CN104530597B - Biodegradable pearlescent pen shell and preparation method thereof - Google Patents
Biodegradable pearlescent pen shell and preparation method thereof Download PDFInfo
- Publication number
- CN104530597B CN104530597B CN201410815155.0A CN201410815155A CN104530597B CN 104530597 B CN104530597 B CN 104530597B CN 201410815155 A CN201410815155 A CN 201410815155A CN 104530597 B CN104530597 B CN 104530597B
- Authority
- CN
- China
- Prior art keywords
- sludge
- parts
- powder
- manufacture method
- value
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 241000180587 Pinnidae Species 0.000 title abstract description 26
- 238000002360 preparation method Methods 0.000 title description 6
- 239000010802 sludge Substances 0.000 claims abstract description 57
- 239000000843 powder Substances 0.000 claims abstract description 28
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical class [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 26
- 238000000034 method Methods 0.000 claims abstract description 22
- 239000000463 material Substances 0.000 claims abstract description 20
- 239000007822 coupling agent Substances 0.000 claims abstract description 17
- RYYKJJJTJZKILX-UHFFFAOYSA-M sodium octadecanoate Chemical compound [Na+].CCCCCCCCCCCCCCCCCC([O-])=O RYYKJJJTJZKILX-UHFFFAOYSA-M 0.000 claims abstract description 15
- 238000004519 manufacturing process Methods 0.000 claims abstract description 13
- 239000000203 mixture Substances 0.000 claims abstract description 11
- 239000004594 Masterbatch (MB) Substances 0.000 claims abstract description 6
- 239000000835 fiber Substances 0.000 claims abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 41
- 239000002351 wastewater Substances 0.000 claims description 22
- 238000003756 stirring Methods 0.000 claims description 16
- 238000005273 aeration Methods 0.000 claims description 9
- 239000012752 auxiliary agent Substances 0.000 claims description 7
- 208000034530 PLAA-associated neurodevelopmental disease Diseases 0.000 claims description 6
- 239000000853 adhesive Substances 0.000 claims description 6
- 230000001070 adhesive effect Effects 0.000 claims description 6
- 238000001035 drying Methods 0.000 claims description 6
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 claims description 4
- 239000003795 chemical substances by application Substances 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 4
- 229910000077 silane Inorganic materials 0.000 claims description 4
- 229920001971 elastomer Polymers 0.000 claims description 2
- 239000000806 elastomer Substances 0.000 claims description 2
- 239000011049 pearl Substances 0.000 claims 11
- 239000012531 culture fluid Substances 0.000 claims 2
- 238000001125 extrusion Methods 0.000 claims 2
- 239000000428 dust Substances 0.000 claims 1
- 239000000686 essence Substances 0.000 claims 1
- 238000009313 farming Methods 0.000 claims 1
- 239000010902 straw Substances 0.000 abstract description 24
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 abstract description 12
- 230000015556 catabolic process Effects 0.000 abstract description 9
- 238000006731 degradation reaction Methods 0.000 abstract description 9
- 239000002699 waste material Substances 0.000 abstract description 9
- 229910000019 calcium carbonate Inorganic materials 0.000 abstract description 6
- 239000002861 polymer material Substances 0.000 abstract description 6
- 239000002689 soil Substances 0.000 abstract description 6
- 239000011230 binding agent Substances 0.000 abstract description 4
- 239000002994 raw material Substances 0.000 abstract description 3
- 238000003912 environmental pollution Methods 0.000 abstract description 2
- 239000003337 fertilizer Substances 0.000 abstract description 2
- 238000000465 moulding Methods 0.000 abstract description 2
- 239000000654 additive Substances 0.000 abstract 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 12
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- 239000007787 solid Substances 0.000 description 9
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 6
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 6
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 6
- 229910052757 nitrogen Inorganic materials 0.000 description 6
- 229910052698 phosphorus Inorganic materials 0.000 description 6
- 239000011574 phosphorus Substances 0.000 description 6
- 229920003023 plastic Polymers 0.000 description 6
- 239000004033 plastic Substances 0.000 description 6
- 239000004433 Thermoplastic polyurethane Substances 0.000 description 5
- 229920002803 thermoplastic polyurethane Polymers 0.000 description 5
- 229920006342 thermoplastic vulcanizate Polymers 0.000 description 5
- 238000013019 agitation Methods 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 229920002725 thermoplastic elastomer Polymers 0.000 description 4
- 238000009423 ventilation Methods 0.000 description 4
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 3
- 241001391944 Commicarpus scandens Species 0.000 description 3
- 244000068988 Glycine max Species 0.000 description 3
- 235000010469 Glycine max Nutrition 0.000 description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 3
- 240000007594 Oryza sativa Species 0.000 description 3
- 235000007164 Oryza sativa Nutrition 0.000 description 3
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 3
- 240000000111 Saccharum officinarum Species 0.000 description 3
- 235000007201 Saccharum officinarum Nutrition 0.000 description 3
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 description 3
- 241000209140 Triticum Species 0.000 description 3
- 235000021307 Triticum Nutrition 0.000 description 3
- 240000008042 Zea mays Species 0.000 description 3
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 3
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 3
- 238000004887 air purification Methods 0.000 description 3
- 229910021529 ammonia Inorganic materials 0.000 description 3
- 235000019270 ammonium chloride Nutrition 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 229920000704 biodegradable plastic Polymers 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 229910052791 calcium Inorganic materials 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 235000005822 corn Nutrition 0.000 description 3
- 230000008878 coupling Effects 0.000 description 3
- 238000010168 coupling process Methods 0.000 description 3
- 238000005859 coupling reaction Methods 0.000 description 3
- 230000032798 delamination Effects 0.000 description 3
- ZPWVASYFFYYZEW-UHFFFAOYSA-L dipotassium hydrogen phosphate Chemical compound [K+].[K+].OP([O-])([O-])=O ZPWVASYFFYYZEW-UHFFFAOYSA-L 0.000 description 3
- 230000004927 fusion Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000001963 growth medium Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000000314 lubricant Substances 0.000 description 3
- 239000011777 magnesium Substances 0.000 description 3
- 229910052749 magnesium Inorganic materials 0.000 description 3
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 235000015097 nutrients Nutrition 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 239000005014 poly(hydroxyalkanoate) Substances 0.000 description 3
- 229920000903 polyhydroxyalkanoate Polymers 0.000 description 3
- 239000004626 polylactic acid Substances 0.000 description 3
- 239000011591 potassium Substances 0.000 description 3
- 229910052700 potassium Inorganic materials 0.000 description 3
- 235000009566 rice Nutrition 0.000 description 3
- 238000004062 sedimentation Methods 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 239000001632 sodium acetate Substances 0.000 description 3
- 235000017281 sodium acetate Nutrition 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 229920003051 synthetic elastomer Polymers 0.000 description 3
- 239000005061 synthetic rubber Substances 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 2
- 239000000976 ink Substances 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 239000006087 Silane Coupling Agent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000003895 organic fertilizer Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L27/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
- C08L27/02—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L27/04—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
- C08L27/06—Homopolymers or copolymers of vinyl chloride
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/10—Homopolymers or copolymers of propene
- C08L23/12—Polypropene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L25/00—Compositions of, homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Compositions of derivatives of such polymers
- C08L25/02—Homopolymers or copolymers of hydrocarbons
- C08L25/04—Homopolymers or copolymers of styrene
- C08L25/06—Polystyrene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2201/00—Properties
- C08L2201/06—Biodegradable
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend
- C08L2205/035—Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/14—Polymer mixtures characterised by other features containing polymeric additives characterised by shape
- C08L2205/16—Fibres; Fibrils
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Fertilizers (AREA)
- Treatment Of Sludge (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
本发明涉及一种可降解珠光笔壳及其制作方法,它包括:1)将35‑55份活性污泥粉末、10‑25份高分子材料、5‑15份纤维粉末、5‑10份活性炭粉、5‑15份粘合剂、3‑5份碳酸钙、3‑5份珠光色母粒,助剂:包括硬脂酸钠、偶联剂以及相容剂,其中,硬脂酸钠为活性炭粉质量的2%;偶联剂为活性炭粉质量的1%;相容剂为总质量的3%‑5%;将以上物质加入到混合机中,混合均匀;2)将步骤1)所得混合物通过单螺杆挤出机塑化挤出,造粒并通过模压二次加工即得到可生物降解珠光笔壳。它采用生活中的废物—污泥和秸秆作为原料,实现了废物的再利用,避免了现有污泥处理方法带来的二次污染,减少了秸秆燃烧对环境的污染;此外,所得笔壳可完全降解,且降解后可作为肥料改良土壤。The present invention relates to a degradable pearl pen case and a manufacturing method thereof, which comprises: 1) 35-55 parts of activated sludge powder, 10-25 parts of polymer material, 5-15 parts of fiber powder, and 5-10 parts of activated carbon Powder, 5-15 parts of binder, 3-5 parts of calcium carbonate, 3-5 parts of pearlescent masterbatch, additives: including sodium stearate, coupling agent and compatibilizer, wherein sodium stearate is 2% of the mass of activated carbon powder; the coupling agent is 1% of the mass of activated carbon powder; the compatibilizer is 3%-5% of the total mass; the above materials are added to the mixer and mixed uniformly; 2) the obtained The mixture is plasticized and extruded by a single-screw extruder, granulated and subjected to secondary processing through molding to obtain a biodegradable pearl pen shell. It uses the waste in life—sludge and straw as raw materials, realizes the reuse of waste, avoids the secondary pollution caused by the existing sludge treatment method, and reduces the environmental pollution caused by straw burning; in addition, the obtained pen shell It can be completely degraded and can be used as fertilizer to improve soil after degradation.
Description
技术领域technical field
本发明涉及一种采用活性污泥粉末做主料生产可降解珠光笔壳及其制作方法,尤其涉及易于降解,净化空气,具有珠光效果笔壳,以及环保材料的应用。The invention relates to a degradable pearlescent pen case produced by using activated sludge powder as the main material and a manufacturing method thereof, in particular to the application of the pen case which is easy to degrade, purifies air, has a pearlescent effect, and an environmental protection material.
背景技术Background technique
随着社会经济的发展,工厂废水排出量越来越多,同时伴随着污泥量的与日俱增,严重影响我国的水环境。报道称,太湖水域底部的淤泥量为6700万立方米,还有珠江三角洲一带有8000万立方米,这会影响到河道水质和航运功能。过去采用的排淤方法是将污泥运到笔壳站,以待其自然风化,这将会二次污染空气,而且浪费物力财力。排污工程中产生的污泥过去采用堆放或者是抛弃的方法处置,这样不仅会造成大量的土地资源的浪费,对生态环境将会造成不可弥补的破坏,而且污泥中含有的重金属离子和有机化合物会对周边的土壤和空气造成二次污染。With the development of society and economy, more and more factory wastewater is discharged, and at the same time, the amount of sludge is increasing day by day, which seriously affects the water environment of our country. According to reports, the amount of silt at the bottom of the Taihu Lake is 67 million cubic meters, and the Pearl River Delta area is 80 million cubic meters, which will affect the water quality and shipping functions of the river. In the past, the method of desilting was to transport the sludge to the pen shell station for natural weathering, which would pollute the air again and waste material and financial resources. In the past, the sludge generated in the sewage project was disposed of by stacking or discarding, which not only caused a lot of waste of land resources, but also caused irreparable damage to the ecological environment, and the heavy metal ions and organic compounds contained in the sludge It will cause secondary pollution to the surrounding soil and air.
传统的笔壳在晚上不易辨认,丢弃后会使白色污染严重化,而且有些笔墨气味较重,尤其一些视力在夜晚明显下降的人群,不易辨认的问题就会更加明显。Traditional pen casings are not easy to identify at night, and white pollution will become serious after being discarded, and some pens and inks have a strong smell, especially for some people whose vision decreases significantly at night, the problem of not being easy to identify will be more obvious.
发明内容Contents of the invention
本发明针对上述存在的问题提供一种工艺简单、成本低廉的利用活性污泥生产可降解珠光笔壳的方法,一方面利用废物的再利用实现污水治理,减少废物对环境的污染,另一方面生产得到的珠光笔壳降解后可以变成有机肥料,同时,带珠光的笔壳有利于夜间对其位置的快速识别,由于活性炭的会减轻墨水的气味。The present invention aims at the above-mentioned problems and provides a method for producing degradable pearl pen shells using activated sludge with simple process and low cost. On the one hand, the recycling of wastes is used to realize sewage treatment and reduce the pollution of wastes to the environment. On the other hand, The produced pearlescent pen shell can be turned into organic fertilizer after degradation. At the same time, the pearlescent pen shell is conducive to the rapid identification of its position at night, and the odor of ink will be reduced due to the activated carbon.
本发明所采用的技术方案是:一种可降解珠光笔壳的制备方法,包括:The technical solution adopted in the present invention is: a preparation method of a degradable pearl pen shell, comprising:
1)将各组分物质按照以下重量份数的配比加入到高速混合机中,混合均匀;1) Add each component material into the high-speed mixer according to the following proportions by weight, and mix evenly;
助剂:包括硬脂酸钠、偶联剂以及相容剂,其中,硬脂酸钠为活性炭粉质量的2%;偶联剂为活性炭粉质量的1%;相容剂为总质量的3%-5%;Auxiliaries: including sodium stearate, coupling agent and compatibilizer, wherein, sodium stearate is 2% of the mass of activated carbon powder; coupling agent is 1% of the mass of activated carbon powder; compatibilizer is 3% of the total mass %-5%;
2)将步骤1)所得混合物通过单螺杆挤出机塑化挤出,造粒并通过模压二次加工即得到可生物降解珠光笔壳。2) The mixture obtained in step 1) is plasticized and extruded by a single-screw extruder, granulated and subjected to secondary processing by molding to obtain a biodegradable pearl pen case.
作为优选,所述活性污泥粉末采用以下驯化方法驯化后干燥得到,As a preference, the activated sludge powder is obtained by drying after domestication by the following domestication method,
首先,按照质量比BOD5:C:N:P=100:75:5:1的比例配制模拟废水作为培养液,备用;First, according to the ratio of mass ratio BOD 5 :C:N:P=100:75:5:1, simulated waste water is prepared as a culture solution for later use;
然后,将来自于市政污泥处理厂的活性污泥及所述培养液加入有效容积15L的SBR反应池中,搅拌曝气,在好氧条件下,每12小时换水一次,即每个泥龄12小时,包括10.5小时的搅拌曝气、1小时的静置和0.5小时的换水;Then, add the activated sludge and the culture solution from the municipal sludge treatment plant into the SBR reaction tank with an effective volume of 15L, stir and aerate, and under aerobic conditions, change the water once every 12 hours, that is, every sludge Aged for 12 hours, including 10.5 hours of agitation and aeration, 1 hour of standing and 0.5 hours of water change;
第1-6天,每次换水3L,并控制DO值为1.5mg/L;On the 1st-6th day, change the water 3L each time, and control the DO value to 1.5mg/L;
第7-12天,每次换水4.5L,并控制DO值为2.0mg/L;On the 7th-12th day, change the water 4.5L each time, and control the DO value to 2.0mg/L;
第13-18天,每次换水6L,并控制DO值为2.5mg/L;On the 13th-18th day, change the water 6L each time, and control the DO value to 2.5mg/L;
其中,在静置和换水阶段,控制DO值不低于0.2mg/L;Among them, in the stage of standing still and changing water, the DO value should not be lower than 0.2mg/L;
驯化过程中保持污泥液的pH值在6.5-8.0之间,温度在24-26℃之间;During the domestication process, keep the pH value of the sludge solution between 6.5-8.0 and the temperature between 24-26°C;
18天后即可得到驯化后的活性污泥。After 18 days, the acclimated activated sludge can be obtained.
作为优选,所述高分子材料包括PVC、PP、PS。Preferably, the polymer material includes PVC, PP, PS.
作为优选,所述纤维粉末为农作物秸秆粉末。Preferably, the fiber powder is crop straw powder.
作为优选,所述的珠光色母粒包括PLA和123珠光粉。Preferably, the pearlescent masterbatch includes PLA and 123 pearlescent powder.
作为优选,所述PLA和123珠光粉的重量比为(25—35):10。Preferably, the weight ratio of PLA and 123 pearl powder is (25-35):10.
作为优选,所述粘合剂为热塑性弹性体,如TPU(热塑性聚氨酯弹性体)、TPV(热塑性硫化橡胶)等。Preferably, the adhesive is a thermoplastic elastomer, such as TPU (thermoplastic polyurethane elastomer), TPV (thermoplastic vulcanizate) and the like.
作为优选,所述偶联剂为硅烷偶联剂。Preferably, the coupling agent is a silane coupling agent.
作为优选,所述相容剂为PE-g-MAH。Preferably, the compatibilizer is PE-g-MAH.
一种采用所述方法制备的可降解珠光笔壳。A degradable pearl pen case prepared by the method.
本发明的有益效果是:The beneficial effects of the present invention are:
1、采用生活中的废物—污泥和秸秆作为原料,一方面实现了废物的再利用,另一方面避免了现有污泥处理方法带来的二次污染,减少了秸秆燃烧对环境的污染;此外,所得笔壳可完全降解,且降解后可作为肥料改良土壤。1. Using domestic waste—sludge and straw as raw materials, on the one hand, it realizes the reuse of waste, on the other hand, it avoids the secondary pollution caused by the existing sludge treatment method, and reduces the environmental pollution caused by straw burning ; In addition, the obtained pen shell can be completely degraded, and can be used as fertilizer to improve soil after degradation.
2、对来自市政污泥处理厂的污泥进行驯化处理并干燥成粉末后作为原料,实现废物再利用的同时,解决了污水的治理问题;此外,污泥经过驯化之后富含聚羟基脂肪酸钠,这种可降解材料性能优异,是一种天然可降解材料。2. The sludge from the municipal sludge treatment plant is domesticated and dried into powder as a raw material, which realizes the reuse of waste and solves the problem of sewage treatment; in addition, the sludge is rich in polyhydroxy fatty acid sodium after domestication , this degradable material has excellent performance and is a natural degradable material.
3、本发明技术通过加入活性炭粉,可以增加笔壳的净化笔尖周围的空气的能力。3. The technology of the present invention can increase the ability of the pen case to purify the air around the pen tip by adding activated carbon powder.
4、具有低碳环保、工艺简单、生产效率高和成本低廉的特点。4. It has the characteristics of low-carbon environmental protection, simple process, high production efficiency and low cost.
5、本发明在产品中加入碳酸钙,可以增强笔壳的强度,使笔壳不易被摔坏。5. The present invention adds calcium carbonate to the product, which can enhance the strength of the pen case and make the pen case not easy to be broken.
6、本发明还可以通过调整生产配方,生产出在半年到五年范围内完全降解掉的可降解笔壳。6. The present invention can also produce degradable pen casings that are completely degraded within half a year to five years by adjusting the production formula.
7、增加了PLA和123珠光粉,制成的珠光笔寒风有利于人们在夜间对珠光笔壳的快速识别。7. PLA and 123 pearlescent powder are added, and the cold wind of the pearlescent pen made is conducive to people's quick recognition of the pearlescent pen shell at night.
