CN1562442A - High density fibrous filter plate and manufacturing method - Google Patents
High density fibrous filter plate and manufacturing method Download PDFInfo
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- CN1562442A CN1562442A CN 200410018781 CN200410018781A CN1562442A CN 1562442 A CN1562442 A CN 1562442A CN 200410018781 CN200410018781 CN 200410018781 CN 200410018781 A CN200410018781 A CN 200410018781A CN 1562442 A CN1562442 A CN 1562442A
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 27
- 239000000835 fiber Substances 0.000 claims abstract description 142
- 239000004113 Sepiolite Substances 0.000 claims abstract description 82
- 229910052624 sepiolite Inorganic materials 0.000 claims abstract description 82
- 235000019355 sepiolite Nutrition 0.000 claims abstract description 82
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 55
- 238000010009 beating Methods 0.000 claims abstract description 37
- 238000001035 drying Methods 0.000 claims abstract description 23
- 239000000853 adhesive Substances 0.000 claims abstract description 22
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- 238000000034 method Methods 0.000 claims abstract description 22
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- 239000004372 Polyvinyl alcohol Substances 0.000 claims abstract description 8
- 229920002451 polyvinyl alcohol Polymers 0.000 claims abstract description 8
- 229920002134 Carboxymethyl cellulose Polymers 0.000 claims abstract description 6
- 229920000877 Melamine resin Polymers 0.000 claims abstract description 6
- 239000001768 carboxy methyl cellulose Substances 0.000 claims abstract description 6
- 235000010948 carboxy methyl cellulose Nutrition 0.000 claims abstract description 6
- 239000008112 carboxymethyl-cellulose Substances 0.000 claims abstract description 6
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 claims abstract description 6
- 230000014759 maintenance of location Effects 0.000 claims description 13
- 239000002002 slurry Substances 0.000 claims description 12
- 238000003756 stirring Methods 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 229920001131 Pulp (paper) Polymers 0.000 claims description 10
- 238000002156 mixing Methods 0.000 claims description 10
- 239000002245 particle Substances 0.000 claims description 6
- 230000001376 precipitating effect Effects 0.000 claims description 5
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 claims description 4
- 238000000465 moulding Methods 0.000 claims description 4
- 238000005728 strengthening Methods 0.000 claims 5
- 239000003153 chemical reaction reagent Substances 0.000 claims 4
- 229920003656 Daiamid® Polymers 0.000 claims 1
- 238000000227 grinding Methods 0.000 claims 1
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- 238000004513 sizing Methods 0.000 claims 1
- 238000001914 filtration Methods 0.000 abstract description 22
- 238000010438 heat treatment Methods 0.000 abstract description 21
- 230000015572 biosynthetic process Effects 0.000 abstract description 11
- 238000003786 synthesis reaction Methods 0.000 abstract description 11
- 229920002873 Polyethylenimine Polymers 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 4
- 230000004907 flux Effects 0.000 abstract description 4
- 239000012784 inorganic fiber Substances 0.000 abstract description 3
- 231100000252 nontoxic Toxicity 0.000 abstract description 3
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- 238000004062 sedimentation Methods 0.000 description 3
- 238000010008 shearing Methods 0.000 description 3
- 241001465754 Metazoa Species 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 244000025254 Cannabis sativa Species 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
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- 229920002522 Wood fibre Polymers 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
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Abstract
本发明涉及一种高密度纤维过滤板及其制造方法技术,其产品的重量百分比配方为:海泡石纤维15-68;纸浆纤维25-84.3;胶粘剂0.1-2;湿强剂0.5-3;干强剂0.1-2,所述海泡石纤维的直径为10-100μm、长度为200-1000μm;纸浆纤维为无机纤维或植物纤维中的任一种、两种或两种以上混合的纸浆纤维;胶粘剂为聚乙烯醇或环氧树脂;湿强剂为聚乙烯亚胺、聚酰胺环氧树脂或三聚氰胺;干强剂为羧甲基纤维素或聚丙烯酰胺。所述制造方法包括:1.制取海泡石纤维;2.海泡石纤维打浆;3.纸浆纤维打浆;4.配置混合浆;5.抄造与合成;6.烘缸加温;7.剪切成型以及它们的相关工艺参数。本发明过滤板孔隙率高,通量大,过滤效果好,同时无毒卫生,制造成本低;其制造方法简单,操作容易,常规设备生产,便于实施。The invention relates to a high-density fiber filter plate and its manufacturing method. The weight percent formula of the product is: sepiolite fiber 15-68; pulp fiber 25-84.3; adhesive 0.1-2; wet strength agent 0.5-3; Dry strength agent 0.1-2, the diameter of the sepiolite fiber is 10-100 μm, the length is 200-1000 μm; the pulp fiber is any one of inorganic fibers or plant fibers, or two or more pulp fibers mixed ; The adhesive is polyvinyl alcohol or epoxy resin; the wet strength agent is polyethyleneimine, polyamide epoxy resin or melamine; the dry strength agent is carboxymethyl cellulose or polyacrylamide. The manufacturing method includes: 1. preparing sepiolite fiber; 2. beating sepiolite fiber; 3. beating pulp fiber; 4. configuring mixed pulp; 5. papermaking and synthesis; 6. drying cylinder heating; 7. Shear forming and their associated process parameters. The filter plate of the invention has high porosity, large flux, good filtering effect, non-toxic sanitation and low manufacturing cost; the manufacturing method is simple, the operation is easy, conventional equipment is produced, and the implementation is convenient.
Description
技术领域technical field
本发明涉及纤维过滤板及其制造方法技术,具体为一种以海泡石纤维作为功能成分的高密度纤维过滤板及其制造方法技术,国际专利分类号拟为Int.Cl7.B01D 29/00。The invention relates to a fiber filter plate and its manufacturing method technology, specifically a high-density fiber filter plate with sepiolite fiber as a functional component and its manufacturing method technology. The international patent classification number is proposed to be Int.Cl7.B01D 29/00 .
背景技术Background technique
纤维过滤板是一种用于牛顿流体过滤的工业材料,主要使用于过滤各种果酒、白酒、啤酒、果汁、饮料,食油以及石油、保健液等。现有的纤维过滤板一般可以分为两种:一种是由合成纤维和植物纤维(如木纤维、草纤维等)材料抄造的过滤板;另一种是由石棉和纸浆制成的过滤板。前者造价较高,且过滤精度低,通量小,易堵塞(使用时间短);后者虽然造价可以降低,但过滤精度和通量同样不高,过滤效果也不好,特别是石棉制品是国家限制使用的材料,如果石棉纤维过滤板用于过滤的液体涉及人用或畜用,将会带来直接危险或潜在的危害。Fiber filter plate is an industrial material used for Newtonian fluid filtration, mainly used for filtering various fruit wine, liquor, beer, fruit juice, beverage, cooking oil, petroleum, health care liquid, etc. The existing fiber filter plates can generally be divided into two types: one is a filter plate made of synthetic fiber and plant fiber (such as wood fiber, grass fiber, etc.); the other is a filter plate made of asbestos and paper pulp. . The former has high cost, low filtration precision, small flux, and is easy to block (short service time); although the latter can reduce the cost, the filtration precision and flux are also not high, and the filtration effect is not good, especially asbestos products. The materials that are restricted by the state, if the liquid used for filtering by asbestos fiber filter board involves human or animal use, it will bring direct or potential harm.
发明内容Contents of the invention
针对现有技术的不足,本发明主要解决的技术问题就是提供一种高密度纤维过滤板及其制造方法技术,该纤维过滤板孔隙率高,通量大,过滤效果好,同时无毒卫生,制造成本也低;该纤维过滤板制造方法具有方法简单,操作容易,可用常规设备生产检测,便于实施等优点。Aiming at the deficiencies of the prior art, the main technical problem to be solved by the present invention is to provide a high-density fiber filter plate and its manufacturing method technology. The fiber filter plate has high porosity, large flux, good filtering effect, and is non-toxic and sanitary. The manufacturing cost is also low; the manufacturing method of the fiber filter plate has the advantages of simple method, easy operation, production and testing with conventional equipment, and convenient implementation.
本发明解决所述高密度纤维过滤板产品技术问题的技术方案是:设计一种高密度纤维过滤板,其重量百分比配方为:The technical solution of the present invention to solve the technical problem of the high-density fiber filter plate product is: to design a high-density fiber filter plate, and its weight percentage formula is:
海泡石纤维 15-68;Sepiolite fiber 15-68;
纸浆纤维 25-84.3;Pulp fiber 25-84.3;
胶粘剂 0.1-2;Adhesive 0.1-2;
湿强剂 0.5-3;Wet strength agent 0.5-3;
干强剂 0.1-2,Dry strength agent 0.1-2,
所述的海泡石纤维是指直径为10-100μm、长度为200-1000μm的海泡石纤维;纸浆纤维是指无机纤维或植物纤维中的任一种、两种或两种以上混合的纸浆纤维;胶粘剂是指聚乙烯醇或环氧树脂;湿强剂是指聚乙烯亚胺、聚酰胺环氧树脂或三聚氰胺;干强剂是指羧甲基纤维素或聚丙烯酰胺。The sepiolite fiber refers to a sepiolite fiber with a diameter of 10-100 μm and a length of 200-1000 μm; pulp fiber refers to any one of inorganic fibers or plant fibers, or a mixture of two or more pulps fiber; adhesive refers to polyvinyl alcohol or epoxy resin; wet strength agent refers to polyethyleneimine, polyamide epoxy resin or melamine; dry strength agent refers to carboxymethyl cellulose or polyacrylamide.
