Production process system for new salt-based multi-mineral roasting fine-grinding nanocrystallization slurry bath material

Abstract

The invention belongs to the technical field of manufacturing of health preserving equipment, and provides a salt-based multi-mineral roasting fine-grinding nanocrystallization slurry bath new material production process system which comprises a various mineral crushing, matching and smelting system, the raw materials are crushed and ground into a nano airflow crushing preparation system, a compatibility metering synthesis salt-based mud soup preparation system, a salt-based mud soup supply system and a mud soup discharging, purifying and recycling system; according to the invention, by improving the existing slurry bath process, the properties of doped slurry components are improved while the basic idea of the existing slurry bath is absorbed, and the original unprocessed common mineral powder is changed into a salt-based compound which needs to be subjected to a processing and calcining process and then is subjected to phase change, and then the salt-based compound is ground into a nanoscale; the novel process is beneficial to improving the stability and dispersity of product quality, is free of pollution, fully utilizes waste heat, is small in investment, quick in effect taking and reusable, and has extremely remarkable comprehensive economic, social and environment-friendly benefits.

Description

Technical Field

[0001] This invention belongs to the field of health and wellness equipment manufacturing technology, specifically a production process system for a new type of salt-based multi-mineral roasted finely ground nano-sized mud bath material. Background Technology

[0002] Mud baths, also known as hot mineral mud baths, use mud from volcanic ash or hot springs. The mud, either naturally heated or finely ground into a mixture of water and powder (1000-3000 mesh), is applied to certain parts of the body. The heat is transferred to the body, and the mud, along with its chemical components and microorganisms, works to achieve health benefits and disease prevention. Ancient Egyptians used mud from the Nile River to treat arthritis as early as the 2nd century AD. Mud baths are recorded in Chinese medical texts from the Jin Dynasty ("Elbow Formulas") and the Tang Dynasty. Regular mud baths are beneficial to health because mud has low thermal conductivity and excellent heat retention, providing a warming effect on the body. When in contact with the skin, it effectively massages the skin, promotes blood circulation, and improves metabolism.

[0003] Mud baths are mainly divided into three categories: volcanic ash mud baths, hot spring mud baths with mud or mineral powder, and mud baths formed by adding mud powder or mineral powder to heated water. Regardless of the type of mud bath, there are certain drawbacks. For example, the mud composition exhibits stratification due to differences in specific gravity, making mud cleaning extremely difficult; recycling issues make it difficult to reuse the mud repeatedly; the anti-inflammatory and sterilization process is almost never effectively addressed during recycling; due to the lack of systematic treatment, the mud has extremely poor dispersion, which can damage the ecosystem; the production process involves repetitive operations, frequent temperature changes, excessive energy consumption, long reaction times, high energy consumption, high production costs, and serious pollution; the process is cumbersome and the production cost is high. Summary of the Invention

[0004] To address the aforementioned technical problems, this invention provides a novel production process system for salt-based multi-mineral roasting, fine grinding, and nano-scale mud bath materials, thereby resolving the issues raised in the background art.

[0005] A novel production process system for salt-based multi-mineral roasting, fine grinding, and nano-sized mud bath materials includes:

[0006] This invention relates to a mineral crushing, blending, and smelting system, a crushing and grinding system for nano-scale airflow pulverization, a blending and metering system for synthesizing salt-based mud soup, a salt-based mud soup supply system, and a mud soup discharge, purification, and recycling system. In this invention, minerals undergo phase transformation and recombination during high-temperature smelting, resulting in a fundamental change in their composition. Single components are transformed into salt-based composite components. The calcined and molten products are then subjected to coarse crushing and fine grinding to nano-scale, achieving a fineness of 1000–3000 mesh nanometers. The solid is also considered a liquid, exhibiting properties similar to a liquid.

[0007] Preferably, the salt-based multi-mineral combination refers to a process system in which a composite molten salt calcined at 1400-1700℃ is cooled and finely ground to ≤2mm particles, then calcined and cooled with a variety of minerals rich in trace elements needed by the human body at different temperature ranges of 850-1300℃, and then further pulverized into nano-sized mineral powder through multiple stages; the soup is prepared by adding 1-20:99-80 salts to 100 parts of water and stirring evenly, and the temperature is controlled at 38-45℃ for therapeutic bathing.

[0008] Preferably, the high-temperature calcined and molten salt mineral combination must be crushed, ground, and then nano-ground to form nano-scale powder, which is the core of the entire system. This powder is equivalent to simulating volcanic ash but is superior to volcanic ash in composition. After repeated use, the waste is purified by a rotary nano-ceramic membrane, then subjected to efficient solid-liquid separation, and then calcined in a ball press. This decomposes the organic residues in the bath and the various flocculants added during sedimentation and sludge removal, as well as other organic and inorganic substances, at high temperatures. Some of these substances evaporate with the gas, while others decompose and carbonize, restoring the original state. After nano-processing, the original function is restored, achieving repeated recycling, reducing emissions, and protecting the environment.

