WO2023109971A1 - Mineralized filter element and preparation method therefor - Google Patents

Mineralized filter element and preparation method therefor Download PDF

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WO2023109971A1
WO2023109971A1 PCT/CN2022/139917 CN2022139917W WO2023109971A1 WO 2023109971 A1 WO2023109971 A1 WO 2023109971A1 CN 2022139917 W CN2022139917 W CN 2022139917W WO 2023109971 A1 WO2023109971 A1 WO 2023109971A1
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modified
zeolite
pumice
hydrozincite
parts
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French (fr)
Chinese (zh)
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武中华
李键
谭俊
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青岛海尔施特劳斯水设备有限公司
海尔智家股份有限公司
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/68Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/281Treatment of water, waste water, or sewage by sorption using inorganic sorbents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/283Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/66Treatment of water, waste water, or sewage by neutralisation; pH adjustment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/02Non-contaminated water, e.g. for industrial water supply

Definitions

  • the modified hydrozincite is prepared by the following method: crushing, sieving, ultrasonic washing, filtering and drying the hydrozincite to obtain pretreated hydrozincite;
  • the pretreated hydrozincite is soaked in 0.8-1.2mol/L inorganic acid solution for 3-5 hours, the soaking temperature is 20-30°C, and acid-modified hydrozincite is obtained after washing; the acid-modified hydrozinc Soak ore in 1.0-1.4mol/L inorganic salt solution for 14-22 hours to obtain salt-modified hydrozincite; shake and shake the salt-modified hydrozincite at 20-30°C, and shake the
  • the hydrozincite is washed and dried to obtain the modified hydrozincite; wherein, the mesh size of the modified hydrozincite is 80-350 mesh.
  • the preparation method of mineralization filter element comprises the following steps:
  • dolomite, calcite, hydrozincite, zeolite and sea pumice The modification methods of dolomite, calcite, hydrozincite, zeolite and sea pumice are described respectively below. Among them, dolomite, calcite, hydrozincite, zeolite and sea pumice are all natural.
  • drying temperature can also be other temperatures such as 80°C and 120°C; the calcining temperature can also be other temperatures such as 700°C and 800°C; the calcining time can also be other times such as 0.5h and 1.5h; the amount of soaking water can also be 150m, 250ml and other water volumes, and can also be soaked in ultrapure water or tap water; the soaking time can also be 20min, 30min and other times; the flow rate of CO 2 gas can also be 0.01L/min, 0.1L/min, 1.0L /min and other flow rates; the carbonization reaction temperature can also be 400°C, 500°C and other temperatures; the carbonization reaction time can also be 1.0h, 2.0h and other times; the carbonization reaction heating time can also be 30min,
  • Modified calcite is prepared by the following method:
  • the calcite is crushed and sieved, and 80-220 mesh calcite is screened out.
  • 80-220 mesh calcite is screened out, and deionized water is used to wash the screened calcite with ultrasonic wave, filter, and put into drying in an oven, and sieving again to obtain modified calcite, that is, physically modified calcite.
  • the mesh number of the modified calcite is 80-220 mesh, and further, the mesh number of the modified calcite is 100-200 mesh.
  • ultrapure water or tap water can also be used to wash the pretreated calcite.
  • the pretreated hydrozincite was soaked in 1.0 mol/L hydrochloric acid solution for 4 hours at a constant temperature of 25° C., and washed with deionized water to obtain the acid-modified hydrozincite.
  • the inorganic acids listed above and their corresponding concentrations, soaking time, and soaking temperature, inorganic salts and their corresponding concentrations, soaking time, soaking temperature, and shaking temperature are only exemplary and not limiting.
  • the inorganic acid can also be other inorganic acids such as sulfuric acid, nitric acid, carbonic acid, etc.
  • the corresponding concentration of any inorganic acid can also be 0.8mol/L, 1.2mol/L, etc.
  • the soaking time can also be 3h, 5h, etc.
  • the soaking temperature can also be other temperatures such as 20°C, 23°C, 27°C, 30°C;
  • the inorganic salt can also be potassium carbonate, sodium chloride, potassium chloride and other inorganic salts, and the corresponding concentration of any inorganic salt can also be It can be 1.0mol/L, 1.4mol/L and other concentrations, and the soaking time can also be 14h, 16h, 20h, 22h and other times;
  • the shaking temperature can also be 20°C, 30°C and other temperatures.
  • ultrapure water or tap water can also be used to wash the hydrozincite.
  • the pretreated zeolite is put into a muffle furnace, calcined at 450° C. for 2.0 h, and after cooling, the calcined modified zeolite is obtained, which is put into a desiccator for airtight storage.
  • the 200W microwave is used to carry out microwave modification on the calcined modified zeolite to obtain the microwave modified zeolite.
  • organic acids listed above and their corresponding concentrations, soaking time, and shaking temperature are only exemplary and not limiting.
  • the organic acids can also be other organic acids such as citric acid and oxalic acid.
  • the soaking time corresponding to the organic acid can also be 27h, 29h, 35h, 37h and other times; the shaking temperature can also be other temperatures such as 20°C and 30°C. In practical applications, those skilled in the art can combine the above parameters arbitrarily.
  • sea pumice can also be washed by soaking in ultrapure water or tap water.
  • modified dolomite, modified calcite, modified hydrozincite, modified zeolite and modified sea pumice should be tested for chroma, turbidity, odor and taste in accordance with the GB 5479-2006 sanitary standard for drinking water. , Visible matter, pH and TDS were inspected, and the obtained modified dolomite and modified The content of aluminum, total chromium, manganese, iron, copper, zinc, arsenic, silver, cadmium, lead, antimony, nickel, tin, barium, etc.
  • modified dolomite, modified calcite, modified hydrozincite, modified zeolite and modified sea pumice can be used if they meet the above standards and specifications, further ensuring the safety of drinking water.
  • modified dolomite, calcite, hydrozincite, zeolite and sea pumice are improved, and particles of different particle sizes are prepared for mixing with activated carbon particles, activated carbon fibers and binders.
  • the main ingredients 50g of modified dolomite, 100g of modified calcite, 30g of modified hydrozincite, 30g of modified zeolite, and 20g of modified sea pumice; Rock, modified calcite, modified hydrozincite, modified zeolite and modified pumice were mixed evenly to obtain 230g of mineralized filter material, that is, more mineralized filter material was mixed in advance for subsequent use.
  • the main ingredients 20g of modified dolomite, 14g of modified calcite, 6g of modified hydrozincite, 6g of modified zeolite, 4g of modified sea pumice; the modified dolomite obtained by weighing Rock, modified calcite, modified hydrozincite, modified zeolite and modified sea pumice are mixed uniformly to obtain 50 g of mineralized filter material;
  • auxiliary materials 120g of activated carbon, 45g of binder.
  • proportions by weight of raw materials in the three examples listed above indicate that those skilled in the art can flexibly adjust and set the proportions by weight of raw materials according to actual water quality requirements in practical applications. Ratio, and adjust the sintering temperature, sintering time and sintering pressure accordingly according to the weight ratio of raw materials.
  • the experimental method is: at room temperature, conduct a water test. When the water is passed, the flow rate of pure water is 2.0L/min. When the water flow reaches 1000L, 2000L, 3500L and 4300L, 250ml water samples are taken for testing.
  • the lead metal precipitation test was carried out on the mineralization filter element prepared by the above method, and the mineralization filter element prepared by the present invention was respectively combined with the hydrozincite filter element, the hydrozinc mineralization filter element with A ore added, and the hydrozinc mineralization filter element with B ore added.
  • the effect of controlling the precipitation of lead metal in the hydrozinc mineralization filter element was compared.
  • the A ore is such as volcanic rock, diatomaceous earth, kaolin and other ores
  • the B ore is medical stone, zeolite, illite and other ores.
  • the mineralization filter element prepared by the present invention includes sea pumice, modified sea pumice and modified hydrozincite.

Abstract

The present invention relates to the technical field of the preparation of mineralized materials, and particularly provides a mineralized filter element and a preparation method therefor, with the aim to solve the problem of the unstable precipitation of mineral substances in existing mineralized filter elements. In order to achieve the purpose, the mineralized filter element of the present invention comprises the following raw materials in parts by weight: main materials: 1-40 parts of modified dolomite, 1-20 parts of modified calcite, 1-6 parts of modified hydrozincite, 1-6 parts of modified zeolite, and 1-4 parts of modified bryozoatum. Water filtered by the mineralized filter element is rich in beneficial mineral substances such as zinc and strontium, and reaches the national drinking water standard in China; moreover, under the interaction of the aforementioned raw materials, especially by means of the combined use of the modified bryozoatum and the modified hydrozincite, the mineralized filter element can effectively inhibit the precipitation of heavy metals such as lead, and there are no heavy metals exceeding the standard, thereby further ensuring the safety of the drinking water.

Description

矿化滤芯及其制备方法Mineralized filter element and preparation method thereof 技术领域technical field
本发明涉及矿化材料制备技术领域,具体提供一种锌和锶矿化滤芯及其制备方法。The invention relates to the technical field of preparation of mineralized materials, and specifically provides a zinc and strontium mineralized filter element and a preparation method thereof.
