WO2019205765A1 - 一种垃圾焚烧中氯吸附材料的制备方法及其应用 - Google Patents

一种垃圾焚烧中氯吸附材料的制备方法及其应用 Download PDF

Info

Publication number
WO2019205765A1
WO2019205765A1 PCT/CN2019/073981 CN2019073981W WO2019205765A1 WO 2019205765 A1 WO2019205765 A1 WO 2019205765A1 CN 2019073981 W CN2019073981 W CN 2019073981W WO 2019205765 A1 WO2019205765 A1 WO 2019205765A1
Authority
WO
WIPO (PCT)
Prior art keywords
powder
sio
chlorine
iron ore
waste incineration
Prior art date
Application number
PCT/CN2019/073981
Other languages
English (en)
French (fr)
Inventor
刘明华
张灵敏
林春香
刘以凡
吕源财
刘登周
Original Assignee
福州大学
福建省博屹环保科技有限公司
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 福州大学, 福建省博屹环保科技有限公司 filed Critical 福州大学
Priority to JP2020556839A priority Critical patent/JP7109580B2/ja
Priority to DE112019002175.3T priority patent/DE112019002175T5/de
Publication of WO2019205765A1 publication Critical patent/WO2019205765A1/zh
Priority to US17/033,965 priority patent/US11896955B2/en

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/06—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30—Processes for preparing, regenerating, or reactivating
    • B01J20/3035—Compressing
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/04—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
    • B01J20/041—Oxides or hydroxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/103—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate comprising silica
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28002—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
    • B01J20/28004—Sorbent size or size distribution, e.g. particle size
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30—Processes for preparing, regenerating, or reactivating
    • B01J20/3021—Milling, crushing or grinding
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30—Processes for preparing, regenerating, or reactivating
    • B01J20/3078—Thermal treatment, e.g. calcining or pyrolizing
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30—Processes for preparing, regenerating, or reactivating
    • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3214—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the method for obtaining this coating or impregnating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/10—Destroying solid waste or transforming solid waste into something useful or harmless involving an adsorption step
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/22—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the deposition of inorganic material, other than metallic material
    • C23C16/30—Deposition of compounds, mixtures or solid solutions, e.g. borides, carbides, nitrides
    • C23C16/40—Oxides
    • C23C16/406—Oxides of iron group metals
    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/56—After-treatment
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/12—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of plastics, e.g. rubber
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10—Inorganic adsorbents
    • B01D2253/106—Silica or silicates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10—Inorganic adsorbents
    • B01D2253/112—Metals or metal compounds not provided for in B01D2253/104 or B01D2253/106
    • B01D2253/1124—Metal oxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/25—Coated, impregnated or composite adsorbents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/20—Halogens or halogen compounds
    • B01D2257/204—Inorganic halogen compounds
    • B01D2257/2045—Hydrochloric acid
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/02—Other waste gases
    • B01D2258/0283—Flue gases
    • B01D2258/0291—Flue gases from waste incineration plants
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00—Pretreatment
    • F23G2201/70—Blending
    • F23G2201/701—Blending with additives
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2208/00—Safety aspects

Definitions

  • the invention relates to the field of chlorine adsorption materials, in particular to the preparation and application of chlorine adsorption materials in waste incineration.
  • the removal of HCl during incineration is usually removed by a flue gas purification collection device.
  • a flue gas purification collection device According to the form of the adsorbent and the reaction product, the solid waste incineration flue gas purification technology can be divided into three types: wet type, semi-dry type and dry type.
  • the wet type generally uses an aqueous solution or a slurry as a dechlorination agent, and has good absorption performance, but the process is complicated and the cost is high;
  • the semi-dry method is a lime slurry, although the price is cheap, the pulping system is complicated, and the slurry conveying route is easy to malfunction;
  • the dry method Dechlorination is a dry state of the added dechlorination agent, high purification efficiency for pollutants, high utilization efficiency of the adsorbent, simple operation, and low production cost.
  • the dechlorination agent for dry dechlorination mainly depends on the specific surface area of the dechlorination agent, the specific surface area is large, the activity of the dechlorination agent is high, the dechlorination reaction is fast, and the chlorine capacity is high.
  • the specific surface area of the active component of the dechlorination agent is not high. Therefore, how to increase the specific surface area of the dechlorination agent is the key to the dechlorination agent under the premise of ensuring the strength of the dechlorination agent.
  • a dry dechlorination agent for removing HCl from a gas and a preparation method thereof are disclosed in the patent CN101773768A.
  • the dechlorination agent uses Na 2 CO 3 , CaCO 3 , CaO, MgO as active components, cross-linked bentonite as pore aid, methyl cellulose as foaming agent and extrusion aid, formed by extrusion, and then dried. , roasting, to make a dechlorination agent.
  • the preparation process of the adsorbent is simple, the dechlorination activity is high, and the low temperature penetrating chlorine capacity is large. However, the adsorbent is not suitable for use under very high temperature conditions, and the adsorbent cannot be recycled.
  • a novel high-efficiency dechlorination agent and a preparation method thereof are disclosed in the patent CN106268832A.
  • the dechlorination agent has one or more of Na 2 CO 3 , CaCO 3 , CaO, MgO, CuO, ZnO and derivatives thereof as an active component, and NH 4 HCO 3 is a pore auxiliary to Al 2 O. 3.
  • At least one of diaspore, kaolin or clay is a carrier and an auxiliary agent, and a part of the modified Zn salt and Ca salt are added as a synergist. According to the corresponding proportion, the appropriate amount of water is mixed and mixed, and then extruded, and then dried and calcined to prepare a dechlorination agent.
  • the adsorbent has high adsorption rate of high concentration and low concentration HCl at normal temperature, high dechlorination precision, and chlorine capacity up to 35% or more; at the same time, it can efficiently and deeply remove catalytic reforming in various sections in the temperature range of 300-600 °C.
  • the HCl gas can penetrate more than 65% of the chlorine capacity.
  • the pore volume and specific surface area of diaspore, kaolin or clay are limited, and the cost of the adsorbent is high.
  • the object of the present invention is to provide a method for preparing a chlorine adsorbing material which is low in cost, high in efficiency, and simple in production process, and an application thereof.
  • a method for preparing a chlorine adsorption material in waste incineration after mixing natural iron ore and quartz powder, adding CaO to the mixed system and modifying the natural iron ore and quartz powder by ultrasonic impregnation to obtain adsorption of chlorine substances Sexual chlorine adsorption material.
  • chlorine species include at least hydrogen chloride and chlorobenzene.
  • SiO 2 -Fe 2 O 3 carrier Preparation of SiO 2 -Fe 2 O 3 carrier:
  • the SiO 2 powder obtained in the step (2) is placed in a quartz tube of a chemical vapor deposition apparatus by chemical vapor deposition, and then SiO 2 powder and iron ore powder are pressed.
  • the iron ore powder obtained in the step (1) is weighed in a ratio of 1:1.7 to 2.7 and placed in a sublimator of a chemical vapor deposition apparatus, wherein the quartz tube and the sublimator are arranged opposite to each other and connected, and the quartz tube is placed therein.
  • the platform of SiO 2 powder the air is introduced into the quartz tube and the vacuum degree is maintained at 0.08 MPa, the SiO 2 powder is fluidized, and then the quartz tube is heated and heated to 200 ° C to remove the SiO 2 powder.
  • Moisture after 2 to 3 hours, the temperature of the quartz tube is raised to 400 ° C and maintained, then nitrogen is introduced into the sublimator and the temperature in the sublimator is adjusted to 110 ° C.
  • the temperature of the sublimator was adjusted to 400 ° C, the sublimator and the quartz tube were formed into a reaction chamber, and the fluidized SiO 2 powder was thoroughly mixed with the sublimated iron ore powder, and the reaction chamber was maintained at 400 ° C for 2 h.
  • the SiO 2 powder with the iron ore fines is formed carrier Iron and iron compound on the complete oxidation allowed to cool to room temperature and subjected to drying at room temperature, and then pulverized, finally the powder is placed in a tubular furnace heated at a ramp rate 3 °C ⁇ min -1 to 400 After being treated for 1 to 2 hours at ° C, a SiO 2 -Fe 2 O 3 carrier can be obtained;
  • processing 2 -Fe 2 O 3 carrier was placed calcined at a temperature of 900 °C, to remove NO x and deposit on the surface thereof prepared CaO, to achieve CaO SiO 2 -Fe 2
  • the O 3 carrier is modified, and then cooled to room temperature, and then ground to a particle diameter of 0.1 to 0.2 mm to prepare a chlorine adsorbent.
  • steps (1), (2) and (4) are as follows:
  • the flow rate of air flowing into the quartz tube in the step (3) is 80 mL ⁇ min -1 .
  • the purity of Ca(NO 3 ) 2 ⁇ 4H 2 O in step (4) is >99.9%, and the particle size is ⁇ 5 ⁇ m.
  • the ultrasonic cleaner in step (5) has an operating frequency of 40,000 Hz and an operating power of 100 watts.
  • the ultrasonic cleaner maintains the temperature of the water tank at 90 ° C during operation.
  • the calcination treatment time of the SiO 2 -Fe 2 O 3 support treated in the step (5) in the step (6) is 1 h.
  • the prepared chlorine adsorbent is used for the adsorption of chlorine species in waste incineration.
  • the beneficial effects of the invention are as follows: by using natural iron ore and quartz powder as raw materials, the chlorine adsorbent is prepared by ultrasonically impregnating with CaO, and the obtained adsorbent material has large pore diameter and high porosity. It has stable structure and high adsorption efficiency and adsorption capacity for chlorine incineration. It can also be reused.
  • the use of low-cost natural iron ore and quartz stone can not only reduce the treatment cost of chlorine substances. It can also greatly realize the utilization of resources and promote the protection of the environment.
  • a method for preparing a chlorine adsorption material in waste incineration which comprises the following steps:
  • SiO 2 -Fe 2 O 3 carrier The SiO 2 powder obtained in the step (2) is placed in a quartz tube of a chemical vapor deposition apparatus by chemical vapor deposition, and then the SiO 2 powder and the iron ore powder are 1:1.7 to 2.7 ratio Weigh iron ore powder obtained in step (1) is placed in a sublimator of a chemical vapor deposition apparatus, wherein the quartz tube and the sublimator are arranged opposite to each other and connected, and the quartz tube is provided with SiO. 2 powder platform, the air is introduced into the quartz tube and the vacuum is maintained at 0.08 MPa, the SiO 2 powder is fluidized, and then the quartz tube is heated to 200 ° C to remove the moisture in the SiO 2 powder.
  • the temperature of the quartz tube was raised to 400 ° C and maintained, then nitrogen was introduced into the sublimator and the temperature in the sublimator was adjusted to 110 ° C. After the iron ore powder was completely sublimated, it was sublimed. The temperature of the device is adjusted to 400 ° C, so that the sublimator and the quartz tube form a reaction chamber and the fluidized SiO 2 powder is thoroughly mixed with the sublimated iron ore powder, and the reaction chamber is maintained at a temperature of 400 ° C for 2 h to make SiO 2 .
  • Powder and iron ore powder form carrier Iron and iron compound completely oxidized, this was cooled down to room temperature and subjected to drying at room temperature, and then pulverized, finally the powder is placed in a tubular furnace heated at a ramp rate 3 °C ⁇ min -1 to 400 °C After maintaining for 1 to 2 hours, the SiO 2 -Fe 2 O 3 carrier can be obtained;
  • 3 carrier 2 is placed calcined at a temperature of 900 °C, to remove NO x and deposit on the surface thereof prepared CaO, to achieve CaO SiO 2 -Fe 2
  • the O 3 carrier is modified, and then cooled to room temperature, and then ground to a particle diameter of 0.1 to 0.2 mm to prepare a chlorine adsorbent.
  • steps (1), (2) and (4) are as follows:
  • the flow rate of air flowing into the quartz tube in the step (3) is 80 mL ⁇ min -1 .
  • the purity of Ca(NO3) 2 ⁇ 4H 2 O in step (4) is >99.9%, and the particle size is ⁇ 5 ⁇ m.
  • the ultrasonic cleaner in step (5) has an operating frequency of 40,000 Hz and an operating power of 100 watts.
  • the ultrasonic cleaner maintains the temperature of the water tank at 90 ° C during operation.
  • the calcination treatment time of the SiO 2 -Fe 2 O 3 support treated in the step (5) in the step (6) is 1 h.
  • the prepared chlorine adsorbent is used for the adsorption of chlorine species in waste incineration.
  • a method for preparing a chlorine adsorption material in waste incineration which comprises the following steps:
  • the air is maintained at a vacuum of 0.08 MPa and an air flow rate of 80 mL ⁇ min -1 , and the SiO 2 powder is fluidized, and then the quartz tube is heated and heated to 200 ° C to remove moisture in the SiO 2 powder.
  • the temperature of the quartz tube was raised to 400 ° C and maintained, then nitrogen was introduced into the sublimator and the temperature in the sublimator was adjusted to 110 ° C.
  • the temperature of the sublimator was adjusted. Adjust to 400 ° C, so that the sublimator and quartz tube form a reaction chamber and mix the fluidized SiO 2 powder with the sublimated iron ore powder, and keep the reaction chamber at 400 ° C for 2 h, then make SiO 2 powder.
  • step (4) adding the solution prepared in the step (4) to the water tank of the ultrasonic cleaner, and then adding the SiO 2 -Fe 2 O 3 carrier obtained in the step (3) to the water tank, and then operating at a frequency of 40,000 Hz.
  • the operating parameter of working power is 100W, ultrasonic mixing of the mixing system in the water tank for 6h, and the mixing temperature in the water tank is maintained at 90 ° C during mixing;
  • processing 2 -Fe 2 O 3 carrier was placed 1h calcined at a temperature of 900 °C, to remove NO x and deposit on the surface thereof prepared CaO, to achieve CaO SiO 2 -Fe
  • the modification of the 2 O 3 carrier, followed by cooling to a normal temperature, and then grinding to a particle diameter of 0.1 to 0.2 mm, can produce a chlorine adsorption material.
  • a method for preparing a chlorine adsorption material in waste incineration which comprises the following steps:
  • the air is maintained at a vacuum of 0.08 MPa and an air flow rate of 80 mL ⁇ min -1 , and the SiO 2 powder is fluidized, and then the quartz tube is heated and heated to 200 ° C to remove moisture in the SiO 2 powder.
  • the temperature of the quartz tube was raised to 400 ° C and maintained, then nitrogen was introduced into the sublimator and the temperature in the sublimator was adjusted to 110 ° C.
  • the temperature of the sublimator was adjusted. Adjust to 400 ° C, so that the sublimator and quartz tube form a reaction chamber and mix the fluidized SiO 2 powder with the sublimated iron ore powder, and keep the reaction chamber at 400 ° C for 2 h, then make SiO 2 powder.
  • processing 2 -Fe 2 O 3 carrier was placed 1h calcined at a temperature of 900 °C, to remove NO x and deposit on the surface thereof prepared CaO, to achieve CaO SiO 2 -Fe
  • the modification of the 2 O 3 carrier, followed by cooling to a normal temperature, and then grinding to a particle diameter of 0.1 to 0.2 mm, can produce a chlorine adsorption material.
  • a method for preparing a chlorine adsorption material in waste incineration which comprises the following steps:
  • the air is maintained at a vacuum of 0.08 MPa and an air flow rate of 80 mL ⁇ min -1 , and the SiO 2 powder is fluidized, and then the quartz tube is heated and heated to 200 ° C to remove moisture in the SiO 2 powder.
  • the temperature of the quartz tube was raised to 400 ° C and maintained, then nitrogen was introduced into the sublimator and the temperature in the sublimator was adjusted to 110 ° C.
  • the temperature of the sublimator was adjusted. Adjust to 400 ° C, so that the sublimator and quartz tube form a reaction chamber and mix the fluidized SiO 2 powder with the sublimated iron ore powder, and keep the reaction chamber at 400 ° C for 2 h, then make SiO 2 powder.
  • processing 2 -Fe 2 O 3 carrier was placed 1h calcined at a temperature of 900 °C, to remove NO x and deposit on the surface thereof prepared CaO, to achieve CaO SiO 2 -Fe
  • the modification of the 2 O 3 carrier, followed by cooling to a normal temperature, and then grinding to a particle diameter of 0.1 to 0.2 mm, can produce a chlorine adsorption material.
  • a method for preparing a chlorine adsorption material in waste incineration which comprises the following steps:
  • the air is maintained at a vacuum of 0.08 MPa and an air flow rate of 80 mL ⁇ min -1 , and the SiO 2 powder is fluidized, and then the quartz tube is heated and heated to 200 ° C to remove moisture in the SiO 2 powder.
  • the temperature of the quartz tube was raised to 400 ° C and maintained, then nitrogen was introduced into the sublimator and the temperature in the sublimator was adjusted to 110 ° C.
  • the temperature of the sublimator was adjusted. Adjust to 400 ° C, so that the sublimator and quartz tube form a reaction chamber and mix the fluidized SiO 2 powder with the sublimated iron ore powder, and keep the reaction chamber at 400 ° C for 2 h, then make SiO 2 powder.
  • processing 2 -Fe 2 O 3 carrier was placed 1h calcined at a temperature of 900 °C, to remove NO x and deposit on the surface thereof prepared CaO, to achieve CaO SiO 2 -Fe
  • the modification of the 2 O 3 carrier, followed by cooling to a normal temperature, and then grinding to a particle diameter of 0.1 to 0.2 mm, can produce a chlorine adsorption material.
  • the chlorine adsorption materials prepared in Examples 1 to 4 were respectively placed in different garbage incineration reactors, and then the temperature in the reactor was heated to 900 ° C in an air atmosphere for 30 minutes to ensure complete oxidation of the chlorine adsorption material.
  • a combustion-supporting synthesis gas (composed of 1% HCl, 21.9% CO, 5.9% CH 4 , 12.7% H 2 , 7.8% CO 2 and 50.7% N 2 ) is introduced, and the gas is pushed into the incinerator through the air nozzle and the garbage And burning, after the combustion is complete, determine the content of HCl in the flue gas, and add a test without adding chlorine adsorption material to measure the content of HCl in the flue gas when no chlorine adsorption material is added, and the results are as follows:
  • the limit of HCl is 60ppm (1 hour average) and 50ppm (24 hour average). It can be seen that the chlorine adsorption material prepared by adding the solution of the present invention can be seen. After that, the chlorine-based substances generated in waste incineration can be adsorbed and meet the requirements of relevant national regulations.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Inorganic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Environmental & Geological Engineering (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • General Engineering & Computer Science (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Processing Of Solid Wastes (AREA)
  • Silicon Compounds (AREA)
  • Treating Waste Gases (AREA)

Abstract

一种垃圾焚烧中氯吸附材料的制备方法及应用，通过以天然铁矿石、石英粉为原料，用CaO通过超声浸渍的方法修饰铁矿石与石英粉，制得吸附剂。所制得的吸附剂用于垃圾焚烧中氯类物质的吸附。吸附剂孔径大、孔隙率高、结构稳定、并且对垃圾焚烧时氯类物质具有较高吸附效率和吸附量。采用成本低廉的天然铁矿石与石英石，不仅能够降低氯类物质的处理成本，还能够极大的实现资源的利用，促进环境保护。

Description

一种垃圾焚烧中氯吸附材料的制备方法及其应用 技术领域
本发明涉及氯吸附材料领域，尤其是一种垃圾焚烧中氯吸附材料的制备及其应用。
背景技术
快速发展的经济给人们带来便利的同时，也产生了许多的固体垃圾。由于固体废物组成复杂，可能含有毒性、燃烧性、传染性与致病性等，因此，固体废物的处置已成为一个迫切需要解决的重大问题。与垃圾填埋场相比，焚烧具有减量化、卫生控制和能量回收等优点，被认为是一种较好的废物管理方法。通常，固体废物通常含有氯源，这可能导致大量HCl的产生。因此，有必要控制塑料废物焚烧过程中氯苯的排放。
对于焚烧时HCl的去除，通常通过烟气净化收集装置进行去除。根据吸附剂和反应产物的物质形态，固体废物焚烧烟气净化技术可以分为湿式、半干式及干式三种。湿式一般以水溶液或者浆液为脱氯剂，吸收性能好，但是工艺复杂，成本高；半干法所用药剂为石灰浆，虽然价格便宜，但是制浆系统复杂，料浆输送路线容易故障；干法脱氯为加入的脱氯剂为干态，对污染物质的净化效率高，吸附剂利用效率高，操作简单，生产费用低。干法脱HCl用的脱氯剂主要看脱氯剂的比表面积，比表面积大，脱氯剂的活性高，脱氯反应快，氯容高。但脱氯剂的活性组分的比表面积不高，因此，如何在保证脱氯剂强度的前提下，增加脱氯剂的比表面积是脱氯剂的关键。
专利CN101773768A中公开了一种从气体中脱除HCl的干法脱氯剂及其制备方法。该脱氯剂以Na 2CO 3、CaCO 3、CaO、MgO为活性组分，交联膨润土为孔性助剂，甲基纤维素为发泡剂和助挤剂，经挤条成型，然后干燥、焙烧，制成脱氯剂。该吸附剂制备工艺简单，脱氯活性高，低温穿透氯容大。但是吸附剂不适合在很高温度条件下使用，且吸附剂不能循环使用。
专利CN106268832A中公开了一种新型高效脱氯剂及其制备方法。该脱氯剂以Na 2CO 3、CaCO 3、CaO、MgO、CuO、ZnO及其衍生物中的一种或几种为活性组分，NH 4HCO 3为孔性助剂，以Al 2O 3、水铝石、高岭土或白土中的至少一种为载体和助剂，加入部分改性Zn盐、Ca盐为增效助剂。按照相应比例加适量水调配混合之后挤条成型，然后干燥、焙烧，制成脱氯剂。该吸附剂常温下对高浓度及低浓度HCl吸附率高，且脱氯精度高、氯容高达35％以上；同时在300～600℃温度范围均可以高效深度的脱除催化重整各工段中的HCl气体，穿透氯容可达到65％以上。但是水铝石、高岭土或白土中孔容与比表面积有限，且该吸附剂的成本高。
上述的专利对脱氯剂进行一定的研究，但是一般只能在常温或者高温条件下使用，重复利用率不高，使用条件限制比较多，且脱氯剂的成本大多比较高，这些问题制约了脱氯剂的应用于制备。
发明内容
针对现有技术的情况与不足，本发明的目的在于提供一种成本低廉、高效安全且生产工艺简单的氯吸附材料的制备方法及其应用。
为了实现上述的技术目的，本发明采用的技术方案为：
一种垃圾焚烧中氯吸附材料的制备方法，将天然铁矿石和石英粉混合后，往混合体系中加入CaO并通过超声浸渍对天然铁矿石和石英粉进行修饰，制得对氯类物质具有吸附性的氯吸附材料。
进一步，所述的氯类物质至少包括氯化氢和氯苯。
进一步，其具体包括如下步骤：
(1)制备铁矿石粉：将天然铁矿石投入研磨机中研磨，然后过筛处理得到粒径为0.2～0.3mm的铁矿石粉；
(2)制备SiO 2：将石英石置于压片机中压成粉末，然后经烘干脱水后，通过60～100目的筛 子进行过筛处理得SiO 2粉末；
(3)制备SiO 2-Fe 2O 3载体：采用化学气相沉积法，将步骤(2)制得的SiO 2粉末置于化学气相沉积设备的石英管中，然后按SiO 2粉末与铁矿石粉为1：1.7～2.7的比例称取步骤(1)制得的铁矿石粉置于化学气相沉积设备的升华器中，其中，石英管与升华器为上下相对设置且连通，石英管内设有放置SiO 2粉末的平台，往石英管中通入空气并保持真空度为0.08MPa的条件下，使SiO 2粉末呈流化状态，然后将石英管加热升温至200℃进行脱除SiO 2粉末中的水分，在保持2～3h后，将石英管的温度升温至400℃并保持，然后再往升华器中通入氮气并将升华器内的温度调节至110℃，待铁矿石粉完全升华后，将升华器的温度调节至400℃，使升华器和石英管形成反应室并令流化状态的SiO 2粉末与升华的铁矿石粉充分混合，令反应室在400℃的温度条件下保持2h后，使SiO 2粉末与铁矿石粉形成载体上的铁及铁化合物完全氧化后，使其降温至室温并对其进行室温干燥，然后再磨成粉末，最后将粉末置于管式炉中以3℃·min -1的升温速率升温至400℃并保持处理1～2h后，即可制得SiO 2-Fe 2O 3载体；
(4)取Ca(NO 3) 2·4H 2O作为前体，将其按固液比为0.4～1.2Kg/L的比值配制成溶液；
(5)将步骤(4)制得的溶液加入到超声波清洗器的水槽中，然后将步骤(3)制得的SiO2-Fe2O3载体加入到水槽中进行超声波混合6～9h；
(6)将经过步骤(5)处理的SiO 2-Fe 2O 3载体置于900℃温度下煅烧，以去除其表面附着物上的NO x和制得CaO，实现CaO对SiO 2-Fe 2O 3载体的修饰，然后将其冷却至常温后，再研磨至粒径为0.1～0.2mm，即可制得氯吸附材料。
优选的，步骤(1)、(2)和(4)中所添加的组分及份数如下：
天然铁矿石         52份～67份；
石英石            25份～30份；
Ca(NO3)2·4H2O        0.03份～0.05份。
优选的，步骤(3)中往石英管中通入空气的流量为80mL·min -1。
优选的，步骤(4)中Ca(NO 3) 2·4H 2O的纯度＞99.9％，粒径＜5μm。
优选的，步骤(5)中超声波清洗器的工作频率为40000Hz，工作功率为100W。
优选的，步骤(5)中超声波清洗器在工作时，将水槽的温度维持在90℃。
优选的，步骤(6)中经过步骤(5)处理的SiO 2-Fe 2O 3载体的煅烧处理时间为1h。
将所制得的氯吸附材料用于垃圾焚烧中氯类物质的吸附。
采用上述的技术方案，本发明的有益效果为：通过以天然铁矿石、石英粉为原料，将其与CaO通过超声浸渍制备氯吸附剂，所制得的吸附剂材料孔径大、孔隙率高、结构稳定、并且对垃圾焚烧时氯类物质具有较高吸附效率和吸附量，还可重复使用，另外，采用成本低廉的天然铁矿石与石英石，不仅能够降低氯类物质的处理成本，还能够极大的实现资源的利用，促进环境的保护。
