WO2018121516A1 - 一种甲醛吸附材料 - Google Patents

一种甲醛吸附材料 Download PDF

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WO2018121516A1
WO2018121516A1 PCT/CN2017/118570 CN2017118570W WO2018121516A1 WO 2018121516 A1 WO2018121516 A1 WO 2018121516A1 CN 2017118570 W CN2017118570 W CN 2017118570W WO 2018121516 A1 WO2018121516 A1 WO 2018121516A1
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parts
formaldehyde
product
sepiolite
glycine
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PCT/CN2017/118570
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English (en)
French (fr)
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顾黎明
张宇
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苏州律点信息科技有限公司
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Publication of WO2018121516A1 publication Critical patent/WO2018121516A1/zh

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    • 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
    • B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26—Synthetic macromolecular compounds
    • B01J20/262—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon to carbon unsaturated bonds, e.g. obtained by polycondensation
    • 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
    • B01J20/0203—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0211—Compounds of Ti, Zr, Hf
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • 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
    • B01J20/0203—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0274—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04 characterised by the type of anion
    • B01J20/0277—Carbonates of compounds other than those provided for in B01J20/043
    • 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
    • B01J20/0203—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0274—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04 characterised by the type of anion
    • B01J20/0292—Phosphates of compounds other than those provided for in B01J20/048
    • 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
    • B01J20/0203—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0274—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04 characterised by the type of anion
    • B01J20/0296—Nitrates of compounds other than those provided for in 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
    • B01J20/02—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
    • B01J20/043—Carbonates or bicarbonates, e.g. limestone, dolomite, aragonite
    • 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
    • B01J20/046—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 containing halogens, e.g. halides
    • 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
    • B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
    • 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
    • B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/708—Volatile organic compounds V.O.C.'s
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/06—Polluted air

