CN107158799B - A kind of composite filtering material fiber and preparation method for SCR dedusting denitration - Google Patents

A kind of composite filtering material fiber and preparation method for SCR dedusting denitration Download PDF

Info

Publication number
CN107158799B
CN107158799B CN201710486860.4A CN201710486860A CN107158799B CN 107158799 B CN107158799 B CN 107158799B CN 201710486860 A CN201710486860 A CN 201710486860A CN 107158799 B CN107158799 B CN 107158799B
Authority
CN
China
Prior art keywords
fiber
preparation
filtering material
composite filtering
scr
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.)
Active
Application number
CN201710486860.4A
Other languages
Chinese (zh)
Other versions
CN107158799A (en
Inventor
王栋
韩奎华
彭悦
路春美
张亢
李兵
王羽
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.)
Shandong University
Original Assignee
Shandong University
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 Shandong University filed Critical Shandong University
Priority to CN201710486860.4A priority Critical patent/CN107158799B/en
Publication of CN107158799A publication Critical patent/CN107158799A/en
Priority to PCT/CN2017/106879 priority patent/WO2018233159A1/en
Application granted granted Critical
Publication of CN107158799B publication Critical patent/CN107158799B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/14Other self-supporting filtering material ; Other filtering material
    • 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
    • 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
    • B01D53/86Catalytic processes
    • B01D53/8621Removing nitrogen compounds
    • B01D53/8625Nitrogen oxides
    • B01D53/8628Processes characterised by a specific catalyst
    • 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
    • B01D53/86Catalytic processes
    • B01D53/90Injecting reactants
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/26Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
    • B01J31/38Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24 of titanium, zirconium or hafnium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/50Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
    • B01J35/58Fabrics or filaments
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2255/00Catalysts
    • B01D2255/40Mixed oxides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2258/00Sources of waste gases
    • B01D2258/02Other waste gases
    • B01D2258/0283Flue gases

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Environmental & Geological Engineering (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Inorganic Chemistry (AREA)
  • Catalysts (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Abstract

The invention discloses a kind of preparation methods of composite filtering material fiber for SCR dedusting denitration, by manganese salt, cerium salt and zirconates, which are dissolved in the water, prepares salting liquid A, prepare the alkaline solution B that pH is 8~12, fiber is immersed to salting liquid A and is infiltrated, ultrasonic wave added infiltration a period of time is carried out in impregnation process, 15~70min of dipper precipitation in alkaline solution B is immersed after fiber after infiltration is drained, aging is carried out after fiber after dipper precipitation is taken out, fiber after aging is subjected to microwave combustion method, it finally carries out being activated up to the composite filtering material fiber of SCR dedusting denitration is used for.It can make the oxide and fiber secure bond of Mn, Ce, Zr, and it is more uniform so that reactive metal oxides is dispersed in the fibre, NO in removing coal-fired flue-gas while can realizing trap particulate matter by the difunctional composite filtering material that the fiber is made intox

Description

A kind of composite filtering material fiber and preparation method for SCR dedusting denitration
Technical field
The present invention relates to after the pollutant dust of the building material industries such as coal-burning power plant and cement, glass, ceramics, nitrogen oxides A kind of reason field, and in particular to composite filtering material fiber and preparation method for SCR dedusting denitration.
Background technique
Nitrogen oxides can jeopardize human health while causing ecological environment destruction, be it is a kind of endanger it is extremely wide big Gas pollutant.Wherein the coal-burning boiler of the industries such as electric power, building materials is the important sources of discharged nitrous oxides.Selective catalytic reduction Method (Selective Catalytic Reduction, SCR) is coal-burning boiler denitration technology most widely used, that technology is most mature, Have denitration efficiency height, stable and reliable operation, selectivity it is good many advantages, such as, in practical applications occupation rate reach 90% with On.NH3To apply reducing agent the most universal in current SCR technology, the technical characterstic of SCR determines that denitration device outlet will not It is evitable that there are not sufficiently reactive NH3, i.e. the escaping of ammonia.If there are oxysulfide, the NH of escape in flue gas3Easily in tail portion cigarette Road, which reacts with it, generates the stronger ammonium sulfate/ammonium hydrogen sulfate of cohesiveness, so that back-end ductwork burn into be caused to block.As can under SCR catalytic denitration material is coupled again in trip equipment (sack cleaner), realizes escape NH in suitable temperature window3With not also Former NOxFurther reaction, then be expected to be effectively treated escape NH3While, further increase system denitration efficiency.
Field is post-processed in coal-fired flue-gas, and high dust collection efficiency, secondary pollution be small, siccative easily returns due to having for sack cleaner The performances such as receipts, application at home and abroad is more and more wider, accounts for about cleaner is applied in market 80%.Sack cleaner filters dedusting Expect that the demand of fiber is huge, especially multifunctional composite fiber has a vast market foreground.China is to every profession and trade coal-burning boiler Discharge proposes requirements at the higher level, and the industries coal-burning boiler such as steel, cement, glass, ceramics is the main source of atmosphere pollution, is also Emphasis is administered, China's steel annual output is more than 900,000,000 tons, prepares standard according to Baosteel sack cleaner and calculates, total that dedusting is needed to filter Expect 63,000,000 square metres, need to change 18,000,000 square metres of filtrate every year, therefore, dedusting filter media fibre market prospects are especially seen It is good.Sack cleaner is arranged in after SCR device more, and according to boiler type and application field difference, running temperature window is normal It is approximate with common low-temperature SCR technical application window between 150~250 DEG C, as can realizing that low-temperature SCR is catalyzed material here The efficient coupling of material and dedusting filter media fibre, will effectively solve the problems, such as above-mentioned the escaping of ammonia and greatly improves system denitration efficiency.
In recent years, the correlative study that the oxide of Mn, Ce, Zr etc. are used as low-temperature SCR catalyst active specy has obtained state The extensive concern of inside and outside scholar, but the selection of relevant carriers is mostly with TiO2、Al2O3, based on the solid materials such as active carbon.Do not have Mn, The relevant report of the coupling of the oxide and dedusting filter media fibre of Ce, Zr etc..
Summary of the invention
Active oxidation species are all made of in patent CN104941319A, CN103252135A, CN105315000A directly to soak Stain carrying method prepares composite filtering material, however the present inventor will using above-mentioned direct impregnation method by research discovery The oxide of Mn, Ce, Zr etc. couple with fiber the fiber filtering of preparation, and active component is insecure with fibres bond, hold Easy powder of detached, industrial production difficulty are larger.
In order to solve the deficiencies in the prior art, an object of the present invention is to provide a kind of answering for SCR dedusting denitration The preparation method for closing filter media fibre, can make the oxide and fiber secure bond of Mn, Ce, Zr, be made by the fiber double NO in removing coal-fired flue-gas while function and service filtrate can realize trap particulate matterx
To achieve the goals above, the technical solution of the present invention is as follows:
A kind of preparation method of the composite filtering material fiber for SCR dedusting denitration, is dissolved in water for manganese salt, cerium salt and zirconates In prepare salting liquid A, prepare pH be 8~12 alkaline solution B, by fiber immerse to salting liquid A infiltrate, in impregnation process into Row ultrasonic wave added infiltration a period of time, 15~70min of dipper precipitation in alkaline solution B is immersed after the fiber after infiltration is drained, Aging is carried out after fiber after dipper precipitation is taken out, the fiber after aging is subjected to microwave combustion method, is finally carried out at activation It manages up to the composite filtering material fiber of SCR dedusting denitration is used for.
The present invention enables to metal ion that can preferably enter to first by fiber impregnation into salting liquid, by ultrasound In the gap of fiber, so that metal ion can be more uniform is dispersed on fiber, it then will be soaked with metal ion again Fiber impregnation into aqueous slkali so that finely dispersed reactive metal oxides can be made on fiber, due to first impregnating Metal ion enter in fiber gap, then metal ion is precipitated, reactive metal oxides can not only be reinforced and existed Bond strength on fiber, and make reactive metal oxides are more uniform to be dispersed on fiber, to improve fiber Catalytic performance.
Meanwhile fiber is a kind of larger molecular organics, under alkaline condition, is easy to degrade and dissolve, not only compromise The structure of fiber, and the metal ion of dipping in the fibre can be dissociateed to come from fiber, it is finally unable to get compound Filter media fibre.For the present invention by many experiments, the pH for adjusting alkaline solution A is 8~12, and controls the infiltrating time of fiber, energy Enough ensure that fiber does not generate irreversible structural failure in alkaline solution A, and enables to precipitate under the alkaline condition Metallic compound wrapping portion fiber afterwards prevents further destruction of the alkaline matter to fibre structure, to finally be lived The composite filtering material fiber for SCR dedusting denitration that property component securely loads.
The second object of the present invention is to provide a kind of composite filtering material fiber of above-mentioned preparation method preparation.With fiber preparation Filtrate can dedusting, moreover it is possible to catalytic denitration.
The third object of the present invention is to provide a kind of filtrate, has above-mentioned composite filtering material fiber to prepare.
The fourth object of the present invention is to provide a kind of application of above-mentioned composite filtering material fiber or filtrate in dedusting denitration.
Compared with prior art, the beneficial effects of the present invention are:
1. the present invention uses completely new precoating depositing technology, realize manganese, cerium, Zirconium oxide on a variety of organic fiber surfaces Secured load, under the process conditions, metallic atom and fiber form strong interaction, and finally formed oxide dispersion is equal It is even, not easily to fall off and have stable denitration efficiency;The process flow is simple, at low cost, and it is rapid to be conducive to filtrate manufacturing enterprise Investment large-scale production.
2. dedusting denitrating technique may be implemented in the application of the composite filtering material fiber produced by the present invention for SCR dedusting denitration Upper integration while solving the problems, such as the escaping of ammonia, greatly improves system denitration efficiency, to rows such as propulsion new round steel, building materials The regulation of industry fire coal boiler fume has positive effect, and application prospect is extensive.
Specific embodiment
It is noted that following detailed description is all illustrative, it is intended to provide further instruction to the application.Unless another It indicates, all technical and scientific terms used herein has usual with the application person of an ordinary skill in the technical field The identical meanings of understanding.
It should be noted that term used herein above is merely to describe specific embodiment, and be not intended to restricted root According to the illustrative embodiments of the application.As used herein, unless the context clearly indicates otherwise, otherwise singular Also it is intended to include plural form, additionally, it should be understood that, when in the present specification using term "comprising" and/or " packet Include " when, indicate existing characteristics, step, operation, device, component and/or their combination.