具体实施方式
一种垃圾焚烧中氯吸附材料的制备方法，其具体包括如下步骤：
(1)制备铁矿石粉：将天然铁矿石投入研磨机中研磨，然后过筛处理得到粒径为0.2～0.3mm的铁矿石粉；
(2)制备SiO 2：将石英石置于压片机中压成粉末，然后经烘干脱水后，通过60～100目的筛子进行过筛处理得SiO 2粉末；
(3)制备SiO 2-Fe 2O 3载体：采用化学气相沉积法，将步骤(2)制得的SiO 2粉末置于化学气相沉积设备的石英管中，然后按SiO2粉末与铁矿石粉为1：1.7～2.7的比例称取步骤(1)制得的铁矿石粉置于化学气相沉积设备的升华器中，其中，石英管与升华器为上下相对设置且连通，石英管内设有放置SiO 2粉末的平台，往石英管中通入空气并保持真空度为0.08MPa的条件下，使SiO 2粉末呈流化状态，然后将石英管加热升温至200℃进行脱除SiO2粉末中的水分，在保持2～3h后，将石英管的温度升温至400℃并保持，然后再往升华器中通入氮气并将升华器内的温度调节至110℃，待铁矿石粉完全升华后，将升华器的温度调节至400℃，使 升华器和石英管形成反应室并令流化状态的SiO2粉末与升华的铁矿石粉充分混合，令反应室在400℃的温度条件下保持2h后，使SiO2粉末与铁矿石粉形成载体上的铁及铁化合物完全氧化后，使其降温至室温并对其进行室温干燥，然后再磨成粉末，最后将粉末置于管式炉中以3℃·min -1的升温速率升温至400℃并保持处理1～2h后，即可制得SiO 2-Fe 2O 3载体；
(4)取Ca(NO 3) 2·4H 2O作为前体，将其按固液比为0.4～1.2Kg/L的比值配制成溶液；
(5)将步骤(4)制得的溶液加入到超声波清洗器的水槽中，然后将步骤(3)制得的SiO2-Fe2O3载体加入到水槽中进行超声波混合6～9h；
(6)将经过步骤(5)处理的SiO 2-Fe 2O 3载体置于900℃温度下煅烧，以去除其表面附着物上的NO x和制得CaO，实现CaO对SiO 2-Fe 2O 3载体的修饰，然后将其冷却至常温后，再研磨至粒径为0.1～0.2mm，即可制得氯吸附材料。
优选的，步骤(1)、(2)和(4)中所添加的组分及份数如下：
天然铁矿石         52份～67份；
石英石            25份～30份；
Ca(NO3)2·4H2O        0.03份～0.05份。
优选的，步骤(3)中往石英管中通入空气的流量为80mL·min -1。
优选的，步骤(4)中Ca(NO3) 2·4H 2O的纯度＞99.9％，粒径＜5μm。
优选的，步骤(5)中超声波清洗器的工作频率为40000Hz，工作功率为100W。
优选的，步骤(5)中超声波清洗器在工作时，将水槽的温度维持在90℃。
优选的，步骤(6)中经过步骤(5)处理的SiO 2-Fe 2O 3载体的煅烧处理时间为1h。
将所制得的氯吸附材料用于垃圾焚烧中氯类物质的吸附。
实施例1
一种垃圾焚烧中氯吸附材料的制备方法，其具体包括如下步骤：
(1)制备铁矿石粉：将天然铁矿石投入研磨机中研磨，然后过筛处理得到粒径为0.2～0.3mm 的铁矿石粉；
(2)制备SiO 2：将石英石置于压片机中压成粉末，然后经烘干脱水后，通过60～100目的筛子进行过筛处理得SiO 2粉末；
(3)制备SiO 2-Fe 2O 3载体：采用化学气相沉积法，称取2Kg步骤(2)制得的SiO 2粉末置于化学气相沉积设备的石英管中，然后称取5.36Kg步骤(1)制得的铁矿石粉置于化学气相沉积设备的升华器中，其中，石英管与升华器为上下相对设置且连通，石英管内设有放置SiO 2粉末的平台，往石英管中通入空气并保持真空度为0.08MPa、空气流量为80mL·min -1的条件下，使SiO 2粉末呈流化状态，然后将石英管加热升温至200℃进行脱除SiO 2粉末中的水分，在保持2h后，将石英管的温度升温至400℃并保持，然后再往升华器中通入氮气并将升华器内的温度调节至110℃，待铁矿石粉完全升华后，将升华器的温度调节至400℃，使升华器和石英管形成反应室并令流化状态的SiO 2粉末与升华的铁矿石粉充分混合，令反应室在400℃的温度条件下保持2h后，使SiO 2粉末与铁矿石粉形成载体上的铁及铁化合物完全氧化后，使其降温至室温并对其进行室温干燥，然后再磨成粉末，最后将粉末置于管式炉中以3℃·min -1的升温速率升温至400℃并保持处理2h后，即可制得SiO 2-Fe 2O 3载体；
(4)取0.4Kg Ca(NO 3) 2·4H 2O作为前体，将其与体积为1L的去离子水配制成溶液，其中，纯度＞99.9％，粒径＜5μm；
(5)将步骤(4)制得的溶液加入到超声波清洗器的水槽中，然后将步骤(3)制得的SiO 2-Fe 2O 3载体加入到水槽中，然后以工作频率为40000Hz，工作功率为100W的工作参数对水槽中的混合体系进行超声波混合6h，混合期间保持水槽内的混合温度为90℃；
(6)将经过步骤(5)处理的SiO 2-Fe 2O 3载体置于900℃温度下煅烧1h，以去除其表面附着物上的NO x和制得CaO，实现CaO对SiO 2-Fe 2O 3载体的修饰，然后将其冷却至常温后，再研磨至粒径为0.1～0.2mm，即可制得氯吸附材料。
实施例2
一种垃圾焚烧中氯吸附材料的制备方法，其具体包括如下步骤：
(1)制备铁矿石粉：将天然铁矿石投入研磨机中研磨，然后过筛处理得到粒径为0.2～0.3mm的铁矿石粉；
(2)制备SiO 2：将石英石置于压片机中压成粉末，然后经烘干脱水后，通过60～100目的筛子进行过筛处理得SiO 2粉末；
(3)制备SiO 2-Fe 2O 3载体：采用化学气相沉积法，称取2Kg步骤(2)制得的SiO 2粉末置于化学气相沉积设备的石英管中，然后称取3.46Kg步骤(1)制得的铁矿石粉置于化学气相沉积设备的升华器中，其中，石英管与升华器为上下相对设置且连通，石英管内设有放置SiO 2粉末的平台，往石英管中通入空气并保持真空度为0.08MPa、空气流量为80mL·min -1的条件下，使SiO 2粉末呈流化状态，然后将石英管加热升温至200℃进行脱除SiO 2粉末中的水分，在保持3h后，将石英管的温度升温至400℃并保持，然后再往升华器中通入氮气并将升华器内的温度调节至110℃，待铁矿石粉完全升华后，将升华器的温度调节至400℃，使升华器和石英管形成反应室并令流化状态的SiO 2粉末与升华的铁矿石粉充分混合，令反应室在400℃的温度条件下保持2h后，使SiO 2粉末与铁矿石粉形成载体上的铁及铁化合物完全氧化后，使其降温至室温并对其进行室温干燥，然后再磨成粉末，最后将粉末置于管式炉中以3℃·min -1的升温速率升温至400℃并保持处理2h后，即可制得SiO 2-Fe 2O 3载体；