Definitions

  • the invention relates to the field of adsorbing materials, in particular to a formaldehyde adsorbing material.
  • Formaldehyde purification adsorbent refers to the adsorption material mainly used in household life to adsorb formaldehyde. It generally has the following characteristics: 1) it has a large specific surface and strong adsorption capacity; 2) it has high adsorption performance for gas and can be quickly Adsorption; 3) Environmental protection, no pollution, low manufacturing costs.
  • Formaldehyde purification adsorbent can effectively absorb harmful substances such as formaldehyde, benzene and xylene released from home decoration.
  • the main component is activated silicon, which is an amorphous substance. It is made from natural quartz sand and processed by special processing. It has a large specific surface area and a rich pore structure matching the size of indoor harmful gas molecules. It also has the functions of regulating air humidity, deodorizing mold, deodorizing and sterilizing, and completely eliminating indoor environmental pollution.
  • various active silicon has been widely used in drug purification, DNA separation, food drying, high-precision electronics, advanced cosmetics, sewage purification, beer purification, advanced coatings and resin production or preservation.
  • the product of the invention is chemically stable and can effectively and stably adsorb the slowly released harmful gas for a long time.
  • the invention provides a formaldehyde adsorption material for the technical problems of low formaldehyde removal rate, short service life and slow adsorption speed.
  • a formaldehyde adsorption material the raw materials are mixed in parts by weight, such as: 100 parts of activated carbon, 10-30 parts of calcium carbonate, 20-60 parts of ethanol, 5-25 parts of medical stone, 20-40 parts of sepiolite, glycine 15 -35 parts, 1-20 parts of perlite, 1-5 parts of sodium nitrate, 6-10 parts of ammonium hydrogencarbonate, 2-6 parts of titanium dioxide, 3-7 parts of methyl cellulose, 13-17 parts of iron orthophosphate, magnesium chloride 5-25 parts, 12-18 parts of talc.
  • the raw material of the formaldehyde adsorbing material is divided into parts by weight: 100 parts of activated carbon, 15-25 parts of calcium carbonate, 30-50 parts of ethanol, and 10-20 parts of medical stone. 25-35 parts of sepiolite, 20-30 parts of glycine, 5-15 parts of perlite, 2-4 parts of sodium nitrate, 7-9 parts of ammonium hydrogencarbonate, 3-5 parts of titanium dioxide, 4-6 parts of methyl cellulose , 14-16 parts of iron orthophosphate, 10-20 parts of magnesium chloride, 13-17 parts of talc.
  • the raw material of the formaldehyde adsorbing material is divided into parts by weight: 100 parts of activated carbon, 15 parts of calcium carbonate, 30 parts of ethanol, 10 parts of medical stone, 25 parts of sepiolite, 20 parts of glycine, 5 parts of perlite, 2 parts of sodium nitrate, 7 parts of ammonium hydrogencarbonate, 3 parts of titanium dioxide, 4 parts of methyl cellulose, 14 parts of iron orthophosphate, 10 parts of magnesium chloride, and 13 parts of talc.
  • the raw material of the formaldehyde adsorbing material is divided into parts by weight: 100 parts of activated carbon, 25 parts of calcium carbonate, 50 parts of ethanol, 20 parts of medical stone, 35 parts of sepiolite, 30 parts of glycine, 15 parts of perlite, 4 parts of sodium nitrate, 9 parts of ammonium hydrogencarbonate, 5 parts of titanium dioxide, 6 parts of methyl cellulose, 16 parts of iron orthophosphate, 20 parts of magnesium chloride and 17 parts of talc.
  • the raw material of the formaldehyde adsorbing material is divided into parts by weight: 100 parts of activated carbon, 20 parts of calcium carbonate, 40 parts of ethanol, 15 parts of medical stone, 30 parts of sepiolite, 25 parts of glycine, 10 parts of perlite, 3 parts of sodium nitrate, 8 parts of ammonium hydrogencarbonate, 4 parts of titanium dioxide, 5 parts of methyl cellulose, 15 parts of iron orthophosphate, 15 parts of magnesium chloride and 15 parts of talc.
  • the formaldehyde adsorbing material of the present invention has the following technical effects: 1.
  • the formaldehyde removal rate of the product is as high as 98-99.8%; 2.
  • the wear resistance is strong, the service life is long, and the product can be repeated.
  • Ethanol, glycine, sodium nitrate, ammonium hydrogencarbonate, titanium oxide, methyl cellulose and iron orthophosphate were placed in a reaction vessel equipped with a stirrer and a thermometer, and the temperature was raised to 60 ° C, stirred for 30 minutes, and the stirring speed was 800 rpm.
  • the activated carbon, calcium carbonate, medical stone, sepiolite, magnesium chloride and talc are dried at a constant temperature at 80 ° C, and then combined with the product which is stirred evenly in the previous step, mixed for 2 hours, and then the mixed product is placed in a vacuum drying oven. In the middle, it can be dried overnight at 25 °C.
  • the formaldehyde removal rate of the product is up to 98%; the wear resistance is strong, the service life is long, it can be reused, the environment is green; the adsorption speed is fast, the adsorption range is wide, and the product is placed in the formaldehyde content of 500 ⁇ g/m 3 in a confined space for 48 hours, formaldehyde
  • the concentration is 8 ⁇ g/m 3 ; the preparation method is simple, the cost is low, the operability is strong, and the existing materials can be widely produced and continuously replaced.