本发明解决所述高密度纤维过滤板制造方法技术问题的技术方案是:设计一种所述高密度纤维过滤板的制造方法,包括如下工艺过程:The technical solution of the present invention to solve the technical problem of the manufacturing method of the high-density fiber filter plate is: to design a manufacturing method of the high-density fiber filter plate, including the following process:
1.制取海泡石纤维:将选好的海泡石矿粒超细粉碎,经风筛选后取得所述直径为10-100μm、长度为200-1000μm的海泡石纤维;1. Preparation of sepiolite fiber: superfinely crush the selected sepiolite ore particles, and obtain the sepiolite fiber with a diameter of 10-100 μm and a length of 200-1000 μm after wind screening;
2.海泡石纤维打浆:先将上述海泡石纤维加温,温度范围30-220℃,加温时间1-3h;再用标准打散器打散2-5min,尔后用打浆机打浆5-10min,打浆度为60-90°SR,打浆浓度为1-3%;2. Sepiolite fiber beating: first heat the above-mentioned sepiolite fiber, the temperature range is 30-220°C, and the heating time is 1-3h; then use a standard beater to break it up for 2-5min, and then beat it with a beater for 5 minutes -10min, the beating degree is 60-90°SR, and the beating concentration is 1-3%;
3.纸浆纤维打浆:把纸浆纤维用标准打散器打散20-50min,再用打浆机打浆20-50min,打浆度为10-50°SR,打浆浓度为2-4%;3. Pulp fiber beating: Disperse the pulp fiber with a standard breaker for 20-50 minutes, and then beat it with a beater for 20-50 minutes. The beating degree is 10-50°SR, and the beating concentration is 2-4%;
4.配置混合浆:在调浆箱中,先放入所述的纸浆纤维浆,再放入所述的海泡石纤维浆,加水搅拌,同时,把所述比例的胶粘剂、湿强剂和干强剂按次序放入调浆箱中,配置成混合浆;4. Configure mixed pulp: in the mixing box, first put the pulp fiber pulp, then put the sepiolite fiber pulp, add water and stir, at the same time, put the adhesive, wet strength agent and The dry strength agent is put into the pulp mixing box in sequence, and is configured into a mixed pulp;
5.抄造与合成:将所述的混合浆送长网机抄造,工艺条件为:5. Copying and synthesis: the mixed pulp is sent to the fourdrinier machine for copying, and the process conditions are:
车速0.5-2m/min;Speed 0.5-2m/min;
抄宽250-550mm;Copy width 250-550mm;
上网抄造浓度0.2-2%;The online copying concentration is 0.2-2%;
湿纸页合成厚度4-8mm;Wet paper composite thickness 4-8mm;
工作面成网花形;The working surface is in the shape of net flower;
6.烘缸加温:6. Drying cylinder heating:
烘缸温度50-150℃之间,烘干总时间为2-4小时,其中The temperature of the drying cylinder is between 50-150°C, and the total drying time is 2-4 hours, of which
初始温度50-80℃,时间为0.5-1小时;The initial temperature is 50-80°C, and the time is 0.5-1 hour;
提升温度80-150℃,时间为1-2小时;然后降温至80℃并保温,保温温度60-80℃,时间为0.5-1小时;Raise the temperature to 80-150°C for 1-2 hours; then lower the temperature to 80°C and keep it warm at 60-80°C for 0.5-1 hour;
成型厚度为3-6mm;Forming thickness is 3-6mm;
7.剪切成型:把烘干的高密度纤维过滤板按要求剪切成形。7. Shear forming: Cut the dried high-density fiber filter plate into shape as required.
本发明所述的高密度纤维过滤板配方中采用了适当比例的海泡石纤维,它是一种天然的非金属矿石,无毒、无味、无任何放射性元素,用其制成的纤维过滤板,用于涉及人或者动物的各种牛顿流体过滤时,没有直接或间接的危害之虞,是一种现代过滤材料,为清洁生产或绿色生产提供了必要而关键的条件。本发明纤维过滤板的过滤精度为0.1-50μm,过滤压力≤5×105Pa,过滤精度高于或优于现有技术,并且造价低,约是现有技术的70%,强度也符合有关行业规定,特别适用于各种带支撑机构的过滤机、板框机或压榨机等过滤设备使用。The high-density fiber filter plate formula of the present invention adopts appropriate proportion of sepiolite fiber, which is a kind of natural non-metallic ore, non-toxic, tasteless, without any radioactive elements, and the fiber filter plate made of it , when used in the filtration of various Newtonian fluids involving humans or animals, there is no direct or indirect risk of harm. It is a modern filter material that provides necessary and critical conditions for clean or green production. The filtration accuracy of the fiber filter plate of the present invention is 0.1-50 μm, the filtration pressure is ≤5×10 5 Pa, the filtration accuracy is higher or better than the prior art, and the cost is low, which is about 70% of the prior art, and the strength also meets the relevant requirements. According to industry regulations, it is especially suitable for the use of filter equipment such as filters with supporting mechanisms, plate and frame machines or presses.
本发明所述纤维过滤板制造方法中的各种材质均设计了加温活化处理和高温消毒工艺,因此可保证纤维过滤板不合任何有毒物质,安全卫生,完全适于涉及人用液体的过滤生产。本发明所述纤维过滤板制造方法对使用设备没有特殊要求,可以使用目前通用的设备和仪器,因此具有简单方便,操作容易,便于实施的优点。Various materials in the manufacturing method of the fiber filter plate of the present invention are designed with heating activation treatment and high-temperature disinfection process, so it can ensure that the fiber filter plate does not contain any toxic substances, is safe and hygienic, and is completely suitable for the filtration production involving liquids for human use . The manufacturing method of the fiber filter plate of the present invention has no special requirements on the equipment used, and can use current common equipment and instruments, so it has the advantages of simplicity, convenience, easy operation and convenient implementation.