Heretofore described manganese salt is the compound that can be dissolved in water that cation is manganese ion, such as manganese nitrate, sulfuric acid Manganese, manganese acetate etc..
Heretofore described cerium salt is the compound that can be dissolved in water that cation is cerium ion, such as cerous nitrate, sulfuric acid Cerium, cerous acetate etc..
Heretofore described zirconates is the compound that can be dissolved in water that cation is zirconium ion, such as zirconium nitrate, sulfuric acid Zirconium etc..
As background technique is introduced, exist in the prior art that active component and fibres bond are insecure, are easy dusting The deficiency to fall off, in order to solve technical problem as above, present applicant proposes a kind of composite filtering material for SCR dedusting denitration is fine The preparation method of dimension.
A kind of exemplary embodiment of the application provides a kind of system of composite filtering material fiber for SCR dedusting denitration Manganese salt, cerium salt and zirconates are dissolved in the water and prepare salting liquid A by Preparation Method, the alkaline solution B that pH is 8~12 are prepared, by fiber It immerses to salting liquid A and infiltrates, ultrasonic wave added infiltration a period of time is carried out in impregnation process, is soaked after the fiber after infiltration is drained Enter 15~70min of dipper precipitation in alkaline solution B, aging is carried out after the fiber after dipper precipitation is taken out, by the fibre after aging Dimension carries out microwave combustion method, finally carries out being activated up to the composite filtering material fiber of SCR dedusting denitration is used for.
The present invention enables to metal ion that can preferably enter to first by fiber impregnation into salting liquid, by ultrasound In the gap of fiber, so that metal ion can be more uniform is dispersed on fiber, it then will be soaked with metal ion again Fiber impregnation into aqueous slkali so that finely dispersed reactive metal oxides can be made on fiber, due to first impregnating Metal ion enter in fiber gap, then metal ion is precipitated, reactive metal oxides can not only be reinforced and existed Bond strength on fiber, and make reactive metal oxides are more uniform to be dispersed on fiber, to improve fiber Catalytic performance.
Meanwhile fiber is a kind of larger molecular organics, under alkaline condition, is easy to degrade and dissolve, not only compromise The structure of fiber, and the metal ion of dipping in the fibre can be dissociateed to come from fiber, it is finally unable to get compound Filter media fibre.For the present invention by many experiments, the pH for adjusting alkaline solution A is 8~12, and controls the infiltrating time of fiber, energy Enough ensure that fiber does not generate irreversible structural failure in alkaline solution A, and enables to precipitate under the alkaline condition Metallic compound wrapping portion fiber afterwards prevents further destruction of the alkaline matter to fibre structure, to finally be lived The composite filtering material fiber for SCR dedusting denitration that property component securely loads.
Preferably, the alkaline solution B is ammonium hydroxide, sodium hydroxide solution, sal volatile or sodium carbonate liquor.
Preferably, the molar ratio of the manganese ion in the salting liquid A, cerium ion and zirconium ion be 1~8:1~4:1~ 4。
Preferably, the time that fiber is immersed to salting liquid A infiltration is 30~80min.
Preferably, the time of ultrasonic wave added infiltration is 5~30min.Ultrasonic wave added infiltration time less than fiber immerse to The infiltrating time of salting liquid A.
Preferably, the time of the aging is 2~6h.
Preferably, the aging is to carry out aging in air atmosphere after taking out the fiber after dipper precipitation.
Preferably, the time of the microwave combustion method is 10~40min, microwave power 100-600W, every 300s microwave hair Raw time 75-225s.
Preferably, it is activated again after being dried after microwave combustion method.
It is further preferred that the condition of the drying is 105 DEG C of drying and processing 5h.
Preferably, described be activated is that fiber is placed in 150~250 DEG C of a period of times.
It is further preferred that the time of the activation processing is 2~8h.
Present invention also provides a kind of composite filtering material fibers of above-mentioned preparation method preparation.Both with the filtrate of fiber preparation Energy dedusting, moreover it is possible to catalytic denitration.
Present invention also provides a kind of filtrates, have above-mentioned composite filtering material fiber to prepare.
Present invention also provides a kind of application of above-mentioned composite filtering material fiber or filtrate in dedusting denitration.
