A system for producing cosmetic products

Abstract

The present invention relates to the technical field of cosmetic production systems, and discloses a system for producing cosmetic products, including a water-phase raw material processing system and an oil-phase raw material processing system, wherein the water-phase raw material processing system and the oil-phase raw material processing system are arranged opposite to each other. When the dissolved material enters the emulsification reactor, the vacuum pump sucks the internal air to the outside, and the solution entering from the control valve falls in the space formed between the feed pipe and the pressure-dividing extrusion rod. During the rotation process, the internal bubbles can be compressed, and the bubbles in the solution can be effectively squeezed out. The solution entering the emulsification reactor is slowly stirred by the stirring rod and the auxiliary stirring rod, so that the internal bubbles flow fully, and then the bubbles generated in the solution can be fully sucked, so that the solution can have a more delicate feeling when supporting the cosmetics, and the solution can be smoother in the later stage and more easily absorbed by the skin.

Description

Technical Field

[0001] The present invention relates to the technical field of cosmetic production systems, and in particular to a system for producing cosmetic products. Background Art

[0002] Cosmetics refer to products that are applied to any part of the human body, such as skin, hair, nails, lips, teeth, etc., by smearing, spraying or other similar methods, for the purpose of cleansing, maintenance, beautification, modification and change of appearance, or correction of body odor and maintenance of good condition.

[0003] In the cosmetic production process, water-phase raw materials and oil-phase raw materials are often used. During production, these two raw materials are set with standard temperatures due to their different dissolution temperatures. In the existing process of dissolving the two raw materials, the solute and the solvent are evenly stirred and then heated at high temperature. This will cause the two raw materials to be incompatible when they are fused, and the heat is not fully utilized. In addition, the existing emulsification device uses heating to eliminate the air in the emulsion by evaporating the air inside the emulsion, which is inefficient and easily causes processing temperature redundancy, resulting in damage to the product molecular structure, resulting in roughness, lack of glossiness, and poor absorption rate of the cosmetics used in the later stage. Summary of the invention

[0004] In view of the deficiencies of the prior art, the present invention provides a system for producing cosmetic products, which solves the problems raised by the background art.

[0005] To achieve the above-mentioned purpose, the present invention provides the following technical solution: a system for producing cosmetic products, comprising a water-phase raw material processing system and an oil-phase raw material processing system, wherein the water-phase raw material processing system and the oil-phase raw material processing system are arranged opposite to each other, the bottoms of the water-phase raw material processing system and the oil-phase raw material processing system are connected with a connecting seat, the tops of the water-phase raw material processing system and the oil-phase raw material processing system are fixedly connected with a raw material supply system, the arc surface on the opposite side of the water-phase raw material processing system and the oil-phase raw material processing system are fixedly connected with a mounting plate, the opposite side of the two mounting plates is arranged in an arc shape, and the opposite side of the two mounting plates is fixedly connected with a temperature controller. Control circulation system, the bottom of the connecting seat is fixedly connected with an emulsification system, the bottom of the emulsification system is fixedly connected with an isolation plate, the isolation plate is used to isolate the heat generated by the emulsification system, the bottom of the isolation plate is fixedly connected with a cooling system, the inner cavity of the cooling system is connected with the inner cavity of the emulsification system, the front sides of the inner cavities of the water-phase raw material processing system and the oil-phase raw material processing system are both provided with a back-suction pump assembly, a mounting part is sleeved on the feed head, one side of the mounting part is fixedly connected to the surface of the water-phase raw material processing system, the top of the back-suction pump assembly is fixedly connected with an L-shaped feed head, and one end of the feed head is located above the water-phase raw material processing system.

[0006] In a system for producing cosmetic products described in the present invention, preferably, the water-phase raw material processing system includes a support block, the top of the support block is fixedly connected to a fixed seat, the top of the fixed seat is fixedly connected to a vertical sleeve support seat, the top of the vertical sleeve support seat is fixedly connected to a driving motor, the output end of the driving motor is fixedly connected to the top of the rotating rod, the output end of the driving motor is fixedly connected to a crushing knife assembly, one side of the vertical sleeve support seat is fixedly connected to a downwardly inclined material sleeve, the top of the downwardly inclined material sleeve is fixedly connected to an open sleeve, the top of the open sleeve is fixedly connected to a material receiving tank, the inner cavity of the material receiving tank is fixedly connected to a forward and reverse motor, the output end of the forward and reverse motor is fixedly connected to a plurality of material guiding and crushing plates, the plurality of material guiding and crushing plates are provided with built-in material guiding rings, the outer wall of the built-in material guiding ring is in contact with the inner wall of the material receiving tank.

[0007] Through the setting of the water-phase raw material processing system, when the output end of the forward and reverse motor drives multiple material guide and crushing plates to rotate, the built-in material guide ring on the material guide and crushing plate rotates. During the rotation of the material guide and crushing plate, the material guide and crushing plate can collide with the coarse particle raw material, so that the raw material is crushed under the impact, and then the crushed raw material falls from the receiving tank into the open sleeve, and contacts with the crushing knife assembly arranged inside the vertical sleeve support seat to form smaller particles, so that the raw material enters the water-phase raw material processing system or the oil-phase raw material processing system and remains in a finer state, which is convenient for rapid heating and helps the rapid dissolution of the raw material. In addition, during the use of the forward and reverse motor, the material guide and crushing plate rotates uninterruptedly in the forward and reverse directions, which also helps to quickly guide the raw material and smoothly feed the material.

