Powerful oil powder heavy oil cold water foaming agent suitable for various scenes
By using powerful oil-powder powder heavy oil cold water foaming agent composed of food-grade granular sodium hydroxide, the problems of high energy consumption, strong corrosiveness and odor irritation of foaming agents are solved, and efficient cleaning and safe use at low temperatures are achieved.
Patent Information
- Application Number
- CN202510424392.2
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2025-04-07
- Publication Date
- 2025-07-08
AI Technical Summary
Existing foaming agents need to be used at high temperatures, with high energy consumption and limited scenarios. They are highly corrosive and prone to damage equipment. They may also produce irritating odors during use and endanger human health.
A strong oil-powder heavy oil cold water foaming agent composed of food-grade granular sodium hydroxide, sodium metasilicate pentahydrate, CAB-35 cocamidopropyl betaine surfactant, etc., is stimulated by low-temperature water and combined with specific process processing to form a cleaning product suitable for various scenarios.
It realizes efficient removal of heavy oil stains at room temperature, reduces the corrosion and odor irritation of equipment, simplifies the use steps, improves work efficiency, and reduces health risks.
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Figure BDA0005346265310000111
Abstract
Description
Technical Field
[0001] The present invention relates to the technical field of strong oil powder heavy oil cold water foaming agents, and in particular to a strong oil powder heavy oil cold water foaming agent applicable to various scenarios. Background Art
[0002] The existing foaming agents on the market mainly rely on Junzheng caustic soda, caustic soda, and strong sodium oxide, which can only be used by heating with hot water or boiling water, that is, high temperature (above 80°C) is required to activate the cleaning power. Due to the high corrosiveness, various equipment parts will be corroded, discolored, and damaged.
[0003] In various occasions on the market, special utensils and tools are also required to heat water for use. When in use, not only will there be a particularly pungent smell that causes great harm to the human respiratory tract, but also a large amount of time will be wasted in use.
[0004] Therefore, in view of the problems that the above-mentioned foaming agents need to rely on high temperature for use, have high energy consumption, limited scenarios, strong corrosiveness that is easy to damage equipment, and will also produce irritating odors that endanger human health when in use, a strong oil powder heavy oil cold water foaming agent applicable to various scenarios can be designed. Summary of the Invention
[0005] In order to overcome the problems that traditional foaming agents need to rely on high temperature for use, have high energy consumption, limited scenarios, strong corrosiveness that is easy to damage equipment, and will also produce irritating odors that endanger human health when in use.
[0006] The technical solution of the present invention is: a strong oil powder heavy oil cold water foaming agent applicable to various scenarios, calculated by mass percentage, includes the following components: 68% - 72% of food-grade granular sodium hydroxide, 8% - 12% of sodium metasilicate pentahydrate, 8% - 12% of CAB-35 coconut oil amide propyl betaine surfactant, 2% - 3% of methyl tert-butyl ether solvent, 0.8% - 1% of sunset yellow pigment, 0.8% - 1% of lemon essence, and 4% - 5% of trace additives.
[0007] Preferably, the trace additives include any one or more of anti-caking agents, pH stabilizers, and dispersants.
[0008] Preferably, the purity of the food-grade granular sodium hydroxide is above 99%, and the particle diameter is between 0.5 - 1.5 millimeters.
[0009] Preferably, the active matter content of the CAB-35 coconut oil amide propyl betaine surfactant is not less than 30%.
[0010] Preferably, the purity of the methyl tert-butyl ether solvent is above 98%.