背景技术Background technique
水是人们生活中不可或缺的物质,因此饮水健康显得尤为重要。目前家用净水器已经逐步进入千家万户,为居民提供安全的饮用水。例如,反渗透净水机采用反渗透膜对自来水进行过滤,精度高达0.1nm,脱盐率高达95%,几乎能够将自来水中所有的物质过滤掉。在全国各地水质差异较大的环境下,反渗透净水机提供了较为安全的水质过滤技术。但是,水质中缺乏矿物质,长时间饮用不利于身体健康。Water is an indispensable substance in people's life, so drinking water health is particularly important. At present, household water purifiers have gradually entered thousands of households to provide residents with safe drinking water. For example, reverse osmosis water purifiers use reverse osmosis membranes to filter tap water, with a precision of up to 0.1nm and a desalination rate of up to 95%, which can filter out almost all substances in tap water. In the environment where the water quality varies greatly across the country, the reverse osmosis water purifier provides a safer water quality filtration technology. However, the lack of minerals in the water quality, long-term drinking is not conducive to health.
为了解决上述问题,现有技术中采用水质矿化技术来提高水中的款物质含量,目前主要有三种矿化方式:第一种在水中添加矿化液,第二种是在水中添加矿物添加剂,第三种是将可溶性钙盐、镁盐、钾盐、钠盐和粘性土混合造粒,制备矿化球。目前,矿化球是市面上的主要产品,但是,其前期溶解不受控制,特别是浸泡条件下,各种矿物质析出不稳定,无法提供真正意义上的健康水。In order to solve the above problems, water quality mineralization technology is used in the prior art to increase the content of minerals in water. At present, there are mainly three mineralization methods: the first is to add mineralization liquid to water, and the second is to add mineral additives to water. The third is to mix and granulate soluble calcium salt, magnesium salt, potassium salt, sodium salt and clay to prepare mineralized balls. At present, mineralized balls are the main product on the market, but their dissolution in the early stage is not controlled, especially under soaking conditions, the precipitation of various minerals is unstable, and it cannot provide healthy water in the true sense.
因此,本领域需要一种新的矿化滤芯及其制备方法来解决上述问题。Therefore, there is a need in the art for a new mineralization filter element and a preparation method thereof to solve the above problems.
发明内容Contents of the invention
本发明旨在解决上述技术问题,即,解决现有矿化滤芯矿物质析出不稳定的问题。The present invention aims to solve the above-mentioned technical problems, that is, solve the problem of unstable mineral precipitation in existing mineralization filter elements.
在第一方面,本发明提供了一种矿化滤芯,包括按以下重量份计的原料:主料:改性白云岩1~40份,改性方解石1~20份,改性水锌矿1~6份,改性沸石1~6份,改性海浮石1~4份。In a first aspect, the present invention provides a mineralization filter element, comprising the following raw materials in parts by weight: main ingredients: 1-40 parts of modified dolomite, 1-20 parts of modified calcite, 1 part of modified hydrozincite ~6 parts, 1~6 parts of modified zeolite, 1~4 parts of modified sea pumice.
在上述矿化滤芯的优选技术方案中,包括按以下重量份计的原料:主料:改性白云岩5~20份,改性方解石10份,改性水锌矿3份,改性沸石3份,改性海浮石2份。In the preferred technical scheme of the above-mentioned mineralization filter element, the raw materials in the following parts by weight are included: main ingredients: 5 to 20 parts of modified dolomite, 10 parts of modified calcite, 3 parts of modified hydrozincite, and 3 parts of modified zeolite Parts, 2 parts of modified sea pumice.
在上述矿化滤芯的优选技术方案中,还包括按以下重量份计的原料:辅料:活性炭50~240份,粘结剂10~90份。In the preferred technical solution of the above mineralization filter element, the following raw materials are also included in parts by weight: auxiliary materials: 50-240 parts of activated carbon, and 10-90 parts of binder.
在上述矿化滤芯的优选技术方案中,由按以下重量份计的原料制成:主料50~70份;辅料130~165份,其中,活性炭100~120份,粘结剂30~45份。In the preferred technical solution of the above-mentioned mineralization filter element, it is made of the following raw materials in parts by weight: 50-70 parts of main materials; 130-165 parts of auxiliary materials, of which 100-120 parts of activated carbon and 30-45 parts of binder .
在第二方面,本发明提供了一种优选技术方案中任一项所述的矿化滤芯的制备方法,所述制备方法包括下列步骤:改性:分别对白云岩、方解石、水锌矿、沸石和海浮石进行改性,得到改性白云岩、改性方解石、改性水锌矿、改性沸石和改性海浮石;配料:按照重量份分别称量所述改性白云岩、所述改性方解石、所述改性水锌矿、所述改性沸石、所述改性海浮石、活性炭和粘结剂;混合:将称量得到的所述改性白云岩、所述改性方解石、所述改性水锌矿、所述改性沸石和所述改性海浮石按照预设方法与所述活性炭和所述粘结剂进行混合,得到混合料;烧结成型:将所述混合料放入磨具中进行烧结,得到所述矿化滤芯。In a second aspect, the present invention provides a method for preparing the mineralized filter element described in any one of the preferred technical solutions, the preparation method comprising the following steps: modifying: respectively treating dolomite, calcite, hydrozincite, Zeolite and sea pumice are modified to obtain modified dolomite, modified calcite, modified hydrozincite, modified zeolite and modified sea pumice; ingredients: weigh the modified dolomite, the Modified calcite, the modified hydrozinsite, the modified zeolite, the modified sea pumice, activated carbon and binder; mixing: the weighed modified dolomite, the modified calcite , the modified hydrozinsite, the modified zeolite and the modified sea pumice are mixed with the activated carbon and the binder according to a preset method to obtain a mixture; sintering molding: the mixture put into a grinding tool for sintering to obtain the mineralized filter element.
在上述制备方法的优选技术方案中,所述改性白云岩通过以下方法制备:对所述白云岩进行超声波洗涤、干燥、粉碎、研磨和过筛处理,得到预处理白云岩;将所述预处理白云岩在700~800℃煅烧0.5~1.5h,冷却后,得到煅烧改性白云岩;将所述煅烧改性白云岩在150~250ml水中浸泡20~40min,将浸泡后的白云岩表面的水分去除之后置于管式炉中,以0.01-1.0L/min的流量通入CO 2气体,在400~500℃碳化反应1.0~3.0h,冷却后,得到所述改性白云岩;其中,所述改性白云岩的目数为20~140目。 In the preferred technical solution of the above preparation method, the modified dolomite is prepared by the following method: ultrasonically washing, drying, pulverizing, grinding and sieving the dolomite to obtain pretreated dolomite; Treat the dolomite at 700-800°C for 0.5-1.5 hours, and after cooling, obtain calcined modified dolomite; soak the calcined modified dolomite in 150-250ml of water for 20-40min, and soak the surface of the dolomite after soaking After the water is removed, put it in a tube furnace, feed CO2 gas at a flow rate of 0.01-1.0L/min, carbonize at 400-500°C for 1.0-3.0h, and cool to obtain the modified dolomite; wherein, The mesh number of the modified dolomite is 20-140 mesh.
在上述制备方法的优选技术方案中,所述改性方解石通过以下方法制备:对所述方解石进行粉碎和过筛处理,得到预处理方解石;对所述预处理方解石进行超生波洗涤、过滤、干燥和筛分处理,得到所述改性方解石;其中,所述改性方解石的目数为80~220目。In the preferred technical solution of the above preparation method, the modified calcite is prepared by the following method: crushing and sieving the calcite to obtain pretreated calcite; performing ultrasonic washing, filtering and drying the pretreated calcite and sieving treatment to obtain the modified calcite; wherein, the mesh number of the modified calcite is 80-220 mesh.
在上述制备方法的优选技术方案中,所述改性水锌矿通过以下方法制备:对所述水锌矿进行粉碎、过筛、超声波洗涤、过滤和干燥处理,得到预处理水锌矿;将所述预处理水锌矿在0.8~1.2mol/L的无机酸溶液中浸泡3~5h,浸泡温度为20~30℃,洗涤后得到酸改性水锌矿;将所述酸改性水锌矿在1.0~1.4mol/L的无机盐溶液中浸泡14~22h,得到盐改性水锌矿;将所述盐改性水锌矿在20~30℃振荡摇匀,并对摇匀后的水锌矿进行洗涤和干燥处理,得到所述改性水锌矿;其中,所述改性水锌矿的目数为80~350目。In the preferred technical solution of the above preparation method, the modified hydrozincite is prepared by the following method: crushing, sieving, ultrasonic washing, filtering and drying the hydrozincite to obtain pretreated hydrozincite; The pretreated hydrozincite is soaked in 0.8-1.2mol/L inorganic acid solution for 3-5 hours, the soaking temperature is 20-30°C, and acid-modified hydrozincite is obtained after washing; the acid-modified hydrozinc Soak ore in 1.0-1.4mol/L inorganic salt solution for 14-22 hours to obtain salt-modified hydrozincite; shake and shake the salt-modified hydrozincite at 20-30°C, and shake the The hydrozincite is washed and dried to obtain the modified hydrozincite; wherein, the mesh size of the modified hydrozincite is 80-350 mesh.