  • 100 parts of activated carbon, 30 parts of calcium carbonate, 60 parts of ethanol, 25 parts of medical stone, 40 parts of sepiolite, 35 parts of glycine, 20 parts of perlite, 5 parts of sodium nitrate, ammonium bicarbonate are weighed according to the parts by weight. 10 parts, 6 parts of titanium dioxide, 7 parts of methyl cellulose, 17 parts of iron orthophosphate, 25 parts of magnesium chloride, and 18 parts of talc.
  • Ethanol, glycine, sodium nitrate, ammonium hydrogencarbonate, titanium oxide, methyl cellulose and iron orthophosphate were placed in a reaction vessel equipped with a stirrer and a thermometer, and the temperature was raised to 80 ° C, stirred for 70 minutes, and the stirring speed was 1200 rpm.
  • Activated carbon, calcium carbonate, medical stone, sepiolite, magnesium chloride and talc are dried at 120 ° C, then combined with the product which was stirred in the previous step, mixed for 6 hours, and then the mixed product is placed in a vacuum drying oven. In the middle, it can be dried overnight at 45 °C.
  • the formaldehyde removal rate of the product is up to 98.5%; the wear resistance is strong, the service life is long, it can be reused, it is green and environmentally friendly; the adsorption speed is fast, the adsorption range is wide, and the product is placed in the formaldehyde content of 500 ⁇ g/m 3 in a confined space for 40h, formaldehyde
  • the concentration is 6 ⁇ g/m 3 ; the preparation method is simple, the cost is low, the operability is strong, and the existing materials can be widely produced and continuously replaced.
  • Ethanol, glycine, sodium nitrate, ammonium hydrogencarbonate, titanium oxide, methyl cellulose and iron orthophosphate were placed in a reaction vessel equipped with a stirrer and a thermometer, and the temperature was raised to 60 ° C, stirred for 30 minutes, and the stirring speed was 800 rpm.
  • the activated carbon, calcium carbonate, medical stone, sepiolite, magnesium chloride and talc are dried at a constant temperature at 80 ° C, and then combined with the product which is stirred evenly in the previous step, mixed for 2 hours, and then the mixed product is placed in a vacuum drying oven. In the middle, it can be dried overnight at 25 °C.
  • the formaldehyde removal rate of the product is up to 99%; the wear resistance is strong, the service life is long, it can be reused, it is green and environmentally friendly; the adsorption speed is fast, the adsorption range is wide, and the product is placed in the formaldehyde content of 450 ⁇ g/m 3 in a confined space for 44h, formaldehyde
  • the concentration is 5 ⁇ g/m 3 ; the preparation method is simple, the cost is low, the operability is strong, and the existing materials can be widely produced and continuously replaced.
  • Ethanol, glycine, sodium nitrate, ammonium hydrogencarbonate, titanium oxide, methyl cellulose and iron orthophosphate were placed in a reaction vessel equipped with a stirrer and a thermometer, and the temperature was raised to 80 ° C, stirred for 70 minutes, and the stirring speed was 1200 rpm.
  • Activated carbon, calcium carbonate, medical stone, sepiolite, magnesium chloride and talc are dried at 120 ° C, then combined with the product which was stirred in the previous step, mixed for 6 hours, and then the mixed product is placed in a vacuum drying oven. In the middle, it can be dried overnight at 45 °C.
  • the formaldehyde removal rate of the product is up to 99.5%; the wear resistance is strong, the service life is long, it can be reused, it is green and environmentally friendly; the adsorption speed is fast, the adsorption range is wide, and the product is placed in the formaldehyde content of 400 ⁇ g/m 3 in a confined space for 48h, formaldehyde
  • the concentration is 2 ⁇ g/m 3 ; the preparation method is simple, the cost is low, the operability is strong, and the existing materials can be widely produced and continuously replaced.
  • activated carbon 100 parts of activated carbon, 20 parts of calcium carbonate, 40 parts of ethanol, 15 parts of medical stone, 30 parts of sepiolite, 25 parts of glycine, 10 parts of perlite, 3 parts of sodium nitrate, ammonium bicarbonate were weighed according to the parts by weight. 8 parts, 4 parts of titanium dioxide, 5 parts of methyl cellulose, 15 parts of iron orthophosphate, 15 parts of magnesium chloride, and 15 parts of talc.
  • Ethanol, glycine, sodium nitrate, ammonium hydrogencarbonate, titanium oxide, methyl cellulose and iron orthophosphate were placed in a reaction vessel equipped with a stirrer and a thermometer, and the temperature was raised to 70 ° C, stirred for 50 minutes, and the stirring speed was 1000 rpm.
  • the activated carbon, calcium carbonate, medical stone, sepiolite, magnesium chloride and talc are dried at a constant temperature at 100 ° C, and then combined with the product which is stirred evenly in the previous step, mixed for 4 hours, and then the mixed product is placed in a vacuum drying oven. In the middle, it can be dried overnight at 35 °C.
  • the formaldehyde removal rate of the product is up to 99.8%; the wear resistance is strong, the service life is long, it can be reused, it is green and environmentally friendly; the adsorption speed is fast, the adsorption range is wide, and the product is placed in the formaldehyde content of 500 ⁇ g/m 3 in a confined space for 40h, formaldehyde
  • the concentration is 1 ⁇ g/m 3 ; the preparation method is simple, the cost is low, the operability is strong, and the existing materials can be widely produced and continuously replaced.