[0008] In the system for producing cosmetic products described in the present invention, preferably, the water-phase raw material processing system has the same structure as the oil-phase raw material processing system, both comprising a pot body, a sealing plate fixedly connected to the top of the pot body, a material discharge chute is provided on the top of the sealing plate, a discharge port is provided at the bottom of the inner wall of the pot body, a rotating rod is axially arranged in the inner cavity of the pot body, and a plurality of dispersion plates are fixedly connected to the surface of the rotating rod.

[0009] Through the improvement of the water-phase raw material processing system and the oil-phase raw material processing system, under the action of the driving motor on the water-phase raw material processing system, the driving motor can drive the rotating rod in the pot body to rotate, and the dispersion plate on the rotating rod stirs the oil-phase raw materials and water-phase raw materials in the water-phase raw material processing system and the oil-phase raw material processing system respectively, so that the raw materials are stirred toward the periphery in the pot body, so that the raw materials are fully in contact with the inner wall of the pot body, so that the temperature control circulation system arranged on the surface of the water-phase raw material processing system and the oil-phase raw material processing system can generate heat contact, so as to ensure that the raw materials quickly reach the required temperature standard, which is conducive to the rapid seepage of the substances in the raw materials, thereby improving the efficiency of raw material extraction and effectively controlling the processing temperature.

[0010] In the system for producing cosmetic products described in the present invention, preferably, the temperature control circulation system includes an oil heating tank, the top of the oil heating tank is fixedly connected to a booster pump, a temperature control heater is arranged in the oil heating tank, one side of the oil heating tank is fixedly connected to a liquid inlet pipe, one end of the liquid inlet pipe is fixedly connected to a first-order temperature circulation pipe, the first-order temperature circulation pipe is sleeved on the water-phase raw material processing system, one end of the first-order temperature circulation pipe is fixedly connected to a delivery pipe, one end of the delivery pipe is fixedly connected to a second-order temperature circulation pipe, and the second-order temperature circulation pipe It is mounted on the oil phase raw material processing system, one end of the second-order temperature circulation pipe is connected to the inner cavity of the oil heating tank, and a one-way valve is provided at one end of the second-order temperature circulation pipe. The one-way valve allows the heat transfer oil to only enter but not exit. The second-order temperature circulation pipe and the first-order temperature circulation pipe have a spiral tube, and an annular oil path is provided in the spiral tube. The inner wall of the spiral tube is fixedly connected to a spiral heat-conducting ring, and the inner side of the spiral heat-conducting ring is located in the inner cavity of the pot body. The upper and lower sides of the spiral heat-conducting ring are fixedly connected to spiral fixing strips, and the spiral fixing strips are fixedly connected to the pot body.

[0011] By setting up the temperature control circulation system, the heat transfer oil in the oil heating tank can be heated to a specified temperature under the heating of the temperature control heater. Under normal circumstances, the suitable temperature of the oil phase raw material is 85 degrees. The temperature control heater heats the heat transfer oil to 90 degrees, so that the heat transfer oil enters the first-order temperature circulation tube. When the heat transfer oil enters the spiral tube, it circulates and flows upward in the spiral tube, and then the heat can enter the pot body, which can dissolve the oil phase raw material in the pot body. After the heat transfer oil that completes one cycle enters the second-order temperature circulation tube from the conveying pipe, due to the heat consumption at the water phase raw material processing system, when the heat transfer oil enters the oil phase raw material processing system, the temperature is controlled at 80 degrees, which is helpful for heating the water phase raw material. The heated heat transfer oil enters the oil heating tank, which can quickly dissolve the raw materials. Moreover, the single multi-cycle heating method can be used to simultaneously realize the heating operation of the water phase raw material processing system and the oil phase raw material processing system, and make full use of the heat without heating the water phase raw material processing system and the oil phase raw material processing system separately.

[0012] In a system for producing cosmetic products described in the present invention, preferably, the emulsification system includes an emulsification reaction kettle, control valves are arranged on the left and right sides of the top of the emulsification reaction kettle, the bottom of the emulsification reaction kettle is fixedly connected with a suction seat, a driving mechanism is arranged in the suction seat, two rotating shafts are arranged at the bottom of the inner wall of the emulsification reaction kettle, a mounting ring is sleeved on the rotating shaft, a stirring rod mounting seat is sleeved on the mounting ring, a stirring rod is fixedly connected to the top of the stirring rod mounting seat, a feeding conduit is fixedly connected to the bottom of the control valve, a pressure-dividing extrusion rod is sleeved in the feeding conduit, the bottom of the pressure-dividing extrusion rod is connected to the top of the rotating shaft The two parts are fixedly connected, and a tooth groove is provided on the outside of the two stirring rod mounting seats, and a tooth ring is meshed between the two stirring rod mounting seats, and a built-in plate is sleeved in the tooth ring, and an auxiliary stirring rod is fixedly connected to the top of the built-in plate, and a mounting groove is provided on the connecting seat, and a vacuum pump is arranged in the mounting groove, and a negative pressure sleeve is arranged below the vacuum pump, and side negative pressure rings are arranged on the left and right sides of the inner wall of the negative pressure sleeve, and an annular hollow plate is sleeved above the left and right inner cavities of the emulsification reactor, and a suction nozzle is arranged in a ring on the top of the annular hollow plate, and a middle negative pressure cotton ball is sleeved on the bottom of the inner wall of the negative pressure sleeve, and the driving mechanism drives the two rotating shafts to rotate.