在上述制备方法的优选技术方案中,所述改性沸石通过以下方法制备:对所述沸石进行粉碎、过筛、超声波洗涤和干燥处理,得到预处理沸石;将所述预处理沸石在400~550℃煅烧1.5~3.5h,冷却后,得到煅烧改性沸石;使用150~350W微波对所述煅烧改性沸石进行微波改性,得到微波改性沸石;将所述微波改性沸石在0.8~1.2mol/L的无机酸溶液中浸泡3~5h,浸泡温度为20~30℃,洗涤后得到酸改性沸石;将所述酸改性沸石在0.5~0.9mol/L的无机盐溶液中浸泡22~26h,且每间隔4~5h振荡3~8min,得到盐改性沸石;对所述盐改性沸石进行固液分离、超声波洗涤、干燥和筛分处理,得到所述改性沸石;其中,所述改性沸石的目数为20~120目。In the preferred technical scheme of the above preparation method, the modified zeolite is prepared by the following method: crushing, sieving, ultrasonic washing and drying the zeolite to obtain a pretreated zeolite; Calcined at 550°C for 1.5 to 3.5 hours, and after cooling, a calcined modified zeolite was obtained; using a 150 to 350W microwave, microwave modified the calcined modified zeolite to obtain a microwave modified zeolite; the microwave modified zeolite was heated at 0.8 to Soak in 1.2mol/L inorganic acid solution for 3-5 hours, the soaking temperature is 20-30°C, and get acid-modified zeolite after washing; soak the acid-modified zeolite in 0.5-0.9mol/L inorganic salt solution 22 to 26 hours, and oscillating for 3 to 8 minutes at intervals of 4 to 5 hours to obtain a salt-modified zeolite; performing solid-liquid separation, ultrasonic washing, drying and sieving on the salt-modified zeolite to obtain the modified zeolite; wherein , the mesh number of the modified zeolite is 20-120 mesh.
在上述制备方法的优选技术方案中,所述改性海浮石通过以下方法制备:对所述海浮石进行粉碎、过筛、超声波洗涤和干燥处理,得到预处理海浮石;将所述预处理海浮石在有机酸溶液中浸泡27~37h,得到酸改性海浮石;将所述酸改性海浮石在20~30℃振荡摇匀,并对摇匀后的海浮石进行洗涤和干燥处理,得到所述改性海浮石;其中,所述改性海浮石的目数为40~220目。In the preferred technical solution of the above preparation method, the modified sea pumice is prepared by the following method: pulverizing, sieving, ultrasonic washing and drying the sea pumice to obtain pretreated sea pumice; The pumice is soaked in the organic acid solution for 27-37 hours to obtain the acid-modified pumice; the acid-modified pumice is shaken at 20-30° C., and the shaken pumice is washed and dried to obtain The modified sea pumice; wherein, the mesh of the modified sea pumice is 40-220 mesh.
在上述制备方法的优选技术方案中,“将称量得到的所述改性白云岩、所述改性方解石、所述改性水锌矿、所述改性沸石和所述改性海浮石按照预设方法与活性炭和粘结剂进行混合,得到混合料”的步骤具体包括:将称量得到的所述改性白云岩、所述改性方解石、所述改性水锌 矿、所述改性沸石和所述改性海浮石混合均匀,得到矿化滤料;将所述矿化滤料、所述活性炭和所述粘结剂混合均匀,得到所述混合料。In the preferred technical scheme of the above-mentioned preparation method, "the modified dolomite, the modified calcite, the modified hydrozinsite, the modified zeolite and the modified sea pumice obtained by weighing are The preset method is mixed with activated carbon and binder to obtain the "mixture". The step specifically includes: weighing the modified dolomite, the modified calcite, the modified hydrozinsite, the modified The non-toxic zeolite and the modified sea pumice are uniformly mixed to obtain a mineralized filter material; the mineralized filter material, the activated carbon and the binder are uniformly mixed to obtain the mixed material.
在上述制备方法的优选技术方案中,“将称量得到的所述改性白云岩、所述改性方解石、所述改性水锌矿、所述改性沸石和所述改性海浮石按照预设方法与活性炭和粘结剂进行混合,得到混合料”的步骤具体包括:将称量得到的所述改性白云岩、所述改性方解石、所述改性水锌矿、所述改性沸石和所述改性海浮石按照密度由小到大的顺序依次与所述活性炭和所述粘结剂进行混合,得到所述混合料。In the preferred technical scheme of the above-mentioned preparation method, "the modified dolomite, the modified calcite, the modified hydrozinsite, the modified zeolite and the modified sea pumice obtained by weighing are The preset method is mixed with activated carbon and binder to obtain the "mixture". The step specifically includes: weighing the modified dolomite, the modified calcite, the modified hydrozinsite, the modified The active zeolite and the modified sea pumice are sequentially mixed with the activated carbon and the binder according to the order of density from small to large to obtain the mixture.
在上述制备方法的优选技术方案中,“将所述混合料放入磨具中进行烧结,得到矿化滤芯”的步骤具体包括:将所述混合料放入磨具中,在100~160℃烧结20~60min,烧结压力为12~18MPa,冷却后得到所述矿化滤芯。In the preferred technical solution of the above preparation method, the step of "putting the mixed material into a grinding tool for sintering to obtain a mineralized filter element" specifically includes: putting the mixed material into a grinding tool, Sintering for 20-60 minutes, the sintering pressure is 12-18 MPa, and the mineralized filter element is obtained after cooling.
在上述矿化滤芯的优选技术方案中,本发明采用改性白云岩、改性方解石、改性水锌矿、改性沸石和改性海浮石为原料制备矿化滤芯,其中,白云岩能够析出锶、钙、镁元素,方解石能够析出钙元素并且调节pH值,沸石能够吸附重金属,水锌矿能够析出锌元素,海浮石能够有效抑制铅等重金属的析出,尤其是改性海浮石和改性水锌矿的配合使用,使得矿化滤芯能够析出锌的同时有效抑制铅等重金属的析出,确保了无重金属超标,确保了饮水用的安全,得到了一种可以稳定的析出锌、锶等有益的矿物质的滤芯。在上述原料的配合作用下,使得采用该矿化滤芯过滤后的水不仅含有钙、镁等元素,而且富含丰富的锌、锶等有益的矿物质,达到了国家饮用水标准,能够为用户提供安全的健康水。In the preferred technical solution of the above-mentioned mineralization filter element, the present invention adopts modified dolomite, modified calcite, modified hydrozincite, modified zeolite and modified sea pumice as raw materials to prepare mineralization filter element, wherein dolomite can be separated out Strontium, calcium, magnesium elements, calcite can precipitate calcium and adjust the pH value, zeolite can absorb heavy metals, hydrozincite can precipitate zinc, sea pumice can effectively inhibit the precipitation of heavy metals such as lead, especially modified sea pumice and modified The combined use of hydrozinc ore enables the mineralization filter element to precipitate zinc while effectively inhibiting the precipitation of heavy metals such as lead, ensuring that no heavy metals exceed the standard, ensuring the safety of drinking water, and obtaining a stable precipitation of zinc, strontium, etc. mineral filter. Under the cooperation of the above raw materials, the water filtered by the mineralized filter element not only contains elements such as calcium and magnesium, but also is rich in beneficial minerals such as zinc and strontium, which meets the national drinking water standard and can serve users Provide safe healthy water.
进一步地,将称量得到的改性白云岩、改性方解石、改性水锌矿、改性沸石和改性海浮石按照密度由小到大的顺序依次与活性炭和粘结剂进行混合,使得原料能够混合的更加均匀,对水的改善效果也更加均匀稳定。Further, the weighed modified dolomite, modified calcite, modified hydrozincite, modified zeolite and modified sea pumice are mixed with activated carbon and binder in order of density from small to large, so that The raw materials can be mixed more evenly, and the water improvement effect is also more uniform and stable.
附图说明Description of drawings
下面参照附图来描述本发明的控制方法,附图中:Describe control method of the present invention below with reference to accompanying drawing, in accompanying drawing:
图1是本发明的矿化滤芯的制备方法的流程图。Fig. 1 is the flow chart of the preparation method of the mineralization filter core of the present invention.
具体实施方式Detailed ways
下面参照附图来描述本发明的优选实施方式。本领域技术人员应当理解的是,这些实施方式仅仅用于解释本发明的技术原理,并非旨在限制本发明的保护范围。例如,尽管本申请是结合盐酸来描述的,但是,本发明的技术方案并不局限于此,在实际应用中,还可以采用硫酸、碳酸、硝酸等其他无机酸。Preferred embodiments of the present invention are described below with reference to the accompanying drawings. Those skilled in the art should understand that these embodiments are only used to explain the technical principles of the present invention, and are not intended to limit the protection scope of the present invention. For example, although the present application is described in conjunction with hydrochloric acid, the technical solution of the present invention is not limited thereto, and other inorganic acids such as sulfuric acid, carbonic acid, and nitric acid can also be used in practical applications.
下述实施例中的试验方法,如无特殊说明,均为常规方法;下述实施例中所用的原料、试剂材料等,如无特殊说明,均为市售购买产品。The test methods in the following examples, unless otherwise specified, are conventional methods; the raw materials, reagent materials, etc. used in the following examples, unless otherwise specified, are commercially available products.
