-09-15 Marmon Water (Singapore) Pte. Ltd. Surface Modified Carbon for Filtration Applications and Process for Making the Same
JP2019051508A (en) * 2017-09-15 2019-04-04 フタムラ化学株式会社 Aldehyde adsorbent and filter body using the same
CN107854981A (en) * 2017-11-08 2018-03-30 山西新华化工有限责任公司 Purifying formaldehyde material and preparation method thereof
CN107930666A (en) * 2017-11-10 2018-04-20 山东格蓝云天环境科技有限公司 Nano cerium Mn oxide/absorbent charcoal composite material of Oxidation at room temperature formaldehyde and preparation method thereof
CN107983152A (en) * 2017-12-14 2018-05-04 天津市联合环保工程设计有限公司 A kind of purifying ball to eliminate the unusual smell except aldehyde and preparation method and application
CN108295816A (en) * 2018-01-19 2018-07-20 深圳中纺滤材科技有限公司 A kind of normal-temperature efficient is except modified formaldehyde charcoal and preparation method thereof

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
郑希;: "氨基酸型甲醛吸附材料制备及净化效果研究" *

Also Published As

Publication number Publication date
CN113304727B (en) 2023-09-15

Similar Documents

Publication Publication Date Title
CN104324692B (en) A kind of preparation method of the activated carbon that can eliminate formaldehyde
CN107362788A (en) A kind of graphene oxide/titanium dioxide activated carbon three-dimensional composite material and preparation method thereof
CN112156752B (en) Modified activated carbon with reproducible adsorbability and application thereof in wastewater treatment
CN111167402B (en) Zinc-cobalt Prussian blue analogue adsorbent with hollow structure and preparation method and application thereof
CN108295816A (en) A kind of normal-temperature efficient is except modified formaldehyde charcoal and preparation method thereof
CN110841606A (en) Composite material for capturing carbon dioxide and preparation method and application thereof
CN109954384A (en) The purifying formaldehyde material and preparation method thereof of amino acid is loaded on porous adsorption carrier
CN110734049A (en) method for preparing nitrogen-doped carbon material with high specific surface area by using potassium phthalimide
CN102500324A (en) Organic-inorganic composite carbon dioxide adsorbing material and preparation method thereof
CN111203182A (en) Modified activated carbon for adsorbing phenol and preparation method and application thereof
CN113648970A (en) Green preparation method of ammonia/chromium-free impregnated activated carbon adsorbent for preventing HCN/CNCl
CN113813927B (en) Foam carbon-based solid amine adsorbent and preparation method and application thereof
CN104353425B (en) A kind of flyash of energy formaldehyde adsorption and preparation method thereof
CN110841595A (en) Preparation method and application of nitrogen-doped graphitized carbon material
CN107961757B (en) A kind of high activity composite calcium-base CO2Absorbent and preparation method thereof
CN106140175A (en) A kind of be catalyzed burning fluorine-containing, the preparation method of chlorine VOCs catalyst
CN113304727A (en) Preparation method of formaldehyde purification activated carbon with low cost and high activity
CN108246328A (en) A kind of three-dimensional carbonitride porous material of paramorph and its preparation method and application
CN108455624B (en) Method for preparing silver-loaded hydrogen sulfide poisoning-resistant 4A molecular sieve by using attapulgite as raw material
CN114272925B (en) Coal gangue-based catalytic material and preparation method and application thereof
CN109575717B (en) Indoor coating capable of efficiently decomposing formaldehyde and toluene and preparation method thereof
CN114768479A (en) Eutectic solvent for efficiently absorbing carbon dioxide gas and preparation method and application thereof
CN110170306B (en) Process for preparing adsorbent for efficiently removing low-concentration formaldehyde in air at normal temperature by two-step modification method, product and application thereof
RU2692344C1 (en) Sorbent for purifying water from toxic organophosphorus compounds, cyanides and arsenous compounds and method for production thereof
Chen et al. Silver catalysts supported over activated carbons for the selective oxidation of CO in excess hydrogen: effects of different treatments on the supports

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant