CN116747833B - Activated carbon wood fiber foam and preparation method thereof - Google Patents
Activated carbon wood fiber foam and preparation method thereof Download PDFInfo
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 258
- 239000006260 foam Substances 0.000 title claims abstract description 72
- 238000002360 preparation method Methods 0.000 title claims abstract description 27
- 229920002522 Wood fibre Polymers 0.000 title claims abstract description 14
- 239000002025 wood fiber Substances 0.000 title claims abstract description 14
- 239000002023 wood Substances 0.000 claims abstract description 111
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims abstract description 86
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 53
- 239000011780 sodium chloride Substances 0.000 claims abstract description 43
- 239000011259 mixed solution Substances 0.000 claims abstract description 38
- 239000000243 solution Substances 0.000 claims abstract description 32
- 239000000463 material Substances 0.000 claims abstract description 19
- 238000003756 stirring Methods 0.000 claims abstract description 17
- 239000000725 suspension Substances 0.000 claims abstract description 17
- 239000000843 powder Substances 0.000 claims abstract description 11
- 238000004108 freeze drying Methods 0.000 claims abstract description 5
- 230000008859 change Effects 0.000 claims abstract description 4
- 239000000835 fiber Substances 0.000 claims abstract description 3
- -1 salt ions Chemical class 0.000 claims abstract description 3
- 238000000034 method Methods 0.000 claims description 12
- 239000012153 distilled water Substances 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 5
- 239000002699 waste material Substances 0.000 claims description 4
- 238000007710 freezing Methods 0.000 claims description 2
- 230000008014 freezing Effects 0.000 claims description 2
- 239000002994 raw material Substances 0.000 abstract description 4
- 238000006243 chemical reaction Methods 0.000 abstract description 2
- 238000000227 grinding Methods 0.000 abstract description 2
- 229920000620 organic polymer Polymers 0.000 abstract description 2
- 239000002861 polymer material Substances 0.000 abstract description 2
- 229910052799 carbon Inorganic materials 0.000 abstract 3
- 231100000252 nontoxic Toxicity 0.000 abstract 1
- 230000003000 nontoxic effect Effects 0.000 abstract 1
- 238000010612 desalination reaction Methods 0.000 description 27
- 238000001704 evaporation Methods 0.000 description 22
- 230000008020 evaporation Effects 0.000 description 22
- 239000000203 mixture Substances 0.000 description 19
- 238000002474 experimental method Methods 0.000 description 17
- 238000010586 diagram Methods 0.000 description 13
- 239000007787 solid Substances 0.000 description 8
- 238000009413 insulation Methods 0.000 description 7
- 239000013505 freshwater Substances 0.000 description 6
- 229910021389 graphene Inorganic materials 0.000 description 6
- 239000002351 wastewater Substances 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- 239000002028 Biomass Substances 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000003575 carbonaceous material Substances 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000037361 pathway Effects 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 229910021393 carbon nanotube Inorganic materials 0.000 description 1
- 239000002041 carbon nanotube Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 238000000909 electrodialysis Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000010097 foam moulding Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 238000002329 infrared spectrum Methods 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 230000031700 light absorption Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical class C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 150000004767 nitrides Chemical class 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000007146 photocatalysis Methods 0.000 description 1
- 230000001699 photocatalysis Effects 0.000 description 1
- 229920001690 polydopamine Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920000128 polypyrrole Polymers 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 230000005068 transpiration Effects 0.000 description 1
Classifications
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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
- B01J20/02—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
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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
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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
- B01J20/28—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
- B01J20/28011—Other properties, e.g. density, crush strength
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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
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—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 form
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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
- B01J20/30—Processes for preparing, regenerating, or reactivating
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/285—Treatment of water, waste water, or sewage by sorption using synthetic organic sorbents
-
- 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
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4812—Sorbents characterised by the starting material used for their preparation the starting material being of organic character
- B01J2220/4825—Polysaccharides or cellulose materials, e.g. starch, chitin, sawdust, wood, straw, cotton
-
- 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
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4875—Sorbents characterised by the starting material used for their preparation the starting material being a waste, residue or of undefined composition
- B01J2220/4887—Residues, wastes, e.g. garbage, municipal or industrial sludges, compost, animal manure; fly-ashes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
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- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Inorganic Chemistry (AREA)
- Chemical And Physical Treatments For Wood And The Like (AREA)
Abstract
Description
技术领域Technical Field
本发明涉及有机高分子材料领域,具体的是一种活性炭木质纤维泡沫及其制备方法。The invention relates to the field of organic polymer materials, in particular to an activated carbon wood fiber foam and a preparation method thereof.