具体实施方式detailed description
本发明利用模拟废水驯化并发酵干燥后的污泥和一些农作物秸秆粉和活性炭粉以及高分子材料、碳酸钙、粘合剂、PLA和123珠光粉等物料,倒入高速混合机中搅拌均匀,再通过单螺杆挤出机塑化挤出,造粒,模压二次加工得到可生物降解笔壳,不同的模具可以得到不同的产品,通风冷却干燥后即可制成所需要的可降解夜光笔壳制品。In the present invention, the simulated waste water is used to domesticate, ferment and dry the sludge, some crop straw powder, activated carbon powder, polymer material, calcium carbonate, adhesive, PLA and 123 pearl powder, and pour them into a high-speed mixer to stir evenly. Then plasticize and extrude through a single-screw extruder, granulate, and mold for secondary processing to obtain a biodegradable pen case. Different molds can obtain different products. After ventilation, cooling and drying, the required biodegradable luminous pen can be made. shell products.
下面对本发明一种可降解珠光笔壳的制备方法的实施步骤作进一步描述:The implementation steps of the preparation method of a kind of degradable pearl pen shell of the present invention are further described below:
实施例1:Example 1:
首先,将各组分物质按照以下重量份数的配比加入到高速混合机中,加热搅拌,2h后搅拌均匀;First, add each component material into the high-speed mixer according to the following proportions by weight, heat and stir, and stir evenly after 2 hours;
助剂:包括硬脂酸钠、偶联剂以及相容剂,其中,硬脂酸钠为活性炭粉质量的2%;偶联剂为活性炭粉质量的1%;相容剂的份数为总质量的3%;Auxiliary agent: comprise sodium stearate, coupling agent and compatibilizer, wherein, sodium stearate is 2% of the quality of activated carbon powder; Coupling agent is 1% of the quality of activated carbon powder; The parts of compatibilizer are total 3% of mass;
其中珠光色母粒为生物降解塑料聚乳酸(PLA)和123珠光粉的混合物,两者的重量比为25:10。Among them, the pearlescent masterbatch is a mixture of biodegradable plastic polylactic acid (PLA) and 123 pearlescent powder, and the weight ratio of the two is 25:10.
然后,将步骤1)所得混合物通过单螺杆挤出机塑化挤出,造粒,模压二次加工得到可生物降解珠光笔壳,不同的模具可以得到不同的产品,通风冷却干燥后即可制成所需要的可降解珠光笔壳制品。Then, the mixture obtained in step 1) is plasticized and extruded by a single-screw extruder, granulated, and molded for secondary processing to obtain a biodegradable pearl pen shell. Different molds can obtain different products, which can be produced after ventilation, cooling and drying. Into the required degradable pearl pen shell products.
所用的活性污泥粉末应该是经梯度动态好养驯化并发酵干燥后的污泥粉末,因为它富含聚羟基脂肪酸酯,可以更好地与其他组分混合,具体制备工艺为:The activated sludge powder used should be the sludge powder that has been domesticated by gradient dynamic cultivation and fermented and dried, because it is rich in polyhydroxyalkanoate and can be better mixed with other components. The specific preparation process is:
1)按照质量比BOD5:C:N:P=100:75:5:1的比例配制模拟废水作为培养液备用;模拟废水中的碳由醋酸钠提供,氮由氯化铵提供,磷由磷酸氢二钾提供;1) According to the ratio of mass ratio BOD 5 :C:N:P=100:75:5:1, the simulated waste water is prepared as the culture medium for standby; the carbon in the simulated waste water is provided by sodium acetate, the nitrogen is provided by ammonium chloride, and the phosphorus is provided by Dipotassium hydrogen phosphate provides;
2)将来自于市政污泥处理厂的活性污泥及步骤1)所得培养液加入到20L的SBR反应池(有效容积15L)中,搅拌曝气,在好氧条件下,每12小时换水一次,即每个泥龄12小时,包括10.5小时的搅拌曝气、1小时的静置和0.5小时的换水;2) Add the activated sludge from the municipal sludge treatment plant and the culture solution obtained in step 1) into a 20L SBR reaction tank (effective volume 15L), stir and aerate, and change the water every 12 hours under aerobic conditions Once, that is, each mud age is 12 hours, including 10.5 hours of agitation and aeration, 1 hour of standing and 0.5 hours of water change;
第1-6天,每次换水3L(先排出3L废水,再加入3L步骤1所得培养液),并控制DO值为1.5mg/L;在静置和换水阶段,控制DO值不低于0.2mg/L;On the first 1-6 days, change the water 3L each time (discharge 3L of waste water first, then add 3L of the culture solution obtained in step 1), and control the DO value to 1.5mg/L; during the static and water change stages, control the DO value is not low At 0.2mg/L;
第7-12天,每次换水4.5L(先排出4.5L废水,再加入4.5L步骤1所得培养液),并控制DO值(溶解氧,下同)为2.0mg/L;在静置和换水阶段,控制DO值不低于0.2mg/L;On the 7th-12th day, change the water 4.5L each time (discharge 4.5L of waste water first, then add 4.5L of the culture solution obtained in step 1), and control the DO value (dissolved oxygen, the same below) to 2.0mg/L; During the water change stage, the DO value should not be lower than 0.2mg/L;
第13-18天,每次换水6L(先排出6L废水,再加入6L步骤1所得培养液),并控制DO值为2.5mg/L;在静置和换水阶段,控制DO值不低于0.2mg/L;保证驯化期间随着换水量的增大适当增加曝气量和搅拌速度。On the 13th-18th day, change the water 6L each time (discharge 6L of waste water first, then add 6L of the culture solution obtained in step 1), and control the DO value to 2.5mg/L; in the stage of standing and changing water, control the DO value is not low at 0.2mg/L; ensure that the aeration rate and stirring speed are appropriately increased with the increase of water exchange volume during the acclimation period.
在整个驯化过程当中,通过1mol/L的HCL或NaOH调节污泥液的pH值,使之维持在6.5-8.0之间;温度通过室内柜式空调或加热棒稳定在24-26℃之间,以保证微生物的平稳生长。During the whole domestication process, adjust the pH value of the sludge liquid by 1mol/L HCL or NaOH to maintain it between 6.5-8.0; the temperature is stabilized between 24-26°C through indoor cabinet air conditioners or heating rods, To ensure the stable growth of microorganisms.
