CN106215886A - Based on diatomite modified for compositions purifying grain-drying tail gas and its preparation method and application - Google Patents

Based on diatomite modified for compositions purifying grain-drying tail gas and its preparation method and application Download PDF

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CN106215886A
CN106215886A CN201610584032.XA CN201610584032A CN106215886A CN 106215886 A CN106215886 A CN 106215886A CN 201610584032 A CN201610584032 A CN 201610584032A CN 106215886 A CN106215886 A CN 106215886A
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powder
preparation
tail gas
consumption
compositions
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CN106215886B (en
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萧鲲
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Wuhu Chang Qilu Industry Co Ltd
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    • 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
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26Synthetic macromolecular compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/30Particle separators, e.g. dust precipitators, using loose filtering material
    • 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
    • B01D53/02Separation 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 by adsorption, e.g. preparative gas chromatography
    • 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
    • B01J20/10Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/12Naturally occurring clays or bleaching earth
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/50Carbon oxides
    • B01D2257/502Carbon monoxide

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Inorganic Chemistry (AREA)
  • Cosmetics (AREA)
  • Detergent Compositions (AREA)

Abstract

The invention discloses a kind of compositions for purifying grain-drying tail gas based on diatomite modified and its preparation method and application, this preparation method includes: 1) in the presence of protection gas, carry out bentonite calcining with prepared bentonite powder;2) active carbon powder, wheat bran powder, flyash and bentonite powder are placed in acid solution and carry out activation processing with prepared activator mixture;3) MDI, TDI, polyether polyol, kieselguhr, butyl titanate are carried out haptoreaction with prepared Foamex with activator mixture in the presence of ultrasound wave;4) Foamex is pulverized to obtain Foamex powder, then mix anion surfactant, water with Foamex powder to prepare the compositions being used for purifying grain-drying tail gas based on diatomite modified.The compositions prepared by the method has excellent detergent power for purifying grain-drying tail gas, and this preparation method is simple to operate simultaneously, and raw material is easy to get.