基于背景技术中提出的技术问题,本发明提供了一种矿化滤料机器制备方法,旨在采用改性白云岩、改性方解石、改性水锌矿、改性沸石和改性海浮石为原料制备矿化滤芯,其中,白云岩能够析出锶、钙、镁元素,方解石能够析出钙元素并且调节pH值,沸石能够吸附重金属,水锌矿能够析出锌元素,海浮石能够有效抑制铅等重金属的析出,尤其是改性海浮石和改性水锌矿的配合使用,使得矿化滤芯能够析出锌的同时有效抑制铅等重金属的析出,确保了无重金属超标,确保了饮水用的安全,得到了一种可以稳定的析出锌、锶等有益的矿物质的滤芯。在上述原料的配合作用下,使得采用该矿化滤芯过滤后的水不仅含有钙、镁等元素,而且富含丰富的锌、锶等有益的矿物质,达到了国家饮用水标准,能够为用户提供安全的健康水。Based on the technical problems proposed in the background technology, the present invention provides a machine preparation method for mineralized filter material, aiming at using modified dolomite, modified calcite, modified hydrozincite, modified zeolite and modified sea pumice as Raw materials are used to prepare mineralized filter elements. Among them, dolomite can precipitate strontium, calcium, and magnesium elements, calcite can precipitate calcium elements and adjust the pH value, zeolite can absorb heavy metals, hydrozincite can precipitate zinc elements, sea pumice can effectively inhibit lead and other heavy metals The precipitation, especially the combined use of modified sea pumice and modified hydrozincite, enables the mineralization filter element to precipitate zinc while effectively inhibiting the precipitation of heavy metals such as lead, ensuring that no heavy metals exceed the standard, ensuring the safety of drinking water, and obtaining A filter element that can stably precipitate beneficial minerals such as zinc and strontium has been developed. Under the cooperation of the above raw materials, the water filtered by the mineralized filter element not only contains elements such as calcium and magnesium, but also is rich in beneficial minerals such as zinc and strontium, which meets the national drinking water standard and can serve users Provide safe healthy water.
首先参照图1,对本发明的矿化滤芯的制备方法进行描述。其中,图1是本发明的矿化滤芯的制备方法的流程图。Referring first to FIG. 1 , the preparation method of the mineralization filter element of the present invention will be described. Wherein, Fig. 1 is a flow chart of the preparation method of the mineralization filter element of the present invention.
如图1所示,矿化滤芯的制备方法包括下列步骤:As shown in Figure 1, the preparation method of mineralization filter element comprises the following steps:
S100、改性:分别对白云岩、方解石、水锌矿、沸石和海浮石进行改性,得到改性白云岩、改性方解石、改性水锌矿、改性沸石和改性海浮石;S100. Modification: modifying dolomite, calcite, hydrozinite, zeolite and sea pumice respectively to obtain modified dolomite, modified calcite, modified hydrozinite, modified zeolite and modified sea pumice;
S200、配料:按照重量份分别称量改性白云岩、改性方解石、改性水锌矿、改性沸石、改性海浮石、活性炭和粘结剂;S200, ingredients: weigh modified dolomite, modified calcite, modified hydrozincite, modified zeolite, modified sea pumice, activated carbon and binder respectively according to parts by weight;
S300、混合:将称量得到的改性白云岩、改性方解石、改性水锌矿、改性沸石和改性海浮石按照预设方法与活性炭和粘结剂进行混合,得到混合料;S300, mixing: mixing the weighed modified dolomite, modified calcite, modified hydrozincite, modified zeolite and modified sea pumice with activated carbon and binder according to a preset method to obtain a mixture;
S400、烧结成型:将混合料放入磨具中进行烧结,得到矿化滤芯。S400, sintering and forming: putting the mixture into a grinding tool for sintering to obtain a mineralized filter element.
其中,粘结剂为聚乙烯、聚氯乙烯等其他粘结剂。Wherein, the binder is other binders such as polyethylene and polyvinyl chloride.
下面分别对白云岩、方解石、水锌矿、沸石和海浮石的改性方法进行描述。其中,白云岩、方解石、水锌矿、沸石和海浮石均是天然的。The modification methods of dolomite, calcite, hydrozincite, zeolite and sea pumice are described respectively below. Among them, dolomite, calcite, hydrozincite, zeolite and sea pumice are all natural.
改性白云岩通过以下方法制备:Modified dolomite is prepared by the following method:
对白云岩进行超声波洗涤,然后在100℃干燥,对干燥后的白云岩进行粉碎、研磨和过筛处理,得到预处理白云岩,优选地,预处理白云岩的目数为20~140目,进一步地,预处理白云岩的目数为40~120目。Dolomite is ultrasonically washed, then dried at 100°C, and the dried dolomite is crushed, ground and sieved to obtain pretreated dolomite. Preferably, the pretreated dolomite has a mesh number of 20 to 140 mesh, Further, the mesh size of the pretreated dolomite is 40-120 mesh.
将预处理白云岩放入马弗炉中,在750℃煅烧1.0h,冷却后,得到煅烧改性白云岩,放入干燥器内密闭保存。The pretreated dolomite is put into a muffle furnace, calcined at 750° C. for 1.0 h, and after cooling, the calcined modified dolomite is obtained, which is put into a desiccator for airtight storage.
将煅烧改性白云岩在200ml去离子水中浸泡30min,将浸泡后的白云岩表面的水分用滤纸吸去、或者自然风干或者烘干之后,铺在坩埚中,并将该坩埚放置于管式炉中,以0.5L/min的流量通入CO 2气体,在450℃碳化反应2.0h,冷却后,得到最终的改性白云岩,放入干燥器内密闭保存。其中,管式炉升温至450℃的时间为40min。其中,改性得到的改性白云岩的目数为20~140目,进一步地,改性白云岩的目数为40~120目。 Soak the calcined modified dolomite in 200ml of deionized water for 30 minutes, absorb the water on the surface of the soaked dolomite with filter paper, or dry it naturally or dry it, spread it in a crucible, and place the crucible in a tube furnace In the process, CO 2 gas was introduced at a flow rate of 0.5L/min, and the carbonization reaction was carried out at 450°C for 2.0h. After cooling, the final modified dolomite was obtained and stored in a desiccator. Wherein, the time for the tube furnace to heat up to 450° C. is 40 minutes. Wherein, the modified dolomite obtained by modification has a mesh size of 20-140 mesh, and further, the modified dolomite has a mesh size of 40-120 mesh.
需要说明的是,上述列举的干燥温度、煅烧温度、煅烧时间、浸泡水量、浸泡时间、CO 2气体的流量、碳化反应温度、碳化反应时间、碳化反应的升温时间,只是示例性地,不是限制性地,干燥温度还可以是80℃、120℃等其他温度;煅烧温度还可以是700℃、800℃等其他温度;煅烧时间还可以是0.5h、1.5h等其他时间;浸泡水量还可以是150m、250ml等其他水量,且也可以采用超纯水或者自来水浸泡;浸泡时间还可以是20min、30min等其他时间;CO 2气体的流量还可以是0.01L/min、0.1L/min、1.0L/min等其他流量;碳化反应温度还可以是400℃、500℃等其他温度;碳化反应时间还可以是1.0h、2.0h等其他时间;碳化反应的升温时间还可以是30min、50min等其他时间。在实际应用中,本领域技术人员可以将上述 参数任意组合。 It should be noted that the drying temperature, calcination temperature, calcination time, immersion water amount, immersion time, CO gas flow rate, carbonization reaction temperature, carbonization reaction time, and carbonization reaction heating time listed above are only exemplary and not limiting. Specifically, the drying temperature can also be other temperatures such as 80°C and 120°C; the calcining temperature can also be other temperatures such as 700°C and 800°C; the calcining time can also be other times such as 0.5h and 1.5h; the amount of soaking water can also be 150m, 250ml and other water volumes, and can also be soaked in ultrapure water or tap water; the soaking time can also be 20min, 30min and other times; the flow rate of CO 2 gas can also be 0.01L/min, 0.1L/min, 1.0L /min and other flow rates; the carbonization reaction temperature can also be 400°C, 500°C and other temperatures; the carbonization reaction time can also be 1.0h, 2.0h and other times; the carbonization reaction heating time can also be 30min, 50min and other times . In practical applications, those skilled in the art can combine the above parameters arbitrarily.
改性方解石通过以下方法制备:Modified calcite is prepared by the following method:
对方解石进行粉碎和过筛处理,筛分出80~220目的方解石,优选地,筛分出100~200目的方解石,采用去离子水,对筛分出的方解石进行超生波洗涤,过滤,放入烘箱内干燥,再次筛分处理,得到改性方解石,即物理改性方解石。其中,改性方解石的目数为80~220目,进一步地,改性方解石的目数为100~200目。当然,也可以采用超纯水或者自来水浸泡来洗涤预处理方解石。The calcite is crushed and sieved, and 80-220 mesh calcite is screened out. Preferably, 100-200 mesh calcite is screened out, and deionized water is used to wash the screened calcite with ultrasonic wave, filter, and put into drying in an oven, and sieving again to obtain modified calcite, that is, physically modified calcite. Wherein, the mesh number of the modified calcite is 80-220 mesh, and further, the mesh number of the modified calcite is 100-200 mesh. Of course, ultrapure water or tap water can also be used to wash the pretreated calcite.
改性水锌矿通过以下方法制备:Modified hydrozincite is prepared by the following method:
对水锌矿进行粉碎和过筛处理,筛分出80~350目的水锌矿,优选地,筛分出100~325目的水锌矿,然后采用去离子水,对筛分出的水锌矿进行超声波洗涤,过滤,放入烘箱内干燥,得到预处理水锌矿。Grinding and sieving the hydrozincite, sieving out 80-350 mesh hydrozincite, preferably, screening out 100-325 mesh hydrozincite, and then using deionized water to treat the screened hydrozincite Ultrasonic washing is performed, filtered, and dried in an oven to obtain pretreated hydrozincite.
将预处理水锌矿在1.0mol/L的盐酸溶液中浸泡4h,浸泡温度为25℃,恒温浸泡,用去离子水洗涤后得到酸改性水锌矿。The pretreated hydrozincite was soaked in 1.0 mol/L hydrochloric acid solution for 4 hours at a constant temperature of 25° C., and washed with deionized water to obtain the acid-modified hydrozincite.