[0013] Through the improvement of the emulsification system, during the process of dissolving the raw materials in the water-phase raw material processing system and the oil-phase raw material processing system, the control valve is always in a closed state, and the use of the vacuum pump can make the emulsification reactor in a negative pressure state. After the raw materials in the water-phase raw material processing system and the oil-phase raw material processing system are completely dissolved, the control valve is opened. Due to the negative pressure inside the emulsification reactor, the dissolved materials in the water-phase raw material processing system and the oil-phase raw material processing system can be sucked into the emulsification reactor, thereby achieving the purpose of feeding operation. When the dissolved materials enter the emulsification reactor, due to the vacuum The pump sucks the internal air to the outside, so that the emulsification reactor is gradually in a state of negative pressure. At this time, the driving mechanism drives the two rotating shafts to rotate, and the solution entering from the control valve falls in the space formed between the discharge conduit and the pressure-dividing extrusion rod. During the rotation, the internal bubbles can be compressed, and the bubbles inside the solution can be effectively squeezed out. The solution entering the emulsification reactor is slowly stirred by the stirring rod and the auxiliary stirring rod, so that the internal bubbles can flow fully, and then the bubbles generated in the solution can be fully sucked out, which can increase the solution's delicate feeling when supporting cosmetics, making the solution smoother in the later stage and easier to be absorbed by the skin.

[0014] In the system for producing cosmetic products described in the present invention, preferably, the cooling system includes a refrigeration device, a discharge port is provided in the middle of the refrigeration device, a cooling jacket is fixedly connected to the top of the refrigeration device, a plurality of annular cooling plates are sequentially sleeved in the cooling jacket, an annular discharge trough is provided between two adjacent annular cooling plates, and a circulating condensation chamber is provided in the annular cooling plate.

[0015] During the use of the cooling system, the control valve arranged in the emulsification reactor conveys the internal emulsified solution to the cooling system, and the solution is dispersed into a plurality of circular discharge troughs. The refrigeration device conveys the cold air to the circulating condensation chamber, so that the surface of the circular cooling plate is in a low temperature state. At this time, after the high-temperature emulsified liquid enters the circular discharge trough, it fully contacts the surface between the two circular cooling plates, so that the cooling effect is achieved during the rapid discharge of the emulsion, which neither affects the discharge speed nor the cooling effect, and the efficiency is greatly improved.

[0016] The present invention provides a system for producing cosmetic products. It has the following beneficial effects:

[0017] (1) Through the arrangement of the water-phase raw material processing system, when the output end of the forward and reverse motor drives multiple material guide and crushing plates to rotate, the built-in material guide ring on the material guide and crushing plate rotates. During the rotation of the material guide and crushing plate, the material guide and crushing plate can collide with the coarse particle raw material. In this way, the raw material is crushed under the impact, and then the crushed raw material falls from the receiving tank into the open sleeve, and contacts with the crushing knife assembly arranged inside the vertical sleeve support seat, so that it forms smaller particles. In this way, the raw material enters the water-phase raw material processing system or the oil-phase raw material processing system in a smaller state, which is convenient for rapid heating and helps the rapid dissolution of the raw material. In addition, during the use of the forward and reverse motor, the material guide and crushing plate rotates uninterruptedly in the forward and reverse directions, which also helps to quickly guide the raw material and smoothly feed the material.

[0018] (2) By improving the water-phase raw material processing system and the oil-phase raw material processing system, the driving motor on the water-phase raw material processing system can drive the rotating rod in the pot body to rotate, and the dispersion plate on the rotating rod stirs the oil-phase raw material and water-phase raw material in the water-phase raw material processing system and the oil-phase raw material processing system respectively, so that the raw materials are stirred toward the periphery in the pot body, so that the raw materials are fully in contact with the inner wall of the pot body, so that the temperature control circulation system arranged on the surface of the water-phase raw material processing system and the oil-phase raw material processing system can generate heat contact, so that the raw materials can quickly reach the required temperature standard, which is conducive to the rapid seepage of the substances in the raw materials, thereby increasing the efficiency of raw material extraction and effectively controlling the processing temperature.

