CN112852044A - Blow molding formula of oil tank and manufacturing process thereof - Google Patents

Blow molding formula of oil tank and manufacturing process thereof Download PDF

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Publication number
CN112852044A
CN112852044A CN202110150728.2A CN202110150728A CN112852044A CN 112852044 A CN112852044 A CN 112852044A CN 202110150728 A CN202110150728 A CN 202110150728A CN 112852044 A CN112852044 A CN 112852044A
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China
Prior art keywords
parts
blow molding
limestone
silicon dioxide
stabilizer
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Pending
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CN202110150728.2A
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Chinese (zh)
Inventor
苏雪琼
张正军
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Quanzhou Kangbo Electromechanical Co ltd
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Quanzhou Kangbo Electromechanical Co ltd
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Priority to CN202110150728.2A priority Critical patent/CN112852044A/en
Publication of CN112852044A publication Critical patent/CN112852044A/en
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K13/00Use of mixtures of ingredients not covered by one single of the preceding main groups, each of these compounds being essential
    • C08K13/04Ingredients characterised by their shape and organic or inorganic ingredients
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24Acids; Salts thereof
    • C08K3/26Carbonates; Bicarbonates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/34Silicon-containing compounds
    • C08K3/36Silica
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K7/00Use of ingredients characterised by shape
    • C08K7/02Fibres or whiskers
    • C08K7/04Fibres or whiskers inorganic
    • C08K7/14Glass
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24Acids; Salts thereof
    • C08K3/26Carbonates; Bicarbonates
    • C08K2003/265Calcium, strontium or barium carbonate
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00Properties
    • C08L2201/08Stabilised against heat, light or radiation or oxydation

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

The invention relates to the field of oil tank manufacturing, in particular to a blow molding formula of an oil tank, which comprises the following raw materials in parts by weight: 90-100 parts of polyethylene resin, 1-5 parts of stabilizer, 0.6-1 part of antioxidant, 0.5-1 part of ultraviolet absorbent, 20-30 parts of limestone, 1-2 parts of short glass fiber and 10-20 parts of silicon dioxide; calcining limestone at 800-1000 ℃, introducing water and CO2, stirring, standing for a period of time to enable precipitates to appear at the bottom of liquid, filtering out the precipitates, drying and grinding the precipitates to obtain powder, then uniformly stirring the powder and stearic acid at 130 ℃, adding polyethylene resin, a stabilizer, an antioxidant, an ultraviolet absorbent and short glass fibers, uniformly stirring, cooling, granulating, sending the granules into a blow molding machine, and performing blow molding to obtain the oil tank. According to the invention, the toughness of the oil drum can be effectively increased through the added limestone, the hardness and rigidity of the oil drum are improved, and the impact strength of the oil drum plastic can be improved through the added short glass fiber.

Description

Blow molding formula of oil tank and manufacturing process thereof
Technical Field
The invention relates to the field of oil tank manufacturing, in particular to a blow molding formula of an oil tank and a manufacturing process thereof.
Background
The traditional metal oil tank has the defects of high price, heavy weight, high welding difficulty, easy deformation in collision and the like, so that the popularization and development of the metal oil tank are limited, and the oil tank is gradually changed from a metal material to a plastic material.
At present, plastic fuel tanks are basically molded by blow molding, and traditionally, in order to increase the toughness of the plastic fuel tanks, the purpose of toughening and modifying is achieved by a method of adding rubber or elastomer, but because the rubber is relatively flexible and the heat resistance is relatively low, the heat resistance of the plastic fuel tanks is easily influenced.
Disclosure of Invention
The invention provides a blow molding formula of an oil tank and a manufacturing process thereof, which aim to solve the problem that the heat resistance of the plastic oil tank is easily influenced by increasing the toughness of the plastic oil tank through rubber in the prior art.
The invention adopts the following technical scheme: a blow molding formula of an oil tank and a manufacturing process thereof comprise the following raw materials in parts by weight: 90-100 parts of polyethylene resin, 1-5 parts of stabilizer, 0.6-1 part of antioxidant, 0.5-1 part of ultraviolet absorbent, 20-30 parts of limestone, 1-2 parts of short glass fiber and 10-20 parts of silicon dioxide.
As a further improvement, the polyethylene resin comprises 90 parts of polyethylene resin, 1 part of stabilizer, 0.6 part of antioxidant, 0.5 part of ultraviolet absorber, 20 parts of limestone, 1 part of short glass fiber and 10 parts of silicon dioxide.
As a further improvement, 95 parts of polyethylene resin, 2.5 parts of stabilizer, 0.8 part of antioxidant, 0.8 part of ultraviolet absorber, 25 parts of limestone, 2 parts of short glass fiber and 15 parts of silicon dioxide.
As a further improvement, 100 parts of polyethylene resin, 5 parts of stabilizer, 1 part of antioxidant, 1 part of ultraviolet absorber, 30 parts of limestone, 2 parts of short glass fiber and 20 parts of silicon dioxide.
A blow molding manufacturing process of an oil tank is characterized in that: the method comprises the following steps:
firstly, preparing raw materials, preparing limestone, calcining the limestone at 800-1000 ℃, introducing water and CO2, stirring, standing for a period of time to enable precipitates to appear at the bottom of liquid, filtering out the precipitates, drying and grinding the precipitates to obtain powder with the average particle size of 0.1-1 mu m, and uniformly stirring the powder and stearic acid at 130 ℃ to obtain lime powder;
preparing silicon dioxide, namely drying the silicon dioxide in an oven at the temperature of 80-100 ℃;
secondly, mixing and granulating raw materials, namely adding dried silicon dioxide, polyethylene resin, a stabilizer, an antioxidant, an ultraviolet absorbent and short glass fibers into lime powder, uniformly stirring and mixing at the stirring speed of 600 plus 700rpm to form an oil drum blow molding raw material, pouring the oil drum blow molding raw material into a granulator, melting, plasticizing and extruding the oil drum blow molding raw material by the granulator, and cutting and granulating by a granulator to obtain granules;
and thirdly, oil drum blow molding, namely feeding the material particles obtained in the second step into a hollow blow molding machine, and carrying out hot melting, extrusion, blow molding and cooling molding on the material particles by the blow molding machine to obtain the oil tank.
As a further improvement, the standing time is 0.5-1 hour.
From the above description of the structure of the present invention, compared with the prior art, the present invention has the following advantages: according to the invention, the limestone, the short glass fiber and the silicon dioxide are added into the plastic raw material, the toughness of the oil drum can be effectively increased through the added limestone and silicon dioxide, meanwhile, the heat resistance of the oil drum can be effectively improved through the added limestone, and the impact strength of the oil drum plastic can be improved through the added short glass fiber.
Detailed Description
The invention is further illustrated by reference to the following examples.
In the first embodiment, the polyethylene resin comprises 90 parts of polyethylene resin, 1 part of stabilizer, 0.6 part of antioxidant, 0.5 part of ultraviolet absorber, 20 parts of limestone, 1 part of short glass fiber and 10 parts of silicon dioxide.
Example two, 95 parts of polyethylene resin, 2.5 parts of stabilizer, 0.8 part of antioxidant, 0.8 part of ultraviolet absorber, 25 parts of limestone, 2 parts of short glass fiber and 15 parts of silicon dioxide.
In the third embodiment, 100 parts of polyethylene resin, 5 parts of stabilizer, 1 part of antioxidant, 1 part of ultraviolet absorber, 30 parts of limestone, 2 parts of short glass fiber and 20 parts of silicon dioxide.
The blow molding manufacturing process of the fuel tank in the first to third embodiments comprises the following steps:
firstly, preparing raw materials, preparing limestone, calcining the limestone at 800-1000 ℃, if the calcining temperature is lower than 800 ℃, the calcining effect of the limestone is insufficient, if the calcining temperature exceeds 1000 ℃, the problems of overburning, quick increase of lime crystal grains and poor lime activity are easy to occur, then introducing water and CO2, stirring, standing for 0.5-1 hour to enable precipitates to appear at the bottom of liquid, filtering out the precipitates, drying the precipitates in a dryer until the water content is less than 0.4%, grinding the precipitates by a ball mill to obtain powder with the average particle size of 0.1-1 mu m, and then uniformly stirring the powder and stearic acid at 130 ℃ to obtain lime powder;
preparing silicon dioxide, namely drying the silicon dioxide in an oven at the temperature of 80-100 ℃;
secondly, mixing and granulating raw materials, namely adding dried silicon dioxide, polyethylene resin, a stabilizer, an antioxidant, an ultraviolet absorbent and short glass fibers into lime powder, uniformly stirring and mixing at the stirring speed of 600 plus 700rpm to form an oil drum blow molding raw material, pouring the oil drum blow molding raw material into a granulator, melting, plasticizing and extruding the oil drum blow molding raw material by the granulator, and cutting and granulating by a granulator to obtain granules; wherein the stabilizer can be a mixture of rare earth stabilizer and auxiliary stabilizer, the antioxidant can be one or more of phenolic antioxidant, bis-cinnamoyl thiodipropionate and bis-stearoyl thiodipropionate, and the ultraviolet absorbent can be 2-hydroxy-4-n-octoxy benzophenone.
And thirdly, oil drum blow molding, namely feeding the material particles obtained in the second step into a hollow blow molding machine, and carrying out hot melting, extrusion, blow molding and cooling molding on the material particles by the blow molding machine to obtain the oil tank.
After the limestone and the silicon dioxide are added, the hardness and the rigidity of the oil tank can be improved due to the large hardness and the good thermal stability of the limestone, the mechanical property is enhanced, the tensile strength and the bending strength can be improved, the manufactured oil tank has toughness, the thermal expansion coefficient and the shrinkage rate are reduced, the effect of reducing the impact strength generated by adding the limestone into plastic can be overcome by the added short glass fiber, and the oil tank can keep strong impact strength.
Heat resistance and bending Property test experiment
The method comprises the following steps of (1) testing heat resistance, respectively carrying out heat resistance tests on oil drums (comparison groups) with the same thickness in the prior art and oil drums in the first to third embodiments of the invention, specifically, respectively heating the oil drums in the prior art and the oil drums in the first to third embodiments to different temperatures, observing the states (solid state, slightly molten state, moderate molten state and molten state) of the oil drums, and judging the heat resistance of the oil drums according to the states of the oil drums at the different temperatures, wherein the oil drums in the prior art are composed of the following raw materials in parts by weight: 90 parts of polyethylene resin, 2 parts of stabilizer, 1 part of antioxidant, 0.5 part of ultraviolet absorber and 5 parts of rubber, wherein the specific experimental results are shown in the following table;
temperature, C Example one Example two EXAMPLE III Comparison group
1-50 In the solid state In the solid state In the solid state In the solid state
51-100 In the solid state In the solid state In the solid state In the solid state
101-150 In the solid state In the solid state In the solid state Micro-molten state
151-200 Micro-molten state In the solid state In the solid state Moderate molten state
201-250 Moderate molten state In the solid state Micro-molten state In the molten state
251-300 In the molten state Micro-molten state Moderate molten state In the molten state
From the above table, the micro-melting state occurs at the temperature of 151-200 ℃, the micro-melting state occurs at the temperature of 251-300 ℃, the micro-melting state occurs at the temperature of 201-250 ℃, and the micro-melting state occurs at the temperature of 101-150 ℃ in the comparison group; that is, the heat resistance of examples one to three was better than that of the comparative group, with the heat resistance of example two being the best;
bending strength test, namely taking oil drums (comparison groups) with the same thickness in the prior art and oil drums in the third embodiment of the invention to perform bending strength test, specifically, extruding the oil drums in the prior art and the first to third embodiments in the same stress area, and observing the pressure used when the oil drums are extruded and deformed to be highly bent, wherein the specific experimental results are shown in the following table;
pressure, MPa Example one Example two EXAMPLE III Comparison group
1-10 Not broken Not broken Not broken Not broken
11-20 Not broken Not broken Not broken Not broken
21-30 Microbend Microbend Microbend Microbend
31-40 Moderate bend Microbend Microbend Moderate bend
41-50 High degree of bending Moderate bend Moderate bend High degree of bending
51-60 Fracture of High degree of bending High degree of bending Fracture of
As can be seen from the above table, the experiment shows that the pressure of the high bending of the example I is 41-50MPa, the pressure of the high bending of the example II is 51-60MPa, the pressure of the high bending of the example III is 51-60MPa, and the pressure of the high bending of the comparison group is 41-50 MPa; that is, the strength properties of examples one to three are not much different from the bending strength properties of the comparative group, with the bending strength property of example two being the best;
according to the heat resistance test and the bending strength test, the added limestone, short glass fiber and silicon dioxide can effectively ensure the toughness of the oil drum and can also effectively improve the heat resistance.
The above description is only an embodiment of the present invention, but the design concept of the present invention is not limited thereto, and any insubstantial modifications made by using the design concept should fall within the scope of infringing the present invention.