背景技术Background Art
地球上的水资源量占据71%的地球面积,河流、海洋、湖泊的自然蒸发和植物的蒸腾作用向全世界提供了大量的淡水资源,淡水是一个具有战略意义的全球问题,对人类的生存以及社会经济发展至关重要。水是地球上最丰富的化合物之一,到目前为止,由于人口增长、气候变化和过去几十年里猖獗的污染,许多人正在遭受淡水短缺的折磨。在技术的不断发展过程中,研究者们相继研究出了包括热蒸馏、反渗透、膜过滤、电渗析和光催化等技术,其中热蒸馏技术可以有效的将盐水转化为淡水资源,获得可用的纯净水。太阳能蒸发利用光热材料将太阳能转化为水蒸发的热量,并产生高品质的饮用淡水。这是一种很有前途的脱盐技术,可以以绿色和可持续的方式缓解淡水短缺问题。Water resources on Earth account for 71% of the Earth's surface. Natural evaporation from rivers, oceans, lakes and transpiration from plants provide a large amount of fresh water resources to the world. Fresh water is a global issue of strategic significance and is essential to human survival and socio-economic development. Water is one of the most abundant compounds on Earth. So far, many people are suffering from fresh water shortages due to population growth, climate change and rampant pollution in the past few decades. In the process of continuous technological development, researchers have successively developed technologies including thermal distillation, reverse osmosis, membrane filtration, electrodialysis and photocatalysis. Among them, thermal distillation technology can effectively convert salt water into fresh water resources and obtain usable pure water. Solar evaporation uses photothermal materials to convert solar energy into heat for water evaporation and produce high-quality drinking fresh water. This is a promising desalination technology that can alleviate the problem of fresh water shortage in a green and sustainable way.
在太阳能蒸发中,光热材料受到了广泛的关注。这些材料可以大致分为三类:碳基材料,例如,炭黑、石墨、碳纳米管、石墨烯、氧化石墨烯和还原氧化石墨烯种基于等离子体的材料,例如金属、金属氧化物、金属氮化物和聚合物基材料,例如聚吡咯和聚多巴胺。然而,这些材料大多不能单独使用,例如石墨和石墨烯,此外这些碳材料制作太阳能驱动器成本较高,且取材不方便,并没有得到实际的应用,例如氧化石墨烯和还原氧化石墨烯。In solar evaporation, photothermal materials have received extensive attention. These materials can be roughly divided into three categories: carbon-based materials, such as carbon black, graphite, carbon nanotubes, graphene, graphene oxide and reduced graphene oxide; plasma-based materials, such as metals, metal oxides, metal nitrides, and polymer-based materials, such as polypyrrole and polydopamine. However, most of these materials cannot be used alone, such as graphite and graphene. In addition, these carbon materials are expensive to make solar drivers and are inconvenient to obtain, so they have not been put into practical use, such as graphene oxide and reduced graphene oxide.
发明内容Summary of the invention
为解决上述背景技术中提到的不足,本发明的目的在于提供一种太阳能脱盐处理的活性炭木质泡沫及其制备方法,本发明法改性后的木质泡沫具有净水效果好、成本低廉、来源丰富、操作简便的优点,符合当前环境下以废治废的清洁生产理念,具有良好的环境效益和社会效益。In order to solve the deficiencies mentioned in the above background technology, the purpose of the present invention is to provide an activated carbon wood foam treated with solar desalination and a preparation method thereof. The wood foam modified by the method of the present invention has the advantages of good water purification effect, low cost, abundant sources and simple operation, which conforms to the clean production concept of treating waste with waste in the current environment and has good environmental and social benefits.
本发明的目的可以通过以下技术方案实现:The purpose of the present invention can be achieved through the following technical solutions:
一种活性炭木质纤维泡沫的制备方法,所述制备方法包括以下步骤:A method for preparing activated carbon wood fiber foam, the preparation method comprising the following steps:
将木质材料进行研磨,得到木质粉末,在木质粉末中加入清水得到木质悬浊液;向木质悬浊液中加入氯化钠溶液,利用盐离子辅助成型,然后进行搅拌处理,得到混合液一;向混合液一中加入活性炭溶液,并进行搅拌,使混合液一变为黑色混合液二;将混合液二进行超声破碎处理,使混合液二内的纤维断裂,最后对混合液二进行冷冻干燥即可制得活性炭木质泡沫;The wood material is ground to obtain wood powder, and water is added to the wood powder to obtain a wood suspension; a sodium chloride solution is added to the wood suspension to assist in forming with salt ions, and then stirred to obtain a mixed solution 1; an activated carbon solution is added to the mixed solution 1, and stirred to change the mixed solution 1 into a black mixed solution 2; the mixed solution 2 is subjected to ultrasonic crushing to break the fibers in the mixed solution 2, and finally the mixed solution 2 is freeze-dried to obtain an activated carbon wood foam;
其中:木质粉末和水的比值为1:20,木质悬浊液和氯化钠溶液的比值为30:1,混合液一和活性炭溶液的比值为1:1。Among them: the ratio of wood powder to water is 1:20, the ratio of wood suspension to sodium chloride solution is 30:1, and the ratio of mixed solution 1 to activated carbon solution is 1:1.
优选地,所述木质材料为林木废弃物。Preferably, the wood material is forest waste.
优选地,所述木质粉末的粒径小于200目。Preferably, the particle size of the wood powder is less than 200 mesh.
优选地,在悬浊液中加入氯化钠后进行搅拌的搅拌的条件为:温度为20℃,搅拌1-2h,转速为300r/min:。Preferably, the stirring conditions after adding sodium chloride to the suspension are: temperature of 20° C., stirring for 1-2 h, and a rotation speed of 300 r/min.