[0009] Preferably, the therapeutic bath system is designed with a high-temperature steam heating and balancing system and an ozone disinfection system. After repeated therapeutic baths, the bath water in the pool is immediately disinfected and sterilized with ozone before the second batch of people enters. This process is repeated n times. During this period, a constant temperature controller is set to keep the temperature within the set temperature range.

[0010] Compared with the prior art, the present invention has the following beneficial effects:

[0011] This invention improves upon existing mud bath processes. While absorbing the basic principles of existing mud baths, it also improves the properties of the mud components. The original ordinary unprocessed mineral powder is replaced with a new process that requires processing and calcination to transform into a base complex, then grinding it into nanoscale particles before applying it as a slurry. This process is beneficial for improving the stability, dispersibility, and penetration of product quality, enabling recycling, eliminating pollution, fully utilizing waste heat, requiring low investment, yielding quick results, allowing for repeated use, and providing significant comprehensive economic, social, and environmental benefits. Attached Figure Description

[0012] Figure 1 This is a flow chart of the salt-based multi-mineral roasting, fine grinding, and nano-scale mud bath process of the present invention. Detailed Implementation

[0013] The embodiments of the present invention will be described in further detail below with reference to the accompanying drawings and examples. The following examples are for illustrative purposes only and should not be construed as limiting the scope of the invention.

[0014] Example 1:

[0015] Please see Figure 1 As shown, a novel production process system for salt-based multi-mineral roasting, fine grinding, and nano-scaled mud bath materials includes:

[0016] This invention relates to a mineral crushing, blending, and smelting system, a crushing and grinding system for nano-airflow pulverization, a blending and metering system for preparing salt-based mud soup, a salt-based mud soup supply system, and a mud soup discharge, purification, and recycling system. In this invention, minerals undergo phase transformation and recombination at high temperatures, resulting in a fundamental change in their composition. Single components become salt-based composite components. The calcined and molten product is then coarsely crushed and finely ground to nano-scale, achieving a fineness of 1000-3000 mesh nanometers. The solid is treated as a liquid, exhibiting liquid-like properties. The salt-based multi-mineral combination refers to a composite molten salt calcined at 1400-1700℃, cooled and finely ground to ≤2mm particles, then calcined with various minerals rich in trace elements needed by the human body at different temperature ranges of 850-1300℃, cooled, and then further pulverized into nano-scale mineral powder through multiple stages. The resulting soup is prepared by adding 1-20 parts salt to 99-80 parts water and stirring until homogeneous. The temperature is controlled at 38-45℃ for therapeutic bathing.

[0017] The high-temperature calcination and melting of salt minerals, after being crushed, ground, and then nano-finely ground, forms nano-sized powder, which is the core of the entire system. This powder is equivalent to, but superior to, volcanic ash in composition. After repeated use, the waste is purified by a rotary nano-ceramic membrane, followed by efficient solid-liquid separation, and then calcined in spheres. This process decomposes organic residues from the therapeutic bath, as well as various flocculants and other organic and inorganic substances added during sedimentation and sludge removal, at high temperatures. Some of these substances evaporate with the gas, while others decompose and carbonize, restoring the original state. After nano-processing, the original function is restored, achieving repeated recycling, reducing emissions, and protecting the environment. The therapeutic bath system is designed with a high-temperature steam heating and balancing system and an ozone disinfection system. After repeated therapeutic baths, the bath water is immediately disinfected and sterilized with ozone before the next batch of people enters. This cycle is repeated many times, with a constant temperature controller set to keep the temperature within the set range.

[0018] As can be seen from the above, natural minerals, including maifanite, glacial till, selenium-rich ore, strontium spar, dolomite, and mokuyu stone, are crushed and screened to particles smaller than or equal to 50mm and larger than 2mm. These particles are then stored in corresponding silos for later use. After being metered below the silos, they are pressed into almond-shaped pellets using a briquetting machine. These pellets are then calcined in a three-stage furnace at 800-1300℃. After calcination and cooling, the materials are ground to 200-400 mesh and stored in their respective silos for later use. Each pellet is then mixed with 0.5-1KG% pure salt and ground at 12... Calcination at 00-1700℃ for 1-5 hours forms a base composite material. Then, the furnace outlet is opened, and the molten slurry (soup) flows through a cast stone scraper conveyor or chain bucket conveyor / membrane trough equipped with water-cooled pipes. During the output process, it is cooled to below 200℃, then crushed by a jaw crusher to particles smaller than or equal to 30mm. This then enters a conical mill, where it is ground into powder smaller than 400 mesh. Next, it enters a high-speed nano-airflow mill and is ground to powder smaller than 3000 mesh before proceeding to the next slurry (soup) preparation process. Different ratios are typically used depending on the specific requirements, such as powder to hot spring (thermal) slurry. The water ratio is generally controlled between 1 and 30:100%, typically between 1 and 30 ± 5%. The slurry (soup) prepared according to the above ratio enters each main pipeline and connects to a single slurry (soup) supply solenoid valve. The solenoid valve is opened automatically or manually, allowing the slurry (soup) to flow into the mud (soup) pool (basin). One to n mud (soup) therapy sessions can be performed. After one to n therapy sessions, when it is necessary to replace the slurry (soup), the bottom discharge valve is opened to discharge the slurry (soup) into the cleaning pool. Then, a certain amount of inorganic flocculant, including aluminum sulfate, aluminum chloride, and sulfuric acid, is added. Commonly used aluminum salts include aluminum sulfate (AL2(SO4)3·18H2O) and alum (AL2(SO4)3·K2SO4·24H2O). Another type of salt is iron salts, such as ferric chloride hydrate (FeCl3·6H2O), ferrous sulfate hydrate (FeSO4·7H2O), and ferric sulfate. Alternatively, a very small amount of organic polymeric flocculant or microbial flocculant can be added. Since the mud (soup) waste is recycled and dried, it undergoes a second high-temperature calcination. The added flocculant decomposes and evaporates at high temperatures, thus not affecting its reuse.

[0019] In addition, after three-stage dredging, the slurry (soup) enters a nano-ceramic membrane filter to further purify the water in the slurry (soup). Then, the purified viscous waste enters a high-speed solid-liquid separator to separate it into a semi-dry state, which is then directly briquetteed. Alternatively, it can be transported to a stockpile for natural drying or dried in a dryer. After drying, it enters a briquetting machine for briquetting and then enters a high-temperature calcining furnace for calcination, completing one cycle. This process is repeated in the future.

[0020] This process unit employs a bubble tank filtration system with a sand-cylinder water pump for disinfection. A fully enclosed, air-cooled motor paired with a self-priming centrifugal pump effectively enhances pump performance. The filter material is made of food-grade, safe, and environmentally friendly materials. The casing is corrosion-resistant, rust-proof, and durable, free of aluminum and copper. Multiple processing steps prevent secondary pollution. The sand-cylinder water pump operates stably at high head, with quiet operation and thermal protection, featuring intelligent temperature control, a safety locking function, and a transparent, robust, one-piece filter cover. The pump operates on 220-240V, with a full-load current of 1.8A, a horsepower of 0.35, and a flow rate of 10m³ / h. 3 / h, power of 400w, interface size (inlet) 50mm, outlet 50mm, head of 9m, insulation class of F, pump casing of PP 30% GF, fastening connection bracket of PP 30% GF, flexible corrugated pipe of PVC, impeller of PPO, guide vane of PP 30% GF, drain cover of PMMA, joint of PVC, fixed surface of PP 30% GF, motor shaft of stainless steel 304-N45, motor model of 6402, rated speed of 2850rpm, thermal overload protection, protection class of IPX5, bearing type of rolling, pool water temperature range of 5-40℃, ambient temperature of 40℃.

[0021] The purification device has three layers of filter media: the upper layer is quartz sand, the middle layer is volcanic slag, and the lower layer is activated carbon. Water enters from the upper layer of quartz sand and exits from the lower layer. Suspended solids in the water are adsorbed and decomposed, allowing the purified water to flow out from the bottom up. The mud (soup) purification device is also equipped with backwashing. Water enters the mud (soup) purification device through the inlet, passes through the quartz sand from the bottom up, washes away the dirt filtered in the quartz sand, and is discharged through the drain outlet.

[0022] All standard parts used in this invention can be purchased commercially, and irregularly shaped parts can be customized according to the description and drawings. The specific connection methods for each part all employ conventional methods such as bolts, rivets, and welding, which are mature technologies in the prior art. The machinery, parts, and equipment all use conventional models in the prior art, and the circuit connections also use conventional connection methods in the prior art, which will not be detailed here. Any content not described in detail in this specification belongs to the prior art known to those skilled in the art.

[0023] In the description of this invention, the terms "first" and "second" are used for descriptive purposes only and should not be construed as indicating or implying relative importance or implicitly specifying the number of indicated technical features. Thus, a feature defined as "first" or "second" may explicitly or implicitly include one or more of that feature. "A plurality of" means two or more, unless otherwise explicitly specified.