Description

Compositions and the system thereof for purifying grain-drying tail gas based on diatomite modified Preparation Method and application
Technical field
The present invention relates to purify the compositions of grain-drying tail gas, in particular it relates to a kind of based on diatomite modified For purifying compositions of grain-drying tail gas and its preparation method and application.
Background technology
Grain drying machine is the assembly of a kind of dehydrator.It it is the general designation of the various equipment of foodstuff drying device.By corn and air-flow Direction of relative movement, dehydrator can be divided into the patterns such as crossing current, mixed flow, following current, adverse current and concurrent-countercurrent, mixed adverse current, suitable mixed flow.Corn The operation principle of dehydrator is: first pass through heater and air is heated into hot-air, be then passed through in corn by hot-air So that corn is heated.
After heat grain completes, the tail gas after hot-air cooling is breathed containing substantial amounts of dust granules and corn and produces Waste gas.At present, the processing mode of grain-drying tail gas is: entered by tail gas in the pipeline of a root length so that in tail gas Dust granules can settle down in the duct, is then directly discharged in air by tail gas.This vent gas treatment mode is not only Needing bigger space and equipment, the effect of the process of tail gas is not very good simultaneously, on the one hand, dust granules has been difficult to All clear Chu, on the other hand, corn is breathed the waste gas (carbon monoxide that mainly corn anaerobic respiration produces) produced and is not obtained Solve.
Summary of the invention
It is an object of the invention to provide a kind of compositions for purifying grain-drying tail gas based on diatomite modified And its preparation method and application, the compositions prepared by the method has excellent purification for purifying grain-drying tail gas Ability, this preparation method is simple to operate simultaneously, and raw material is easy to get.
To achieve these goals, the invention provides a kind of based on diatomite modified for purifying grain-drying tail The preparation method of the compositions of gas, this preparation method includes:
1) in the presence of protection gas, carry out bentonite calcining with prepared bentonite powder;
2) active carbon powder, wheat bran powder, flyash and bentonite powder are placed in acid solution and carry out activation processing with system Obtain activator mixture;
3) by MDI (4,4 ,-methyl diphenylene diisocyanate), TDI (toluene di-isocyanate(TDI)), polyether polyol, silicon Diatomaceous earth, butyl titanate, kieselguhr and activator mixture carry out haptoreaction with prepared Foamex in the presence of ultrasound wave;
4) Foamex is pulverized to obtain Foamex powder, then by anion surfactant, water and foaming tree The mixing of cosmetics end is to prepare the compositions for purifying grain-drying tail gas based on diatomite modified.
Present invention also offers a kind of compositions for purifying grain-drying tail gas based on diatomite modified, this group Compound is prepared by above-mentioned method.
Invention further provides a kind of above-mentioned based on diatomite modified for purifying grain-drying tail gas Compositions application in purifying grain-drying tail gas.
By technique scheme, the present invention by the synergism of each raw material and each step make to prepare based on diatom The compositions for purifying grain-drying tail gas of land reform is for having the clean of excellence for purification grain-drying tail gas Change ability, can not only remove the dust granules in tail gas, and the waste gas simultaneously produced corn breathing (exhale by mainly corn anaerobic Inhale the carbon monoxide produced) there is excellent absorbability.Additionally, the preparation method that provides of the present invention to have step simple, former The advantage that material is easy to get, is easy to popularization.
Other features and advantages of the present invention will be described in detail in detailed description of the invention part subsequently.
Detailed description of the invention
Hereinafter the detailed description of the invention of the present invention is described in detail.It should be appreciated that described herein specifically Embodiment is merely to illustrate and explains the present invention, is not limited to the present invention.
The invention provides the preparation of a kind of compositions for purifying grain-drying tail gas based on diatomite modified Method, this preparation method includes:
1) in the presence of protection gas, carry out bentonite calcining with prepared bentonite powder;
2) active carbon powder, wheat bran powder, flyash and bentonite powder are placed in acid solution and carry out activation processing with system Obtain activator mixture;
3) by MDI (4,4 ,-methyl diphenylene diisocyanate), TDI (toluene di-isocyanate(TDI)), polyether polyol, silicon Diatomaceous earth, butyl titanate and activator mixture carry out haptoreaction with prepared Foamex in the presence of ultrasound wave;
4) Foamex is pulverized to obtain Foamex powder, then by anion surfactant, water and foaming tree The mixing of cosmetics end is to prepare the compositions for purifying grain-drying tail gas based on diatomite modified.