In order to enable those skilled in the art can clearly understand the technical solution of the application, below with reference to tool The technical solution of the application is described in detail in the embodiment and comparative example of body.
Embodiment 1:
Using polyimide fiber as the composite filtering material fiber for SCR dedusting denitration of substrate, steps are as follows:
Step 1: manganese nitrate solution 14.32g, the six nitric hydrate cerium 4.34g, five nitric hydrate zirconiums of 50wt% are weighed 4.29g is dissolved in deionized water 250mL, is stirred evenly, and solution A is obtained.The ammonia spirit 16mL for taking 25wt%, using deionization Water is settled to 200mL, is uniformly mixing to obtain solution B (pH 10).
Step 2: polyimide fiber is immersed into solution A 40min, ultrasonic wave added time 7min, later by the polyamides of infiltration Imine fiber takes out from solution A, and solution B is immersed after draining, fiber is taken out after dipper precipitation 21min, it is old to be placed in air atmosphere Change 4h.
Step 3: the fiber after aging is placed in microwave reactor, microwave combustion method 20min, reaction condition: microwave function Rate 200W, every 20s microwave time of origin 10s;Be placed on 105 DEG C of drying and processing 5h of air blast drying box.Drying is completely gathered Imide fiber is placed in Muffle furnace, and heat treatment activation 4h under the conditions of 250 DEG C is obtained securely metal oxide-loaded difunctional Composite fibre #1.
Embodiment 2
The present embodiment is same as Example 1, the difference is that, the manganese nitrate solution 3.58g of the present embodiment 50wt%, six Nitric hydrate cerium 17.36g, five nitric hydrate zirconium 4.29g obtain securely metal oxide-loaded difunctional composite fibre #2.
Embodiment 3
The present embodiment is same as Example 1, the difference is that, the manganese nitrate solution 3.58g of the present embodiment 50wt%, six Nitric hydrate cerium 4.34g, five nitric hydrate zirconium 17.16g obtain securely metal oxide-loaded difunctional composite fibre #3.
Embodiment 4:
Using PTFE fiber as the composite filtering material fiber for SCR dedusting denitration of substrate, steps are as follows:
Step 1: manganese nitrate solution 14.32g, the six nitric hydrate cerium 4.34g, five nitric hydrate zirconiums of 50wt% are weighed 4.29g is dissolved in deionized water 250mL, is stirred evenly, and solution A is obtained.The ammonia spirit 16mL for taking 25wt%, using deionization Water is settled to 200mL, is uniformly mixing to obtain solution B (pH 11).
Step 2: PTFE fiber is immersed into solution A 30min, ultrasonic wave added time 7min, later by the PTFE fiber of infiltration It is taken out from solution A, solution B is immersed after draining, takes out fiber after dipper precipitation 15min, be placed in air atmosphere aging 4h.
Step 3: the fiber after aging is placed in microwave reactor, microwave combustion method 20min, reaction condition: microwave function Rate 200W, every 20s microwave time of origin 10s;Be placed on 105 DEG C of drying and processing 5h of air blast drying box.It will dry complete PTFE fiber is placed in Muffle furnace, and heat treatment activation 4h under the conditions of 250 DEG C is obtained securely metal oxide-loaded difunctional multiple Condensating fiber #4.
Embodiment 5
The present embodiment is same as Example 4, the difference is that, the manganese nitrate solution 3.58g of the present embodiment 50wt%, six Nitric hydrate cerium 17.36g, five nitric hydrate zirconium 4.29g obtain securely metal oxide-loaded difunctional composite fibre #5.
Embodiment 6
The present embodiment is same as Example 4, the difference is that, the manganese nitrate solution 3.58g of the present embodiment 50wt%, six Nitric hydrate cerium 4.34g, five nitric hydrate zirconium 17.16g obtain securely metal oxide-loaded difunctional composite fibre #6.
Embodiment 7:
Using PTFE fiber as the composite filtering material fiber for SCR dedusting denitration of substrate, steps are as follows:
Step 1: manganese nitrate solution 14.32g, the six nitric hydrate cerium 17.36g, five nitric hydrate zirconiums of 50wt% are weighed 4.29g is dissolved in deionized water 250mL, is stirred evenly, and solution A is obtained.Sodium hydroxide 16g is weighed, deionized water is dissolved in and is determined Hold to 200mL, stirring is completely dissolved to sodium hydrate solid, obtains homogeneous solution B (pH 12).
Step 2: PTFE fiber is immersed into solution A 50min, ultrasonic wave added time 7min, later by the PTFE fiber of infiltration It is taken out from solution A, solution B is immersed after draining, takes out fiber after dipper precipitation 15min, be placed in air atmosphere aging 4h.