经过18天的培养驯化,污泥颜色由黑色变成红褐色,有明显的腥味,沉降性能取得了明显的提高,最终结果30分钟的SV(settling velocity,污泥沉降比,又称30分钟沉降率)为25-30%,SVI(sludge volume index,污泥容积指数)的值为75-90,并且MLVSS(mixed liquorvolatile suspended solids,混合液挥发性悬浮固体浓度,表示混合液活性污泥中有机性固体物质部分的浓度)稳定在3500-4500mg/L之间,排出去的废水的CODCR降解率大于85%。After 18 days of cultivation and acclimatization, the sludge color changed from black to reddish brown, with obvious fishy smell, and the settling performance was significantly improved. The final result was 30 minutes of SV (settling velocity, sludge sedimentation ratio, also known as 30 minutes Settling rate) is 25-30%, the value of SVI (sludge volume index, sludge volume index) is 75-90, and MLVSS (mixed liquorvolatile suspended solids, the concentration of volatile suspended solids in the mixed liquor indicates that the mixed liquor activated sludge The concentration of the organic solid matter part) is stable between 3500-4500 mg/L, and the COD CR degradation rate of the discharged wastewater is greater than 85%.
所述高分子材料可以为PVC、PP、PS等。The polymer material can be PVC, PP, PS and so on.
所述纤维粉末取自于过去常常被燃烧产生污染和浪费的农作物秸秆(比如玉米秸秆、小麦秸秆、大豆秸秆、甘蔗秸秆、水稻秸秆等),并将其碾碎成粉末至20目;;秸秆富含氮、磷、钾、钙、镁和有机质等,是一种具有多用途的可再生的生物资源,降解后可以变成土壤养分。The fiber powder is taken from crop straws (such as corn straw, wheat straw, soybean straw, sugarcane straw, rice straw, etc.) that are often burned to produce pollution and waste, and crushed into powder to 20 mesh; Rich in nitrogen, phosphorus, potassium, calcium, magnesium and organic matter, etc., it is a multi-purpose renewable biological resource that can be turned into soil nutrients after degradation.
活性炭粉用来加入其中提高材料的空气净化能力,它的加入可以吸附甲醛、甲苯、二氧化硫、二氧化碳、氨等有害气体,具有一定的空气净化功能,能够减轻笔壳周围的难闻异味,并使发明的笔壳具有可降解的性质,使笔壳的性能更加优异。Activated carbon powder is used to improve the air purification ability of the material. Its addition can absorb harmful gases such as formaldehyde, toluene, sulfur dioxide, carbon dioxide, and ammonia. The invented pen case is degradable, which makes the performance of the pen case more excellent.
所述粘合剂为热塑性弹性体、合成橡胶等常用于将两种分离的材料连接在一起的溶剂,如TPU、TPV等。The adhesive is a solvent such as thermoplastic elastomer, synthetic rubber, etc. commonly used to connect two separated materials together, such as TPU, TPV, and the like.
碳酸钙的加入可以增强笔壳的强度,使笔壳不易破碎。The addition of calcium carbonate can enhance the strength of the pen shell and make the pen shell not easy to break.
助剂整体用于促进物料混合均匀,其中,硬脂酸钠在这里作为润滑剂,用来提高塑料的熔融状态下的融合性,增加可加工性;偶联剂(本例中为硅烷偶联剂)是用来改良塑料的分散性,使其易于混合,粘合性增大;相容剂(本例中为PE-g-MAH)的加入是为了防止制成的笔壳制品发生脱层现象,主要是活性炭粉和粘合剂之间的相容性。The auxiliary agent is used as a whole to promote the uniform mixing of materials. Among them, sodium stearate is used as a lubricant here to improve the fusion of the plastic in the molten state and increase the processability; the coupling agent (silane coupling in this example) agent) is used to improve the dispersibility of the plastic, making it easy to mix and increase the adhesiveness; the addition of the compatibilizer (PE-g-MAH in this case) is to prevent the delamination of the pen shell products made Phenomenon, mainly the compatibility between activated carbon powder and binder.
实施例2:Example 2:
首先,将各组分物质按照以下重量份数的配比加入到高速混合机中,加热搅拌,2h后搅拌均匀;First, add each component material into the high-speed mixer according to the following proportions by weight, heat and stir, and stir evenly after 2 hours;
助剂:包括硬脂酸钠、偶联剂以及相容剂,其中,硬脂酸钠为活性炭粉质量的2%;偶联剂为活性炭粉质量的1%;相容剂为总质量的5%。Auxiliary agent: including sodium stearate, coupling agent and compatibilizer, wherein, sodium stearate is 2% of the quality of activated carbon powder; Coupling agent is 1% of the quality of activated carbon powder; Compatibilizer is 5% of the total mass %.
其中,珠光色母粒为生物降解塑料聚乳酸(PLA)和123珠光粉的混合物,两者的重量比为30:10。Among them, the pearlescent masterbatch is a mixture of biodegradable plastic polylactic acid (PLA) and 123 pearlescent powder, and the weight ratio of the two is 30:10.
然后,将步骤1)所得混合物通过单螺杆挤出机塑化挤出,造粒,模压二次加工得到可生物降解珠光笔壳,不同的模具可以得到不同的产品,通风冷却干燥后即可制成所需要的可降解珠光笔壳制品。Then, the mixture obtained in step 1) is plasticized and extruded by a single-screw extruder, granulated, and molded for secondary processing to obtain a biodegradable pearl pen shell. Different molds can obtain different products, which can be produced after ventilation, cooling and drying. Into the required degradable pearl pen shell products.