[0019] (3) By setting up the temperature control circulation system, the heat transfer oil in the oil heating tank can be heated to a specified temperature under the heating of the temperature control heater. Under normal circumstances, the suitable temperature of the oil phase raw material is 85 degrees. The temperature control heater heats the heat transfer oil to 90 degrees, so that the heat transfer oil enters the first-order temperature circulation tube. When the heat transfer oil enters the spiral tube, it circulates and flows upward in the spiral tube, and then the heat can enter the pot body, which can dissolve the oil phase raw material in the pot body. After the heat transfer oil that has completed one cycle enters the second-order temperature circulation tube from the conveying pipe, due to the heat consumption in the water phase raw material processing system, when the heat transfer oil enters the oil phase raw material processing system, the temperature is controlled at 80 degrees, which is helpful for heating the water phase raw material. The heated heat transfer oil enters the oil heating tank, which can quickly dissolve the raw material. In addition, by adopting a single multi-cycle heating method, the water phase raw material processing system and the oil phase raw material processing system can be heated at the same time, and the heat is fully utilized without heating the water phase raw material processing system and the oil phase raw material processing system separately.

[0020] (4) Through the improvement of the emulsification system, during the process of dissolving the raw materials in the water-phase raw material processing system and the oil-phase raw material processing system, the control valve is always in a closed state. The use of the vacuum pump can make the emulsification reactor in a negative pressure state. After the raw materials in the water-phase raw material processing system and the oil-phase raw material processing system are completely dissolved, the control valve is opened. Due to the negative pressure inside the emulsification reactor, the dissolved materials in the water-phase raw material processing system and the oil-phase raw material processing system can be sucked into the emulsification reactor, thereby achieving the purpose of feeding operation. When the dissolved materials enter the emulsification reactor, they are The vacuum pump sucks the internal air to the outside, so that the emulsification reactor is gradually in a state of negative pressure. At this time, the driving mechanism drives the two rotating shafts to rotate, and the solution entering from the control valve falls in the space formed between the discharge conduit and the pressure-dividing extrusion rod. During the rotation, the internal bubbles can be compressed, and the bubbles inside the solution can be effectively squeezed out. The solution entering the emulsification reactor is slowly stirred by the stirring rod and the auxiliary stirring rod, so that the internal bubbles can flow fully, and then the bubbles generated in the solution can be fully sucked, which can increase the solution's delicate feeling when supporting cosmetics, making the solution smoother in the later stage and easier to be absorbed by the skin.

[0021] (5) During the use of the cooling system, the control valve set in the emulsification reactor transports the internal emulsified solution to the cooling system, and the solution is dispersed into multiple circular feed troughs. The refrigeration device transports cold air to the circulating condensation chamber, so that the surface of the circular cooling plate is in a low temperature state. At this time, after the high-temperature emulsified liquid enters the circular feed trough, it fully contacts the surface between the two circular cooling plates, so that the cooling effect is achieved during the rapid discharge of the emulsion, which does not affect the discharge speed or the cooling effect, and the efficiency is greatly improved. BRIEF DESCRIPTION OF THE DRAWINGS

[0022] Figure 1 A schematic diagram of a system for producing cosmetic products according to the present invention;

[0023] Figure 2 It is a structural schematic diagram of a system for producing cosmetic products according to the present invention;

[0024] Figure 3 A schematic diagram of an oil phase raw material processing system in a system structure for producing cosmetic products according to the present invention;

[0025] Figure 4 A schematic diagram of an emulsifying system in a system structure for producing cosmetic products according to the present invention;

[0026] Figure 5The present invention is a schematic diagram of a cooling system in a system structure for producing cosmetic products.

[0027] In the figure: water phase raw material processing system 1, oil phase raw material processing system 2, raw material supply system 3, temperature control circulation system 4, mounting plate 5, connecting seat 6, emulsification system 7, isolation plate 8, cooling system 9, pot body 10, cover plate 11, material discharge chute 12, rotating rod 13, dispersion plate 14, discharge port 15, oil heating tank 16, booster pump 17, second-order temperature circulation pipe 18, first-order temperature circulation pipe 19, liquid inlet pipe 20, conveying pipe 21, spiral pipe 22, spiral fixing strip 23, spiral heat conduction ring 24, annular oil circuit 25, support block 26, fixing seat 27, vertical sleeve support seat 28, drive motor 29, oblique downward material sleeve 30, open sleeve 3 1. Material receiving tank 32, forward and reverse motor 33, back-suction pump assembly 34, material discharge head 35, built-in material guide ring 36, material guide crushing plate 37, mounting part 38, emulsification reactor 39, suction seat 40, mounting groove 41, vacuum pump 42, control valve 43, negative pressure sleeve 44, side negative pressure ring 45, middle negative pressure cotton ball 46, annular hollow plate 47, suction nozzle 48, material discharge conduit 49, pressure dividing extrusion rod 50, stirring rod 51, rotating shaft 52, mounting ring 53, stirring rod mounting seat 54, gear ring 55, auxiliary stirring rod 56, built-in plate 57, cooling sleeve 58, ring-shaped cooling plate 59, ring-shaped material discharge chute 60, refrigeration device 61, and material discharge port 62. DETAILED DESCRIPTION

[0028] The following will be combined with the drawings in the embodiments of the present invention to clearly and completely describe the technical solutions in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.