将酸改性水锌矿在1.2mol/L的碳酸钠溶液中浸泡18h,得到盐改性水锌矿,将盐改性水锌矿在25℃振荡摇匀,并采用去离子水对摇匀后的水锌矿进行洗涤,放入烘箱内干燥,得到改性水锌矿;优选地,改性水锌矿的目数为80~350目,进一步地,改性水锌矿的目数为100~325目。Soak acid-modified hydrozincite in 1.2mol/L sodium carbonate solution for 18 hours to obtain salt-modified hydrozincite. Shake the salt-modified hydrozincite at 25°C, and use deionized water to shake well. The final hydrozincite is washed, put into oven and dried to obtain modified hydrozincite; preferably, the mesh number of modified hydrozincite is 80~350 meshes, and further, the mesh number of modified hydrozincite is 100-325 mesh.
需要说明的是,上述列举的无机酸及其对应的浓度、浸泡时间、浸泡温度,无机盐及其对应的浓度、浸泡时间、浸泡温度,摇匀温度,只是示例性地,不是限制性地,无机酸还可以是硫酸、硝酸、碳酸等其他无机酸,任一种无机酸对应的浓度还可以是0.8mol/L、1.2mol/L等其他浓度,浸泡时间还可以是3h、5h等其他时间,浸泡温度还可以是20℃、23℃、27℃、30℃等他温度;无机盐还可以是碳酸钾、氯化钠、氯化钾等其他无机盐,任一种无机盐对应的浓度还可以是1.0mol/L、1.4mol/L等其他浓度,浸泡时间还可以是14h、16h、20h、22h等其他时间;摇匀温度还可以是20℃、30℃等他温度。在实际应用中,本领域技术人员可以将上述参数任意组合。此外,也可以采用超纯水或者自来水浸泡来洗涤水锌矿。It should be noted that the inorganic acids listed above and their corresponding concentrations, soaking time, and soaking temperature, inorganic salts and their corresponding concentrations, soaking time, soaking temperature, and shaking temperature are only exemplary and not limiting. The inorganic acid can also be other inorganic acids such as sulfuric acid, nitric acid, carbonic acid, etc. The corresponding concentration of any inorganic acid can also be 0.8mol/L, 1.2mol/L, etc. The soaking time can also be 3h, 5h, etc. , the soaking temperature can also be other temperatures such as 20°C, 23°C, 27°C, 30°C; the inorganic salt can also be potassium carbonate, sodium chloride, potassium chloride and other inorganic salts, and the corresponding concentration of any inorganic salt can also be It can be 1.0mol/L, 1.4mol/L and other concentrations, and the soaking time can also be 14h, 16h, 20h, 22h and other times; the shaking temperature can also be 20℃, 30℃ and other temperatures. In practical applications, those skilled in the art can combine the above parameters arbitrarily. In addition, ultrapure water or tap water can also be used to wash the hydrozincite.
改性沸石通过以下方法制备:Modified zeolites are prepared by the following methods:
对沸石进行粉碎和过筛处理,筛分出20~120目的沸石,优选地,筛分出40~100目的沸石,然后采用去离子水,对筛分出的沸石进行超声波洗涤1h,过滤,放入烘箱内干燥,得到预处理沸石。The zeolite is pulverized and sieved, and 20-120 mesh zeolite is screened out. Preferably, 40-100 mesh zeolite is screened out, and then deionized water is used to ultrasonically wash the screened zeolite for 1 hour, filter, and put Dry in an oven to obtain pretreated zeolite.
将预处理沸石放入马弗炉中,在450℃煅烧2.0h,冷却后,得到煅烧改性沸石,放入干燥器内密闭保存。The pretreated zeolite is put into a muffle furnace, calcined at 450° C. for 2.0 h, and after cooling, the calcined modified zeolite is obtained, which is put into a desiccator for airtight storage.
使用200W微波对煅烧改性沸石进行微波改性,得到微波改性沸石。The 200W microwave is used to carry out microwave modification on the calcined modified zeolite to obtain the microwave modified zeolite.
将微波改性沸石在1.0mol/L的盐酸溶液中浸泡4h,浸泡温度为25℃,恒温浸泡,用去离子水洗涤后得到酸改性沸石。Soak the microwave-modified zeolite in a 1.0 mol/L hydrochloric acid solution for 4 hours at a temperature of 25° C., soak at a constant temperature, and wash with deionized water to obtain the acid-modified zeolite.
将酸改性沸石在0.7mol/L的氯化钠溶液中浸泡24h,且每间隔6h振荡5min,得到盐改性沸石。Soak the acid-modified zeolite in 0.7 mol/L sodium chloride solution for 24 hours, and shake it for 5 minutes every 6 hours to obtain the salt-modified zeolite.
对盐改性沸石进行固液分离、采用去离子水反复进行多次超声波洗涤、干燥和筛分处理,得到改性沸石;其中,改性沸石的目数为20~120目,优选地,改性沸石的目数为40~100目。The salt-modified zeolite is subjected to solid-liquid separation, repeated ultrasonic washing, drying and sieving treatment with deionized water to obtain a modified zeolite; wherein, the mesh number of the modified zeolite is 20-120 mesh, preferably, the modified zeolite is The mesh number of the non-toxic zeolite is 40-100 mesh.
需要说明的是,上述列举的超声波洗涤时间、煅烧温度、煅烧时间、微波、无机酸及其对应的浓度、浸泡时间、浸泡温度,无机盐及其对应的浓度、浸泡时间,间隔时间和振荡时间,只是示例性地,不是限制性地,超声波洗涤时间还可以是0.5h、1.5h等其他时间;煅烧温度还可以是400℃、500℃、550℃等其他温度;煅烧时间还可以是1.5h、3.0h、3.5h等其他时间;还可以采用150W微波、300W微波、350W微波等其他微波;无机酸还可以是硫酸、硝酸、碳酸等其他无机酸,任一种无机酸对应的浓度还可以是0.8mol/L、1.2mol/L等其他浓度,浸泡时间还可以是3h、5h等其他时间,浸泡温度还可以是20℃、23℃、27℃、30℃等他温度;无机盐还可以是碳酸钾、碳酸钠、氯化钾等其他无机盐,任一种无机盐对应的浓度还可以是0.5mol/L、0.9mol/L等其他浓度,浸泡时间还可以是22h、26h等其他时间;间隔时间还可以是5h、7h等其他时间;振荡时间还可以是3min、8min等其他时间。在实际应用中,本领域技术人员可以将上述参数任意组合。此外,也可以采用超纯水或者自来水浸泡来洗涤沸石。It should be noted that the above listed ultrasonic cleaning time, calcination temperature, calcination time, microwave, inorganic acid and its corresponding concentration, soaking time, soaking temperature, inorganic salt and its corresponding concentration, soaking time, interval time and oscillation time , is only illustrative, not restrictive, the ultrasonic cleaning time can also be 0.5h, 1.5h and other times; the calcination temperature can also be 400°C, 500°C, 550°C and other temperatures; the calcination time can also be 1.5h , 3.0h, 3.5h and other times; 150W microwave, 300W microwave, 350W microwave and other microwaves can also be used; the inorganic acid can also be sulfuric acid, nitric acid, carbonic acid and other inorganic acids, and the corresponding concentration of any inorganic acid can also be 0.8mol/L, 1.2mol/L and other concentrations, soaking time can also be 3h, 5h and other times, soaking temperature can also be other temperatures such as 20°C, 23°C, 27°C, 30°C; inorganic salts can also be Potassium carbonate, sodium carbonate, potassium chloride and other inorganic salts, the concentration of any inorganic salt can be 0.5mol/L, 0.9mol/L and other concentrations, and the soaking time can also be 22h, 26h and other times ; The interval time can also be 5h, 7h and other times; the oscillation time can also be 3min, 8min and other times. In practical applications, those skilled in the art can combine the above parameters arbitrarily. In addition, ultrapure water or tap water can also be used to wash the zeolite.
改性海浮石通过以下方法制备:Modified sea pumice is prepared by the following method:
对海浮石进行粉碎和过筛处理,筛分出40~220目的海浮石,优选地, 筛分出60~200目的海浮石,采用去离子水,对筛分出的海浮石进行超生波洗涤,过滤,放入烘箱内干燥,得到预处理海浮石。Pulverize and sieve the sea pumice, sieve out 40-220 mesh sea pumice, preferably, sieve out 60-200 mesh sea pumice, and use deionized water to perform ultrasonic wave washing on the screened sea pumice, Filter and dry in an oven to obtain pretreated sea pumice.
将预处理海浮石在醋酸溶液中浸泡32h,得到酸改性海浮石;Soak the pretreated sea pumice in acetic acid solution for 32 hours to obtain acid-modified sea pumice;
将酸改性海浮石在25℃恒温振荡摇匀,并采用去离子水对摇匀后的海浮石进行洗涤,放入烘箱内干燥,得到改性海浮石;优选地,改性海浮石的目数为40~220目,进一步地,改性海浮石的目数为60~200目。Shake the acid-modified sea pumice at a constant temperature of 25°C, wash the shaken sea pumice with deionized water, dry it in an oven, and obtain the modified sea pumice; preferably, the purpose of the modified sea pumice is The number is 40-220 mesh, and further, the mesh number of the modified sea pumice is 60-200 mesh.