[0011] A powerful oil powder and heavy oil cold water foaming agent suitable for various scenarios, and its preparation steps are as follows:
[0012] S1: Raw material pretreatment
[0013] S11: Remove lumps and impurities of food-grade granular sodium hydroxide through a vibrating sieve with a pore diameter of 200 μm to ensure uniform particles, store in a dry environment with a humidity ≤ 30%, and avoid moisture absorption and caking;
[0014] S12: Premix sodium metasilicate pentahydrate and CAB-35 coconut oil amide propyl betaine surfactant in a mass ratio of 1:1 to form a premixed solution, where the premixing temperature is controlled at 25 ± 2 °C to avoid surfactant stratification;
[0015] S13: When pretreating methyl tert-butyl ether solvent, introduce nitrogen gas into a closed container for 5 minutes to remove oxygen and prevent oxidation;
[0016] S14: Dilute sunset yellow pigment and lemon essence with 0.5% of the total mass of methyl tert-butyl ether to make a premixed solution;
[0017] S2: Mixing and stirring
[0018] S21: Sequentially pour the sodium hydroxide particles treated in S11, the premixed solution of S12, the methyl tert-butyl ether solvent treated in S13, the pigment and essence premixed solution of S14, and trace additives into a double-helix conical mixer for mixing treatment;
[0019] S22: After mixing, turn on a vacuum pump with a vacuum degree of -0.08 MPa to defoam for 5 minutes to avoid particle pores;
[0020] S3: Molding and drying
[0021] S31: Granulation treatment
[0022] Use a rotary granulator with a 1.5 mm sieve plate, control the feeding speed at 20 kg / min, and the rotation speed at 150 rpm to obtain preliminary particles;
[0023] S32: Drying and solidification
[0024] Use a belt dryer to solidify the above-mentioned particles, where the temperature of the feeding section is 45 °C, the time is between 10 - 12 minutes to remove the surface solvent; the temperature of the solidification section is 60 °C, the time is between 19 - 21 minutes to complete the crystal form transformation; the temperature of the cooling section is 30 °C, the time is between 3 - 5 minutes to prevent caking;
[0025] S33: Screening treatment
[0026] First, a primary sieve with an aperture of 800 μm is used to remove oversized particles; then, a secondary sieve with an aperture of 100 μm is used, and the material passing through the sieve is returned to the granulator.
[0027] S4: Packaging
[0028] An aluminum foil composite bag with a barrier property ≥ 95% is used, lined with a PE film, and each bag has a net weight of 25 kg.
[0029] Preferably, in the dry mixing and stirring stage of S21, the rotation speed of the double - screw conical mixer is 200 rpm and the time is 10 minutes to ensure uniform dispersion of the solid components; in the wet mixing and stirring stage, the solvent is slowly added, the rotation speed is adjusted to 400 rpm, and the time is 25 minutes to form a uniform paste.
[0030] Preferably, the granular finished product is purple or gray, the particle size distribution is 100 - 500 microns, the dissolution time in water at 25 °C is less than 3 minutes, and the pH value of the solution is controlled between 12.6 and 13.
[0031] Preferably, the decomposition rate of the finished product for heavy oil stains at room temperature is ≥ 95%, and the corrosion rate for metal substrates is ≤ 0.05 mm / year.
[0032] The beneficial effects of the present invention: The food - grade granular sodium hydroxide in the formula of the present invention, by virtue of its strong alkalinity, undergoes a saponification reaction with grease, can effectively decompose heavy - oil dirt. Sodium metasilicate pentahydrate plays a role in dispersion, emulsification and corrosion inhibition, assisting sodium hydroxide to strengthen decontamination. Whether it is the oil stains on hotel purifiers, range hoods or the stubborn stains on the surface of factory machinery, it can be efficiently removed. The components work synergistically, making the foaming agent applicable to different places such as hotels, shopping malls, factories, etc. Whether it is the oil stains on the ground, walls or various domestic and industrial equipment, it can play an excellent cleaning role, and there is no need to replace cleaning products for different scenarios.
[0033] Traditional cleaning products need to be prepared with hot water or boiling water. This foaming agent only needs to add normal - temperature water, greatly simplifying the use steps and saving the preparation time. Users do not need to prepare special heating equipment and utensils. In the domestic and household appliance cleaning industries, when used for the disassembly and cleaning of hotel purifiers and range hoods, it can quickly decompose oil stains, reduce the soaking and cleaning time, and greatly improve work efficiency.