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  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Medicinal Preparation (AREA)
  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)

Abstract

一种甲醛吸附材料，其原料按重量份数配比如下：活性炭100份，碳酸钙10‑30份，乙醇20‑60份，麦饭石5‑25份，海泡石20‑40份，甘氨酸15‑35份，珍珠岩1‑20份，硝酸钠1‑5份，碳酸氢铵6‑10份，二氧化钛2‑6份，甲基纤维素3‑7份，正磷酸铁13‑17份，氯化镁5‑25份，滑石粉12‑18份。该产品甲醛去除率高达98‑99.8%；耐磨性强，使用寿命长，可以重复使用，绿色环保；吸附速度快，吸附范围广，取本品放在甲醛含量400‑500μg/m3密闭空间内40‑48h后，甲醛浓度为1‑8μg/m3；制备方法简单，成本低廉，操作性强，可以广泛生产并不断代替现有材料。

Description

一种甲醛吸附材料 技术领域
本发明涉及吸附材料领域，尤其涉及一种甲醛吸附材料。
 背景技术
甲醛净化吸附剂是指主要用于家居生活之中用来吸附甲醛的吸附材料，一般具有如下特点：1）比表面极大，吸附能力强；2）对气体有较高的吸附性能，能迅速吸附；3）环保，无污染，制造成本低。
甲醛净化吸附剂可有效吸附因家居装修而释放出来的甲醛、苯、二甲苯等有害物质，主要成分是活性硅，属非晶态物质，取材于天然的石英砂，经过特殊加工工艺处理提炼而成，使其具备了大比表面积以及丰富的与室内有害气体分子大小相匹配的孔隙结构，同时还具有调节空气湿度、去味防霉、除臭杀菌等功效，彻底清除室内环境污染。加之近年来不断地创新开发，各种活性硅已被广泛用于药物提纯、DNA分离、食品干燥、高精电子、高级化妆品、污水净化、啤酒提纯、高级涂料以及树脂生产或保存等方面。
室内甲醛、苯等有害气体作为家居生活中不可避免的隐性杀手，时刻威胁人们的身体健康。而这些有害气体的释放是一个缓慢的过程，即使再好的空气净洁产品，也不可能一次性、彻底净化空气。
随着社会城市化、科技化、人性化的发展，设计一种甲醛去除率高、使用寿命长和吸附速度快的甲醛吸附材料以满足市场需求，是非常必要的。本发明产品化学性质稳定，能够长期有效稳定地吸附缓慢释放的有害气体。
 技术问题
本发明针对现有甲醛吸附剂去除率较低、使用寿命短和吸附速度慢的技术问题而提供一种甲醛吸附材料。
 技术解决方案
一种甲醛吸附材料，原料按重量份数配比如下：活性炭100份，碳酸钙10-30份，乙醇20-60份，麦饭石5-25份，海泡石20-40份，甘氨酸15-35份，珍珠岩1-20份，硝酸钠1-5份，碳酸氢铵6-10份，二氧化钛2-6份，甲基纤维素3-7份，正磷酸铁13-17份，氯化镁5-25份，滑石粉12-18份。
作为本发明的一种优选技术方案：所述甲醛吸附材料的原料按重量份数配比如下：活性炭100份，碳酸钙15-25份，乙醇30-50份，麦饭石10-20份，海泡石25-35份，甘氨酸20-30份，珍珠岩5-15份，硝酸钠2-4份，碳酸氢铵7-9份，二氧化钛3-5份，甲基纤维素4-6份，正磷酸铁14-16份，氯化镁10-20份，滑石粉13-17份。
作为本发明的一种优选技术方案：所述甲醛吸附材料的原料按重量份数配比如下：活性炭100份，碳酸钙15份，乙醇30份，麦饭石10份，海泡石25份，甘氨酸20份，珍珠岩5份，硝酸钠2份，碳酸氢铵7份，二氧化钛3份，甲基纤维素4份，正磷酸铁14份，氯化镁10份，滑石粉13份。
作为本发明的一种优选技术方案：所述甲醛吸附材料的原料按重量份数配比如下：活性炭100份，碳酸钙25份，乙醇50份，麦饭石20份，海泡石35份，甘氨酸30份，珍珠岩15份，硝酸钠4份，碳酸氢铵9份，二氧化钛5份，甲基纤维素6份，正磷酸铁16份，氯化镁20份，滑石粉17份。
作为本发明的一种优选技术方案：所述甲醛吸附材料的原料按重量份数配比如下：活性炭100份，碳酸钙20份，乙醇40份，麦饭石15份，海泡石30份，甘氨酸25份，珍珠岩10份，硝酸钠3份，碳酸氢铵8份，二氧化钛4份，甲基纤维素5份，正磷酸铁15份，氯化镁15份，滑石粉15份。
 有益效果
本发明所述一种甲醛吸附材料采用以上技术方案和现有技术相比，具有以下技术效果：1、产品甲醛去除率高达98-99.8%；2、耐磨性强，使用寿命长，可以重复使用，绿色环保；3、吸附速度快，吸附范围广，取本品放在甲醛含量400-500μg/m 3密闭空间内40-48h后，甲醛浓度为1-8μg/m 3；4、制备方法简单，成本低廉，操作性强，可以广泛生产并不断代替现有材料。 
本发明的实施方式
下面结合实施例对本发明做进一步描述。
实施例 1