优选地,所述氯化钠溶液的浓度为100ml 5wt%。Preferably, the concentration of the sodium chloride solution is 100 ml 5 wt %.
优选地,所述活性炭溶液由活性炭和蒸馏水混合制备而成,其中活性炭为为粉状活性炭,活性炭粒径小于200目,活性炭和蒸馏水的比值为1:20。Preferably, the activated carbon solution is prepared by mixing activated carbon and distilled water, wherein the activated carbon is powdered activated carbon, the activated carbon particle size is less than 200 mesh, and the ratio of activated carbon to distilled water is 1:20.
优选地,向混合液一中加入活性炭溶液,并进行搅拌的搅拌条件为:温度为20℃,搅拌1-2h,转速为300r/min:Preferably, the activated carbon solution is added to the mixed solution 1, and the stirring conditions for stirring are: temperature of 20° C., stirring for 1-2 hours, and a speed of 300 r/min:
优选地,所述超声震碎时采用的是超声波细胞破碎仪,使用时超声波细胞破碎仪的功率比设置为20%,超声破碎时间为10min。Preferably, the ultrasonic cell disruptor is used for the ultrasonic disruption. When in use, the power ratio of the ultrasonic cell disruptor is set to 20%, and the ultrasonic disruption time is 10 minutes.
优选地,所述冷冻干燥具体步骤为:将混合液二先在-40℃冷冻6h使混合液二冷冻成型,然后将成型后的混合液二在真空条件下冷冻干燥48h,使水分升华。Preferably, the freeze-drying step is as follows: first freezing the mixed solution 2 at -40°C for 6 hours to freeze-form the mixed solution 2, and then freeze-drying the formed mixed solution 2 under vacuum conditions for 48 hours to sublime the water.
优选地,活性炭木质泡沫由活性炭木质泡沫的制备方法制备而成。Preferably, the activated carbon wood foam is prepared by a method for preparing activated carbon wood foam.
本发明的有益效果:Beneficial effects of the present invention:
(1)传统对生物质材料进行改性来进行水处理,其规模大小会受到生物质本身特点影响,无法进行大规模水处理,本申请采用木质为原材料可以控制材料的大小,可以实现规模化生产和大面积脱盐处理。(1) Traditionally, biomass materials are modified for water treatment, but the scale of the modification is affected by the characteristics of the biomass itself and cannot be used for large-scale water treatment. The present application uses wood as the raw material to control the size of the material, and can achieve large-scale production and large-scale desalination treatment.
(2)本申请采用活性炭进行木质改性制备的活性炭木质泡沫,具有较好的脱盐处理效果,具有抗酸抗碱性和抗高盐的特性,处理效率可达90%以上。(2) The activated carbon wood foam prepared by wood modification using activated carbon in the present application has a good desalination treatment effect, has the characteristics of acid, alkali and high salt resistance, and the treatment efficiency can reach more than 90%.
(3)本申请使用的材料为生物质材料,是一种自然可降解材料,对环境无二次污染。(3) The material used in this application is biomass material, which is a naturally degradable material and does not cause secondary pollution to the environment.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
下面结合附图对本发明作进一步的说明。The present invention will be further described below in conjunction with the accompanying drawings.
图1:活性炭含量为0%、10%、20%、30%、40%和50%活性炭木质泡沫实物图;Figure 1: Physical pictures of activated carbon wood foam with activated carbon content of 0%, 10%, 20%, 30%, 40% and 50%;
图2:不同活性炭含量木质泡沫红外光谱图;Figure 2: Infrared spectra of wood foam with different activated carbon contents;
图3:不同活性炭含量木质泡沫室内蒸发质量损失图和蒸发速度图;(a)为活性炭含量为0%、10%、20%、30%、40%和50%活性炭木质泡沫的质量损失图;(b)为活性炭含量为0%、10%、20%、30%、40%和50%活性炭木质泡沫的脱盐蒸发速度;Figure 3: Indoor evaporation mass loss and evaporation rate diagram of wood foam with different activated carbon contents; (a) is the mass loss diagram of activated carbon wood foam with activated carbon contents of 0%, 10%, 20%, 30%, 40% and 50%; (b) is the desalination evaporation rate of activated carbon wood foam with activated carbon contents of 0%, 10%, 20%, 30%, 40% and 50%;
图4:不同保温条件下木质泡沫界面温度图、水温图、室内蒸发质量损失图和蒸发速度图;Figure 4: Wood foam interface temperature diagram, water temperature diagram, indoor evaporation mass loss diagram and evaporation rate diagram under different insulation conditions;
图5:氯化钠含量为0%、0.5%、1.0%、1.5%、2.0%、2.5%、3.0%、3.5%、4.0%、4.5%和5.0%活性炭木质泡沫实物图;Figure 5: Physical pictures of activated carbon wood foam with sodium chloride content of 0%, 0.5%, 1.0%, 1.5%, 2.0%, 2.5%, 3.0%, 3.5%, 4.0%, 4.5% and 5.0%;
图6:不同氯化钠含量活性炭/木质泡沫室内蒸发质量损失图和蒸发速度图;(a)为氯化钠含量为0%、0.5%、1.0%、1.5%、2.0%、2.5%、3.0%、3.5%、4.0%、4.5%和5.0%活性炭木质泡沫的质量损失图;(b)为活性炭含量为0%、0.5%、1.0%、1.5%、2.0%、2.5%、3.0%、3.5%、4.0%、4.5%和5.0%活性炭木质泡沫的脱盐蒸发速度;Figure 6: Indoor evaporation mass loss diagram and evaporation rate diagram of activated carbon/wood foam with different sodium chloride contents; (a) is the mass loss diagram of activated carbon wood foam with sodium chloride contents of 0%, 0.5%, 1.0%, 1.5%, 2.0%, 2.5%, 3.0%, 3.5%, 4.0%, 4.5% and 5.0%; (b) is the desalination evaporation rate of activated carbon wood foam with activated carbon contents of 0%, 0.5%, 1.0%, 1.5%, 2.0%, 2.5%, 3.0%, 3.5%, 4.0%, 4.5% and 5.0%;
具体实施方式DETAILED DESCRIPTION
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其它实施例,都属于本发明保护的范围。The following will be combined with the drawings in the embodiments of the present invention to clearly and completely describe the technical solutions in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.