需要说明的是,上述列举的有机酸及其对应的浓度、浸泡时间,摇匀温度,只是示例性地,不是限制性地,有机酸还可以是柠檬酸、草酸等其他有机酸,任一种有机酸对应的浸泡时间还可以是27h、29h、35h、37h等其他时间;摇匀温度还可以是20℃、30℃等他温度。在实际应用中,本领域技术人员可以将上述参数任意组合。此外,也可以采用超纯水或者自来水浸泡来洗涤海浮石。It should be noted that the organic acids listed above and their corresponding concentrations, soaking time, and shaking temperature are only exemplary and not limiting. The organic acids can also be other organic acids such as citric acid and oxalic acid. The soaking time corresponding to the organic acid can also be 27h, 29h, 35h, 37h and other times; the shaking temperature can also be other temperatures such as 20°C and 30°C. In practical applications, those skilled in the art can combine the above parameters arbitrarily. In addition, sea pumice can also be washed by soaking in ultrapure water or tap water.
此外,还需要对得到的改性白云岩、改性方解石、改性水锌矿、改性沸石和改性海浮石按照GB 5479-2006生活饮用水卫生标准进行色度、浑浊度、臭和味、肉眼可见物、pH和TDS进行检验,并按照卫法监发【2001】生活饮用水卫生规范--生活饮用水输配水设备及防护材料卫生安全评价规范对得到的改性白云岩、改性方解石、改性水锌矿、改性沸石和改性海浮石进行铝、总铬、猛、铁、铜、锌、砷、银、镉、铅、锑、镍、锡、钡等元素的含量进行检验,只有改性白云岩、改性方解石、改性水锌矿、改性沸石和改性海浮石符合上述标准和规范时,才能够使用,进一步确保了饮水用的安全。通过上述改性方法,使得白云岩、方解石、水锌矿、沸石和海浮石的性能得到提升,并制备成不同粒径尺寸的颗粒,以便与活性炭颗粒、活性炭纤维和粘结剂混合。In addition, the obtained modified dolomite, modified calcite, modified hydrozincite, modified zeolite and modified sea pumice should be tested for chroma, turbidity, odor and taste in accordance with the GB 5479-2006 sanitary standard for drinking water. , Visible matter, pH and TDS were inspected, and the obtained modified dolomite and modified The content of aluminum, total chromium, manganese, iron, copper, zinc, arsenic, silver, cadmium, lead, antimony, nickel, tin, barium, etc. After inspection, only modified dolomite, modified calcite, modified hydrozincite, modified zeolite and modified sea pumice can be used if they meet the above standards and specifications, further ensuring the safety of drinking water. Through the above-mentioned modification method, the properties of dolomite, calcite, hydrozincite, zeolite and sea pumice are improved, and particles of different particle sizes are prepared for mixing with activated carbon particles, activated carbon fibers and binders.
下面参照三个实施例,对本发明的矿化滤芯的制备方法进一步描述。The preparation method of the mineralized filter element of the present invention will be further described below with reference to three examples.
实施例一Embodiment one
称量如下原料:Weigh the following ingredients:
以每一份的重量为10g计,主料:改性白云岩50g,改性方解石100g,改性水锌矿30g,改性沸石30g,改性海浮石20g;将称量得到的改性白 云岩、改性方解石、改性水锌矿、改性沸石和改性海浮石混合均匀,得到矿化滤料230g,即,提前混合好较多的矿化滤料备用。Based on the weight of each serving as 10g, the main ingredients: 50g of modified dolomite, 100g of modified calcite, 30g of modified hydrozincite, 30g of modified zeolite, and 20g of modified sea pumice; Rock, modified calcite, modified hydrozincite, modified zeolite and modified pumice were mixed evenly to obtain 230g of mineralized filter material, that is, more mineralized filter material was mixed in advance for subsequent use.
以每一份的重量为1g计,称量70g矿化滤料(即混合之后的主料);辅料:活性炭100g,粘结剂30g。Based on the weight of each part as 1g, weigh 70g of mineralized filter material (ie the main material after mixing); auxiliary materials: 100g of activated carbon, 30g of binder.
将70g矿化滤料、100g活性炭和30g粘结剂混合均匀,得到混合料。Mix 70g of mineralized filter material, 100g of activated carbon and 30g of binder evenly to obtain a mixture.
将混合料放入磨具中,在100℃烧结60min,烧结压力为12MPa,将烧结好的富锶偏硅酸炭棒冷却后装入滤壳中,即得到矿化滤芯。Put the mixture into the grinding tool, sinter at 100°C for 60min, and the sintering pressure is 12MPa, cool the sintered strontium-rich metasilicate carbon rod and put it into the filter shell to obtain the mineralized filter element.
实施例二Embodiment two
称量如下原料:Weigh the following ingredients:
以每一份的重量为1g计,主料:改性白云岩20g,改性方解石14g,改性水锌矿6g,改性沸石6g,改性海浮石4g;将称量得到的改性白云岩、改性方解石、改性水锌矿、改性沸石和改性海浮石混合均匀,得到矿化滤料50g;Based on the weight of each part as 1g, the main ingredients: 20g of modified dolomite, 14g of modified calcite, 6g of modified hydrozincite, 6g of modified zeolite, 4g of modified sea pumice; the modified dolomite obtained by weighing Rock, modified calcite, modified hydrozincite, modified zeolite and modified sea pumice are mixed uniformly to obtain 50 g of mineralized filter material;
以每一份的重量为1g计,辅料:活性炭120g,粘结剂45g。Based on the weight of each serving as 1g, auxiliary materials: 120g of activated carbon, 45g of binder.
将50g矿化滤料、120g活性炭和45g粘结剂混合均匀,得到混合料。Mix 50g of mineralized filter material, 120g of activated carbon and 45g of binder evenly to obtain a mixture.
将混合料放入磨具中,在160℃烧结20min,烧结压力为18MPa,将烧结好的富锶偏硅酸炭棒冷却后装入滤壳中,即得到矿化滤芯。Put the mixture into the grinding tool, sinter at 160°C for 20min, and the sintering pressure is 18MPa, cool the sintered strontium-rich metasilicate carbon rod and put it into the filter shell to obtain the mineralized filter element.
实施例三Embodiment three
称量如下原料:Weigh the following ingredients:
以每一份的重量为1g计,主料:改性白云岩25g,改性方解石15g,改性水锌矿5g,改性沸石5g,改性海浮石3g;辅料:活性炭110g,粘结剂40g。Based on the weight of each serving as 1g, main ingredients: 25g of modified dolomite, 15g of modified calcite, 5g of modified hydrozincite, 5g of modified zeolite, 3g of modified sea pumice; auxiliary materials: 110g of activated carbon, binder 40g.
将称量得到的25g改性白云岩、15g改性方解石、5g改性水锌矿、5g改性沸石和3g改性海浮石按照密度由小到大的顺序依次与110g活性炭和40g粘结剂进行混合,得到混合料。例如,先将细颗粒、密度小的改性白云岩与活性炭和粘结剂进行混合,再将改性沸石、改性方解石、改性水锌矿和改性海浮石依次与活性炭和粘结剂进行混合。当然,在实际添加原料的过程中,如果两个原料的密度比较接近,也可以根据原料的目数确定添加的顺序,例如先添加目数小的,再添加目数大的。25g modified dolomite, 15g modified calcite, 5g modified hydrozincite, 5g modified zeolite and 3g modified sea pumice were mixed with 110g activated carbon and 40g binder in order of density from small to large. Mixed to obtain a mixture. For example, fine-grained, low-density modified dolomite is mixed with activated carbon and binder first, and then modified zeolite, modified calcite, modified hydrozincite and modified sea pumice are mixed with activated carbon and binder in turn. to mix. Of course, in the process of actually adding raw materials, if the densities of the two raw materials are relatively close, the order of addition can also be determined according to the mesh number of the raw materials, for example, add the one with the smaller mesh number first, and then add the one with the larger mesh number.
将混合料放入磨具中,在140℃烧结40min,烧结压力为16MPa,将烧结好的富锶偏硅酸炭棒冷却后装入滤壳中,即得到矿化滤芯。Put the mixture into the grinding tool, sinter at 140°C for 40min, and the sintering pressure is 16MPa, cool the sintered strontium-rich metasilicate carbon rod and put it into the filter shell to obtain the mineralized filter element.
需要说明的是,上述列举的三个实施例中的原料的重量份配比指示示例性地,本领域技术人员在实际应用中可以根据实际的水质需求等灵活地调整和设置原料的重量份配比,并根据原料的重量份配比相应地调整烧结温度、烧结时间和烧结压力。It should be noted that the proportions by weight of raw materials in the three examples listed above indicate that those skilled in the art can flexibly adjust and set the proportions by weight of raw materials according to actual water quality requirements in practical applications. Ratio, and adjust the sintering temperature, sintering time and sintering pressure accordingly according to the weight ratio of raw materials.
进一步地,对通过上述方法制备得到的矿化滤芯进行了性能测试,详见表1。实验方法为:在室温条件下,进行通水测试,通水时,纯水流速为2.0L/min,当通水量达到1000L、2000L、3500L和4300L时分别取250ml水样进行测试。Further, a performance test was carried out on the mineralized filter element prepared by the above method, see Table 1 for details. The experimental method is: at room temperature, conduct a water test. When the water is passed, the flow rate of pure water is 2.0L/min. When the water flow reaches 1000L, 2000L, 3500L and 4300L, 250ml water samples are taken for testing.