[0034] Using food - grade granular sodium hydroxide, combined with sodium metasilicate pentahydrate, CAB - 35 coconut oil amide propyl betaine surfactant, etc., reduces the corrosiveness of the product. Compared with traditional products mainly based on Junzheng caustic soda and caustic soda, it causes less damage to equipment and objects, reducing the risk of equipment corrosion, discoloration and damage.
[0035] Add lemon essence, which can effectively reduce the pungent smell, reduce the harm to the human respiratory tract, improve the working environment, and reduce the health risks of long-term use. At the same time, add sunset yellow pigment to make the product show purple or slightly gray granular on the surface, with eye-catching appearance, easy to identify and distinguish, and improve the product recognition. Detailed implementation mode
[0036] Example 1
[0037] The present invention will be further described below in conjunction with examples.
[0038] The present invention provides an example: a strong oil-dissolving powder heavy oil cold water foaming agent applicable to various scenarios, which includes the following components in mass percentage: 68% of food-grade granular sodium hydroxide, 8% of sodium metasilicate pentahydrate, 8% of CAB-35 coconut oil amide propyl betaine surfactant, 2% of methyl tert-butyl ether solvent, 0.8% of sunset yellow pigment, 0.8% of lemon essence, and 4% of trace additives. The trace additives include any one or more of anti-caking agents, pH stabilizers, and dispersants. The purity of the food-grade granular sodium hydroxide is above 99%, the particle diameter is between 0.5 and 1.5 mm, the active matter content of the CAB-35 coconut oil amide propyl betaine surfactant is not less than 30%, and the purity of the methyl tert-butyl ether solvent is above 98%.
[0039] A strong oil-dissolving powder heavy oil cold water foaming agent applicable to various scenarios, and its preparation steps are as follows:
[0040] S1: Pretreatment of raw materials
[0041] S11: Remove the caking and impurities of the food-grade granular sodium hydroxide through a 200μm vibrating sieve to ensure uniform particles, and store them in a dry environment with a humidity ≤ 30% to avoid moisture absorption and caking;
[0042] S12: Premix sodium metasilicate pentahydrate and CAB-35 coconut oil amide propyl betaine surfactant in a mass ratio of 1:1 to form a premixed solution, and control the premixing temperature at 25 ± 2°C to avoid surfactant stratification;
[0043] S13: When pretreating the methyl tert-butyl ether solvent, introduce nitrogen into a closed container for 5 minutes to remove oxygen and prevent oxidation;
[0044] S14: Dilute sunset yellow pigment and lemon essence with 0.5% of the total mass of methyl tert-butyl ether to make a premixed solution;
[0045] S2: Mixing and stirring
[0046] S21: Pour the sodium hydroxide particles processed in S11, the premixed solution in S12, the methyl tert-butyl ether solvent processed in S13, the pigment and flavor premixed solution in S14, and trace additives into a double-helix conical mixer in sequence for mixing. During the dry mixing stage, the rotation speed of the double-helix conical mixer is 200 rpm and the time is 10 minutes to ensure uniform dispersion of solid components. During the wet mixing stage, slowly add the solvent, adjust the rotation speed to 400 rpm, and the time is 25 minutes to form a uniform paste.
[0047] S22: After mixing, turn on a vacuum pump with a vacuum degree of -0.08 MPa for defoaming for 5 minutes to avoid particle pores.
[0048] S3: Molding and drying
[0049] S31: Granulation
[0050] Use a rotary granulator with a 1.5 mm aperture sieve plate, control the feeding speed at 20 kg / min, and the rotation speed at 150 rpm to obtain preliminary particles.