具体实施方式Detailed ways
下面结合实施例对本发明作进一步叙述:The present invention will be further described below in conjunction with embodiment:
本发明设计的一种高密度纤维过滤板(以下简称过滤板)的重量百分比配方为:The weight percent formula of a kind of high-density fiber filter plate (hereinafter referred to as filter plate) designed by the present invention is:
海泡石纤维 15-68;Sepiolite fiber 15-68;
纸浆纤维 25-84.3;Pulp fiber 25-84.3;
胶粘剂 0.1-2;Adhesive 0.1-2;
湿强剂 0.5-3;Wet strength agent 0.5-3;
干强剂 0.1-2Dry strength agent 0.1-2
所述的海泡石纤维是指直径为10-100μm、长度为200-1000μm的海泡石纤维;纸浆纤维是指无机纤维或植物纤维中的任一种、两种或两种以上混合的纸浆纤维;胶粘剂是指聚乙烯醇或环氧树脂;湿强剂是指聚乙烯亚胺(PEI)、聚酰胺环氧树脂(PAE)或三聚氰胺;干强剂是指羧甲基纤维素或聚丙烯酰胺(PAM)。The sepiolite fiber refers to a sepiolite fiber with a diameter of 10-100 μm and a length of 200-1000 μm; pulp fiber refers to any one of inorganic fibers or plant fibers, or a mixture of two or more pulps fiber; adhesive refers to polyvinyl alcohol or epoxy resin; wet strength agent refers to polyethyleneimine (PEI), polyamide epoxy resin (PAE) or melamine; dry strength agent refers to carboxymethylcellulose or polypropylene amide (PAM).
现有技术的过滤板配方不含任何海泡石纤维,因此不具备海泡石纤维产生的功效性。本发明的过滤板之所以选取海泡石纤维含量为10-65%是经过了大量的试验研究的,因为海泡石纤维的含量多少会直接影响到本发明过滤板的过滤精度和强度。一般而言,海泡石纤维的含量多,则过滤板的过滤精度较高,且过滤板的柔软性较好,但其含量多则会削弱过滤板的强度,所以海泡石纤维的含量应控制在合理的范围内。海泡石有两大类:α型海泡石与β型海泡石。α型海泡石是一种纤维状物质,粉碎后即成为海泡石纤维。而β型海泡石粉碎后则为颗粒状。本发明过滤板需选用α型海泡石。所述的海泡石纤维即是指α型海泡石适当粉碎后的所得物。The filter plate formulations of the prior art do not contain any sepiolite fibers and therefore do not have the efficacy provided by the sepiolite fibers. The reason why the sepiolite fiber content of the filter plate of the present invention is selected as 10-65% is through a large number of experimental studies, because the content of the sepiolite fiber will directly affect the filtration accuracy and strength of the filter plate of the present invention. Generally speaking, if the content of sepiolite fiber is high, the filtration accuracy of the filter plate will be higher, and the flexibility of the filter plate will be better, but if the content is too high, the strength of the filter plate will be weakened, so the content of sepiolite fiber should be controlled within a reasonable range. There are two types of sepiolite: α-type sepiolite and β-type sepiolite. α-type sepiolite is a fibrous substance, which becomes sepiolite fiber after crushing. The β-type sepiolite is granular after crushing. The filter plate of the present invention needs to use α-type sepiolite. The said sepiolite fiber refers to the product obtained after proper pulverization of α-type sepiolite.
本发明过滤板配方中的胶粘剂可以增加纤维间的结合力,从而增加过滤板的强度;配方中选用湿强剂是考虑到过滤板的工作环境是在液体中,海泡石受到水的浸泡后强度会变低的原因。为了保证过滤板在液体中的工作强度,设计添加了湿强剂。湿强剂过多是一种浪费,太少则起不到所述的作用,应当设计合理的比例;同样道理,配方所选的干强剂是为使过滤板在干燥后能够保持一定强度,含量比例也应当合理。The adhesive in the filter plate formula of the present invention can increase the binding force between the fibers, thereby increasing the strength of the filter plate; the wet strength agent is selected in the formula to consider that the working environment of the filter plate is in the liquid, and the sepiolite is soaked in water. The reason why the intensity will become lower. In order to ensure the working strength of the filter plate in the liquid, a wet strength agent is added in the design. Too much wet strength agent is a waste, too little will not achieve the above effect, and a reasonable ratio should be designed; in the same way, the dry strength agent selected in the formula is to make the filter plate maintain a certain strength after drying. The content ratio should also be reasonable.