Claims (6)

1. A blow molding formula of a fuel tank is characterized in that: the feed comprises the following raw materials in parts by weight: 90-100 parts of polyethylene resin, 1-5 parts of stabilizer, 0.6-1 part of antioxidant, 0.5-1 part of ultraviolet absorbent, 20-30 parts of limestone, 1-2 parts of short glass fiber and 10-20 parts of silicon dioxide.
2. A tank blow molding formulation as claimed in claim 1, wherein: 90 parts of polyethylene resin, 1 part of stabilizer, 0.6 part of antioxidant, 0.5 part of ultraviolet absorbent, 20 parts of limestone, 1 part of short glass fiber and 10 parts of silicon dioxide.
3. A tank blow molding formulation as claimed in claim 1, wherein: 95 parts of polyethylene resin, 2.5 parts of stabilizer, 0.8 part of antioxidant, 0.8 part of ultraviolet absorber, 25 parts of limestone, 2 parts of short glass fiber and 15 parts of silicon dioxide.
4. A tank blow molding formulation as claimed in claim 1, wherein: 100 parts of polyethylene resin, 5 parts of stabilizer, 1 part of antioxidant, 1 part of ultraviolet absorbent, 30 parts of limestone, 2 parts of short glass fiber and 20 parts of silicon dioxide.
5. A tank blow molding process according to any one of claims 1 to 4, wherein: the method comprises the following steps: firstly, preparing raw materials, preparing limestone, calcining the limestone at 800-1000 ℃, introducing water and CO2, stirring, standing for a period of time to enable precipitates to appear at the bottom of liquid, filtering out the precipitates, drying and grinding the precipitates to obtain powder with the average particle size of 0.1-1 mu m, and uniformly stirring the powder and stearic acid at 130 ℃ to obtain lime powder; preparing silicon dioxide, namely drying the silicon dioxide in an oven at the temperature of 80-100 ℃; secondly, mixing and granulating raw materials, namely adding dried silicon dioxide, polyethylene resin, a stabilizer, an antioxidant, an ultraviolet absorbent and short glass fibers into lime powder, uniformly stirring and mixing at the stirring speed of 600 plus 700rpm to form an oil drum blow molding raw material, pouring the oil drum blow molding raw material into a granulator, melting, plasticizing and extruding the oil drum blow molding raw material by the granulator, and cutting and granulating by a granulator to obtain granules; and thirdly, oil drum blow molding, namely feeding the material particles obtained in the second step into a hollow blow molding machine, and carrying out hot melting, extrusion, blow molding and cooling molding on the material particles by the blow molding machine to obtain the oil tank.
6. The blow molding formula of the fuel tank and the manufacturing process thereof according to claim 5 are characterized in that: the standing time is 0.5-1 hour.
CN202110150728.2A 2021-02-04 2021-02-04 Blow molding formula of oil tank and manufacturing process thereof Pending CN112852044A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113372670A (en) * 2021-06-28 2021-09-10 江苏惠源新材料股份有限公司 Method for manufacturing high-hardness plastic oil drum
CN116554571A (en) * 2023-04-27 2023-08-08 浙江大晋新材料科技有限公司 High-strength plastic bucket and preparation method thereof

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CN101722697A (en) * 2008-10-29 2010-06-09 帝人化成株式会社 Resin shaping body
CN103483779A (en) * 2009-09-30 2014-01-01 株式会社Adeka Manufacturing method of plastic bottle
WO2018045932A1 (en) * 2016-09-07 2018-03-15 金发科技股份有限公司 Liquid crystal polyester molded composition and application thereof
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US20190062527A1 (en) * 2016-03-02 2019-02-28 Adeka Corporation Resin additive composition, thermoplastic resin composition, and molded article thereof
CN111978686A (en) * 2020-08-25 2020-11-24 广州大学 Regenerated polyester material and preparation method thereof

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Publication number Priority date Publication date Assignee Title
US20030050378A1 (en) * 2000-02-14 2003-03-13 Pierre Blanchard Filler concentrates for use in thermoplastic materials
CN101722697A (en) * 2008-10-29 2010-06-09 帝人化成株式会社 Resin shaping body
CN103483779A (en) * 2009-09-30 2014-01-01 株式会社Adeka Manufacturing method of plastic bottle
US20190062527A1 (en) * 2016-03-02 2019-02-28 Adeka Corporation Resin additive composition, thermoplastic resin composition, and molded article thereof
WO2018045932A1 (en) * 2016-09-07 2018-03-15 金发科技股份有限公司 Liquid crystal polyester molded composition and application thereof
CN108342007A (en) * 2018-02-13 2018-07-31 南京精工新材料有限公司 A kind of blowing oil tank material and preparation method thereof
CN111978686A (en) * 2020-08-25 2020-11-24 广州大学 Regenerated polyester material and preparation method thereof

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113372670A (en) * 2021-06-28 2021-09-10 江苏惠源新材料股份有限公司 Method for manufacturing high-hardness plastic oil drum
CN116554571A (en) * 2023-04-27 2023-08-08 浙江大晋新材料科技有限公司 High-strength plastic bucket and preparation method thereof

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