[0051] S32: Drying and curing
[0052] Use a belt dryer to cure the above-mentioned particles. The temperature of the feeding section is 45 °C and the time is between 10 - 12 minutes to remove the surface solvent. The temperature of the curing section is 60 °C and the time is between 19 - 21 minutes to complete the crystal form transformation. The temperature of the cooling section is 30 °C and the time is between 3 - 5 minutes to prevent caking.
[0053] S33: Screening
[0054] First, use a primary sieve with an aperture of 800 μm to remove oversized particles. Then, use a secondary sieve with an aperture of 100 μm, and the undersize material is returned to the granulator.
[0055] S4: Packaging
[0056] Use an aluminum foil composite bag with a barrier property ≥ 95%, lined with a PE film, and the net weight of each bag is 25 kg.
[0057] The granular finished product is purple or gray, with a particle size distribution of 100 - 500 microns, a dissolution time in water at 25 °C of less than 3 minutes, the pH value of the solution controlled between 12.6 - 13, the decomposition rate of the finished product for heavy oil stains at normal temperature ≥ 95%, and the corrosion rate for metal substrates ≤ 0.05 mm / year.
[0058] Example 2
[0059] The present invention will be further described below in conjunction with the examples.
[0060] The present invention provides an embodiment: a powerful oil-dissolving powder heavy oil cold water foaming agent applicable to various scenarios, which, by mass percentage, comprises the following components: 70% of food-grade granular sodium hydroxide, 10% of sodium metasilicate pentahydrate, 10% of CAB-35 coconut oil amide propyl betaine surfactant, 3% of methyl tert-butyl ether solvent, 1% of sunset yellow pigment, 1% of lemon essence, and 4% of trace additives. The trace additives include any one or more of anti-caking agents, pH stabilizers, and dispersants. The purity of the food-grade granular sodium hydroxide is above 99%, the particle diameter is between 0.5 and 1.5 mm, the active matter content of the CAB-35 coconut oil amide propyl betaine surfactant is not less than 30%, and the purity of the methyl tert-butyl ether solvent is above 98%.
[0061] A powerful oil-dissolving powder heavy oil cold water foaming agent applicable to various scenarios, and its preparation steps are as follows:
[0062] S1: Raw material pretreatment
[0063] S11: Remove the caking and impurities of the food-grade granular sodium hydroxide through a 200μm aperture vibrating screen to ensure uniform particles, store it in a dry environment with a humidity ≤ 30% to avoid moisture absorption and caking;
[0064] S12: Premix sodium metasilicate pentahydrate and CAB-35 coconut oil amide propyl betaine surfactant in a mass ratio of 1:1 to form a premixed solution, and control the premixing temperature at 25 ± 2°C to avoid surfactant stratification;
[0065] S13: When pretreating the methyl tert-butyl ether solvent, introduce nitrogen into a closed container for 5 minutes to remove oxygen and prevent oxidation;
[0066] S14: Dilute sunset yellow pigment and lemon essence with 0.5% of the total mass of methyl tert-butyl ether to make a premixed solution;
[0067] S2: Mixing and stirring
[0068] S21: Sequentially pour the sodium hydroxide particles treated in S11, the premixed solution of S12, the methyl tert-butyl ether solvent treated in S13, the pigment and essence premixed solution of S14, and trace additives into a double helix conical mixer for mixing. During the dry mixing and stirring stage, the rotation speed of the double helix conical mixer is 200 rpm and the time is 10 minutes to ensure uniform dispersion of the solid components; during the wet mixing and stirring stage, slowly add the solvent, adjust the rotation speed to 400 rpm, and the time is 25 minutes to form a uniform paste;
[0069] S22: After mixing, turn on a vacuum pump with a vacuum degree of -0.08 MPa to defoam for 5 minutes to avoid particle pores;
[0070] S3: Molding and drying
[0071] S31: Granulation treatment
[0072] Using a rotary granulator with a 1.5 mm sieve plate aperture, controlling the feeding speed at 20 kg / min and the rotation speed at 150 rpm to obtain preliminary granules;
[0073] S32: Drying and curing
[0074] Using a belt dryer to cure the above-mentioned granules. The temperature in the feeding section is 45°C, and the time is between 10 - 12 minutes to remove the surface solvent; the temperature in the curing section is 60°C, and the time is between 19 - 21 minutes to complete the crystal form transformation; the temperature in the cooling section is 30°C, and the time is between 3 - 5 minutes to prevent caking;
[0075] S33: Screening treatment
[0076] First, use a primary sieve with an aperture of 800 μm to remove oversized granules; then use a secondary sieve with an aperture of 100 μm, and the undersize material is returned to the granulator;
[0077] S4: Packaging
[0078] Use an aluminum foil composite bag with a barrier property ≥ 95%, lined with a PE film, and the net weight per bag is 25 kg.