Step 1 in above-mentioned preparation method) in, the actual conditions of calcining can select in wide scope, but in order to Make the compositions prepared that the tail gas purifying grain drying machine is had more excellent detergent power, it is preferable that in step 1) in, Calcining at least meets following condition: calcining heat is 420-450 DEG C, and calcination time is 4-6h.
Step 1 in above-mentioned preparation method) in, the concrete kind of protection gas can select in wide scope, but from Consider on protected effect, it is preferable that one or more in nitrogen, helium, neon and argon of protection gas.
Step 2 in above-mentioned preparation method) in, the consumption of each material can select in wide scope, but in order to make The compositions that must prepare has more excellent detergent power to the tail gas purifying grain drying machine, it is preferable that in step 2) in, phase For the active carbon powder of 100 weight portions, the consumption of wheat bran powder is 20-26 weight portion, and the consumption of flyash is 12-17 weight Part, the consumption of bentonite powder is 35-52 weight portion.
Step 2 in above-mentioned preparation method) in, the consumption of acid solution can select in wide scope, but so that The compositions prepared has more excellent detergent power to the tail gas purifying grain drying machine, it is preferable that in step 2) in, relatively In the active carbon powder of 100 weight portions, the consumption of acid solution is 300-500 weight portion, and the pH of acid solution is 3.5-5.
Step 2 in above-mentioned preparation method) in, active carbon powder, wheat bran powder, flyash and the particle diameter of bentonite powder Can select in wide scope, but so that the tail gas purifying grain drying machine is had more excellent by the compositions prepared Detergent power, it is preferable that in step 2) in, active carbon powder, wheat bran powder, flyash are with the particle diameter of bentonite powder Less than 10 microns.
Step 2 in above-mentioned preparation method) in, the actual conditions of activation processing can select in wide scope, but So that the compositions prepared has more excellent detergent power to the tail gas purifying grain drying machine, it is preferable that in step 2) in, activation processing at least meets following condition: activation temperature is 45-50 DEG C, and soak time is 1-1.5h.
Step 3 in above-mentioned preparation method) in, the consumption of each material can select in wide scope, but in order to make The compositions that must prepare has more excellent detergent power to the tail gas purifying grain drying machine, it is preferable that in step 3) in, phase For the MDI of 100 weight portions, the consumption of TDI is 15-24 weight portion, and the consumption of polyether polyol is 110-130 weight portion, silicon The consumption of diatomaceous earth is 34-42 weight portion, and the consumption of butyl titanate is 3-5 weight portion, and the consumption of activator mixture is 33-40 weight Amount part.
Step 3 in above-mentioned preparation method) in, catalytic actual conditions can select in wide scope, but So that the compositions prepared has more excellent detergent power to the tail gas purifying grain drying machine, it is preferable that in step 3) in, haptoreaction at least meets following condition: reaction temperature is 60-85 DEG C, and the response time is 6-10h, the frequency of ultrasound wave For 20-30MHz.
Step 3 in above-mentioned preparation method) in, the concrete kind of polyether polyol can select in wide scope, but It is so that the compositions prepared has more excellent detergent power to the tail gas purifying grain drying machine, it is preferable that in step Rapid 3) in, one or more in the polyether polyol of trade mark L61, trade mark L64 and trade mark F68 of polyether polyol.
Step 4 in above-mentioned preparation method) in, the consumption of each material can select in wide scope, but in order to make The compositions that must prepare has more excellent detergent power to the tail gas purifying grain drying machine, it is preferable that in step 4) in, phase For the Foamex powder of 100 weight portions, the consumption of anion surfactant is 3-5 weight portion, and the consumption of water is 30-50 Weight portion.
Step 4 in above-mentioned preparation method) in, the particle diameter of Foamex powder can select in wide scope, but So that the compositions prepared has more excellent detergent power to the tail gas purifying grain drying machine, it is preferable that in step 4), in, the particle diameter of Foamex powder is less than 10 microns.
Step 4 in above-mentioned preparation method) in, the concrete kind of anion surfactant can be selected in wide scope Select, but so that the compositions prepared has more excellent detergent power to the tail gas purifying grain drying machine, it is preferable that In step 4) in, anion surfactant selected from sodium lauryl sulphate, dodecylbenzene sodium sulfonate, sodium laurylsulfate and One or more in dodecyl sodium naphthalene sulfonate.
Present invention also offers a kind of compositions for purifying grain-drying tail gas based on diatomite modified, this group Compound is prepared by above-mentioned method.
Invention further provides a kind of above-mentioned based on diatomite modified for purifying grain-drying tail gas Compositions application in purifying grain-drying tail gas.
Hereinafter will be described the present invention by embodiment.
Embodiment 1