[0024] In this invention, unless otherwise explicitly specified and limited, the terms "installation," "connection," "linking," and "fixing," etc., should be interpreted broadly. For example, they can refer to a fixed connection, a detachable connection, or an integral part; they can refer to a mechanical connection or an electrical connection; they can refer to a direct connection or an indirect connection through an intermediate medium; they can refer to the internal communication of two components or the interaction between two components. Those skilled in the art can understand the specific meaning of the above terms in this invention according to the specific circumstances.

[0025] In this invention, unless otherwise explicitly specified and limited, "above" or "below" the second feature can mean that the first feature is in direct contact with the second feature, or that the first feature is in indirect contact with the second feature through an intermediate medium. Furthermore, "above," "over," and "on top" of the second feature can mean that the first feature is directly above or diagonally above the second feature, or simply that the first feature is at a higher horizontal level than the second feature. "Below," "below," and "under" the second feature can mean that the first feature is directly below or diagonally below the second feature, or simply that the first feature is at a lower horizontal level than the second feature.

[0026] In the description of this specification, the terms "one embodiment," "some embodiments," "example," "specific example," or "some examples," etc., refer to specific features, structures, materials, or characteristics described in connection with that embodiment or example, which are included in at least one embodiment or example of the present invention. In this specification, the illustrative expressions of the above terms do not necessarily refer to the same embodiment or example. Furthermore, the specific features, structures, materials, or characteristics described may be combined in any suitable manner in one or more embodiments or examples. Moreover, without contradiction, those skilled in the art can combine and integrate the different embodiments or examples described in this specification, as well as the features of different embodiments or examples.

[0027] The accompanying drawings of the embodiments disclosed in this invention only involve structures relevant to the embodiments disclosed in this invention. Other structures can be referred to with common designs. Unless otherwise specified, the same embodiment and different embodiments of this invention can be combined with each other.

[0028] Although the present invention has been described in detail with reference to the foregoing embodiments, those skilled in the art can still modify the technical solutions described in the foregoing embodiments or make equivalent substitutions for some of the technical features. Any modifications, equivalent substitutions, improvements, etc., made within the spirit and principles of the present invention should be included within the protection scope of the present invention.

Claims

1. A salt-based multi-mineral roasting fine grinding nano-slurry bath new material production process system, characterized in that: include: Various types of mineral crushing and smelting systems, crushing and grinding to nanometer air flow crushing preparation system, compound metering synthesis salt-based mud soup preparation system, salt-based mud soup supply system and mud soup discharge purification and recycling system. The minerals of the present invention are smelted at high temperature and reorganized in the phase change process, and the material composition undergoes fundamental changes. The single component becomes a salt-based composite component. The product after calcination and melting is then coarsely crushed and finely ground to nanometer size. The powder grinding fineness reaches 1000-3000 mesh nanometer level. The solid is also regarded as a liquid and has liquid-like properties.

2. A salt-based multi-mineral roasting fine grinding nano-slurry bath new material production process system as claimed in claim 1, characterized in that: The salt-based multi-mineral combination refers to a composite molten salt calcined at 1400-1700°C, which is cooled and finely ground into particles ≤ 2mm, and then calcined at different temperature ranges of 850-1300°C with a variety of trace element minerals rich in human needs, and then crushed into nano-scale mineral powder through multiple stages: the salt-based multi-mineral combination is added to 100 parts of water according to a ratio of 1-20:99-80, and the soup is evenly stirred, and the temperature is controlled at 38-45°C for therapeutic bathing. A process system.

3. A salt-based multi-mineral roasting fine grinding nano-slurry bath new material production process system as claimed in claim 2, characterized in that: The high-temperature calcined molten salt mineral combination must be crushed, ground and then nano-finely ground to form a nano-scale powder, which is the core of the entire system. It is equivalent to simulating the composition of volcanic ash and is superior to that of volcanic ash. After repeated use, the discharged matter is purified by a rotary nano-ceramic membrane, and then separated by high-efficiency solid-liquid separation, and then pressed into balls and calcined, so that the residual organic matter in the therapeutic bath and the various flocculants and other organic and inorganic substances added during sedimentation and silt removal are decomposed at high temperature, some of which evaporate with the gas, and some are decomposed and carbonized, restoring the original state, and then being nano-sized to restore the original function, thereby realizing repeated recycling, reducing emissions and protecting the environment.

4. The salt-based multi-mineral roasting fine grinding nano-slurry bath new material production process system as claimed in claim 1, characterized in that: The therapeutic bath system is designed with a high-temperature steam heating balance system and an ozone disinfection system. After repeated therapeutic baths, the soup in the pool is immediately disinfected and sterilized with ozone, and then the second group of people enter. This cycle is repeated n times, during which a constant temperature controller is set to keep the temperature always maintained within the set temperature range.

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