本发明过滤板的进一步特征是在配方中还设计了助留助滤剂和沉淀剂。添加助留助滤剂的作用是为了进一步增强过滤板的过滤功能,而添加沉淀剂的作用是为了进一步增加湿板纤维的结合力。所述的助留助滤剂是指聚丙烯酰胺或聚酰胺(PPE);所述的沉淀剂是指硫酸铝。本发明添加了助留助滤剂和沉淀剂后的重量百分比配方为:A further feature of the filter plate of the present invention is that a retention and drainage aid and a sedimentation agent are also designed in the formula. The role of adding retention and drainage aids is to further enhance the filtration function of the filter plate, and the role of adding a precipitant is to further increase the binding force of the wet plate fibers. The retention and drainage aid refers to polyacrylamide or polyamide (PPE); the precipitation agent refers to aluminum sulfate. The present invention has added the retention and drainage aid and the weight percent formula after the precipitating agent is:
海泡石纤维 15-64;Sepiolite fiber 15-64;
纸浆纤维 25-83.7;Pulp fiber 25-83.7;
胶粘剂 0.1-2;Adhesive 0.1-2;
湿强剂 0.5-3;Wet strength agent 0.5-3;
干强剂 0.1-2;Dry strength agent 0.1-2;
助留助滤剂 0.5-2;Retention and drainage aid 0.5-2;
沉淀剂 0.1-2。Precipitant 0.1-2.
本发明所述的过滤板制造方法包括如下工艺过程:Filter plate manufacturing method of the present invention comprises following process:
1.制取海泡石纤维:将选好的α型海泡石矿粒超细粉碎,采用先筛分后风选的方法制取得所述直径为10-100μm、长度为200-1000μm的海泡石纤维;1. Preparation of sepiolite fiber: superfinely pulverize the selected α-type sepiolite ore particles, and use the method of first screening and then winnowing to obtain the sea foam with a diameter of 10-100 μm and a length of 200-1000 μm. Foam fiber;
2.海泡石纤维打浆:先将上述海泡石纤维加温,温度范围30-220℃,加温时间1-3h;再用标准打散器打散2-5min,尔后用打浆机打浆5-10min,打浆度为60-90°SR,打浆浓度为1-3%;海泡石纤维打浆度不能过低,否则会把纤维切断;2. Sepiolite fiber beating: first heat the above-mentioned sepiolite fiber, the temperature range is 30-220°C, and the heating time is 1-3h; then use a standard beater to break it up for 2-5min, and then beat it with a beater for 5 minutes -10min, the beating degree is 60-90°SR, and the beating concentration is 1-3%; the beating degree of sepiolite fiber should not be too low, otherwise the fiber will be cut off;
3.纸浆纤维打浆:把纸浆纤维用标准打散器打散20-50min,再用打浆机打浆20-50min,打浆度为10-50°SR,打浆浓度为2-4%;3. Pulp fiber beating: Disperse the pulp fiber with a standard breaker for 20-50 minutes, and then beat it with a beater for 20-50 minutes. The beating degree is 10-50°SR, and the beating concentration is 2-4%;
4.配置混合浆:在调浆箱中,先放入所述的纸浆纤维浆,再放入所述的海泡石纤维浆,加水搅拌均匀,同时,把所述比例的胶粘剂、湿强剂和干强剂按次序放入调浆箱中,配置成混合浆;4. Configure mixed pulp: in the mixing box, first put the pulp fiber pulp, then put the sepiolite fiber pulp, add water and stir evenly, at the same time, put the adhesive and wet strength agent in the stated proportion and dry strength agent into the slurry mixing box in order to configure a mixed slurry;
5.抄造与合成:将所述的混合浆送长网机抄造,工艺条件为:5. Copying and synthesis: the mixed pulp is sent to the fourdrinier machine for copying, and the process conditions are:
车速0.5-2m/min;Speed 0.5-2m/min;
抄宽250-550mm;Copy width 250-550mm;
上网抄造浓度0.2-2%;The online copying concentration is 0.2-2%;
湿纸页合成厚度4-8mm;Wet paper composite thickness 4-8mm;
工作面成网花形;The working surface is in the shape of net flower;
6.烘缸加温:6. Drying cylinder heating:
烘缸温度50-150℃之间,烘干总时间为2-4小时,其中The temperature of the drying cylinder is between 50-150°C, and the total drying time is 2-4 hours, of which
初始温度50-80℃,时间为0.5-1小时;The initial temperature is 50-80°C, and the time is 0.5-1 hour;
提升温度80-150℃,时间为1-2小时;保温温度70-100℃,时间为0.5-1小时;Raise the temperature to 80-150°C, and the time is 1-2 hours; hold the temperature at 70-100°C, and the time is 0.5-1 hour;
成型厚度为3-6mm;Forming thickness is 3-6mm;
7.剪切成型:把烘干的纤维过滤板按要求剪切成形。例如,可以把本发明产品海泡石高密度纤维过滤板剪切成200×200、300×300、400×400或500×500mm的方形板材,或直径φ=200-400mm的圆形板材,或者符合各种带支撑机构的过滤机要求形状的板材等。7. Cutting and forming: cut and shape the dried fiber filter plate according to the requirements. For example, the sepiolite high-density fiber filter plate of the present invention can be cut into a square plate of 200×200, 300×300, 400×400 or 500×500mm, or a circular plate with a diameter of φ=200-400mm, or Plates, etc. that meet the shape requirements of various filters with support mechanisms.