[0029] like Figure 1-5As shown, the present invention provides a technical solution: a system for producing cosmetic products, comprising a water-phase raw material processing system 1 and an oil-phase raw material processing system 2, the water-phase raw material processing system 1 and the oil-phase raw material processing system 2 are arranged opposite to each other, the bottoms of the water-phase raw material processing system 1 and the oil-phase raw material processing system 2 are connected with a connecting seat 6, the tops of the water-phase raw material processing system 1 and the oil-phase raw material processing system 2 are fixedly connected with a raw material supply system 3, the arc surface on the opposite side of the water-phase raw material processing system 1 and the oil-phase raw material processing system 2 is fixedly connected with a mounting plate 5, the opposite side of the two mounting plates 5 is arranged in an arc shape, and the opposite side of the two mounting plates 5 is fixedly connected with a temperature control circulation system 4 The bottom of the connecting seat 6 is fixedly connected to the emulsification system 7, and the bottom of the emulsification system 7 is fixedly connected to the isolation plate 8, which is used to isolate the heat generated by the emulsification system 7. The bottom of the isolation plate 8 is fixedly connected to the cooling system 9, and the inner cavity of the cooling system 9 is connected to the inner cavity of the emulsification system 7. A back-suction pump assembly 34 is provided on the front side of the inner cavity of the water-phase raw material processing system 1 and the oil-phase raw material processing system 2. A mounting member 38 is sleeved on the discharge head 35, and one side of the mounting member 38 is fixedly connected to the surface of the water-phase raw material processing system 1. The top of the back-suction pump assembly 34 is fixedly connected to an L-shaped discharge head 35, and one end of the discharge head 35 is located above the water-phase raw material processing system 1.

[0030] The aqueous phase raw material processing system 1 includes a support block 26, the top of the support block 26 is fixedly connected to a fixed seat 27, the top of the fixed seat 27 is fixedly connected to a vertical sleeve support seat 28, the top of the vertical sleeve support seat 28 is fixedly connected to a drive motor 29, the output end of the drive motor 29 is fixedly connected to the top of the rotating rod 13, the output end of the drive motor 29 is fixedly connected to a crushing knife assembly, one side of the vertical sleeve support seat 28 is fixedly connected to a downwardly inclined material sleeve 30, the top of the downwardly inclined material sleeve 30 is fixedly connected to an open sleeve 31, the top of the open sleeve 31 is fixedly connected to a material receiving tank 32, the inner cavity of the material receiving tank 32 is fixedly connected to a forward and reverse motor 33, the output end of the forward and reverse motor 33 is fixedly connected to a plurality of material guiding and crushing plates 37, the plurality of material guiding and crushing plates 37 are sleeved with built-in material guiding rings 36, and the outer wall of the built-in material guiding ring 36 is in contact with the inner wall of the material receiving tank 32.

[0031] Through the setting of the water-phase raw material processing system 1, when the output end of the forward and reverse motor 33 drives multiple material guide and crushing plates 37 to rotate, the built-in material guide ring 36 on the material guide and crushing plate 37 rotates. During the rotation of the material guide and crushing plate 37, the material guide and crushing plate 37 can collide with the coarse particle raw material, so that the raw material is crushed under the impact, and then the crushed raw material falls from the receiving tank 32 to the open sleeve 31, and contacts with the crushing knife assembly arranged inside the vertical sleeve support seat 28 to form smaller particles, so that the raw material enters the water-phase raw material processing system 1 or the oil-phase raw material processing system 2 and remains in a smaller state, which is convenient for rapid heating and helps the rapid dissolution of the raw material. In addition, during the use of the forward and reverse motor 33, the material guide and crushing plate 37 rotates uninterruptedly in the forward and reverse directions, which also helps to quickly guide the raw material and smoothly feed the material.

[0032] The water-phase raw material processing system 1 has the same structure as the oil-phase raw material processing system 2, and both include a pot body 10, a sealing plate 11 is fixedly connected to the top of the pot body 10, a material discharge chute 12 is provided on the top of the sealing plate 11, a discharge port 15 is provided on the bottom of the inner wall of the pot body 10, a rotating rod 13 is axially arranged in the inner cavity of the pot body 10, and a plurality of dispersion plates 14 are fixedly connected to the surface of the rotating rod 13.

[0033] By improving the water-phase raw material processing system 1 and the oil-phase raw material processing system 2, the driving motor 29 on the water-phase raw material processing system 1 can drive the rotating rod 13 in the pot body 10 to rotate, and the dispersion plate 14 on the rotating rod 13 stirs the oil-phase raw materials and water-phase raw materials in the water-phase raw material processing system 1 and the oil-phase raw material processing system 2 respectively, so that the raw materials are stirred toward the periphery in the pot body 10, so that the raw materials are fully in contact with the inner wall of the pot body 10, so that the temperature control circulation system 4 arranged on the surface of the water-phase raw material processing system 1 and the oil-phase raw material processing system 2 can generate heat contact, so that the raw materials can quickly reach the required temperature standard, which is conducive to the rapid seepage of the substances in the raw materials, thereby increasing the efficiency of raw material extraction and effectively controlling the processing temperature.