(4)取0.4Kg Ca(NO 3) 2·4H 2O作为前体，将其与体积为1L的去离子水配制成溶液，其中，纯度＞99.9％，粒径＜5μm；
(5)将步骤(4)制得的溶液加入到超声波清洗器的水槽中，然后将步骤(3)制得的SiO 2-Fe 2O 3载体加入到水槽中，然后以工作频率为40000Hz，工作功率为100W的工作参数对水槽中的混合体系进行超声波混合8h，混合期间保持水槽内的混合温度为90℃；
(6)将经过步骤(5)处理的SiO 2-Fe 2O 3载体置于900℃温度下煅烧1h，以去除其表面附着物上的NO x和制得CaO，实现CaO对SiO 2-Fe 2O 3载体的修饰，然后将其冷却至常温后，再研 磨至粒径为0.1～0.2mm，即可制得氯吸附材料。
实施例3
一种垃圾焚烧中氯吸附材料的制备方法，其具体包括如下步骤：
(1)制备铁矿石粉：将天然铁矿石投入研磨机中研磨，然后过筛处理得到粒径为0.2～0.3mm的铁矿石粉；
(2)制备SiO 2：将石英石置于压片机中压成粉末，然后经烘干脱水后，通过60～100目的筛子进行过筛处理得SiO 2粉末；
(3)制备SiO 2-Fe 2O 3载体：采用化学气相沉积法，称取2Kg步骤(2)制得的SiO 2粉末置于化学气相沉积设备的石英管中，然后称取5.36Kg步骤(1)制得的铁矿石粉置于化学气相沉积设备的升华器中，其中，石英管与升华器为上下相对设置且连通，石英管内设有放置SiO 2粉末的平台，往石英管中通入空气并保持真空度为0.08MPa、空气流量为80mL·min -1的条件下，使SiO 2粉末呈流化状态，然后将石英管加热升温至200℃进行脱除SiO 2粉末中的水分，在保持3h后，将石英管的温度升温至400℃并保持，然后再往升华器中通入氮气并将升华器内的温度调节至110℃，待铁矿石粉完全升华后，将升华器的温度调节至400℃，使升华器和石英管形成反应室并令流化状态的SiO 2粉末与升华的铁矿石粉充分混合，令反应室在400℃的温度条件下保持2h后，使SiO 2粉末与铁矿石粉形成载体上的铁及铁化合物完全氧化后，使其降温至室温并对其进行室温干燥，然后再磨成粉末，最后将粉末置于管式炉中以3℃·min -1的升温速率升温至400℃并保持处理1h后，即可制得SiO 2-Fe 2O 3载体；
(4)取0.8Kg Ca(NO 3) 2·4H 2O作为前体，将其与体积为1L的去离子水配制成溶液，其中，纯度＞99.9％，粒径＜5μm；
(5)将步骤(4)制得的溶液加入到超声波清洗器的水槽中，然后将步骤(3)制得的SiO 2-Fe 2O 3载体加入到水槽中，然后以工作频率为40000Hz，工作功率为100W的工作参数对水槽中的混合体系进行超声波混合9h，混合期间保持水槽内的混合温度为90℃；
(6)将经过步骤(5)处理的SiO 2-Fe 2O 3载体置于900℃温度下煅烧1h，以去除其表面附着物上的NO x和制得CaO，实现CaO对SiO 2-Fe 2O 3载体的修饰，然后将其冷却至常温后，再研磨至粒径为0.1～0.2mm，即可制得氯吸附材料。
实施例4
一种垃圾焚烧中氯吸附材料的制备方法，其具体包括如下步骤：
(1)制备铁矿石粉：将天然铁矿石投入研磨机中研磨，然后过筛处理得到粒径为0.2～0.3mm的铁矿石粉；
(2)制备SiO 2：将石英石置于压片机中压成粉末，然后经烘干脱水后，通过60～100目的筛子进行过筛处理得SiO 2粉末；
(3)制备SiO 2-Fe 2O 3载体：采用化学气相沉积法，称取2Kg步骤(2)制得的SiO 2粉末置于化学气相沉积设备的石英管中，然后称取3.46Kg步骤(1)制得的铁矿石粉置于化学气相沉积设备的升华器中，其中，石英管与升华器为上下相对设置且连通，石英管内设有放置SiO 2粉末的平台，往石英管中通入空气并保持真空度为0.08MPa、空气流量为80mL·min -1的条件下，使SiO 2粉末呈流化状态，然后将石英管加热升温至200℃进行脱除SiO 2粉末中的水分，在保持2h后，将石英管的温度升温至400℃并保持，然后再往升华器中通入氮气并将升华器内的温度调节至110℃，待铁矿石粉完全升华后，将升华器的温度调节至400℃，使升华器和石英管形成反应室并令流化状态的SiO 2粉末与升华的铁矿石粉充分混合，令反应室在400℃的温度条件下保持2h后，使SiO 2粉末与铁矿石粉形成载体上的铁及铁化合物完全氧化后，使其降温至室温并对其进行室温干燥，然后再磨成粉末，最后将粉末置于管式炉中以3℃·min -1的升温速率升温至400℃并保持处理1h后，即可制得SiO 2-Fe 2O 3载体；
(4)取1.2Kg Ca(NO 3) 2·4H 2O作为前体，将其与体积为1L的去离子水配制成溶液，其中，纯度＞99.9％，粒径＜5μm；
(5)将步骤(4)制得的溶液加入到超声波清洗器的水槽中，然后将步骤(3)制得的SiO 2-Fe 2O 3 载体加入到水槽中，然后以工作频率为40000Hz，工作功率为100W的工作参数对水槽中的混合体系进行超声波混合9h，混合期间保持水槽内的混合温度为90℃；
(6)将经过步骤(5)处理的SiO 2-Fe 2O 3载体置于900℃温度下煅烧1h，以去除其表面附着物上的NO x和制得CaO，实现CaO对SiO 2-Fe 2O 3载体的修饰，然后将其冷却至常温后，再研磨至粒径为0.1～0.2mm，即可制得氯吸附材料。
性能测试
将实施例1至4所制得的氯吸附材料分别置于不同的垃圾焚烧反应器中，然后将反应器内的温度在空气氛围下加热至900℃并保持30min以保证氯吸附材料完全氧化，继而投入助燃合成气(由1％HCl，21.9％CO，5.9％CH 4，12.7％H 2，7.8％CO 2和50.7％N 2组成)，通过空气喷嘴将气体推入焚烧炉中与垃圾一并燃烧，待燃烧完全后，测定烟气中HCl的含量，另，新增一不加入氯吸附材料的测试，以测得未添加氯吸附材料时，烟气中HCl的含量，所得结果如下：
Figure PCTCN2019073981-appb-000001
根据《生活垃圾焚烧污染控制标准》(GB 18485-2014)规定HCl的限值为60ppm(1小时均值)、50ppm(24小时均值)，由此可见，在加入本发明方案制得的氯吸附材料后能够使得垃圾焚烧中产生的氯类物质得以吸附且符合国家相关规定要求的指标。
以上所述为本发明的实施例，对于本领域的普通技术人员而言，根据本发明的教导，在不脱离本发明的原理和精神的情况下凡依本发明申请专利范围所做的均等变化、修改、替换和变型，皆应属本发明的涵盖范围。