实施案例一:Implementation case 1:
活性炭木质泡沫的制备方法如下:The preparation method of activated carbon wood foam is as follows:
原料研磨:本发明使用的原材料为10g木质木粉。将其倒入200m l清水进行加热搅拌,之后将其再次进行机械高压均质,使得木质颗粒物直径接近纳米级别。Raw material grinding: The raw material used in the present invention is 10 g of wood powder, which is poured into 200 ml of clean water for heating and stirring, and then subjected to mechanical high-pressure homogenization again, so that the diameter of the wood particles is close to the nanometer level.
混合搅拌:将200m l 5wt%活性炭溶液和100ml 5wt%氯化钠溶液倒入木质悬浊液中,在室温条件下搅拌1-2h,之后悬浊液超声波破碎,继续搅拌1-2h,使木质变为黑色。Mixing and stirring: Pour 200 ml of 5wt% activated carbon solution and 100 ml of 5wt% sodium chloride solution into the wood suspension, stir at room temperature for 1-2 hours, then ultrasonically break the suspension and continue stirring for 1-2 hours to turn the wood into black.
(3)泡沫成型:将(2)中制备好的悬浊液倒入10cm×10cm×5cm(长×宽×高)的敞口亚克力盒中,利用温度梯度调节将其进行冷冻,在-40℃冷冻6h以上;再通过液氮冷冻干燥48h以上即可,也可以采用冷冻机进行冷冻干燥。制备好的活性炭木质泡沫为为长方体的3D结构,且内部含毛细通道纹路。(3) Foam molding: Pour the suspension prepared in (2) into an open acrylic box of 10 cm × 10 cm × 5 cm (length × width × height), freeze it by adjusting the temperature gradient, and freeze it at -40 ° C for more than 6 hours; then freeze-dry it with liquid nitrogen for more than 48 hours, or freeze-dry it in a freezer. The prepared activated carbon wood foam has a 3D structure of a cuboid and contains capillary channel patterns inside.
(4)室内太阳能脱盐处理:将(3)中制备好的活性炭木质泡沫放入废水中,将整个装置放入水槽内,以LED灯作为光源,进行室内太阳能脱盐处理。(4) Indoor solar desalination treatment: The activated carbon wood foam prepared in (3) is placed in the wastewater, the entire device is placed in a water tank, and an LED lamp is used as a light source to perform indoor solar desalination treatment.
实施案例二:Implementation Case 2:
本实施案例与实施案例一的不同之处在于步骤(4)。The difference between this implementation case and implementation case 1 lies in step (4).
实施案例一中的水槽未采取保温措施,本实施案例中制备好的活性炭木质泡沫放入废水中,将整个装置放入保温水槽内,以LED灯作为光源,构成以水槽保温条件为变量的实验序列,进行室内太阳能脱盐处理实验。The water tank in Implementation Case 1 did not take insulation measures. In this implementation case, the activated carbon wood foam prepared was placed in the wastewater, and the entire device was placed in an insulated water tank. LED lights were used as light sources to form an experimental sequence with the water tank insulation conditions as variables, and indoor solar desalination treatment experiments were carried out.
实施案例三:Implementation case three:
本实施案例与实施案例一的不同之处在于步骤(2)。The difference between this implementation case and implementation case 1 lies in step (2).
实施案例一中的活性炭质量占活性炭/木质混合体质量为50%,本实施案例中活性炭溶液和木质悬浊液的比值为1:10,木质的固含量保持在5.4%不变,水槽保温,泡沫高度为1cm,其余制备方案不变,构成以活性炭质量为变量的实验序列,进行室内太阳能脱盐处理实验。The mass of activated carbon in Implementation Case 1 accounts for 50% of the mass of the activated carbon/wood mixture. In this implementation case, the ratio of activated carbon solution to wood suspension is 1:10, the solid content of wood is kept unchanged at 5.4%, the water tank is kept warm, the foam height is 1 cm, and the rest of the preparation plan remains unchanged, forming an experimental sequence with activated carbon mass as a variable, and conducting indoor solar desalination treatment experiments.