[0034] The temperature control circulation system 4 includes an oil heating tank 16, the top of the oil heating tank 16 is fixedly connected to a booster pump 17, a temperature control heater is arranged in the oil heating tank 16, one side of the oil heating tank 16 is fixedly connected to a liquid inlet pipe 20, one end of the liquid inlet pipe 20 is fixedly connected to a first-order temperature circulation pipe 19, the first-order temperature circulation pipe 19 is sleeved on the water phase raw material processing system 1, one end of the first-order temperature circulation pipe 19 is fixedly connected to a delivery pipe 21, one end of the delivery pipe 21 is fixedly connected to a second-order temperature circulation pipe 18, the second-order temperature circulation pipe 18 is sleeved on the oil phase raw material processing system 2 One end of the second-order temperature circulation pipe 18 is connected to the inner cavity of the oil heating tank 16. A one-way valve is provided at one end of the second-order temperature circulation pipe 18. The one-way valve allows the heat transfer oil to only enter but not exit. The second-order temperature circulation pipe 18 and the first-order temperature circulation pipe 19 have a spiral pipe 22. An annular oil path 25 is provided in the spiral pipe 22. The inner wall of the spiral pipe 22 is fixedly connected to a spiral heat-conducting ring 24. The inner side of the spiral heat-conducting ring 24 is located in the inner cavity of the pot body 10. The upper and lower sides of the spiral heat-conducting ring 24 are fixedly connected with spiral fixing strips 23, and the spiral fixing strips 23 are fixedly connected to the pot body 10.

[0035] By setting the temperature control circulation system 4, the heat transfer oil in the oil heating tank 16 can be heated to a specified temperature under the heating of the temperature control heater. Under normal circumstances, the suitable temperature of the oil phase raw material is 85 degrees. The temperature control heater heats the heat transfer oil to 90 degrees, so that the heat transfer oil enters the first-stage temperature circulation pipe 19. When the heat transfer oil enters the spiral pipe 22, it circulates upward in the spiral pipe 22, and then the heat can enter the pot body 10, which can dissolve the oil phase raw material in the pot body 10. The heat transfer oil that completes one cycle enters the second stage temperature circulation pipe from the delivery pipe 21. After entering the temperature circulation pipe 18, due to the consumption of heat in the water-phase raw material processing system 1, when the heat transfer oil enters the oil-phase raw material processing system 2, the temperature is controlled at 80 degrees, which is helpful to heat the water-phase raw material. The heated heat transfer oil enters the oil heating tank 16, which can make the raw material dissolve quickly. In addition, a single-time multi-cycle heating method is adopted, which can realize the heating operation of the water-phase raw material processing system 1 and the oil-phase raw material processing system 2 at the same time, and make full use of the heat. There is no need to heat the water-phase raw material processing system 1 and the oil-phase raw material processing system 2 separately.

[0036] The emulsification system 7 includes an emulsification reaction kettle 39, and control valves 43 are arranged on both sides of the top of the emulsification reaction kettle 39. The bottom of the emulsification reaction kettle 39 is fixedly connected with a suction seat 40, and a driving mechanism is arranged in the suction seat 40. Two rotating shafts 52 are arranged at the bottom of the inner wall of the emulsification reaction kettle 39, and a mounting ring 53 is sleeved on the rotating shaft 52. A stirring rod mounting seat 54 is sleeved on the mounting ring 53, and a stirring rod 51 is fixedly connected to the top of the stirring rod mounting seat 54. The bottom of the control valve 43 is fixedly connected with a feeding conduit 49, and a pressure-dividing extrusion rod 50 is sleeved in the feeding conduit 49. The bottom of the pressure-dividing extrusion rod 50 is fixedly connected to the top of the rotating shaft 52. The two stirring rod mounting seats A tooth groove is provided on the outside of 54, and a tooth ring 55 is meshed between the two stirring rod mounting seats 54. An internal plate 57 is sleeved inside the tooth ring 55, and an auxiliary stirring rod 56 is fixedly connected to the top of the internal plate 57. A mounting groove 41 is provided on the connecting seat 6, and a vacuum pump 42 is arranged in the mounting groove 41. A negative pressure sleeve 44 is arranged below the vacuum pump 42, and side negative pressure rings 45 are arranged on the left and right sides of the inner wall of the negative pressure sleeve 44. An annular hollow plate 47 is sleeved above the left and right inner cavities of the emulsification reactor 39, and a suction nozzle 48 is arranged in a ring on the top of the annular hollow plate 47. A middle negative pressure cotton ball 46 is sleeved on the bottom of the inner wall of the negative pressure sleeve 44, and a driving mechanism drives the two rotating shafts 52 to rotate.