当本发明过滤板的制造方法在采用所述的改进配方时,所添加的助留助滤剂和沉淀剂用于所述的工艺过程(4)配置混合浆中。具体工艺方法是,在把所述比例的胶粘剂、湿强剂和干强剂按次序放入调浆箱中后,再把所述比例的助留助滤剂和沉淀剂按次序放入调浆箱中,配置成混合浆。其余工艺方法与前相同。When the improved formula is used in the manufacturing method of the filter plate of the present invention, the added retention and drainage aids and sedimentation agents are used in the process (4) to configure the mixed slurry. The specific process is that after putting the adhesive, wet strength agent and dry strength agent in the stated proportions into the slurry mixing box in sequence, then put the retention and drainage aids and sedimentation aids in the stated proportions into the slurry mixing box in sequence In the box, it is configured as a mixed slurry. The rest of the process is the same as before.
本发明方法中没特别说明的技术内容均与现有制造纤维过滤板技术相同,本领域一般技术人员不经创造性劳动均可以具体实施。The technical content not specified in the method of the present invention is all the same as the existing technology of manufacturing fiber filter plates, and those skilled in the art can implement it without creative work.
下面给出本发明具体的实施例:Provide specific embodiments of the present invention below:
实施例1Example 1
过滤板的配方为(重量%):海泡石纤维30、纸浆纤维65、胶粘剂聚乙烯醇2、湿强剂聚乙烯亚胺2和干强剂聚丙烯酰胺1。其制造方法为:The formula of the filter plate is (% by weight): sepiolite fiber 30, pulp fiber 65, adhesive polyvinyl alcohol 2, wet strength agent polyethyleneimine 2 and dry strength agent polyacrylamide 1. Its manufacturing method is:
1.制取海泡石纤维:将选好的海泡石矿粒用粉碎机进行超细粉碎,经风筛选后制取得300g直径为10μm、长度为200μm的海泡石纤维;1. Preparation of sepiolite fiber: Superfinely pulverize the selected sepiolite ore particles with a pulverizer, and obtain 300g of sepiolite fiber with a diameter of 10 μm and a length of 200 μm after wind screening;
2.海泡石纤维打浆:先将上述海泡石纤维加温,加温温度为220℃,加温时间3小时,在标准打散器打散3min,在VALLEY打浆机打浆10min,打浆浓度为3%(即加水10Kg),打浆度为90°SR,制得海泡石纤维浆;2. Sepiolite fiber beating: first heat the above-mentioned sepiolite fiber, the heating temperature is 220°C, the heating time is 3 hours, it is dispersed in a standard beater for 3 minutes, and it is beaten in a VALLEY beater for 10 minutes. The beating concentration is 3% (i.e. adding 10Kg of water), the beating degree is 90 ° SR, and the sepiolite fiber pulp is obtained;
3.纸浆纤维打浆:用700g的木棉纤维在标准打散器打散30min,再用VALLEY打浆机打浆30min,打浆浓度为3%(即加水23Kg),打浆时间30min,打浆度30°SR;3. Pulp fiber beating: use 700g of kapok fiber to break up in a standard breaker for 30 minutes, then use a VALLEY beater to beat for 30 minutes, the beating concentration is 3% (that is, add water 23Kg), the beating time is 30 minutes, and the beating degree is 30°SR;
4.配置混合浆:把以上所得木棉纤维浆和海泡石纤维浆两种浆液依次先后放入调浆罐中,加水66Kg,搅拌均匀,浆浓度为1%,然后依次放入胶粘剂聚乙烯醇500g,搅拌;放入湿强剂聚乙烯亚胺500g,搅拌;放入干强剂聚丙烯酰胺300g;配置成混合浆。4. Configure the mixed pulp: put the above-mentioned kapok fiber pulp and sepiolite fiber pulp into the pulp mixing tank in sequence, add 66Kg of water, stir evenly, the pulp concentration is 1%, and then put the adhesive polyvinyl alcohol in turn 500g, stir; add 500g of wet strength agent polyethylenimine, stir; add 300g of dry strength agent polyacrylamide; configure as a mixed slurry.
5.抄造与合成:将所述的混合浆送长网机抄造,工艺条件为:车速1m/min、抄宽400mm、上网抄造浓度1%、纸页合成,合成厚度(湿纸页)为5mm、正面贴网纹纸0.2mm厚;5. Papermaking and synthesis: the mixed pulp is sent to fourdrinier machine for papermaking, and the process conditions are: speed 1m/min, papermaking width 400mm, papermaking concentration 1% on the Internet, paper synthesis, and synthetic thickness (wet paper) is 5mm , The front side is pasted with textured paper 0.2mm thick;
6.烘缸加温:烘缸温度控制在50-120℃之间,烘干总时间为3.5小时,其中初始温度为50℃,加温时间0.5小时;升温度到120℃,加温时间2小时;自然降到温度80℃后,保温时间1小时,成型厚度为4mm;6. Drying cylinder heating: the temperature of the drying cylinder is controlled between 50-120°C, and the total drying time is 3.5 hours, of which the initial temperature is 50°C, and the heating time is 0.5 hours; when the temperature is raised to 120°C, the heating time is 2 Hours; after the temperature is naturally lowered to 80°C, the holding time is 1 hour, and the molding thickness is 4mm;
7.剪切成型:将烘干好的过滤板整形,并剪切为300×300mm、厚度为4mm±(0.5mm)的产品海泡石高密度纤维过滤板。7. Shearing and forming: shape the dried filter plate and cut it into a sepiolite high-density fiber filter plate of 300×300mm and thickness of 4mm±(0.5mm).