1) in the presence of protection gas (nitrogen), carry out bentonite at 430 DEG C calcining 5h with prepared bentonite powder (below particle diameter 10 μm);
2) by active carbon powder (below particle diameter 10 μm), wheat bran powder (below particle diameter 10 μm), flyash (particle diameter 10 μm with Under), bentonite powder mixes according to the weight ratio of 100:24:15:42:400 with acid solution (pH is 4), and lives at 48 DEG C Change processes 1.2h with prepared activator mixture;
3) by MDI, TDI, polyether polyol (trade mark L61), kieselguhr, butyl titanate and activator mixture are according to 100: The weight ratio of 18:120:40:4:37 carries out haptoreaction 8h with system in the presence of the ultrasound wave that frequency is 25MHz and at 75 DEG C Obtain Foamex;
4) Foamex is pulverized to obtain Foamex powder (less than 10 microns), then by anion surfactant (sodium lauryl sulphate), water mix to prepare based on diatomite modified with Foamex powder according to 100:4:40 weight ratio For purifying compositions A1 of grain-drying tail gas.
Embodiment 2
1) in the presence of protection gas (neon), carry out bentonite at 420 DEG C calcining 4h with prepared bentonite powder (below particle diameter 10 μm);
2) by active carbon powder (below particle diameter 10 μm), wheat bran powder (below particle diameter 10 μm), flyash (particle diameter 10 μm with Under), bentonite powder mixes according to the weight ratio of 100:20:12:35:300 with acid solution (pH is 3.5), and carries out at 45 DEG C Activation processing 1h is with prepared activator mixture;
3) by MDI, TDI, polyether polyol (trade mark L64), kieselguhr, butyl titanate and activator mixture according to 100: The weight ratio of 15:110:34:3:33 carries out haptoreaction 6h with system in the presence of the ultrasound wave that frequency is 20MHz and at 60 DEG C Obtain Foamex;
4) Foamex is pulverized to obtain Foamex powder (less than 10 microns), then by anion surfactant (sodium laurylsulfate), water mix to prepare use based on diatomite modified according to 100:3:30 weight ratio with Foamex powder In compositions A2 purifying grain-drying tail gas.
Embodiment 3
1) in the presence of protection gas (argon), carry out bentonite at 450 DEG C calcining 6h with prepared bentonite powder (below particle diameter 10 μm);
2) by active carbon powder (below particle diameter 10 μm), wheat bran powder (below particle diameter 10 μm), flyash (particle diameter 10 μm with Under), bentonite powder mixes according to the weight ratio of 100:26:17:52:500 with acid solution (pH is 5), and lives at 50 DEG C Change processes 1.5h with prepared activator mixture;
3) by MDI, TDI, polyether polyol (trade mark F68), kieselguhr, butyl titanate and activator mixture according to 100: The weight ratio of 24:130:42:5:40 carry out in the presence of the ultrasound wave that frequency is 30MHz and at 85 DEG C haptoreaction 10h with Prepare Foamex;
4) Foamex is pulverized to obtain Foamex powder (less than 10 microns), then by anion surfactant (dodecyl sodium naphthalene sulfonate), water mix to prepare based on diatomite modified according to 100:5:50 weight ratio with Foamex powder For purifying compositions A3 of grain-drying tail gas.
Comparative example 1
Carry out preparing compositions B1, except for the difference that, step 3 according to the method for embodiment 1) in do not use activator mixture.
Comparative example 2
Carry out preparing compositions B2, except for the difference that, step 3 according to the method for embodiment 1) in do not use butyl titanate.
Comparative example 3
Carry out preparing compositions B3, except for the difference that, step 3 according to the method for embodiment 1) in do not use kieselguhr.
Comparative example 4
Carry out preparing compositions B4, except for the difference that, step 4 according to the method for embodiment 1) in do not use anionic surface to live Property agent.
Detection example 1
Detection purifies PM10.0 in grain-drying tail gas, and (particle diameter is less than or equal to the concentration of the dust granules of 10.0 μm, μ g/m3) and concentration (the μ g/m of CO3);Above-mentioned composition is filled in respectively composition filter in double-layer filtering net, then by tail Edema caused by disorder of QI not Tong Guo filter, then detect the concentration of PM10.0 and CO in the tail gas after purified treatment.
Table 1
By above-described embodiment, comparative example and detection example, what the present invention provided is used for purifying grain-drying tail The compositions of gas has the detergent power of excellence for purifying grain-drying tail gas.
The preferred embodiment of the present invention described in detail above, but, the present invention is not limited in above-mentioned embodiment Detail, in the technology concept of the present invention, technical scheme can be carried out multiple simple variant, this A little simple variant belong to protection scope of the present invention.
It is further to note that each the concrete technical characteristic described in above-mentioned detailed description of the invention, at not lance In the case of shield, can be combined by any suitable means, in order to avoid unnecessary repetition, the present invention to various can The compound mode of energy illustrates the most separately.
Additionally, combination in any can also be carried out between the various different embodiment of the present invention, as long as it is without prejudice to this The thought of invention, it should be considered as content disclosed in this invention equally.