[0079] The granular finished product is purple or gray, with a particle size distribution of 100 - 500 microns, a dissolution time in water at 25°C of less than 3 minutes, the solution pH value controlled between 12.6 - 13, the decomposition rate of the finished product for heavy oil stains at normal temperature ≥ 95%, and the corrosion rate on the metal substrate ≤ 0.05 mm / year.
[0080] Example 3
[0081] The present invention will be further described below in conjunction with the examples.
[0082] The present invention provides an example: A powerful oil-dissolving powder heavy oil cold water foaming agent applicable to various scenarios, calculated by mass percentage, includes the following components: 72% of food-grade granular sodium hydroxide, 12% of sodium metasilicate pentahydrate, 12% of CAB-35 coconut oil amide propyl betaine surfactant, 3% of methyl tert-butyl ether solvent, 1% of sunset yellow pigment, 1% of lemon essence, and 5% of trace additives. The trace additives include any one or more of anti-caking agents, pH stabilizers, and dispersants. The purity of the food-grade granular sodium hydroxide is above 99%, the particle diameter is between 0.5 - 1.5 mm, the active matter content of the CAB-35 coconut oil amide propyl betaine surfactant is not less than 30%, and the purity of the methyl tert-butyl ether solvent is above 98%.
[0083] A powerful oil-dissolving powder heavy oil cold water foaming agent applicable to various scenarios, and its preparation steps are as follows:
[0084] S1: Raw material pretreatment
[0085] S11: Remove caking and impurities of food-grade granular sodium hydroxide through a vibrating sieve with a pore size of 200 μm to ensure uniform particles, store in a dry environment with a humidity ≤ 30%, and avoid moisture absorption and caking;
[0086] S12: Premix sodium metasilicate pentahydrate and CAB-35 cocamidopropyl betaine surfactant in a mass ratio of 1:1 to form a premixed solution, with the premixing temperature controlled at 25 ± 2°C to avoid surfactant stratification;
[0087] S13: When pretreating methyl tert-butyl ether solvent, introduce nitrogen into a closed container for 5 minutes to remove oxygen and prevent oxidation;
[0088] S14: Dilute sunset yellow pigment and lemon essence with methyl tert-butyl ether accounting for 0.5% of the total mass to form a premixed solution;
[0089] S2: Mixing and stirring
[0090] S21: Sequentially pour the sodium hydroxide particles treated in S11, the premixed solution of S12, the methyl tert-butyl ether solvent treated in S13, the pigment and essence premixed solution of S14, and trace additives into a double-helix conical mixer for mixing treatment. During the dry mixing stage, the rotation speed of the double-helix conical mixer is 200 rpm and the time is 10 minutes to ensure uniform dispersion of solid components; during the wet mixing stage, slowly add the solvent, adjust the rotation speed to 400 rpm, and the time is 25 minutes to form a uniform paste;
[0091] S22: After mixing, start a vacuum pump with a vacuum degree of -0.08 MPa to defoam for 5 minutes to avoid particle pores;
[0092] S3: Molding and drying
[0093] S31: Granulation treatment
[0094] Use a rotary granulator with a 1.5 mm sieve plate, control the feeding speed at 20 kg / min, and the rotation speed at 150 rpm to obtain preliminary particles;
[0095] S32: Drying and curing
[0096] Use a belt dryer to cure the above particles. The temperature of the feeding section is 45°C and the time is between 10 - 12 minutes to remove the surface solvent; the temperature of the curing section is 60°C and the time is between 19 - 21 minutes to complete the crystal form transformation; the temperature of the cooling section is 30°C and the time is between 3 - 5 minutes to prevent caking;
[0097] S33: Screening treatment
[0098] First, use a primary sieve with a pore size of 800 μm to remove oversized particles; then use a secondary sieve with a pore size of 100 μm, and the undersize material is returned to the granulator.