实施案例四:Implementation Case 4:
本实施案例与实施案例一的不同之处在于步骤(2)。The difference between this implementation case and implementation case 1 lies in step (2).
实施案例一中的活性炭质量占活性炭/木质混合体质量为50%,本实施案例中活性炭溶液和木质悬浊液的比值为1:5,木质的固含量保持在5.4%不变,水槽保温,泡沫高度为1cm,其余制备方案不变,构成以活性炭质量为变量的实验序列,进行室内太阳能脱盐处理实验。The mass of activated carbon in Implementation Case 1 accounts for 50% of the mass of the activated carbon/wood mixture. In this implementation case, the ratio of activated carbon solution to wood suspension is 1:5, the solid content of wood is kept unchanged at 5.4%, the water tank is kept warm, the foam height is 1 cm, and the rest of the preparation plan remains unchanged, forming an experimental sequence with activated carbon mass as a variable, and conducting indoor solar desalination treatment experiments.
实施案例五:Implementation Case 5:
本实施案例与实施案例一的不同之处在于步骤(2)。The difference between this implementation case and implementation case 1 lies in step (2).
实施案例一中的活性炭质量占活性炭/木质混合体质量为50%,本实施案例中活性炭溶液和木质悬浊液的比值为1:3,木质的固含量保持在5.4%不变,水槽保温,泡沫高度为1cm,其余制备方案不变,构成以活性炭质量为变量的实验序列,进行室内太阳能脱盐处理实验。The mass of activated carbon in Implementation Case 1 accounts for 50% of the mass of the activated carbon/wood mixture. In this implementation case, the ratio of activated carbon solution to wood suspension is 1:3, the solid content of wood is kept unchanged at 5.4%, the water tank is kept warm, the foam height is 1 cm, and the rest of the preparation plan remains unchanged, forming an experimental sequence with activated carbon mass as a variable, and conducting indoor solar desalination treatment experiments.
实施案例六:Implementation Case 6:
本实施案例与实施案例一的不同之处在于步骤(2)。The difference between this implementation case and implementation case 1 lies in step (2).
实施案例一中的活性炭质量占活性炭/木质混合体质量为50%,本实施案例中活性炭溶液和木质悬浊液的比值为1:2.5,木质的固含量保持在5.4%不变,水槽保温,泡沫高度为1cm,其余制备方案不变,构成以活性炭质量为变量的实验序列,进行室内太阳能脱盐处理实验。The mass of activated carbon in Implementation Case 1 accounts for 50% of the mass of the activated carbon/wood mixture. In this implementation case, the ratio of activated carbon solution to wood suspension is 1:2.5, the solid content of wood is kept unchanged at 5.4%, the water tank is kept warm, the foam height is 1 cm, and the rest of the preparation plan remains unchanged, forming an experimental sequence with activated carbon mass as a variable, and conducting indoor solar desalination treatment experiments.
实施案例七:Implementation Case 7:
本实施案例与实施案例一的不同之处在于步骤(2)。The difference between this implementation case and implementation case 1 lies in step (2).
实施案例一中的活性炭质量占活性炭/木质混合体质量为50%,本实施案例中活性炭溶液和木质悬浊液的比值为1:2,木质的固含量保持在5.4%不变,水槽保温,泡沫高度为1cm,其余制备方案不变,构成以活性炭质量为变量的实验序列,进行室内太阳能脱盐处理实验。The mass of activated carbon in Implementation Case 1 accounts for 50% of the mass of the activated carbon/wood mixture. In this implementation case, the ratio of activated carbon solution to wood suspension is 1:2, the solid content of wood is kept unchanged at 5.4%, the water tank is kept warm, the foam height is 1 cm, and the rest of the preparation plan remains unchanged, forming an experimental sequence with activated carbon mass as a variable, and conducting indoor solar desalination treatment experiments.
实施案例八:Implementation Case 8:
本实施案例与实施案例一的不同之处在于步骤(2)。The difference between this implementation case and implementation case 1 lies in step (2).
实施案例一中的氯化钠的质量占活性炭/木质混合体质量的1%,本实施案例中氯化钠溶液和活性炭/木质混合溶液的比值为1:200,水槽保温,泡沫高度为1cm,其余制备方案不变,构成以氯化钠质量为变量的实验序列,进行室内太阳能脱盐处理实验。The mass of sodium chloride in Implementation Case 1 accounts for 1% of the mass of the activated carbon/wood mixture. In this implementation case, the ratio of sodium chloride solution to activated carbon/wood mixed solution is 1:200, the water tank is insulated, the foam height is 1 cm, and the rest of the preparation plan remains unchanged. An experimental sequence with the mass of sodium chloride as a variable is constructed to conduct indoor solar desalination treatment experiments.
实施案例九:Implementation Case 9:
本实施案例与实施案例一的不同之处在于步骤(2)。The difference between this implementation case and implementation case 1 lies in step (2).