Claims (10)

1. a preparation method for the compositions for purifying grain-drying tail gas based on diatomite modified, its feature exists In, described preparation method includes:
1) in the presence of protection gas, carry out bentonite calcining with prepared bentonite powder;
2) active carbon powder, wheat bran powder, flyash and described bentonite powder are placed in acid solution and carry out activation processing with system Obtain activator mixture;
3) by MDI (4,4 ,-methyl diphenylene diisocyanate), TDI (toluene di-isocyanate(TDI)), polyether polyol, kieselguhr, Butyl titanate and described activator mixture carry out haptoreaction with prepared Foamex in the presence of ultrasound wave;
4) described Foamex is pulverized to obtain Foamex powder, then by anion surfactant, water and described Bubble toner mixing is to prepare the described compositions for purifying grain-drying tail gas based on diatomite modified.
Preparation method the most according to claim 1, wherein, in step 1) in, described calcining at least meets following condition: forge Burning temperature and be 420-450 DEG C, calcination time is 4-6h;
Preferably, one or more in nitrogen, helium, neon and argon of described protection gas.
Preparation method the most according to claim 1, wherein, in step 2) in, relative to the described activated carbon of 100 weight portions Powder, the consumption of described wheat bran powder is 20-26 weight portion, and the consumption of described flyash is 12-17 weight portion, described bentonite The consumption of powder is 35-52 weight portion;
Preferably, in step 2) in, relative to the described active carbon powder of 100 weight portions, the consumption of described acid solution is 300-500 Weight portion, and the pH of described acid solution is 3.5-5.
Preparation method the most according to claim 3, wherein, in step 2) in, described active carbon powder, wheat bran powder, powder Coal ash is less than 10 microns with the particle diameter of described bentonite powder;
Preferably, in step 2) in, described activation processing at least meets following condition: activation temperature is 45-50 DEG C, soak time For 1-1.5h.
5. according to the preparation method described in claim 3 or 4, wherein, in step 3) in, described in 100 weight portions MDI, the consumption of described TDI is 15-24 weight portion, and the consumption of described polyether polyol is 110-130 weight portion, described kieselguhr Consumption be 34-42 weight portion, the consumption of described butyl titanate is 3-5 weight portion, and the consumption of described activator mixture is 33- 40 weight portions.
Preparation method the most according to claim 5, wherein, in step 3) in, described haptoreaction at least meets following bar Part: reaction temperature is 60-85 DEG C, the response time is 6-10h, and the frequency of ultrasound wave is 20-30MHz;
Preferably, in step 3) in, described polyether polyol is selected from trade mark L61, trade mark L64 and the polyether polyol of trade mark F68 In one or more.
Preparation method the most according to claim 6, wherein, in step 4) in, relative to the described foaming tree of 100 weight portions Cosmetics end, the consumption of described anion surfactant is 3-5 weight portion, and the consumption of described water is 30-50 weight portion.
Preparation method the most according to claim 7, wherein, in step 4) in, the particle diameter of described Foamex powder is 10 Below Wei meter;
Preferably, in step 4) in, described anion surfactant is selected from sodium lauryl sulphate, DBSA One or more in sodium, sodium laurylsulfate and dodecyl sodium naphthalene sulfonate.
9. the compositions for purifying grain-drying tail gas based on diatomite modified, it is characterised in that described combination Thing is prepared by the method described in any one in claim 1-8.
10. the compositions for purifying grain-drying tail gas based on diatomite modified exists Purify the application in grain-drying tail gas.
CN201610584032.XA 2016-07-23 2016-07-23 The composition and its preparation method and application for purifying grain-drying tail gas based on diatomite modified Active CN106215886B (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107433185A (en) * 2017-09-05 2017-12-05 霍邱金木鱼农业科技有限公司 A kind of material for air purification and preparation method thereof
CN107537451A (en) * 2017-09-05 2018-01-05 霍邱金木鱼农业科技有限公司 A kind of porous zeolite material for air purification and preparation method thereof

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4039290A (en) * 1972-05-15 1977-08-02 Kureha Kagaku Kogyo Kabushiki Kaisha Spent activated carbon regenerator
JPS577545B2 (en) * 1977-12-12 1982-02-10
CN1074630A (en) * 1992-01-24 1993-07-28 北京大学 Burning catalyst for composite oxide and method for making thereof and application
CN102631903A (en) * 2012-05-08 2012-08-15 福建农林大学 In-situ preparation method of activated carbon loaded with ionic liquid

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4039290A (en) * 1972-05-15 1977-08-02 Kureha Kagaku Kogyo Kabushiki Kaisha Spent activated carbon regenerator
JPS577545B2 (en) * 1977-12-12 1982-02-10
CN1074630A (en) * 1992-01-24 1993-07-28 北京大学 Burning catalyst for composite oxide and method for making thereof and application
CN102631903A (en) * 2012-05-08 2012-08-15 福建农林大学 In-situ preparation method of activated carbon loaded with ionic liquid

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
MOHAMMAD SALEH SHAFEEYAN: "A review on surface modification of activated carbon for carbon dioxide adsorption", 《JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS》 *
何冬萍: "不同前处理方法对活性炭吸附一氧化碳的影响", 《四川环境》 *

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107433185A (en) * 2017-09-05 2017-12-05 霍邱金木鱼农业科技有限公司 A kind of material for air purification and preparation method thereof
CN107537451A (en) * 2017-09-05 2018-01-05 霍邱金木鱼农业科技有限公司 A kind of porous zeolite material for air purification and preparation method thereof
CN107537451B (en) * 2017-09-05 2019-12-13 国投盛世承德科技股份有限公司 porous zeolite air purification material and preparation method thereof
CN107433185B (en) * 2017-09-05 2020-04-28 王武成 Air purification material and preparation method thereof

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