所用的活性污泥粉末应该是经梯度动态好养驯化并发酵干燥后的污泥粉末,因为它富含聚羟基脂肪酸酯,可以更好地与其他组分混合,具体制备工艺为:The activated sludge powder used should be the sludge powder that has been domesticated by gradient dynamic cultivation and fermented and dried, because it is rich in polyhydroxyalkanoate and can be better mixed with other components. The specific preparation process is:
1)按照质量比BOD5:C:N:P=100:75:5:1的比例配制模拟废水作为培养液备用;模拟废水中的碳由醋酸钠提供,氮由氯化铵提供,磷由磷酸氢二钾提供;1) According to the ratio of mass ratio BOD 5 :C:N:P=100:75:5:1, the simulated waste water is prepared as the culture medium for standby; the carbon in the simulated waste water is provided by sodium acetate, the nitrogen is provided by ammonium chloride, and the phosphorus is provided by Dipotassium hydrogen phosphate provides;
2)将来自于市政污泥处理厂的活性污泥及步骤1)所得培养液加入到20L的SBR反应池(有效容积15L)中,搅拌曝气,在好氧条件下,每12小时换水一次,即每个泥龄12小时,包括10.5小时的搅拌曝气、1小时的静置和0.5小时的换水;2) Add the activated sludge from the municipal sludge treatment plant and the culture solution obtained in step 1) into a 20L SBR reaction tank (effective volume 15L), stir and aerate, and change the water every 12 hours under aerobic conditions Once, that is, each mud age is 12 hours, including 10.5 hours of agitation and aeration, 1 hour of standing and 0.5 hours of water change;
第1-6天,每次换水3L(先排出3L废水,再加入3L步骤1所得培养液),并控制DO值为1.5mg/L;在静置和换水阶段,控制DO值不低于0.2mg/L;On the 1st to 6th day, change the water 3L each time (discharge 3L of waste water first, then add 3L of the culture solution obtained in step 1), and control the DO value to 1.5mg/L; in the stage of standing and changing water, control the DO value is not low at 0.2mg/L;
第7-12天,每次换水4.5L(先排出4.5L废水,再加入4.5L步骤1所得培养液),并控制DO值(溶解氧,下同)为2.0mg/L;在静置和换水阶段,控制DO值不低于0.2mg/L;On the 7th-12th day, change the water 4.5L each time (discharge 4.5L of waste water first, then add 4.5L of the culture solution obtained in step 1), and control the DO value (dissolved oxygen, the same below) to 2.0mg/L; During the water change stage, the DO value should not be lower than 0.2mg/L;
第13-18天,每次换水6L(先排出6L废水,再加入6L步骤1所得培养液),并控制DO值为2.5mg/L;在静置和换水阶段,控制DO值不低于0.2mg/L;保证驯化期间随着换水量的增大适当增加曝气量和搅拌速度。On the 13th-18th day, change the water 6L each time (discharge 6L of waste water first, then add 6L of the culture solution obtained in step 1), and control the DO value to 2.5mg/L; in the stage of standing and changing water, control the DO value is not low at 0.2mg/L; ensure that the aeration rate and stirring speed are appropriately increased with the increase of water exchange volume during the acclimation period.
在整个驯化过程当中,通过1mol/L的HCL或NaOH调节污泥液的pH值,使之维持在6.5-8.0之间;温度通过室内柜式空调或加热棒稳定在24-26℃之间,以保证微生物的平稳生长。During the whole domestication process, adjust the pH value of the sludge liquid by 1mol/L HCL or NaOH to maintain it between 6.5-8.0; the temperature is stabilized between 24-26°C through indoor cabinet air conditioners or heating rods, To ensure the stable growth of microorganisms.
经过18天的培养驯化,污泥颜色由黑色变成红褐色,有明显的腥味,沉降性能取得了明显的提高,最终结果30分钟的SV(settling velocity,污泥沉降比,又称30分钟沉降率)为25-30%,SVI(sludge volume index,污泥容积指数)的值为75-90,并且MLVSS(mixed liquorvolatile suspended solids,混合液挥发性悬浮固体浓度,表示混合液活性污泥中有机性固体物质部分的浓度)稳定在3500-4500mg/L之间,排出去的废水的CODCR降解率大于85%。After 18 days of cultivation and acclimatization, the sludge color changed from black to reddish brown, with obvious fishy smell, and the settling performance was significantly improved. The final result was 30 minutes of SV (settling velocity, sludge sedimentation ratio, also known as 30 minutes Settling rate) is 25-30%, the value of SVI (sludge volume index, sludge volume index) is 75-90, and MLVSS (mixed liquorvolatile suspended solids, the concentration of volatile suspended solids in the mixed liquor indicates that the mixed liquor activated sludge The concentration of the organic solid matter part) is stable between 3500-4500 mg/L, and the COD CR degradation rate of the discharged wastewater is greater than 85%.
所述高分子材料可以为PVC、PP、PS等。The polymer material can be PVC, PP, PS and so on.
所述纤维粉末取自于过去常常被燃烧产生污染和浪费的农作物秸秆(比如玉米秸秆、小麦秸秆、大豆秸秆、甘蔗秸秆、水稻秸秆等),并将其碾碎成粉末至30目;秸秆富含氮、磷、钾、钙、镁和有机质等,是一种具有多用途的可再生的生物资源,降解后可以变成土壤养分。The fiber powder is taken from crop straws (such as corn straw, wheat straw, soybean straw, sugarcane straw, rice straw, etc.) Containing nitrogen, phosphorus, potassium, calcium, magnesium and organic matter, etc., it is a multi-purpose renewable biological resource that can be turned into soil nutrients after degradation.
活性炭粉用来加入其中提高材料的空气净化能力,它的加入可以吸附甲醛、甲苯、二氧化硫、二氧化碳、氨等有害气体,具有一定的空气净化功能,能够减轻笔壳周围的难闻异味,并使发明的笔壳具有可降解的性质,使笔壳的性能更加优异。Activated carbon powder is used to improve the air purification ability of the material. Its addition can absorb harmful gases such as formaldehyde, toluene, sulfur dioxide, carbon dioxide, and ammonia. The invented pen case is degradable, which makes the performance of the pen case more excellent.
所述粘合剂为热塑性弹性体、合成橡胶等常用于将两种分离的材料连接在一起的溶剂,如TPU、TPV等。The adhesive is a solvent such as thermoplastic elastomer, synthetic rubber, etc. commonly used to connect two separated materials together, such as TPU, TPV, and the like.
碳酸钙的加入可以增强笔壳的强度,使笔壳不易破碎。The addition of calcium carbonate can enhance the strength of the pen shell and make the pen shell not easy to break.
助剂整体用于促进物料混合均匀,其中,硬脂酸钠在这里作为润滑剂,用来提高塑料的熔融状态下的融合性,增加可加工性;偶联剂(本例中为硅烷偶联剂)是用来改良塑料的分散性,使其易于混合,粘合性增大;相容剂(本例中为PE-g-MAH)的加入是为了防止制成的笔壳制品发生脱层现象,主要是活性炭粉和粘合剂之间的相容性。The auxiliary agent is used as a whole to promote the uniform mixing of materials. Among them, sodium stearate is used as a lubricant here to improve the fusion of the plastic in the molten state and increase the processability; the coupling agent (silane coupling in this example) agent) is used to improve the dispersibility of the plastic, making it easy to mix and increase the adhesiveness; the addition of the compatibilizer (PE-g-MAH in this case) is to prevent delamination of the finished pen shell product Phenomenon, mainly the compatibility between activated carbon powder and binder.