实施案例一中的氯化钠的质量占活性炭/木质混合体质量的1%,本实施案例中氯化钠溶液和活性炭/木质混合溶液的比值为1:66,水槽保温,泡沫高度为1cm,其余制备方案不变,构成以氯化钠质量为变量的实验序列,进行室内太阳能脱盐处理实验。The mass of sodium chloride in Implementation Case 1 accounts for 1% of the mass of the activated carbon/wood mixture. In this implementation case, the ratio of sodium chloride solution to activated carbon/wood mixed solution is 1:66, the water tank is insulated, the foam height is 1 cm, and the rest of the preparation plan remains unchanged. An experimental sequence with the mass of sodium chloride as a variable is constructed to conduct indoor solar desalination treatment experiments.
实施案例十:Implementation Case 10:
本实施案例与实施案例一的不同之处在于步骤(2)。The difference between this implementation case and implementation case 1 lies in step (2).
实施案例一中的氯化钠的质量占活性炭/木质混合体质量的1%,本实施案例中氯化钠溶液和活性炭/木质混合溶液的比值为1:49,水槽保温,泡沫高度为1cm,其余制备方案不变,构成以氯化钠质量为变量的实验序列,进行室内太阳能脱盐处理实验。The mass of sodium chloride in Implementation Case 1 accounts for 1% of the mass of the activated carbon/wood mixture. In this implementation case, the ratio of sodium chloride solution to activated carbon/wood mixed solution is 1:49, the water tank is insulated, the foam height is 1 cm, and the rest of the preparation plan remains unchanged, forming an experimental sequence with the mass of sodium chloride as a variable, and conducting indoor solar desalination treatment experiments.
实施案例十一:Implementation Case 11:
本实施案例与实施案例一的不同之处在于步骤(2)。The difference between this implementation case and implementation case 1 lies in step (2).
实施案例一中的氯化钠的质量占活性炭/木质混合体质量的1%,本实施案例中氯化钠溶液和活性炭/木质混合溶液的比值为1:39,水槽保温,泡沫高度为1cm,其余制备方案不变,构成以氯化钠质量为变量的实验序列,进行室内太阳能脱盐处理实验。The mass of sodium chloride in Implementation Case 1 accounts for 1% of the mass of the activated carbon/wood mixture. In this implementation case, the ratio of sodium chloride solution to activated carbon/wood mixed solution is 1:39, the water tank is insulated, the foam height is 1 cm, and the rest of the preparation plan remains unchanged, forming an experimental sequence with the mass of sodium chloride as a variable, and conducting indoor solar desalination treatment experiments.
实施案例十二:Implementation Case 12:
本实施案例与实施案例一的不同之处在于步骤(2)。The difference between this implementation case and implementation case 1 lies in step (2).
实施案例一中的氯化钠的质量占活性炭/木质混合体质量的1%,本实施案例中氯化钠溶液和活性炭/木质混合溶液的比值为1:33,水槽保温,泡沫高度为1cm,其余制备方案不变,构成以氯化钠质量为变量的实验序列,进行室内太阳能脱盐处理实验。The mass of sodium chloride in Implementation Case 1 accounts for 1% of the mass of the activated carbon/wood mixture. In this implementation case, the ratio of sodium chloride solution to activated carbon/wood mixed solution is 1:33, the water tank is kept warm, the foam height is 1 cm, and the rest of the preparation plan remains unchanged. An experimental sequence with the mass of sodium chloride as a variable is constructed to conduct indoor solar desalination treatment experiments.
实施案例十三:Implementation Case Thirteen:
本实施案例与实施案例一的不同之处在于步骤(2)。The difference between this implementation case and implementation case 1 lies in step (2).
实施案例一中的氯化钠的质量占活性炭/木质混合体质量的1%,本实施案例中氯化钠溶液和活性炭/木质混合溶液的比值为1:28,水槽保温,泡沫高度为1cm,其余制备方案不变,构成以氯化钠质量为变量的实验序列,进行室内太阳能脱盐处理实验。The mass of sodium chloride in Implementation Case 1 accounts for 1% of the mass of the activated carbon/wood mixture. In this implementation case, the ratio of sodium chloride solution to activated carbon/wood mixed solution is 1:28, the water tank is insulated, the foam height is 1 cm, and the rest of the preparation plan remains unchanged. An experimental sequence with the mass of sodium chloride as a variable is constructed to conduct indoor solar desalination treatment experiments.
实施案例十四:Implementation Case 14:
本实施案例与实施案例一的不同之处在于步骤(2)。The difference between this implementation case and implementation case 1 lies in step (2).
实施案例一中的氯化钠的质量占活性炭/木质混合体质量的1%,本实施案例中氯化钠溶液和活性炭/木质混合溶液的比值为1:24,水槽保温,泡沫高度为1cm,其余制备方案不变,构成以氯化钠质量为变量的实验序列,进行室内太阳能脱盐处理实验。The mass of sodium chloride in Implementation Case 1 accounts for 1% of the mass of the activated carbon/wood mixture. In this implementation case, the ratio of sodium chloride solution to activated carbon/wood mixed solution is 1:24, the water tank is insulated, the foam height is 1 cm, and the rest of the preparation plan remains unchanged. An experimental sequence with the mass of sodium chloride as a variable is constructed to conduct indoor solar desalination treatment experiments.
实施案例十五:Implementation Case 15:
本实施案例与实施案例一的不同之处在于步骤(2)。The difference between this implementation case and implementation case 1 lies in step (2).