按重量份数配比称取活性炭100份，碳酸钙10份，乙醇20份，麦饭石5份，海泡石20份，甘氨酸15份，珍珠岩1份，硝酸钠1份，碳酸氢铵6份，二氧化钛2份，甲基纤维素3份，正磷酸铁13份，氯化镁5份，滑石粉12份。
将乙醇、甘氨酸、硝酸钠、碳酸氢铵、二氧化钛、甲基纤维素和正磷酸铁投入设有搅拌器和温度计的反应釜中，升温至60℃，搅拌30min，搅拌速度为800转/分钟。
将活性炭、碳酸钙、麦饭石、海泡石、氯化镁和滑石粉在80℃下恒温干燥，然后再与上一步搅拌均匀的产物合并，混合2h，再将混合后的产物放入真空干燥箱中，在25℃下干燥过夜即可。
产品甲醛去除率高达98%；耐磨性强，使用寿命长，可以重复使用，绿色环保；吸附速度快，吸附范围广，取本品放在甲醛含量500μg/m 3密闭空间内48h后，甲醛浓度为8μg/m 3；制备方法简单，成本低廉，操作性强，可以广泛生产并不断代替现有材料。
实施例 2
按重量份数配比称取活性炭100份，碳酸钙30份，乙醇60份，麦饭石25份，海泡石40份，甘氨酸35份，珍珠岩20份，硝酸钠5份，碳酸氢铵10份，二氧化钛6份，甲基纤维素7份，正磷酸铁17份，氯化镁25份，滑石粉18份。
将乙醇、甘氨酸、硝酸钠、碳酸氢铵、二氧化钛、甲基纤维素和正磷酸铁投入设有搅拌器和温度计的反应釜中，升温至80℃，搅拌70min，搅拌速度为1200转/分钟。
将活性炭、碳酸钙、麦饭石、海泡石、氯化镁和滑石粉在120℃下恒温干燥，然后再与上一步搅拌均匀的产物合并，混合6h，再将混合后的产物放入真空干燥箱中，在45℃下干燥过夜即可。
产品甲醛去除率高达98.5%；耐磨性强，使用寿命长，可以重复使用，绿色环保；吸附速度快，吸附范围广，取本品放在甲醛含量500μg/m 3密闭空间内40h后，甲醛浓度为6μg/m 3；制备方法简单，成本低廉，操作性强，可以广泛生产并不断代替现有材料。
实施例 3
按重量份数配比称取活性炭100份，碳酸钙15份，乙醇30份，麦饭石10份，海泡石25份，甘氨酸20份，珍珠岩5份，硝酸钠2份，碳酸氢铵7份，二氧化钛3份，甲基纤维素4份，正磷酸铁14份，氯化镁10份，滑石粉13份。
将乙醇、甘氨酸、硝酸钠、碳酸氢铵、二氧化钛、甲基纤维素和正磷酸铁投入设有搅拌器和温度计的反应釜中，升温至60℃，搅拌30min，搅拌速度为800转/分钟。
将活性炭、碳酸钙、麦饭石、海泡石、氯化镁和滑石粉在80℃下恒温干燥，然后再与上一步搅拌均匀的产物合并，混合2h，再将混合后的产物放入真空干燥箱中，在25℃下干燥过夜即可。
产品甲醛去除率高达99%；耐磨性强，使用寿命长，可以重复使用，绿色环保；吸附速度快，吸附范围广，取本品放在甲醛含量450μg/m 3密闭空间内44h后，甲醛浓度为5μg/m 3；制备方法简单，成本低廉，操作性强，可以广泛生产并不断代替现有材料。
实施例 4
按重量份数配比称取活性炭100份，碳酸钙25份，乙醇50份，麦饭石20份，海泡石35份，甘氨酸30份，珍珠岩15份，硝酸钠4份，碳酸氢铵9份，二氧化钛5份，甲基纤维素6份，正磷酸铁16份，氯化镁20份，滑石粉17份。
将乙醇、甘氨酸、硝酸钠、碳酸氢铵、二氧化钛、甲基纤维素和正磷酸铁投入设有搅拌器和温度计的反应釜中，升温至80℃，搅拌70min，搅拌速度为1200转/分钟。
将活性炭、碳酸钙、麦饭石、海泡石、氯化镁和滑石粉在120℃下恒温干燥，然后再与上一步搅拌均匀的产物合并，混合6h，再将混合后的产物放入真空干燥箱中，在45℃下干燥过夜即可。
产品甲醛去除率高达99.5%；耐磨性强，使用寿命长，可以重复使用，绿色环保；吸附速度快，吸附范围广，取本品放在甲醛含量400μg/m 3密闭空间内48h后，甲醛浓度为2μg/m 3；制备方法简单，成本低廉，操作性强，可以广泛生产并不断代替现有材料。
实施例 5
按重量份数配比称取活性炭100份，碳酸钙20份，乙醇40份，麦饭石15份，海泡石30份，甘氨酸25份，珍珠岩10份，硝酸钠3份，碳酸氢铵8份，二氧化钛4份，甲基纤维素5份，正磷酸铁15份，氯化镁15份，滑石粉15份。
将乙醇、甘氨酸、硝酸钠、碳酸氢铵、二氧化钛、甲基纤维素和正磷酸铁投入设有搅拌器和温度计的反应釜中，升温至70℃，搅拌50min，搅拌速度为1000转/分钟。
将活性炭、碳酸钙、麦饭石、海泡石、氯化镁和滑石粉在100℃下恒温干燥，然后再与上一步搅拌均匀的产物合并，混合4h，再将混合后的产物放入真空干燥箱中，在35℃下干燥过夜即可。
产品甲醛去除率高达99.8%；耐磨性强，使用寿命长，可以重复使用，绿色环保；吸附速度快，吸附范围广，取本品放在甲醛含量500μg/m 3密闭空间内40h后，甲醛浓度为1μg/m 3；制备方法简单，成本低廉，操作性强，可以广泛生产并不断代替现有材料。
以上实施例中的所有组分均可以商业购买。
上述实施例只是用于对本发明的内容进行阐述，而不是限制，因此在和本发明的权利要求书相当的含义和范围内的任何改变，都应该认为是包括在权利要求书的范围内。