[0099] S4: Packaging
[0100] Use an aluminum foil composite bag with a barrier property ≥ 95%, lined with a PE film, and the net weight of each bag is 25 kg.
[0101] The granular finished product is purple or gray, with a particle size distribution of 100 - 500 microns, a dissolution time in water at 25°C less than 3 minutes, the solution pH value controlled between 12.6 - 13, the decomposition rate of the finished product for heavy oil stains at room temperature ≥ 95%, and the corrosion rate for metal substrates ≤ 0.05 mm / year.
[0102] The usage method is as follows: It can be used directly after being prepared in proportion regardless of the occasion. Especially for domestic service companies and personnel in the household appliance cleaning industry, it helps to save a lot of time in cleaning hotel purifiers and disassembling and cleaning range hoods. In addition, it has a good effect on removing oil stains on various machines, hotel floors, shopping mall floors, and the surfaces of factory machinery in daily life, and is safer and more convenient to use.
[0103] Experimental Examples
[0104] Take the products of Example 1, 2, and 3 and the traditional foaming agent as a comparative example and set them as a group for experiments. The foaming agent in this case uses water at 25°C, and the traditional foaming agent uses water at 80°C. The foaming agent: water is diluted at 1:50, and is used to clean catering heavy oil containing animal fats and mechanical lubricating oil. Use infrared spectroscopy to measure the residual amount of oil stains, calculate the decomposition rate, and record the stratification time of the oil-water mixture. The detection data of the oil stain decomposition rate is as follows:
[0105] Immerse the materials in a foaming agent solution with a concentration of 1:20 and soak at 25°C for 72 hours. Measure the corrosion current density by the polarization curve method, and observe whether pitting or cracks appear by SEM. The detection data of the metal corrosion rate is as follows:
[0106] Mix the test substance with a mineral medium inoculated with microorganisms, and regularly measure the CO2 release amount within 28 days. The degradation rate calculation formula: Degradation rate = (CO2 release amount of the test substance / theoretical maximum CO2 release amount) × 100%; Simulate the wastewater treatment process and calculate the dosage of the neutralizing agent (such as sulfuric acid). The detection data of the biodegradability is as follows:
[0107] Recruit 20 volunteers to conduct an olfactory score (1 - 5 points) on the diluted solution (1:50). The scoring results are as follows:
[0108] Store the foaming agent sealed in an environment of 30°C / 70% humidity and detect it once a month. Measure the caking rate by the screening method. The detection data during the storage period is as follows:
[0109]
[0110]
Claims
1. A powerful oil-dissolving powder and heavy oil cold water foaming agent applicable to various scenarios, calculated by mass percentage, includes the following components: 68% - 72% of food-grade granular sodium hydroxide, 8% - 12% of sodium metasilicate pentahydrate, 8% - 12% of CAB-35 coconut oil amide propyl betaine surfactant, 2% - 3% of methyl tert-butyl ether solvent, 0.8% - 1% of sunset yellow pigment, 0.8% - 1% of lemon essence, and 4% - 5% of trace additives.
2. The powerful oil powder heavy oil cold water foaming agent applicable to various scenarios according to claim 1, characterized in that: The trace additives include any one or more of anti-caking agents, pH stabilizers, and dispersants.