[0037] By improving the emulsification system 7, during the dissolution of the raw materials in the water-phase raw material processing system 1 and the oil-phase raw material processing system 2, the control valve 43 is always in a closed state, and the use of the vacuum pump 42 can make the emulsification reactor 39 in a negative pressure state. After the raw materials in the water-phase raw material processing system 1 and the oil-phase raw material processing system 2 are completely dissolved, the control valve 43 is opened. Due to the negative pressure inside the emulsification reactor 39, the dissolved materials in the water-phase raw material processing system 1 and the oil-phase raw material processing system 2 can be sucked into the emulsification reactor 39, thereby achieving the purpose of the feeding operation. When the dissolved materials enter the emulsification reactor 39, due to the vacuum pump 42, the control valve 43 is opened. The air pump 42 sucks the internal air to the outside, so that the emulsification reaction kettle 39 is gradually in a negative pressure state. At this time, the driving mechanism drives the two rotating shafts 52 to rotate, and the solution entering from the control valve 43 into 499 falls in the space formed between the discharge conduit 49 and the pressure-dividing extrusion rod 50. During the rotation, the internal bubbles can be compressed and the bubbles in the solution can be effectively squeezed out. The solution entering the emulsification reaction kettle 39 is slowly stirred by the stirring rod 51 and the auxiliary stirring rod 56, so that the internal bubbles flow fully, and then the bubbles generated in the solution can be fully sucked, which can increase the solution's delicate feeling when supporting cosmetics, making the solution smoother in the later stage and easier to be absorbed by the skin.

[0038] The cooling system 9 includes a refrigeration device 61, a discharge port 62 is arranged in the middle of the refrigeration device 61, a cooling jacket 58 is fixedly connected to the top of the refrigeration device 61, a plurality of annular cooling plates 59 are sequentially arranged in the cooling jacket 58, an annular discharge trough 60 is arranged between two adjacent annular cooling plates 59, and a circulating condensation chamber is arranged in the annular cooling plate 59.

[0039] During the use of the cooling system 9, the control valve arranged in the emulsification reactor 39 transports the internal emulsified solution to the cooling system 9, and the solution is dispersed into a plurality of circular discharge troughs 60. The refrigeration device 61 transports cold air to the circulating condensation chamber, so that the surface of the circular cooling plate 59 is in a low-temperature state. At this time, after the high-temperature emulsified liquid enters the circular discharge trough 60, it fully contacts the surface between the two circular cooling plates 59, so that the cooling effect is achieved during the rapid discharge of the emulsion, which neither affects the discharge speed nor the cooling effect, and the efficiency is greatly improved.

[0040] It should be noted that, in this article, relational terms such as first and second, etc. are only used to distinguish one entity or operation from another entity or operation, and do not necessarily require or imply any such actual relationship or order between these entities or operations. Moreover, the terms "include", "comprise" or any other variants thereof are intended to cover non-exclusive inclusion, so that a process, method, article or device including a series of elements includes not only those elements, but also other elements not explicitly listed, or also includes elements inherent to such process, method, article or device. In the absence of further restrictions, the elements defined by the statement "comprising a reference structure" do not exclude the existence of other identical elements in the process, method, article or device including the elements.

[0041] Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions and variations may be made to the embodiments without departing from the principles and spirit of the present invention, and that the scope of the present invention is defined by the appended claims and their equivalents.