实施例3:Example 3:
首先,将各组分物质按照以下重量份数的配比加入到高速混合机中,加热搅拌,2h后搅拌均匀;First, add each component material into the high-speed mixer according to the following proportions by weight, heat and stir, and stir evenly after 2 hours;
助剂:包括硬脂酸钠、偶联剂以及相容剂,其中,硬脂酸钠为活性炭粉质量的2%;偶联剂为活性炭粉质量的1%;相容剂的份数为总质量的4%。Auxiliary agent: comprise sodium stearate, coupling agent and compatibilizer, wherein, sodium stearate is 2% of the quality of activated carbon powder; Coupling agent is 1% of the quality of activated carbon powder; The parts of compatibilizer are total 4% of mass.
其中,珠光色母粒为生物降解塑料聚乳酸(PLA)和123珠光粉的混合物,两者的重量比为35:10。Among them, the pearlescent masterbatch is a mixture of biodegradable plastic polylactic acid (PLA) and 123 pearlescent powder, and the weight ratio of the two is 35:10.
然后,将步骤1)所得混合物通过单螺杆挤出机塑化挤出,造粒,模压二次加工得到可生物降解珠光笔壳,不同的模具可以得到不同的产品,通风冷却干燥后即可制成所需要的可降解珠光笔壳制品。Then, the mixture obtained in step 1) is plasticized and extruded by a single-screw extruder, granulated, and molded for secondary processing to obtain a biodegradable pearl pen shell. Different molds can obtain different products, which can be produced after ventilation, cooling and drying. Into the required degradable pearl pen shell products.
所用的活性污泥粉末应该是经梯度动态好养驯化并发酵干燥后的污泥粉末,因为它富含聚羟基脂肪酸酯,可以更好地与其他组分混合,具体制备工艺为:The activated sludge powder used should be the sludge powder that has been domesticated by gradient dynamic cultivation and fermented and dried, because it is rich in polyhydroxyalkanoate and can be better mixed with other components. The specific preparation process is:
1)按照质量比BOD5:C:N:P=100:75:5:1的比例配制模拟废水作为培养液备用;模拟废水中的碳由醋酸钠提供,氮由氯化铵提供,磷由磷酸氢二钾提供;1) According to the ratio of mass ratio BOD 5 :C:N:P=100:75:5:1, the simulated waste water is prepared as the culture medium for standby; the carbon in the simulated waste water is provided by sodium acetate, the nitrogen is provided by ammonium chloride, and the phosphorus is provided by Dipotassium hydrogen phosphate provides;
2)将来自于市政污泥处理厂的活性污泥及步骤1)所得培养液加入到20L的SBR反应池(有效容积15L)中,搅拌曝气,在好氧条件下,每12小时换水一次,即每个泥龄12小时,包括10.5小时的搅拌曝气、1小时的静置和0.5小时的换水;2) Add the activated sludge from the municipal sludge treatment plant and the culture solution obtained in step 1) into a 20L SBR reaction tank (effective volume 15L), stir and aerate, and change the water every 12 hours under aerobic conditions Once, that is, each mud age is 12 hours, including 10.5 hours of agitation and aeration, 1 hour of standing and 0.5 hours of water change;
第1-6天,每次换水3L(先排出3L废水,再加入3L步骤1所得培养液),并控制DO值为1.5mg/L;在静置和换水阶段,控制DO值不低于0.2mg/L;On the first 1-6 days, change the water 3L each time (discharge 3L of waste water first, then add 3L of the culture solution obtained in step 1), and control the DO value to 1.5mg/L; during the static and water change stages, control the DO value is not low at 0.2mg/L;
第7-12天,每次换水4.5L(先排出4.5L废水,再加入4.5L步骤1所得培养液),并控制DO值(溶解氧,下同)为2.0mg/L;在静置和换水阶段,控制DO值不低于0.2mg/L;On the 7th-12th day, change the water 4.5L each time (discharge 4.5L of waste water first, then add 4.5L of the culture solution obtained in step 1), and control the DO value (dissolved oxygen, the same below) to 2.0mg/L; During the water change stage, the DO value should not be lower than 0.2mg/L;
第13-18天,每次换水6L(先排出6L废水,再加入6L步骤1所得培养液),并控制DO值为2.5mg/L;在静置和换水阶段,控制DO值不低于0.2mg/L;且随着换水量的增大适当增加曝气量和搅拌速度。On the 13th-18th day, change the water 6L each time (discharge 6L of waste water first, then add 6L of the culture solution obtained in step 1), and control the DO value to 2.5mg/L; in the stage of standing and changing water, control the DO value is not low at 0.2mg/L; and increase the aeration rate and stirring speed appropriately with the increase of water exchange volume.
在整个驯化过程当中,通过1mol/L的HCL或NaOH调节污泥液的pH值,使之维持在6.5-8.0之间;温度通过室内柜式空调或加热棒稳定在24-26℃之间,以保证微生物的平稳生长。During the whole domestication process, adjust the pH value of the sludge liquid by 1mol/L HCL or NaOH to maintain it between 6.5-8.0; the temperature is stabilized between 24-26°C through indoor cabinet air conditioners or heating rods, To ensure the stable growth of microorganisms.
经过18天的培养驯化,污泥颜色由黑色变成红褐色,有明显的腥味,沉降性能取得了明显的提高,最终结果30分钟的SV(settling velocity,污泥沉降比,又称30分钟沉降率)为25-30%,SVI(sludge volume index,污泥容积指数)的值为75-90,并且MLVSS(mixed liquorvolatile suspended solids,混合液挥发性悬浮固体浓度,表示混合液活性污泥中有机性固体物质部分的浓度)稳定在3500-4500mg/L之间,排出去的废水的CODCR降解率大于85%。After 18 days of cultivation and acclimatization, the sludge color changed from black to reddish brown, with obvious fishy smell, and the settling performance was significantly improved. The final result was 30 minutes of SV (settling velocity, sludge sedimentation ratio, also known as 30 minutes Settling rate) is 25-30%, the value of SVI (sludge volume index, sludge volume index) is 75-90, and MLVSS (mixed liquorvolatile suspended solids, the concentration of volatile suspended solids in the mixed liquor indicates that the mixed liquor activated sludge The concentration of the organic solid matter part) is stable between 3500-4500 mg/L, and the COD CR degradation rate of the discharged wastewater is greater than 85%.
所述高分子材料可以为PVC、PP、PS等。The polymer material can be PVC, PP, PS and so on.