3. The powerful oil-dispersing powder for heavy oil cold water foaming agent applicable to various scenarios according to claim 1, wherein: The purity of the food-grade granular sodium hydroxide is above 99%, and the particle diameter is between 0.5 - 1.5 mm.
4. A powerful oil powder heavy oil cold water foaming agent applicable to various scenarios according to claim 1, characterized in that: The active matter content of the CAB-35 coconut oil amide propyl betaine surfactant is not less than 30%.
5. The strong oil powder heavy oil cold water foaming agent applicable to various scenarios according to claim 1, characterized in that: The purity of the methyl tert-butyl ether solvent is above 98%.
6. The powerful oil powder heavy oil cold water foaming agent applicable to various scenarios according to claim 1 is characterized in that: Its preparation steps are as follows: S1: Raw material pretreatment S11: Remove caking and impurities of the food-grade granular sodium hydroxide through a 200μm aperture vibrating screen to ensure uniform particles, store in a dry environment with humidity ≤ 30% to avoid moisture absorption and caking; S12: Premix sodium metasilicate pentahydrate and CAB-35 coconut oil amide propyl betaine surfactant in a mass ratio of 1:1 to form a premixed solution, with the premixing temperature controlled at 25 ± 2°C to avoid surfactant stratification; S13: When pretreating the methyl tert-butyl ether solvent, introduce nitrogen into a closed container for 5 minutes to remove oxygen and prevent oxidation; S14: Dilute sunset yellow pigment and lemon essence with 0.5% of the total mass of methyl tert-butyl ether to make a premixed solution; S2: Mixing and stirring S21: Sequentially pour the sodium hydroxide particles treated in S11, the premixed solution in S12, the methyl tert-butyl ether solvent treated in S13, the pigment and essence premixed solution in S14, and the trace additives into a double helix conical mixer for mixing; S22: After mixing, start a vacuum pump with a vacuum degree of -0.08 MPa to defoam for 5 minutes to avoid particle pores; S3: Molding and drying S31: Granulation Use a rotary granulator with a 1.5mm aperture sieve plate, control the feeding speed at 20 kg / min, and the rotation speed at 150 rpm to obtain preliminary particles; S32: Drying and solidifying Use a belt dryer to solidify the above particles. The temperature of the feeding section is 45°C, and the time is between 10 - 12 minutes to remove surface solvents; the temperature of the solidifying section is 60°C, and the time is between 19 - 21 minutes to complete crystal form transformation; the temperature of the cooling section is 30°C, and the time is between 3 - 5 minutes to prevent caking; S33: Screening First, use a primary sieve with an aperture of 800μm to remove oversized particles; then use a secondary sieve with an aperture of 100μm, and the undersize material is returned to the granulator; S4: Packaging Use an aluminum foil composite bag with a barrier property ≥ 95%, lined with a PE film, and each bag has a net weight of 25 kg.
7. A powerful oil powder heavy oil cold water foaming agent applicable to various scenarios according to claim 1, characterized in that: In the dry mixing and stirring stage of S21, the rotation speed of the double helix conical mixer is 200 rpm, and the time is 10 minutes to ensure uniform dispersion of solid components; in the wet mixing and stirring stage, slowly add the solvent, adjust the rotation speed to 400 rpm, and the time is 25 minutes to form a uniform paste.
8. The strong oil powder heavy oil cold water foaming agent applicable to various scenarios according to claim 1, characterized in that: The granular finished product is purple or gray, with a particle size distribution of 100 to 500 microns, a dissolution time in water at 25°C of less than 3 minutes, and the pH value of the solution is controlled between 12.6 and 13.
9. The powerful oil-dissolving powder heavy oil cold water foaming agent applicable to various scenarios according to claim 1, characterized in that: The decomposition rate of this finished product for heavy oil stains at room temperature is ≥95%, and the corrosion rate for metal substrates is ≤0.05 mm / year.