从表1中可以看出,在进水为纯水情况下,在4300L通水量的条件下,锌、锶元素仍然能够进行稳定析出,且衰减速度较慢,即该矿化滤芯过滤后的富含丰富的锌、锶等有益的矿物质,达到了国家饮用水标准。It can be seen from Table 1 that when the influent water is pure water, zinc and strontium elements can still be precipitated stably under the condition of 4300L water flow, and the attenuation speed is slow, that is, the rich It is rich in beneficial minerals such as zinc and strontium, and has reached the national drinking water standard.
表1.矿化滤芯功能性测试数据统计表Table 1. Statistical table of functional test data of mineralized filter element
Figure PCTCN2022139917-appb-000001
Figure PCTCN2022139917-appb-000001
进一步地,对通过上述方法制备得到的矿化滤芯进行了铅金属析出测试,将本发明制备的矿化滤芯分别与水锌矿滤芯、添加了A矿石的水锌矿化滤芯、添加了B矿石的水锌矿化滤芯的控制铅金属的析出的效果进行了对比,其中,A矿石为如火山石、硅藻土、高岭土等矿石,B矿石为麦饭石、沸石、伊利石等矿石。经比较可知,本发明制备得到的矿化滤芯由于包括海浮石,改性海浮石和改性水锌矿的配合使用。从表2中可以看出,采用本发明制备的矿化滤芯,当其添加量在达到20g时,就能够有效控制铅金属的析出,避免了铅等重金属超标,进一步确保了饮水用的安全。Further, the lead metal precipitation test was carried out on the mineralization filter element prepared by the above method, and the mineralization filter element prepared by the present invention was respectively combined with the hydrozincite filter element, the hydrozinc mineralization filter element with A ore added, and the hydrozinc mineralization filter element with B ore added. The effect of controlling the precipitation of lead metal in the hydrozinc mineralization filter element was compared. Among them, the A ore is such as volcanic rock, diatomaceous earth, kaolin and other ores, and the B ore is medical stone, zeolite, illite and other ores. Through comparison, it can be seen that the mineralization filter element prepared by the present invention includes sea pumice, modified sea pumice and modified hydrozincite. As can be seen from Table 2, adopting the mineralization filter element prepared by the present invention, when its addition amount reaches 20g, the precipitation of lead metal can be effectively controlled, heavy metals such as lead have been avoided exceeding the standard, and the safety of drinking water has been further ensured.
表2.矿化滤芯铅含量测试统计表Table 2. Mineralization filter lead content test statistics
Figure PCTCN2022139917-appb-000002
Figure PCTCN2022139917-appb-000002
应该指出的是,上述实施例只是本发明的一种较佳的实施方式中,仅用来阐述本发明方法的原理,并非旨在限制本发明的保护范围,在实际应用中,本领域技术人员可以根据需要而将上述功能分配由不同的步骤来完成,即将本发明实施例中的步骤再分解或者组合。例如,上述实施例的步骤可以合并为一个步骤,也可以进一步拆分成多个子步骤,以 完成以上描述的全部或者部分功能。对于本发明实施例中涉及的步骤的名称,其仅仅是为了区分各个步骤,不视为对本发明的限制。It should be pointed out that the above-mentioned embodiment is only a preferred embodiment of the present invention, and is only used to illustrate the principle of the method of the present invention, and is not intended to limit the protection scope of the present invention. In practical application, those skilled in the art The above function allocation can be completed by different steps according to needs, that is, the steps in the embodiment of the present invention are decomposed or combined. For example, the steps in the above embodiments may be combined into one step, or further divided into multiple sub-steps, so as to complete all or part of the functions described above. The names of the steps involved in the embodiments of the present invention are only used to distinguish each step, and are not considered to limit the present invention.
至此,已经结合附图所示的优选实施方式描述了本发明的技术方案,但是,本领域技术人员容易理解的是,本发明的保护范围显然不局限于这些具体实施方式。在不偏离本发明的原理的前提下,本领域技术人员可以对相关技术特征作出等同的更改或替换,这些更改或替换之后的技术方案都将落入本发明的保护范围之内。So far, the technical solutions of the present invention have been described in conjunction with the preferred embodiments shown in the accompanying drawings, but those skilled in the art will easily understand that the protection scope of the present invention is obviously not limited to these specific embodiments. Without departing from the principles of the present invention, those skilled in the art can make equivalent changes or substitutions to relevant technical features, and the technical solutions after these changes or substitutions will all fall within the protection scope of the present invention.

Claims (13)

  1. 一种矿化滤芯,其特征在于,包括按以下重量份计的原料:A mineralization filter element is characterized in that it comprises raw materials in the following parts by weight:
    主料:改性白云岩1~40份,改性方解石1~20份,改性水锌矿1~6份,改性沸石1~6份,改性海浮石1~4份。Main ingredients: 1-40 parts of modified dolomite, 1-20 parts of modified calcite, 1-6 parts of modified hydrozincite, 1-6 parts of modified zeolite, and 1-4 parts of modified sea pumice.
  2. 根据权利要求1所述的矿化滤芯,其特征在于,包括按以下重量份计的原料:The mineralization filter element according to claim 1, is characterized in that, comprises the raw material by following weight part:
    主料:改性白云岩5~20份,改性方解石10份,改性水锌矿3份,改性沸石3份,改性海浮石2份。Main ingredients: 5-20 parts of modified dolomite, 10 parts of modified calcite, 3 parts of modified hydrozincite, 3 parts of modified zeolite, and 2 parts of modified sea pumice.
  3. 根据权利要求1所述的矿化滤芯,其特征在于,还包括按以下重量份计的原料:The mineralization filter element according to claim 1, is characterized in that, also comprises the raw material by following weight parts:
    辅料:活性炭50~240份,粘结剂10~90份。Excipients: 50-240 parts of activated carbon, 10-90 parts of binder.
  4. 根据权利要求3所述的矿化滤芯,其特征在于,由按以下重量份计的原料制成:The mineralization filter element according to claim 3, characterized in that, it is made of the following raw materials in parts by weight:
    主料50~70份;50-70 parts of main ingredients;
    辅料130~165份,其中,活性炭100~120份,粘结剂30~45份。130-165 parts of auxiliary materials, including 100-120 parts of activated carbon and 30-45 parts of binder.
  5. 一种权利要求3或4所述的矿化滤芯的制备方法,其特征在于,所述制备方法包括下列步骤:A preparation method of the mineralization filter core described in claim 3 or 4, is characterized in that, described preparation method comprises the following steps:
    改性:分别对白云岩、方解石、水锌矿、沸石和海浮石进行改性,得到改性白云岩、改性方解石、改性水锌矿、改性沸石和改性海浮石;Modification: modify dolomite, calcite, hydrozincite, zeolite and sea pumice respectively to obtain modified dolomite, modified calcite, modified hydrozincite, modified zeolite and sea pumice;
    配料:按照重量份分别称量所述改性白云岩、所述改性方解石、所述改性水锌矿、所述改性沸石、所述改性海浮石、活性炭和粘结剂;Ingredients: weighing the modified dolomite, the modified calcite, the modified hydrozincite, the modified zeolite, the modified sea pumice, activated carbon and binder respectively according to parts by weight;
    混合:将称量得到的所述改性白云岩、所述改性方解石、所述改性水锌矿、所述改性沸石和所述改性海浮石按照预设方法与所述活性炭和 所述粘结剂进行混合,得到混合料;Mixing: mix the weighed modified dolomite, the modified calcite, the modified hydrozincite, the modified zeolite and the modified sea pumice with the activated carbon and the The binder is mixed to obtain a mixture;
    烧结成型:将所述混合料放入磨具中进行烧结,得到所述矿化滤芯。Sintering molding: put the mixture into a grinding tool for sintering to obtain the mineralized filter element.
  6. 根据权利要求5所述的制备方法,其特征在于,所述改性白云岩通过以下方法制备:The preparation method according to claim 5, wherein the modified dolomite is prepared by the following method:
    对所述白云岩进行超声波洗涤、干燥、粉碎、研磨和过筛处理,得到预处理白云岩;Ultrasonic washing, drying, crushing, grinding and sieving are performed on the dolomite to obtain pretreated dolomite;
    将所述预处理白云岩在700~800℃煅烧0.5~1.5h,冷却后,得到煅烧改性白云岩;calcining the pretreated dolomite at 700-800° C. for 0.5-1.5 hours, and cooling to obtain calcined modified dolomite;
    将所述煅烧改性白云岩在150~250ml水中浸泡20~40min,将浸泡后的白云岩表面的水分去除之后置于管式炉中,以0.01-1.0L/min的流量通入CO 2气体,在400~500℃碳化反应1.0~3.0h,冷却后,得到所述改性白云岩; Soak the calcined modified dolomite in 150-250ml of water for 20-40min, remove the moisture on the surface of the soaked dolomite, place it in a tube furnace, and feed CO2 gas at a flow rate of 0.01-1.0L/min , carbonization reaction at 400-500° C. for 1.0-3.0 hours, and after cooling, the modified dolomite is obtained;
    其中,所述改性白云岩的目数为40~120目。Wherein, the mesh number of the modified dolomite is 40-120 mesh.
  7. 根据权利要求5所述的制备方法,其特征在于,所述改性方解石通过以下方法制备:The preparation method according to claim 5, wherein the modified calcite is prepared by the following method:
    对所述方解石进行粉碎和过筛处理,得到预处理方解石;The calcite is crushed and sieved to obtain pretreated calcite;
    对所述预处理方解石进行超生波洗涤、过滤、干燥和筛分处理,得到所述改性方解石;Performing ultrasonic washing, filtering, drying and sieving on the pretreated calcite to obtain the modified calcite;
    其中,所述改性方解石的目数为80~220目。Wherein, the mesh number of the modified calcite is 80-220 mesh.