Claims

1. A system for producing a cosmetic product, characterized in that The invention comprises a water-phase raw material processing system (1) and an oil-phase raw material processing system (2), wherein the water-phase raw material processing system (1) and the oil-phase raw material processing system (2) are arranged opposite to each other, the bottoms of the water-phase raw material processing system (1) and the oil-phase raw material processing system (2) are connected to a connecting seat (6), the tops of the water-phase raw material processing system (1) and the oil-phase raw material processing system (2) are fixedly connected to a raw material supply system (3), the arc-shaped surfaces on the opposite sides of the water-phase raw material processing system (1) and the oil-phase raw material processing system (2) are fixedly connected to mounting plates (5), the opposite sides of the two mounting plates (5) are arranged in an arc shape, the opposite sides of the two mounting plates (5) are fixedly connected to a temperature control circulation system (4), and the bottom of the connecting seat (6) is fixedly connected to an emulsification system (7) The bottom of the emulsification system (7) is fixedly connected to an isolation plate (8), and the isolation plate (8) is used to isolate the heat generated by the emulsification system (7). The bottom of the isolation plate (8) is fixedly connected to a cooling system (9), and the inner cavity of the cooling system (9) is connected to the inner cavity of the emulsification system (7). The front sides of the inner cavities of the water-phase raw material processing system (1) and the oil-phase raw material processing system (2) are both provided with a back-suction pump assembly (34), and the top of the back-suction pump assembly (34) is fixedly connected to an L-shaped feed head (35), one end of the feed head (35) is located above the water-phase raw material processing system (1), and a mounting member (38) is sleeved on the feed head (35), and one side of the mounting member (38) is fixedly connected to the surface of the water-phase raw material processing system (1); The aqueous raw material processing system (1) comprises a support block (26), the top of the support block (26) is fixedly connected to a fixed seat (27), the top of the fixed seat (27) is fixedly connected to a vertical sleeve support seat (28), the top of the vertical sleeve support seat (28) is fixedly connected to a drive motor (29), the output end of the drive motor (29) is fixedly connected to a crushing knife assembly, one side of the vertical sleeve support seat (28) is fixedly connected to a downwardly inclined material sleeve (30), the top of the downwardly inclined material sleeve (30) is fixedly connected to an open sleeve (31), the top of the open sleeve (31) is fixedly connected to a material receiving tank (32), the inner cavity of the material receiving tank (32) is fixedly connected to a forward and reverse motor (33), the output end of the forward and reverse motor (33) is fixedly connected to a plurality of material guide and crushing plates (37), the plurality of material guide and crushing plates (37) are sleeved with an internal material guide ring (36), the outer wall of the internal material guide ring (36) is in contact with the inner wall of the material receiving tank (32); By setting the aqueous raw material processing system (1), when the output end of the forward and reverse motor (33) drives the plurality of material guide and crushing plates (37) to rotate, the built-in material guide ring (36) on the material guide and crushing plates (37) rotates. During the rotation of the material guide and crushing plates (37), the material guide and crushing plates (37) can collide with the coarse particle raw material, and the raw material is crushed under the collision. Then, the crushed raw material falls from the material receiving tank (32) into the open sleeve (31), and contacts the crushing knife assembly provided inside the vertical sleeve support seat (28), so that the raw material is formed into smaller particles. The water-phase raw material processing system (1) and the oil-phase raw material processing system (2) have the same structure, both comprising a pot body (10), a sealing plate (11) being fixedly connected to the top of the pot body (10), a material discharge chute (12) being provided on the top of the sealing plate (11), a material discharge port (15) being provided on the bottom of the inner wall of the pot body (10), a rotating rod (13) being axially arranged in the inner cavity of the pot body (10), a plurality of dispersion plates (14) being fixedly connected to the surface of the rotating rod (13), and an output end of the driving motor (29) being fixedly connected to the top of the rotating rod (13); The temperature control circulation system (4) comprises an oil heating tank (16), the top of the oil heating tank (16) is fixedly connected to a booster pump (17), a temperature control heater is arranged in the oil heating tank (16), one side of the oil heating tank (16) is fixedly connected to a liquid inlet pipe (20), one end of the liquid inlet pipe (20) is fixedly connected to a first-order temperature circulation pipe (19), the first-order temperature circulation pipe (19) is sleeved on the water-phase raw material processing system (1), one end of the first-order temperature circulation pipe (19) is fixedly connected to a delivery pipe (21), one end of the delivery pipe (21) is fixedly connected to a second-order temperature circulation pipe (18), the second-order temperature circulation pipe (18) is sleeved on the oil-phase raw material processing system (2 ), one end of the second-order temperature circulation tube (18) is connected to the inner cavity of the oil heating tank (16), one end of the second-order temperature circulation tube (18) is provided with a one-way valve, and the one-way valve allows the heat transfer oil to only enter but not exit, the second-order temperature circulation tube (18) and the first-order temperature circulation tube (19) have a spiral tube (22), an annular oil path (25) is provided in the spiral tube (22), the inner wall of the spiral tube (22) is fixedly connected to a spiral heat transfer ring (24), the inner side of the spiral heat transfer ring (24) is located in the inner cavity of the pot body (10), and the upper and lower sides of the spiral heat transfer ring (24) are fixedly connected to spiral fixing strips (23), and the spiral fixing strips (23) are fixedly connected to the pot body (10); The emulsification system (7) comprises an emulsification reaction kettle (39), wherein control valves (43) are arranged on both left and right sides of the top of the emulsification reaction kettle (39), the bottom of the emulsification reaction kettle (39) is fixedly connected to a suction seat (40), a driving mechanism is arranged in the suction seat (40), two rotating shafts (52) are arranged at the bottom of the inner wall of the emulsification reaction kettle (39), a mounting ring (53) is sleeved on the rotating shaft (52), a stirring rod mounting seat (54) is sleeved on the mounting ring (53), a stirring rod (51) is fixedly connected to the top of the stirring rod mounting seat (54), a feeding conduit (49) is fixedly connected to the bottom of the control valve (43), a pressure dividing extrusion rod (50) is sleeved in the feeding conduit (49), the bottom of the pressure dividing extrusion rod (50) is fixedly connected to the top of the rotating shaft (52), and the two stirring rod mounting seats A tooth groove is provided on the outside of (54), and a tooth ring (55) is meshed between the two stirring rod mounting seats (54). An internal plate (57) is sleeved inside the tooth ring (55), and an auxiliary stirring rod (56) is fixedly connected to the top of the internal plate (57). A mounting groove (41) is provided on the connecting seat (6), and a vacuum pump (42) is arranged in the mounting groove (41). A negative pressure sleeve (44) is arranged below the vacuum pump (42), and side negative pressure rings (45) are arranged on the left and right sides of the inner wall of the negative pressure sleeve (44). An annular hollow plate (47) is sleeved above the left and right inner cavities of the emulsification reactor (39), and a suction nozzle (48) is arranged in an annular shape on the top of the annular hollow plate (47). A middle negative pressure cotton ball (46) is sleeved on the bottom of the inner wall of the negative pressure sleeve (44), and the driving mechanism drives the two rotating shafts (52) to rotate.

2. A system for producing cosmetic products according to claim 1, characterized in that: The cooling system (9) comprises a refrigeration device (61), a discharge port (62) is arranged in the middle of the refrigeration device (61), a cooling jacket (58) is fixedly connected to the top of the refrigeration device (61), a plurality of ring-shaped cooling plates (59) are sequentially arranged in the cooling jacket (58), a ring-shaped discharge trough (60) is arranged between two adjacent ring-shaped cooling plates (59), and a circulating condensation chamber is arranged in the ring-shaped cooling plate (59).

Images