Ingredient production equipment

Abstract

The present invention provides a batching production device, which relates to the technical field of cosmetics. The batching production device includes an emulsifier and at least two batching systems, and the at least two batching systems are respectively connected to the emulsifier; a weighing device is respectively provided at the material outlet of each batching system, and the weighing device is used to weigh the material, and the weighed material can be transported to the emulsifier, so as to alleviate the technical problems in the prior art that a large amount of manpower and material resources are consumed when producing cosmetics, and the ratio accuracy of the materials is low, resulting in low quality of the finished product.

Description

Technical Field

[0001] The invention relates to the technical field of cosmetics, and in particular to a batching production device. Background Art

[0002] In traditional cosmetic production, the batcher needs to go to the raw material warehouse to collect the raw materials according to the formula requirements, weigh them according to the formula dosage under the supervision of the reviewer, record the raw material batching information, place the prepared materials in the emulsification area, and return the excess materials to the warehouse. The emulsifier feeds the prepared materials according to the production process, operates the emulsification equipment under the supervision of the reviewer, and can record the production process in time. However, this method requires a lot of manpower and material resources during the production process, and the accuracy of the material ratio is low, so the quality of the finished product is difficult to guarantee.

[0003] In view of this, there is an urgent need for a batching production device that can solve the above problems.

[0004] The information disclosed in this background technology section is only intended to deepen the understanding of the overall background technology of the present invention, and should not be regarded as acknowledging or suggesting in any form that the information constitutes the prior art already known to those skilled in the art. Summary of the invention

[0005] The present invention provides a batching production device to alleviate the technical problems in the prior art that a large amount of manpower and material resources are consumed in the production of cosmetics, and the ratio accuracy of materials is low, resulting in low quality of finished products.

[0006] In order to achieve the above object, the present invention adopts the following technical solutions:

[0007] The present invention provides a batching production device, comprising an emulsifier and at least two batching systems, wherein the at least two batching systems are respectively connected to the emulsifier;

[0008] A weighing device is respectively arranged at the discharge port of each batching system, and the weighing device is used to weigh the material, and the weighed material can be conveyed to the emulsifier.

[0009] In any of the above technical solutions, further, the batching system includes at least one storage tank, the discharge port of the storage tank is connected to the feed port of the emulsifier, and a flow meter is provided at the discharge port of the storage tank.

[0010] In any of the above technical solutions, further, the batching system also includes a material phase pot, the feed port of the material phase pot is connected to the discharge port of the storage tank, the discharge port of the material phase pot is connected to the feed port of the emulsifier, and the weighing device is arranged at the discharge port of the material phase pot.

[0011] In any of the above technical solutions, further, a pump is provided on the passage connecting the material storage tank and the material phase pot, and the pump is used to transport the material in the material storage tank to the material phase pot.

[0012] In any of the above technical solutions, further, when there are multiple storage tanks, the multiple storage tanks are arranged in parallel;

[0013] The batching system further comprises a manifold, the discharge ports of the plurality of storage tanks are respectively connected to the manifold, and the output port of the manifold is connected to the feed port of the material phase pot.

[0014] In any of the above technical solutions, further, the ingredient production device also includes a hot water tank, and the hot water tank is connected to the input port of the manifold.

[0015] In any of the above technical solutions, further, a valve is provided at the discharge port of the storage tank, and the valve is used to open or close the storage tank.

[0016] In any of the above technical solutions, further, the emulsifier has a material storage chamber, and the material outlet of the batching system is connected to the material storage chamber;

[0017] The material storage cavity is provided with a jacket layer, and the jacket layer can be filled with a coolant, and the coolant is used to cool the material in the material storage cavity.

[0018] In any of the above technical solutions, further, a filter screen is detachably connected to the discharge port of the emulsifier.

[0019] In any of the above technical solutions, further, the number of the batching systems is two groups, and the two groups of the batching systems include a water system and an oil system respectively;

[0020] The weighing device arranged in the water material system is a first weighing device, and the first weighing device is arranged at the discharge port of the water material system; the weighing device arranged in the oil material system is a second weighing device, and the second weighing device is arranged at the discharge port of the oil material system.