  8. 根据权利要求5所述的制备方法,其特征在于,所述改性水锌矿通过以下方法制备:The preparation method according to claim 5, wherein the modified hydrozincite is prepared by the following method:
    对所述水锌矿进行粉碎、过筛、超声波洗涤、过滤和干燥处理,得到预处理水锌矿;crushing, sieving, ultrasonic washing, filtering and drying the hydrozincite to obtain pretreated hydrozincite;
    将所述预处理水锌矿在0.8~1.2mol/L的无机酸溶液中浸泡3~5h,浸泡温度为20~30℃,洗涤后得到酸改性水锌矿;Soak the pretreated hydrozincite in 0.8-1.2 mol/L inorganic acid solution for 3-5 hours, the soaking temperature is 20-30°C, and obtain acid-modified hydrozincite after washing;
    将所述酸改性水锌矿在1.0~1.4mol/L的无机盐溶液中浸泡14~22h,得到盐改性水锌矿;Soaking the acid-modified hydrozincite in 1.0-1.4 mol/L inorganic salt solution for 14-22 hours to obtain salt-modified hydrozincite;
    将所述盐改性水锌矿在20~30℃振荡摇匀,并对摇匀后的水锌矿进行洗涤和干燥处理,得到所述改性水锌矿;Shaking the salt-modified hydrozincite at 20-30° C., washing and drying the shaken hydrozincite to obtain the modified hydrozincite;
    其中,所述改性水锌矿的目数为80~350目。Wherein, the mesh size of the modified hydrozincite is 80-350 mesh.
  9. 根据权利要求5所述的制备方法,其特征在于,所述改性沸石通过以下方法制备:The preparation method according to claim 5, wherein the modified zeolite is prepared by the following method:
    对所述沸石进行粉碎、过筛、超声波洗涤和干燥处理,得到预处理沸石;The zeolite is pulverized, sieved, ultrasonically washed and dried to obtain a pretreated zeolite;
    将所述预处理沸石在400~550℃煅烧1.5~3.5h,冷却后,得到煅烧改性沸石;Calcining the pretreated zeolite at 400-550° C. for 1.5-3.5 hours, and cooling to obtain a calcined modified zeolite;
    使用150~350W微波对所述煅烧改性沸石进行微波改性,得到微波改性沸石;Using 150-350W microwaves to carry out microwave modification on the calcined modified zeolite to obtain microwave modified zeolite;
    将所述微波改性沸石在0.8~1.2mol/L的无机酸溶液中浸泡3~5h,浸泡温度为20~30℃,洗涤后得到酸改性沸石;soaking the microwave-modified zeolite in a 0.8-1.2 mol/L inorganic acid solution for 3-5 hours at a temperature of 20-30°C, and obtaining the acid-modified zeolite after washing;
    将所述酸改性沸石在0.5~0.9mol/L的无机盐溶液中浸泡22~26h,且每间隔5~7h振荡3~8min,得到盐改性沸石;Soak the acid-modified zeolite in a 0.5-0.9 mol/L inorganic salt solution for 22-26 hours, and vibrate for 3-8 minutes every 5-7 hours to obtain a salt-modified zeolite;
    对所述盐改性沸石进行固液分离、超声波洗涤、干燥和筛分处理,得到所述改性沸石;performing solid-liquid separation, ultrasonic washing, drying and sieving on the salt-modified zeolite to obtain the modified zeolite;
    其中,所述改性沸石的目数为20~120目。Wherein, the mesh number of the modified zeolite is 20-120 mesh.
  10. 根据权利要求5所述的制备方法,其特征在于,所述改性海浮石通过以下方法制备:The preparation method according to claim 5, wherein the modified sea pumice is prepared by the following method:
    对所述海浮石进行粉碎、过筛、超声波洗涤和干燥处理,得到预处理海浮石;crushing, sieving, ultrasonic washing and drying the sea pumice to obtain pretreated sea pumice;
    将所述预处理海浮石在有机酸溶液中浸泡27~37h,得到酸改性海浮石;soaking the pretreated sea pumice in an organic acid solution for 27 to 37 hours to obtain acid-modified sea pumice;
    将所述酸改性海浮石在20~30℃振荡摇匀,并对摇匀后的海浮石进行洗涤和干燥处理,得到所述改性海浮石;Shaking the acid-modified sea pumice at 20-30°C, washing and drying the shaken sea pumice to obtain the modified sea pumice;
    其中,所述改性海浮石的目数为40~220目。Wherein, the mesh number of the modified sea pumice is 40-220 mesh.
  11. 根据权利要求5所述的制备方法,其特征在于,“将称量得到的所述改性白云岩、所述改性方解石、所述改性水锌矿、所述改性沸石和所述改性海浮石按照预设方法与活性炭和粘结剂进行混合,得到混合料”的步骤具体包括:The preparation method according to claim 5, characterized in that, "the modified dolomite, the modified calcite, the modified hydrozinsite, the modified zeolite and the modified According to the pre-set method, the sea pumice is mixed with activated carbon and binder to obtain the mixture" The steps specifically include:
    将称量得到的所述改性白云岩、所述改性方解石、所述改性水锌矿、所述改性沸石和所述改性海浮石混合均匀,得到矿化滤料;Mixing the weighed modified dolomite, the modified calcite, the modified hydrozincite, the modified zeolite and the modified sea pumice to obtain a mineralized filter material;
    将所述矿化滤料、所述活性炭和所述粘结剂混合均匀,得到所述混合料。The mineralized filter material, the activated carbon and the binder are uniformly mixed to obtain the mixed material.
  12. 根据权利要求5所述的制备方法,其特征在于,“将称量得到的所述改性白云岩、所述改性方解石、所述改性水锌矿、所述改性沸石和所述改性海浮石按照预设方法与活性炭和粘结剂进行混合,得到混合料”的步骤具体包括:The preparation method according to claim 5, characterized in that, "the modified dolomite, the modified calcite, the modified hydrozinsite, the modified zeolite and the modified According to the pre-set method, the sea pumice is mixed with activated carbon and binder to obtain the mixture" The steps specifically include:
    将称量得到的所述改性白云岩、所述改性方解石、所述改性水锌矿、所述改性沸石和所述改性海浮石按照密度由小到大的顺序依次与所述活性炭和所述粘结剂进行混合,得到所述混合料。The modified dolomite, the modified calcite, the modified hydrozinsite, the modified zeolite and the modified sea pumice obtained by weighing are sequentially mixed with the Activated carbon is mixed with the binder to obtain the mixture.
  13. 根据权利要求5所述的制备方法,其特征在于,“将所述混合料放入磨具中进行烧结,得到矿化滤芯”的步骤具体包括:The preparation method according to claim 5, characterized in that, the step of "putting the mixture into a grinding tool for sintering to obtain a mineralized filter element" specifically includes:
    将所述混合料放入磨具中,在100~160℃烧结20~60min,烧结压力为12~18MPa,冷却后得到所述矿化滤芯。The mixture is put into a grinding tool, sintered at 100-160°C for 20-60min, the sintering pressure is 12-18MPa, and the mineralized filter element is obtained after cooling.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117164351A (en) * 2023-08-10 2023-12-05 山东鑫永恒新材料有限公司 Calcium-rich slow-release mineralized material and preparation method thereof

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114229981A (en) * 2021-12-17 2022-03-25 青岛海尔施特劳斯水设备有限公司 Mineralized filter element and preparation method thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002301482A (en) * 2001-04-09 2002-10-15 San Friend Medical Kk Sintered natural ore activating city water
CN108675429A (en) * 2018-05-21 2018-10-19 中国地质大学(武汉) A kind of alkalescent zinc, the complex sintered active carbon filter core of strontium mineralising and preparation method thereof
CN108722018A (en) * 2018-05-03 2018-11-02 武汉中地水石环保科技有限公司 A kind of strontium mineralising filter core and preparation method thereof based on natural rock material
CN110124392A (en) * 2019-04-01 2019-08-16 武汉中地水石环保科技有限公司 A kind of zinc for teenagers growth, calcium mineralising composite filter element and preparation method thereof
CN114229981A (en) * 2021-12-17 2022-03-25 青岛海尔施特劳斯水设备有限公司 Mineralized filter element and preparation method thereof

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002301482A (en) * 2001-04-09 2002-10-15 San Friend Medical Kk Sintered natural ore activating city water
CN108722018A (en) * 2018-05-03 2018-11-02 武汉中地水石环保科技有限公司 A kind of strontium mineralising filter core and preparation method thereof based on natural rock material
CN108675429A (en) * 2018-05-21 2018-10-19 中国地质大学(武汉) A kind of alkalescent zinc, the complex sintered active carbon filter core of strontium mineralising and preparation method thereof
CN110124392A (en) * 2019-04-01 2019-08-16 武汉中地水石环保科技有限公司 A kind of zinc for teenagers growth, calcium mineralising composite filter element and preparation method thereof
CN114229981A (en) * 2021-12-17 2022-03-25 青岛海尔施特劳斯水设备有限公司 Mineralized filter element and preparation method thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117164351A (en) * 2023-08-10 2023-12-05 山东鑫永恒新材料有限公司 Calcium-rich slow-release mineralized material and preparation method thereof
CN117164351B (en) * 2023-08-10 2024-03-19 山东鑫永恒新材料有限公司 Calcium-rich slow-release mineralized material and preparation method thereof

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