所述纤维粉末取自于过去常常被燃烧产生污染和浪费的农作物秸秆(比如玉米秸秆、小麦秸秆、大豆秸秆、甘蔗秸秆、水稻秸秆等),并将其碾碎成粉末至40目;秸秆富含氮、磷、钾、钙、镁和有机质等,是一种具有多用途的可再生的生物资源,降解后可以变成土壤养分。The fiber powder is taken from crop straws (such as corn straw, wheat straw, soybean straw, sugarcane straw, rice straw, etc.) Containing nitrogen, phosphorus, potassium, calcium, magnesium and organic matter, etc., it is a multi-purpose renewable biological resource that can be turned into soil nutrients after degradation.
活性炭粉用来加入其中提高材料的空气净化能力,它的加入可以吸附甲醛、甲苯、二氧化硫、二氧化碳、氨等有害气体,具有一定的空气净化功能,能够减轻笔壳周围的难闻异味,并使发明的笔壳具有可降解的性质,使笔壳的性能更加优异。Activated carbon powder is used to improve the air purification ability of the material. Its addition can absorb harmful gases such as formaldehyde, toluene, sulfur dioxide, carbon dioxide, and ammonia. The invented pen case is degradable, which makes the performance of the pen case more excellent.
所述粘合剂为热塑性弹性体、合成橡胶等常用于将两种分离的材料连接在一起的溶剂,如TPU、TPV等。The adhesive is a solvent such as thermoplastic elastomer, synthetic rubber, etc. commonly used to connect two separated materials together, such as TPU, TPV, and the like.
碳酸钙的加入可以增强笔壳的强度,使笔壳不易破碎。The addition of calcium carbonate can enhance the strength of the pen shell and make the pen shell not easy to break.
助剂整体用于促进物料混合均匀,其中,硬脂酸钠在这里作为润滑剂,用来提高塑料的熔融状态下的融合性,增加可加工性;偶联剂(本例中为硅烷偶联剂)是用来改良塑料的分散性,使其易于混合,粘合性增大;相容剂(本例中为PE-g-MAH)的加入是为了防止制成的笔壳制品发生脱层现象,主要是活性炭粉和粘合剂之间的相容性。The auxiliary agent is used as a whole to promote the uniform mixing of materials. Among them, sodium stearate is used as a lubricant here to improve the fusion of the plastic in the molten state and increase the processability; the coupling agent (silane coupling in this example) agent) is used to improve the dispersibility of the plastic, making it easy to mix and increase the adhesiveness; the addition of the compatibilizer (PE-g-MAH in this case) is to prevent delamination of the finished pen shell product Phenomenon, mainly the compatibility between activated carbon powder and binder.
Claims (9)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410815155.0A CN104530597B (en) | 2014-12-24 | 2014-12-24 | Biodegradable pearlescent pen shell and preparation method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410815155.0A CN104530597B (en) | 2014-12-24 | 2014-12-24 | Biodegradable pearlescent pen shell and preparation method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN104530597A CN104530597A (en) | 2015-04-22 |
CN104530597B true CN104530597B (en) | 2017-02-08 |
Family
ID=52846245
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201410815155.0A Expired - Fee Related CN104530597B (en) | 2014-12-24 | 2014-12-24 | Biodegradable pearlescent pen shell and preparation method thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN104530597B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105440621B (en) * | 2016-01-15 | 2017-05-03 | 大连晶彩色母粒有限公司 | PLA noctilucence master batch and preparation method thereof |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101864104B (en) * | 2010-07-09 | 2012-07-11 | 安徽科聚新材料有限公司 | Sludge-filled polyethylene material and preparation method thereof |
CN102226020B (en) * | 2011-04-08 | 2012-11-21 | 吉林市龙运化工有限公司 | Easily degradable and environment friendly plastic and manufacturing method thereof |
CN103665524A (en) * | 2013-12-11 | 2014-03-26 | 南京聚锋新材料有限公司 | Paper sludge-polyolefin type composite sectional bar and preparation method thereof |
-
2014
- 2014-12-24 CN CN201410815155.0A patent/CN104530597B/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
CN104530597A (en) | 2015-04-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104530596B (en) | A kind of method utilizing activated sludge to produce degradation plastic | |
CN102936169B (en) | Starch-base material capable of achieving fertilizer slow release and enriching radionuclide and preparation method of material | |
CN109535670B (en) | A kind of fully degradable simulation material and preparation method thereof | |
CN1037515C (en) | Biodegradable starch-containing polymer composition and preparation method thereof | |
CN107118428B (en) | High-strength easily-degradable polyethylene plastic bag | |
CN102924939B (en) | Waste tire rubber powder-filled plastic wood profile and preparation method thereof | |
CN1415651A (en) | Method for preparing amylaceous fully degradable plastic | |
CN110902821A (en) | Solid carbon source suitable for denitrification of high-concentration nitrate-nitrogen sewage and preparation method thereof | |
WO2007134492A1 (en) | Fully biodegradable plastic resin, film article made therefrom and method for preparing the same | |
CN103756270A (en) | Full biodegrade mulch master batch as well as preparation method and application thereof | |
CN107586441B (en) | Wine lees-based composite material and process for preparing 3D printing wire by using same | |
CN101654528B (en) | Biodegradable resin for agricultural film and production method thereof | |
CN103665524A (en) | Paper sludge-polyolefin type composite sectional bar and preparation method thereof | |
CN104370581A (en) | Method for producing high-quality organic fertilizer from household refuse | |
US20220049077A1 (en) | Method of producing bioplastic pellets using livestock manure method of producing bioplastic pellets using livestock manure | |
CN108517076A (en) | A kind of degradable plastic uptake sheet material and preparation method thereof | |
CN103435986B (en) | A kind of residual actived sludge that utilizes is for the method for degradable mulch and mulch film | |
CN112940389A (en) | Anaerobic degradation material and preparation method thereof | |
CN104548921B (en) | Biological deodorizing filler and preparation method thereof | |
CN104558959B (en) | Degradable noctilucent dust bin and manufacturing method thereof | |
CN104530597B (en) | Biodegradable pearlescent pen shell and preparation method thereof | |
CN103771584B (en) | Anaerobic granular sludge and engineering fast culture method thereof | |
CN108410090A (en) | A kind of degradable environmentally-friendly plastic and preparation method thereof | |
CN106854014B (en) | Biological carrier for anaerobic anoxic section of sewage treatment and preparation method and application thereof | |
CN104530599B (en) | A method of using activated sludge to produce degradable garbage bins |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
CB03 | Change of inventor or designer information |
Inventor after: Wan Junmin Inventor after: Wei Meng Inventor before: Wei Meng Inventor before: Wan Junmin |
|
COR | Change of bibliographic data | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170208 Termination date: 20201224 |