实施案例一中的氯化钠的质量占活性炭/木质混合体质量的1%,本实施案例中氯化钠溶液和活性炭/木质混合溶液的比值为1:21,水槽保温,泡沫高度为1cm,其余制备方案不变,构成以氯化钠质量为变量的实验序列,进行室内太阳能脱盐处理实验。The mass of sodium chloride in Implementation Case 1 accounts for 1% of the mass of the activated carbon/wood mixture. In this implementation case, the ratio of sodium chloride solution to activated carbon/wood mixed solution is 1:21, the water tank is insulated, the foam height is 1 cm, and the rest of the preparation plan remains unchanged. An experimental sequence with the mass of sodium chloride as a variable is constructed to conduct indoor solar desalination treatment experiments.
实施案例十六:Implementation Case 16:
本实施案例与实施案例一的不同之处在于步骤(4)。The difference between this implementation case and implementation case 1 lies in step (4).
实施案例一中的活性炭质量占活性炭/木质混合体质量为50%,本实施案例中氯化钠和蒸馏水的比值为1:32,木质的固含量保持在5.4%不变,水槽保温,泡沫高度为1cm,其余制备方案不变,构成以废水盐度为变量的实验序列,进行室内太阳能脱盐处理实验。The mass of activated carbon in Implementation Case 1 accounts for 50% of the mass of the activated carbon/wood mixture. In this implementation case, the ratio of sodium chloride to distilled water is 1:32, the solid content of the wood is kept unchanged at 5.4%, the water tank is kept warm, the foam height is 1 cm, and the rest of the preparation plan remains unchanged, forming an experimental sequence with wastewater salinity as a variable, and conducting indoor solar desalination treatment experiments.
实施案例十七:Implementation Case 17:
本实施案例与实施案例一的不同之处在于步骤(4)。The difference between this implementation case and implementation case 1 lies in step (4).
实施案例一中的活性炭质量占活性炭/木质混合体质量为50%,本实施案例中氯化钠和蒸馏水的比值为1:10,木质的固含量保持在5.4%不变,水槽保温,泡沫高度为1cm,其余制备方案不变,构成以废水盐度为变量的实验序列,进行室内太阳能脱盐处理实验。The mass of activated carbon in Implementation Case 1 accounts for 50% of the mass of the activated carbon/wood mixture. In this implementation case, the ratio of sodium chloride to distilled water is 1:10, the solid content of the wood is kept unchanged at 5.4%, the water tank is kept warm, the foam height is 1 cm, and the rest of the preparation plan remains unchanged, forming an experimental sequence with wastewater salinity as a variable, and conducting indoor solar desalination treatment experiments.
实施案例十八:Implementation Case 18:
本实施案例与实施案例一的不同之处在于步骤(4)。The difference between this implementation case and implementation case 1 lies in step (4).
实施案例一中的活性炭质量占活性炭/木质混合体质量为50%,本实施案例中氯化钠和蒸馏水的比值为1:17,木质的固含量保持在5.4%不变,水槽保温,泡沫高度为1cm,其余制备方案不变,构成以废水盐度为变量的实验序列,进行室内太阳能脱盐处理实验。The mass of activated carbon in Implementation Case 1 accounts for 50% of the mass of the activated carbon/wood mixture. In this implementation case, the ratio of sodium chloride to distilled water is 1:17, the solid content of the wood is kept unchanged at 5.4%, the water tank is kept warm, the foam height is 1 cm, and the rest of the preparation plan remains unchanged, forming an experimental sequence with wastewater salinity as a variable, and conducting indoor solar desalination treatment experiments.
从图1可以看出,通过实施案例一制备的活性炭木质泡沫中的活性炭未破坏木质本身的结构。在蒸发脱盐之后,其组成结构也未发生过改变。可见本专利制备方法简单且不会给环境带来二次污染。As can be seen from Figure 1, the activated carbon in the activated carbon wood foam prepared by Example 1 does not destroy the structure of the wood itself. After evaporation and desalination, its composition structure has not changed. It can be seen that the preparation method of this patent is simple and will not cause secondary pollution to the environment.
图2为活性炭质量占活性炭/木质混合体质量的0%、10%、20%、30%、40%和50%的活性炭木质泡沫实物图,从图中可以看出活性炭木质泡沫具有明显的毛细管结构和毛细孔洞,为水分的运输提供了良好的通路;且混合后木质泡沫为灰黑色,其中活性炭含量为50%时泡沫颜色最黑,活性炭含量为10%时泡沫颜色最浅,可知活性炭含量的不同可以影响泡沫颜色的深浅。Figure 2 shows actual pictures of activated carbon wood foams with activated carbon mass accounting for 0%, 10%, 20%, 30%, 40% and 50% of the mass of the activated carbon/wood mixture. It can be seen from the figure that the activated carbon wood foam has an obvious capillary structure and capillary pores, which provide a good pathway for the transport of water; and the wood foam is gray-black after mixing, among which the foam color is the darkest when the activated carbon content is 50%, and the foam color is the lightest when the activated carbon content is 10%. It can be seen that different activated carbon contents can affect the depth of the foam color.