Step 3: the fiber after aging is placed in microwave reactor, microwave combustion method 20min, reaction condition: microwave function Rate 400W, every 30s microwave time of origin 10s;Be placed on 105 DEG C of drying and processing 5h of air blast drying box.It will dry complete PTFE fiber is placed in Muffle furnace, and heat treatment activation 4h under the conditions of 250 DEG C is obtained securely metal oxide-loaded difunctional multiple Condensating fiber #7.
Embodiment 8
The present embodiment is same as Example 4, the difference is that, the manganese nitrate solution 3.58g of the present embodiment 50wt%, six Nitric hydrate cerium 17.36g, five nitric hydrate zirconium 17.16g obtain securely metal oxide-loaded difunctional composite fibre #8.
Embodiment 9
The present embodiment is same as Example 4, the difference is that, the manganese nitrate solution 14.32g of the present embodiment 50wt%, Six nitric hydrate cerium 4.34g, five nitric hydrate zirconium 17.16g obtain securely metal oxide-loaded difunctional composite fibre # 9。
Embodiment 10:
Using polyimide fiber as the composite filtering material fiber for SCR dedusting denitration of substrate, steps are as follows:
Step 1: manganese nitrate solution 3.58g, the six nitric hydrate cerium 4.34g, five nitric hydrate zirconiums of 50wt% are weighed 4.29g is dissolved in deionized water 250mL, is stirred evenly, and solution A is obtained.Ammonium carbonate 19.2g is weighed, deionized water is dissolved in and is determined Hold to 200mL, stirring is completely dissolved to ammonium carbonate solid, obtains homogeneous solution B (pH 9).
Step 2: immersing solution A 60min, ultrasonic wave added time 20min for polyimide fiber, later by the poly- of infiltration Imide fiber takes out from solution A, and solution B is immersed after draining, fiber is taken out after dipper precipitation 50min, is placed in air atmosphere Aging 4h.
Step 3: the fiber after aging is placed in microwave reactor, microwave combustion method 20min, reaction condition: microwave function Rate 300W, every 30s microwave time of origin 10s;Be placed on 105 DEG C of drying and processing 5h of air blast drying box.It will dry complete PTFE fiber is placed in Muffle furnace, and heat treatment activation 4h under the conditions of 250 DEG C is obtained securely metal oxide-loaded difunctional multiple Condensating fiber #10.
Embodiment 11
The present embodiment is same as in Example 10, the difference is that, when the present embodiment changes infiltration of the fiber in solution A Between be 80min, infiltrating time is 30min in B solution, obtains securely metal oxide-loaded difunctional composite fibre #11.
Embodiment 12
The present embodiment is same as in Example 10, the difference is that, when the present embodiment changes infiltration of the fiber in solution A Between be changed to 60min, infiltrating time is changed to 40min in B solution, obtains securely metal oxide-loaded difunctional compound fibre Tie up #12.
Embodiment 13
The present embodiment is same as in Example 10, the difference is that, the present embodiment changes the step the ammonium carbonate 19.2g in one For sodium carbonate 21.2g, securely metal oxide-loaded difunctional composite fibre #13 is obtained.
SCR denitration active testing is carried out to 13 catalyst samples on the fixed bed Benitration reactor of laboratory, denitration is anti- The test condition answered are as follows: 125~250 DEG C of reaction temperature, 30 000h of air speed-1, NH3Concentration 500ppm, NO concentration 500ppm, O2 Concentration 3.5%, N2For Balance Air.The results are shown in Table 1.
Table 1 is used for the composite filtering material fiber denitration activity test result of SCR dedusting denitration
Comparative example 1
The manganese nitrate solution 14.32g, six nitric hydrate cerium 4.34g, five nitric hydrate zirconium 4.29g for weighing 50wt% are dissolved in It in deionized water 250mL, stirs evenly, obtains solution A.Preparing pH is 13 sodium hydroxide solution as solution B, by polyamides Asia Amine fiber immerses solution A 40min, and ultrasonic wave added time 7min later takes out the polyimide fiber of infiltration from solution A, Solution B, dipper precipitation 21min are immersed after draining, polyimide fiber dissolution is not available.
Comparative example 2
This comparative example is same as Example 1, the difference is that, prepare the sal volatile that pH is 7.5 as solution B, There is no the performances of catalytic denitration for the fiber prepared by the comparative example.
The foregoing is merely preferred embodiment of the present application, are not intended to limit this application, for the skill of this field For art personnel, various changes and changes are possible in this application.Within the spirit and principles of this application, made any to repair Change, equivalent replacement, improvement etc., should be included within the scope of protection of this application.