经检测,该海泡石高密度纤维过滤板的过滤精度为0.3-0.5μm,过滤压力≤5×105Pa。After testing, the filtration accuracy of the sepiolite high-density fiber filter plate is 0.3-0.5 μm, and the filtration pressure is ≤5×10 5 Pa.
实施例2Example 2
过滤板的配方为(重量%):海泡石纤维19、纸浆纤维75、胶粘剂聚乙烯醇1.5、湿强剂聚酰胺环氧树脂2、干强剂羧甲基纤维素1、助留助滤剂聚酰胺1、沉淀剂硫酸铝0.5。其制造方法为:The formula of the filter plate is (% by weight): sepiolite fiber 19, pulp fiber 75, adhesive polyvinyl alcohol 1.5, wet strength agent polyamide epoxy resin 2, dry strength agent carboxymethyl cellulose 1, retention and drainage aid Agent polyamide 1, precipitant aluminum sulfate 0.5. Its manufacturing method is:
1.制取海泡石纤维:将选好的海泡石矿粒用粉碎机进行超细粉碎,经风筛选后制取得200g直径为10μm、长度为200μm的海泡石纤维;1. Preparation of sepiolite fiber: the selected sepiolite ore particles are ultra-finely crushed with a pulverizer, and 200g of sepiolite fiber with a diameter of 10 μm and a length of 200 μm is obtained after wind screening;
2.海泡石纤维打浆:先将上述海泡石纤维加温,加温温度为100℃,加温时间2小时,在标准打散器打散4min,在VALLEY打浆机打浆10min,打浆浓度为2%(即加水10Kg),打浆度为80°SR,制得海泡石纤维浆;2. Sepiolite fiber beating: first heat the above-mentioned sepiolite fiber, the heating temperature is 100°C, the heating time is 2 hours, it is dispersed in a standard beater for 4 minutes, and it is beaten in a VALLEY beater for 10 minutes. The beating concentration is 2% (i.e. adding 10Kg of water), the degree of beating is 80 ° SR, and the sepiolite fiber pulp is obtained;
3.纸浆纤维打浆:用400g的木浆纤维,400g的草浆纤维,在标准打散器打散40min,再用VALLEY打浆机打浆40min,打浆浓度为2%(即加水40Kg),打浆时间40min,打浆度40°SR;3. Pulp fiber beating: use 400g of wood pulp fiber and 400g of straw pulp fiber to break up for 40 minutes in a standard breaker, and then beat for 40 minutes with a VALLEY beater. , beating degree 40°SR;
4.配置混合浆:把以上所得木棉纤维浆和海泡石纤维浆两种浆液依次先后放入调浆罐中,加水16Kg,搅拌均匀,浆浓度为1%,然后依次放入胶粘剂聚乙烯醇200g,搅拌;放入湿强剂聚酰胺环氧树脂200g,搅拌;放入干强剂羧甲基纤维素200g;放入助留助滤剂聚酰胺200g;放入沉淀剂硫酸铝200g,配置成混合浆。4. Configure mixed pulp: Put the two kinds of pulp obtained above, kapok fiber pulp and sepiolite fiber pulp, into the slurry mixing tank one after another, add 16Kg of water, stir evenly, the pulp concentration is 1%, and then put the adhesive polyvinyl alcohol in turn 200g, stir; put in 200g of wet strength agent polyamide epoxy resin, stir; put in 200g of dry strength agent carboxymethyl cellulose; put in 200g of retention and drainage aid polyamide; put in 200g of precipitant aluminum sulfate, configure into a mixed slurry.
5.抄造与合成:将所述的混合浆送长网机抄造,工艺条件为:车速2m/min、抄宽450mm、上网抄造浓度1.5%、纸页合成,合成厚度(湿纸页)为5.3mm、正面贴网纹纸0.2mm厚;5. Papermaking and synthesis: the mixed pulp is sent to fourdrinier machine for papermaking, the process conditions are: speed of vehicle 2m/min, papermaking width 450mm, online papermaking concentration 1.5%, paper synthesis, synthesis thickness (wet paper) is 5.3 mm, front textured paper 0.2mm thick;
6.烘缸加温:烘缸温度控制在50-120℃之间,烘干总时间为2小时,其中初始温度为70℃,加温时间0.5小时;升温度到130℃,加温时间1小时;自然降到温度70℃后,保温时间0.5小时,成型厚度为5mm;6. Drying cylinder heating: The temperature of the drying cylinder is controlled between 50-120°C, and the total drying time is 2 hours, of which the initial temperature is 70°C, and the heating time is 0.5 hours; when the temperature is raised to 130°C, the heating time is 1 Hours; after the temperature is naturally lowered to 70°C, the holding time is 0.5 hours, and the molding thickness is 5mm;
7.剪切成型:将烘干好的过滤板整形,并剪切为400×400mm、厚度为5mm±(0.5mm)的产品海泡石高密度纤维过滤板。7. Shearing and forming: shape the dried filter plate and cut it into a sepiolite high-density fiber filter plate with a thickness of 5mm±(0.5mm) of 400×400mm.