Claims (9)

  1. 一种垃圾焚烧中氯吸附材料的制备方法，其特征在于：将天然铁矿石和石英粉混合后，往混合体系中加入CaO并通过超声浸渍对天然铁矿石和石英粉进行修饰，制得对氯类物质具有吸附性的氯吸附材料。
  2. 根据权利要求1所述的一种垃圾焚烧中氯吸附材料的制备方法，其特征在于：所述的氯类物质至少包括氯化氢和氯苯。
  3. 根据权利要求1所述的一种垃圾焚烧中氯吸附材料的制备方法，其特征在于：其具体包括如下步骤：
    (1)制备铁矿石粉：将天然铁矿石投入研磨机中研磨，然后过筛处理得到粒径为0.2～0.3mm的铁矿石粉；
    (2)制备SiO 2：将石英石置于压片机中压成粉末，然后经烘干脱水后，通过60～100目的筛子进行过筛处理得SiO 2粉末；
    (3)制备SiO 2-Fe 2O 3载体：采用化学气相沉积法，将步骤(2)制得的SiO 2粉末置于化学气相沉积设备的石英管中，然后按SiO 2粉末与铁矿石粉为1：1.7～2.7的比例称取步骤(1)制得的铁矿石粉置于化学气相沉积设备的升华器中，其中，石英管与升华器为上下相对设置且连通，石英管内设有放置SiO 2粉末的平台，往石英管中通入空气并保持真空度为0.08MPa的条件下，使SiO 2粉末呈流化状态，然后将石英管加热升温至200℃进行脱除SiO 2粉末中的水分，在保持2～3h后，将石英管的温度升温至400℃并保持，然后再往升华器中通入氮气并将升华器内的温度调节至110℃，待铁矿石粉完全升华后，将升华器的温度调节至400℃，使升华器和石英管形成反应室并令流化状态的SiO 2粉末与升华的铁矿石粉充分混合，令反应室在400℃的温度条件下保持2h后，使SiO 2粉末与铁矿石粉形成载体上的铁及铁化合物完全氧化后，使其降温至室温并对其进行室温干燥，然后再磨成粉末，最后将粉末置于管式炉中以3℃·min -1的升温速率升温至400℃并保持处理1～2h后，即可制得SiO 2-Fe 2O 3载体；
    (4)取Ca(NO 3) 2·4H 2O作为前体，将其按固液比为0.4～1.2Kg/L的比值配制成溶液；
    (5)将步骤(4)制得的溶液加入到超声波清洗器的水槽中，然后将步骤(3)制得的SiO 2-Fe 2O 3载体加入到水槽中进行超声波混合6～9h；
    (6)将经过步骤(5)处理的SiO 2-Fe 2O 3载体置于900℃温度下煅烧，以去除其表面附着物上的NO x和制得CaO，实现CaO对SiO 2-Fe 2O 3载体的修饰，然后将其冷却至常温后，再研磨至粒径为0.1～0.2mm，即可制得氯吸附材料。
  4. 根据权利要求3所述的一种垃圾焚烧中氯吸附材料的制备方法，其特征在于：步骤(1)、(2)和(4)中所添加的组分及份数如下：
    天然铁矿石    52份～67份；
    石英石            25份～30份；
    Ca(NO 3) 2·4H 2O      0.03份～0.05份。
  5. 根据权利要求3所述的一种垃圾焚烧中氯吸附材料的制备方法，其特征在于：步骤(3)中往石英管中通入空气的流量为80mL·min -1。
  6. 根据权利要求3所述的一种垃圾焚烧中氯吸附材料的制备方法，其特征在于：步骤(4)中Ca(NO 3) 2·4H 2O的纯度＞99.9％，粒径＜5μm。
  7. 根据权利要求3所述的一种垃圾焚烧中氯吸附材料的制备方法，其特征在于：步骤(5)中超声波清洗器在工作时，将水槽的温度维持在90℃。
  8. 根据权利要求3所述的一种垃圾焚烧中氯吸附材料的制备方法，其特征在于：步骤(5)中超声波清洗器的工作频率为40000Hz，工作功率为100W。
  9. 根据权利要求1至7之一所述的一种垃圾焚烧中氯吸附材料的制备方法制得所得的氯吸附材料的应用，其特征在于：将所制得的氯吸附材料用于垃圾焚烧中氯类物质的吸附。
PCT/CN2019/073981 2018-04-27 2019-01-30 一种垃圾焚烧中氯吸附材料的制备方法及其应用 WO2019205765A1 (zh)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP2020556839A JP7109580B2 (ja) 2018-04-27 2019-01-30 ごみ焼却に用いる塩素吸着材の調製方法およびその応用
DE112019002175.3T DE112019002175T5 (de) 2018-04-27 2019-01-30 Verfahren zum herstellen eines chloradsorptionsmaterials zur verwendung in der abfallverbrennung und anwendung des chloradsorptionsmaterials
US17/033,965 US11896955B2 (en) 2018-04-27 2020-09-28 Method for preparing chlorine adsorption material for use in waste incineration and application of chlorine adsorption material

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201810394407.5 2018-04-27
CN201810394407.5A CN108525639B (zh) 2018-04-27 2018-04-27 一种垃圾焚烧中氯吸附材料的制备方法及其应用

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US17/033,965 Continuation US11896955B2 (en) 2018-04-27 2020-09-28 Method for preparing chlorine adsorption material for use in waste incineration and application of chlorine adsorption material

Publications (1)

Publication Number Publication Date
WO2019205765A1 true WO2019205765A1 (zh) 2019-10-31

Family

ID=63479392

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2019/073981 WO2019205765A1 (zh) 2018-04-27 2019-01-30 一种垃圾焚烧中氯吸附材料的制备方法及其应用

Country Status (5)