图4(a、c)为不同保温条件下50%活性炭含量的木制泡沫的界面温度图和太阳能水蒸发池水温图,从图中可以看出保温条件下界面温度和水温有明显提高,有利于太阳能脱盐处理;图4(b、d)为不同保温条件下50%活性炭含量的木制泡沫的室内蒸发质量损失图和蒸发速度图,从图中可以看出保温条件下蒸发速率最快。Figure 4 (a, c) shows the interface temperature diagram of wood foam with 50% activated carbon content under different insulation conditions and the water temperature diagram of the solar water evaporation pool. It can be seen from the figure that the interface temperature and water temperature are significantly improved under the insulation conditions, which is beneficial to solar desalination treatment; Figure 4 (b, d) shows the indoor evaporation mass loss diagram and evaporation rate diagram of wood foam with 50% activated carbon content under different insulation conditions. It can be seen from the figure that the evaporation rate is fastest under the insulation conditions.
从图3中可知,活性炭木质泡沫遇水后颜色加深,呈墨黑色,说明该泡沫具有亲水性,可以实现水分的运输,活性炭泡沫吸收水分后颜色加深,可以提高对光的吸收,增强光热转换效果,促进水分的快速蒸发。当活性炭含量占木质含量的50%时,活性炭木质泡沫蒸发速度最快,活性炭含量为30%时,蒸发速度最慢,其他含量的活性炭木质泡沫蒸发速度介于两者之间。As can be seen from Figure 3, the color of the activated carbon wood foam deepens after it comes into contact with water, and it becomes jet black, indicating that the foam is hydrophilic and can transport water. The color of the activated carbon foam deepens after absorbing water, which can improve the absorption of light, enhance the photothermal conversion effect, and promote the rapid evaporation of water. When the activated carbon content accounts for 50% of the wood content, the activated carbon wood foam evaporates the fastest, and when the activated carbon content is 30%, the evaporation rate is the slowest. The evaporation rates of activated carbon wood foams with other contents are between the two.
图5为氯化钠的质量分别占活性炭/木质混合体质量的0%、0.5%、1.0%、1.5%、2.0%、2.5%、3.0%、3.5%、4.0%、4.5%和5.0%的活性炭木质泡沫实物图,从图中可以看出活性炭木质泡沫具有明显的毛细管结构和毛细孔洞,为水分的运输提供了良好的通路。Figure 5 shows actual pictures of activated carbon wood foam when the mass of sodium chloride accounts for 0%, 0.5%, 1.0%, 1.5%, 2.0%, 2.5%, 3.0%, 3.5%, 4.0%, 4.5% and 5.0% of the mass of the activated carbon/wood mixture, respectively. It can be seen from the figure that the activated carbon wood foam has a significant capillary structure and capillary pores, which provide a good pathway for the transport of water.
从图6中可知,活性炭木质泡沫具有明显的毛细管结构,为水分的运输提供了良好的通路。且混合后木质泡沫表面有不同程度的白色盐分附着,可知NaCl含量的不同可以影响泡沫表面盐分附着。当NaCl含量占活性炭/木质含量的4.5%时,活性炭木质泡沫蒸发速度最快,NaCl含量占活性炭/木质含量的0.0%时,蒸发速度最慢,其他含量的活性炭木质泡沫蒸发速度介于两者之间。As can be seen from Figure 6, the activated carbon wood foam has an obvious capillary structure, which provides a good channel for the transport of water. And after mixing, there are different degrees of white salt attached to the surface of the wood foam, which shows that different NaCl contents can affect the salt attachment on the foam surface. When the NaCl content accounts for 4.5% of the activated carbon/wood content, the activated carbon wood foam evaporates the fastest, and when the NaCl content accounts for 0.0% of the activated carbon/wood content, the evaporation rate is the slowest. The evaporation rates of activated carbon wood foams with other contents are between the two.
在本说明书的描述中,参考术语“一个实施例”、“示例”、“具体示例”等的描述意指结合该实施例或示例描述的具体特征、结构、材料或者特点包含于本发明的至少一个实施例或示例中。在本说明书中,对上述术语的示意性表述不一定指的是相同的实施例或示例。而且,描述的具体特征、结构、材料或者特点可以在任何的一个或多个实施例或示例中以合适的方式结合。In the description of this specification, the description with reference to the terms "one embodiment", "example", "specific example", etc. means that the specific features, structures, materials or characteristics described in conjunction with the embodiment or example are included in at least one embodiment or example of the present invention. In this specification, the schematic representation of the above terms does not necessarily refer to the same embodiment or example. Moreover, the specific features, structures, materials or characteristics described can be combined in any one or more embodiments or examples in a suitable manner.
以上显示和描述了本发明的基本原理、主要特征和本发明的优点。本行业的技术人员应该了解,本发明不受上述实施例的限制,上述实施例和说明书中描述的只是说明本发明的原理,在不脱离本发明精神和范围的前提下,本发明还会有各种变化和改进,这些变化和改进都落入要求保护的本发明范围内。The above shows and describes the basic principles, main features and advantages of the present invention. Those skilled in the art should understand that the present invention is not limited to the above embodiments, and the above embodiments and descriptions are only for explaining the principles of the present invention. Without departing from the spirit and scope of the present invention, the present invention may have various changes and improvements, and these changes and improvements all fall within the scope of the present invention to be protected.
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