Claims (12)

1. a kind of preparation method of the composite filtering material fiber for SCR dedusting denitration, characterized in that by manganese salt, cerium salt and zirconates It is dissolved in the water and prepares salting liquid A, prepare the alkaline solution B that pH is 8~12, fiber is immersed to salting liquid A and is infiltrated, is being infiltrated Ultrasonic wave added infiltration a period of time is carried out in the process, and dipper precipitation 15 in alkaline solution B is immersed after the fiber after infiltration is drained ~70min carries out aging after taking out the fiber after dipper precipitation, and the fiber after aging is carried out microwave combustion method, most laggard Row is activated to be used for the composite filtering material fiber of SCR dedusting denitration.
2. preparation method as described in claim 1, characterized in that the alkaline solution B is ammonium hydroxide, sodium hydroxide solution, carbon Acid ammonium solution or sodium carbonate liquor;
Or, the molar ratio of manganese ion, cerium ion and zirconium ion in the salting liquid A is 1~8:1~4:1~4.
3. preparation method as described in claim 1, characterized in that the time of ultrasonic wave added infiltration is 5~30min;
Or, the time that fiber is immersed to salting liquid A infiltration is 30~80min.
4. preparation method as described in claim 1, characterized in that the time of the aging is 2~6h;
Or, the aging is to carry out aging in air atmosphere after taking out the fiber after dipper precipitation.
5. preparation method as described in claim 1, characterized in that the time of the microwave combustion method is 10~40min, microwave Power 100-600W, every 300s microwave time of origin 75-225s.
6. preparation method as described in claim 1, characterized in that activated again after being dried after microwave combustion method.
7. preparation method as claimed in claim 6, characterized in that the condition of the drying is 105 DEG C of drying and processing 5h.
8. preparation method as described in claim 1, characterized in that the activation processing is that fiber is placed in 150~250 DEG C one The section time.
9. preparation method as claimed in claim 8, characterized in that the time of the activation processing is 2~8h.
10. a kind of composite filtering material fiber of any preparation method preparation of claim 1~9.
11. a kind of filtrate, characterized in that prepared by composite filtering material fiber described in any one of claim 10.
12. filtrate answering in dedusting denitration described in a kind of composite filtering material fiber described in any one of claim 10 or claim 11 With.
CN201710486860.4A 2017-06-23 2017-06-23 A kind of composite filtering material fiber and preparation method for SCR dedusting denitration Active CN107158799B (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN201710486860.4A CN107158799B (en) 2017-06-23 2017-06-23 A kind of composite filtering material fiber and preparation method for SCR dedusting denitration
PCT/CN2017/106879 WO2018233159A1 (en) 2017-06-23 2017-10-19 Difunctional composite filter medium fiber and preparation method therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710486860.4A CN107158799B (en) 2017-06-23 2017-06-23 A kind of composite filtering material fiber and preparation method for SCR dedusting denitration