Country Link
US (1) US11896955B2 (zh)
JP (1) JP7109580B2 (zh)
CN (1) CN108525639B (zh)
DE (1) DE112019002175T5 (zh)
WO (1) WO2019205765A1 (zh)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108525639B (zh) 2018-04-27 2019-07-30 福州大学 一种垃圾焚烧中氯吸附材料的制备方法及其应用
CN111974345B (zh) * 2020-08-24 2021-11-19 华中科技大学 一种基于堇青石载体的重金属固化剂、制备方法及其应用

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000033947A1 (de) * 1998-12-07 2000-06-15 Bbp Environment Gmbh Verfahren zur verringerung der konzentration von pcdd und pcdf im abgasstrom einer sinteranlage und sinteranlage zur durchführung des verfahrens
CN1623648A (zh) * 2004-10-29 2005-06-08 清华大学 用于焚烧烟气净化的改性钙基吸附剂及其制备方法
CN103041769A (zh) * 2012-12-31 2013-04-17 东南大学 高温脱氯剂及其制备方法
CN104930518A (zh) * 2015-05-18 2015-09-23 华中科技大学 一种低碳处理固体垃圾并抑制二噁英生成的方法
CN108525639A (zh) * 2018-04-27 2018-09-14 福州大学 一种垃圾焚烧中氯吸附材料的制备方法及其应用

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3646245B2 (ja) * 1998-11-13 2005-05-11 同和鉱業株式会社 重金属含有飛灰の処理方法
JP2000335916A (ja) 1999-05-31 2000-12-05 Akio Henmi スラグより人工ゼオライトを製造する方法およびその装置
JP4084533B2 (ja) * 2000-07-13 2008-04-30 新日本製鐵株式会社 ダイオキシン類の吸着除去方法および分解方法
JP4593964B2 (ja) 2003-11-06 2010-12-08 義雄 小林 熱分解ガスの乾式精製方法
US20070163476A1 (en) 2006-01-18 2007-07-19 Comrie Douglas C Apparatus for delivery of sorbent to a furnace during combustion
PL2516926T3 (pl) * 2009-12-22 2017-11-30 Accordant Energy, Llc Przerobione surowce paliwowe zawierające sorbent
CN101773768A (zh) 2010-03-16 2010-07-14 长春惠工净化工业有限公司 从气体中脱除HCl的干法脱氯剂及其制备方法
CA2846324A1 (en) 2013-03-15 2014-09-15 Nox Ii, Ltd. Reducing environmental pollution and fouling when burning coal
JP2015014594A (ja) 2013-06-07 2015-01-22 株式会社オプテック 無機系発泡体による放射性物質の吸着材及びその吸着方法
CN105135447A (zh) * 2015-09-25 2015-12-09 华中科技大学 一种固定挥发性重金属铬、镉、铅的方法
CN106268832B (zh) 2016-09-19 2018-10-23 武汉纺织大学 一种新型高效脱氯剂及其制备方法
CN107930579B (zh) 2017-11-29 2020-12-25 安徽工业大学 一种用于烟气脱砷的吸附剂及其脱砷方法

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000033947A1 (de) * 1998-12-07 2000-06-15 Bbp Environment Gmbh Verfahren zur verringerung der konzentration von pcdd und pcdf im abgasstrom einer sinteranlage und sinteranlage zur durchführung des verfahrens
CN1623648A (zh) * 2004-10-29 2005-06-08 清华大学 用于焚烧烟气净化的改性钙基吸附剂及其制备方法
CN103041769A (zh) * 2012-12-31 2013-04-17 东南大学 高温脱氯剂及其制备方法
CN104930518A (zh) * 2015-05-18 2015-09-23 华中科技大学 一种低碳处理固体垃圾并抑制二噁英生成的方法
CN108525639A (zh) * 2018-04-27 2018-09-14 福州大学 一种垃圾焚烧中氯吸附材料的制备方法及其应用

Also Published As

Publication number Publication date
JP2021519689A (ja) 2021-08-12
US20210031170A1 (en) 2021-02-04
JP7109580B2 (ja) 2022-07-29
US11896955B2 (en) 2024-02-13
DE112019002175T5 (de) 2021-01-07
CN108525639B (zh) 2019-07-30
CN108525639A (zh) 2018-09-14

Similar Documents

Publication Publication Date Title
CN106944053A (zh) 一种污泥炭基类Fenton催化剂及其制备方法和应用
CN110078070A (zh) 一种用于含油污水处理的含油污泥基吸附碳材料的制备方法
CN106076335B (zh) 一种非均相Fenton催化剂的制备方法和应用
CN105903436A (zh) 一种生物质碳负载纳米零价铁材料、制备方法及其应用
CN106423051A (zh) 一种磁性活化水热生物炭微球的制备方法与应用
CN111068612B (zh) 利用固体废弃物制备类沸石型多孔材料的方法、类沸石型多孔材料及其应用
CN108380214B (zh) 一种改性海泡石的制备及应用于废水处理的方法
CN104525119A (zh) 一种g-C3N4/ZnO/活性炭的功能性炭吸附材料及其制备方法
CN104930518B (zh) 一种低碳处理固体垃圾并抑制二噁英生成的方法
CN109499573A (zh) 一种磁性木基材料的原位制备方法
CN109835897B (zh) 一种金属/杂原子改性白酒糟基活性炭及其制备方法
CN104858446A (zh) 一种零价铁陶粒及其制备方法
CN106115698A (zh) 一种利用回收废炭制备含氮多孔炭的方法及其产品和应用
CN108786779A (zh) 一种石墨炔/多孔二氧化钛光催化剂及其制备方法和应用
CN106824069B (zh) 用于处理含砷废水的稀土掺杂铁炭材料的制备方法
CN110508236A (zh) 一种微波协同处理废渣制备高效烧结烟气吸附剂及方法
CN109569525A (zh) 一种氨基修饰磁性稻壳生物炭的制备及利用其吸附水体中铀的方法
WO2019205765A1 (zh) 一种垃圾焚烧中氯吸附材料的制备方法及其应用
CN103007954B (zh) 一种多相催化臭氧氧化催化剂及其制备方法
CN105709689A (zh) 碳基功能材料及其制备方法
CN108855018A (zh) 一种精细化工废气吸附剂及其制备方法
CN105921138A (zh) 一种用于吸附半挥发性重金属的高岭土改性制备方法
CN103978006A (zh) 一种高效低耗低污染的铬渣热解处理方法
CN110115975A (zh) 一种氧化锰改性氮化碳吸附剂及其制备方法与应用
CN108579715A (zh) 一种多孔易分离二氧化钛纳米催化剂的制备方法

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 19792695

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 2020556839

Country of ref document: JP

Kind code of ref document: A

122 Ep: pct application non-entry in european phase

Ref document number: 19792695

Country of ref document: EP

Kind code of ref document: A1