Claims (5)

  1. 一种甲醛吸附材料，其特征在于：所述甲醛吸附材料，其原料按重量份数配比如下：活性炭100份，碳酸钙10-30份，乙醇20-60份，麦饭石5-25份，海泡石20-40份，甘氨酸15-35份，珍珠岩1-20份，硝酸钠1-5份，碳酸氢铵6-10份，二氧化钛2-6份，甲基纤维素3-7份，正磷酸铁13-17份，氯化镁5-25份，滑石粉12-18份。
  2. 根据权利要求1所述的一种甲醛吸附材料，其特征在于：所述甲醛吸附材料，其原料按重量份数配比如下：活性炭100份，碳酸钙15-25份，乙醇30-50份，麦饭石10-20份，海泡石25-35份，甘氨酸20-30份，珍珠岩5-15份，硝酸钠2-4份，碳酸氢铵7-9份，二氧化钛3-5份，甲基纤维素4-6份，正磷酸铁14-16份，氯化镁10-20份，滑石粉13-17份。
  3. 根据权利要求1所述的一种甲醛吸附材料，其特征在于：所述甲醛吸附材料，其原料按重量份数配比如下：活性炭100份，碳酸钙15份，乙醇30份，麦饭石10份，海泡石25份，甘氨酸20份，珍珠岩5份，硝酸钠2份，碳酸氢铵7份，二氧化钛3份，甲基纤维素4份，正磷酸铁14份，氯化镁10份，滑石粉13份。
  4. 根据权利要求1所述的一种甲醛吸附材料，其特征在于：所述甲醛吸附材料，其原料按重量份数配比如下：活性炭100份，碳酸钙25份，乙醇50份，麦饭石20份，海泡石35份，甘氨酸30份，珍珠岩15份，硝酸钠4份，碳酸氢铵9份，二氧化钛5份，甲基纤维素6份，正磷酸铁16份，氯化镁20份，滑石粉17份。
  5. 根据权利要求1所述的一种甲醛吸附材料，其特征在于：所述甲醛吸附材料，其原料按重量份数配比如下：活性炭100份，碳酸钙20份，乙醇40份，麦饭石15份，海泡石30份，甘氨酸25份，珍珠岩10份，硝酸钠3份，碳酸氢铵8份，二氧化钛4份，甲基纤维素5份，正磷酸铁15份，氯化镁15份，滑石粉15份。
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