Publications (2)

Publication Number Publication Date
CN107158799A CN107158799A (en) 2017-09-15
CN107158799B true CN107158799B (en) 2018-12-18

Family

ID=59819188

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710486860.4A Active CN107158799B (en) 2017-06-23 2017-06-23 A kind of composite filtering material fiber and preparation method for SCR dedusting denitration

Country Status (1)

Country Link
CN (1) CN107158799B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018233159A1 (en) * 2017-06-23 2018-12-27 山东大学 Difunctional composite filter medium fiber and preparation method therefor
CN107963893A (en) * 2017-11-10 2018-04-27 安徽顺成耐火构件科技有限公司 A kind of preparation method of ceramic fiber cloth basket strainer
CN108926911B (en) * 2018-06-26 2021-02-26 清华大学盐城环境工程技术研发中心 Preparation method of denitration and demercuration integral filter material
CN113476958B (en) * 2021-06-22 2022-07-12 南京玻璃纤维研究设计院有限公司 Filter material and preparation method and application thereof

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102114424B (en) * 2010-12-29 2012-10-24 国电科学技术研究院 Low-temperature smoke denitration SCR (silicon controlled rectifier) catalyst and preparation method
CN102145241B (en) * 2011-02-18 2013-02-27 福州大学 Preparation method of denitration-catalyst-supported polyphenylene sulfide (PPS) filter material
CN105435534A (en) * 2015-11-17 2016-03-30 安徽省元琛环保科技有限公司 Modified functional filter material loaded with low temperature denitration catalyst and preparation method thereof

Also Published As

Publication number Publication date
CN107158799A (en) 2017-09-15

Similar Documents

Publication Publication Date Title
CN107158799B (en) A kind of composite filtering material fiber and preparation method for SCR dedusting denitration
CN105327698B (en) Using titanium-containing blast furnace slag as the preparation method of the Novel SCR catalyst for denitrating flue gas of carrier
CN105597817B (en) A kind of MnOx/ SAPO-11 low-temperature SCRs catalyst for denitrating flue gas and preparation method and application
WO2015161627A1 (en) Honeycomb denitration catalyst for flue gas at 400°c-600°c and preparation method therefor
JP6257775B2 (en) Catalyst having NOx removal performance and mercury oxidation performance and its production method
CN107362807A (en) A kind of Mn/Co bases low temperature SCO catalyst and preparation method thereof
CN103433033A (en) Low-temperature denitration catalyst MnOx-CeO2-TiO2-Al2O3, and preparation method and application thereof
CN107261644B (en) A kind of difunctional composite filtering material fiber of low temperature dedusting-denitration and preparation method
CN113413904A (en) g-C3N4Low-temperature NH of loaded manganese cerium composite oxide3-SCR catalyst, preparation method and application thereof
CN105561982B (en) A kind of γ-MnO2Nanometer sheet low-temperature SCR catalyst for denitrating flue gas and preparation method and application
CN107694575A (en) A kind of complex carrier SCR denitration and preparation method
CN107837826A (en) Inactivate the process of regenerating of catalyst for denitrating flue gas
CN110372875A (en) A kind of application of the more metal-organic framework materials of heteronuclear and preparation and denitration demercuration
CN108554398B (en) Preparation method and application of wide-temperature-window denitration catalyst
CN103736481A (en) CeO2-MoO3/graphene low-temperature denitration catalyst and preparation method
CN103894186B (en) A kind of acid-dissolved titanium slag prepares the method for manganese titanium system low-temperature denitration catalysis material
CN109772265A (en) A kind of red mud from sintering process modified activated carbon and preparation method thereof for flue gas desulfurization and denitrification
CN109433217A (en) A kind of red mud denitrating catalyst and preparation method thereof
CN113877591A (en) Preparation method of acid-treated iron mud denitration catalyst
CN111375407B (en) Low-temperature denitration catalyst and preparation method and application thereof
CN112642495A (en) Realize low SO2Catalyst regeneration and modification method for conversion rate and high zero-valent mercury oxidation performance
CN107469811A (en) A kind of wide temperature window denitrating catalyst and its preparation method and application
CN103331140A (en) Demercuration adsorbent and preparation method thereof
CN103537273A (en) Denitration catalyst for collaborative mercury removal and preparation method thereof
CN105056950A (en) Microwave NOx removal catalyst based on coal-based carbon and preparation method thereof

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