经检测,该海泡石高密度纤维过滤板的过滤精度为0.5-1μm,过滤压力≤5×105Pa。After testing, the filtration precision of the sepiolite high-density fiber filter plate is 0.5-1 μm, and the filtration pressure is ≤5×10 5 Pa.
实施例3Example 3
过滤板的配方为(重量%):海泡石纤维65、纸浆纤维28、胶粘剂环氧树脂2、湿强剂三聚氰胺3、干强剂聚丙烯酰胺2。The formula of the filter plate is (weight%): sepiolite fiber 65, pulp fiber 28, adhesive epoxy resin 2, wet strength agent melamine 3, dry strength agent polyacrylamide 2.
纤维过滤板制造方法为:The manufacturing method of fiber filter plate is:
1.制取海泡石纤维:将选好的海泡石矿粒用粉碎机进行超细粉碎,经风筛选后制取得700g直径为10μm、长度为200μm的海泡石纤维;1. Preparation of sepiolite fiber: Superfine crush the selected sepiolite ore particles with a pulverizer, and obtain 700g of sepiolite fiber with a diameter of 10 μm and a length of 200 μm after wind screening;
2.海泡石纤维打浆:先将上述海泡石纤维加温,加温温度为50℃,加温时间2小时,在标准打散器打散3min,在VALLEY打浆机打浆5min,打浆浓度为1%(即加水70Kg),打浆度为85°SR,制得海泡石纤维浆;2. Sepiolite fiber beating: first heat the above-mentioned sepiolite fiber, the heating temperature is 50°C, the heating time is 2 hours, it is dispersed in a standard beater for 3 minutes, and it is beaten in a VALLEY beater for 5 minutes. The beating concentration is 1% (i.e. adding 70Kg of water), the degree of beating is 85 ° SR, and the sepiolite fiber slurry is obtained;
3.纸浆纤维打浆:用300g的木浆纤维,在标准打散器打散20min,再用VALLEY打浆机打浆50min,打浆浓度为4%(即加水7.5Kg),打浆时间40min,打浆度10°SR;3. Pulp fiber beating: Use 300g of wood pulp fiber, break it in a standard breaker for 20 minutes, and then use a VALLEY beater to beat it for 50 minutes. SR;
4.配置混合浆:把以上所得木棉纤维浆和海泡石纤维浆两种浆液依次先后放入调浆罐中,加水122.5Kg,搅拌均匀,浆浓度为0.5%,然后依次放入胶粘剂环氧树脂200g,搅拌;放入湿强剂三聚氰胺500g,搅拌;放入干强剂聚丙烯酰胺200g;配置成混合浆。4. Configure the mixed pulp: Put the above-mentioned kapok fiber pulp and sepiolite fiber pulp into the slurry mixing tank one after another, add 122.5Kg of water, stir evenly, the pulp concentration is 0.5%, and then put the adhesive epoxy in turn Add 200g of resin and stir; put in 500g of wet strength agent melamine and stir; put in 200g of dry strength agent polyacrylamide; configure it into a mixed slurry.
5.抄造与合成:将所述的混合浆送长网机抄造,工艺条件为:车速0.5m/min、抄宽350mm、上网抄造浓度0.5%、纸页合成,合成厚度(湿纸页)为4.5mm、正面贴网纹纸0.15mm厚;5. papermaking and synthesis: the mixed pulp is sent to fourdrinier machine for papermaking, the process conditions are: speed of vehicle 0.5m/min, papermaking width 350mm, online papermaking concentration 0.5%, paper synthesis, synthesis thickness (wet paper) is 4.5mm, front textured paper 0.15mm thick;
6.烘缸加温:烘缸温度控制在80-150℃之间,烘干总时间为4小时,其中初始温度为80℃,加温时间1小时;升温度到150℃,加温时间2小时;自然降到温度80℃后,保温时间1小时,成型厚度为4mm;6. Drying cylinder heating: The temperature of the drying cylinder is controlled between 80-150°C, and the total drying time is 4 hours, of which the initial temperature is 80°C, and the heating time is 1 hour; when the temperature is raised to 150°C, the heating time is 2 hours. Hours; after the temperature is naturally lowered to 80°C, the holding time is 1 hour, and the molding thickness is 4mm;
7.剪切成型:将烘干好的过滤板整形,并剪切为300×300mm、厚度为4mm±(0.5mm)的产品海泡石高密度纤维过滤板。7. Shearing and forming: shape the dried filter plate and cut it into a sepiolite high-density fiber filter plate of 300×300mm and thickness of 4mm±(0.5mm).
经检测,该海泡石高密度纤维过滤板的过滤精度为0.1-0.3μm,过滤压力≤5×105Pa。After testing, the filtration accuracy of the sepiolite high-density fiber filter plate is 0.1-0.3 μm, and the filtration pressure is ≤5×10 5 Pa.
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| CN109414637A (en) * | 2016-05-25 | 2019-03-01 | 尤尼弗瑞克斯 I 有限责任公司 | Filter cell and its manufacturing method |
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