[0021] The beneficial effects of the present invention are:

[0022] The present invention provides a batching production device, including an emulsifier and at least two batching systems, and at least two batching systems are respectively connected to the emulsifier. A weighing device is respectively provided at the discharge port of each batching system, and the materials in the batching system are weighed by the weighing device and then transported to the emulsifier. Compared with the prior art, which requires the batcher to weigh first, then the reviewer to review, the emulsifier to find the materials, and then to add the materials, the batching production device directly weighs the materials through the weighing device, which is easy to operate and saves manpower and material resources. At the same time, when weighing by the weighing device, the weighing accuracy is easy to control, thereby improving the quality of the finished product. BRIEF DESCRIPTION OF THE DRAWINGS

[0023] In order to more clearly illustrate the specific implementation methods of the present invention or the technical solutions in the prior art, the drawings required for use in the specific implementation methods or the description of the prior art will be briefly introduced below. Obviously, the drawings described below are some implementation methods of the present invention. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying creative work.

[0024] Figure 1 A schematic diagram of a process flow of a batching production device provided in an embodiment of the present invention.

[0025] Icons: 10 - emulsifier; 21 - water system; 22 - oil system; 31 - first hot water tank; 32 - second hot water tank; 41 - connecting pipe; 42 - third pump; 50 - control unit; 211 - first weighing device; 212 - water tank; 213 - first flow meter; 214 - water phase pot; 215 - first pump; 216 - first valve; 217 - first manifold; 218 - third valve; 221 - second weighing device; 222 - oil tank; 223 - second flow meter; 224 - oil phase pot; 225 - second pump; 226 - second valve; 227 - second manifold; 228 - fourth valve. DETAILED DESCRIPTION

[0026] The technical solution of the present invention will be described clearly and completely below in conjunction with the accompanying drawings. 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.

[0027] In the description of the present invention, it should be noted that the terms “first” and “second” are only used for descriptive purposes and cannot be understood as indicating or implying relative importance.

[0028] In the description of the present invention, it should be noted that, unless otherwise clearly specified and limited, the terms "installed", "connected", and "connected" should be understood in a broad sense, for example, it can be a fixed connection, a detachable connection, or an integral connection; it can be a mechanical connection or an electrical connection; it can be a direct connection, or it can be indirectly connected through an intermediate medium, or it can be the internal communication of two components. For ordinary technicians in this field, the specific meanings of the above terms in the present invention can be understood according to specific circumstances.

[0029] like Figure 1 As shown, the batching production device provided in this embodiment includes an emulsifier 10 and at least two batching systems, and the at least two batching systems are respectively connected to the emulsifier 10; a weighing device is respectively provided at the discharge port of each batching system, and the weighing device is used to weigh the material, and the weighed material can be transported to the emulsifier 10.

[0030] Specifically, multiple batching systems are provided, and the multiple batching systems are arranged in parallel and respectively connected to the emulsifier 10, and the materials in each batching system can be respectively transported to the emulsifier 10 for emulsification operation. Each batching system can be used to store different materials, or each batching system can be used to store the same materials, as long as the materials stored in the batching system can be transported to the emulsifier 10 for emulsification operation.

[0031] In actual use, a weighing device is provided at the discharge port of each batching system, that is to say, when the batching system conveys materials into the emulsifier 10, the materials output from the batching system can be weighed by the weighing device before being added to the emulsifier 10. Compared with the prior art, which requires the batcher to weigh, the reviewer to review, the emulsifier to find materials, and the emulsifier to add materials, the weighing device can directly weigh the materials output by the batching system, and the operation is simple. Only one weighing is required to reach the set material quantity, and there is no need for at least two staff members to weigh, thereby saving manpower and material resources. At the same time, when the materials are weighed by the weighing device, the weighing accuracy is easy to control, so the weighing accuracy is high to improve the quality of the finished product.

[0032] Among them, the weighing device adopts electronic weighing, which is easy to control and has higher weighing accuracy.

[0033] It should be added that the multiple batching systems can also be arranged in series, or several batching systems can be arranged in series and other batching systems can be arranged in parallel, or the multiple batching systems can have both series and parallel arrangements. Regardless of how the multiple batching systems are arranged, as long as a weighing device is arranged at the material outlet of each batching system, the material can be added to the emulsifier 10 in a certain amount.

[0034] Please continue to refer to Figure 1Preferably, there are two batching systems, and the two batching systems respectively include a water system 21 and an oil system 22; the weighing device arranged in the water system 21 is a first weighing device 211, and the first weighing device 211 is arranged at the discharge port of the water system 21; the weighing device arranged in the oil system 22 is a second weighing device 221, and the second weighing device 221 is arranged at the discharge port of the oil system 22.

[0035] Taking the application of the batching production device in the field of cosmetics production as an example, in this embodiment, the number of batching systems is two groups, and the two groups of batching systems are respectively a water system 21 and an oil system 22. The water system 21 is used to transport water phase materials, and the oil system 22 is used to transport oil phase materials. A first weighing device 211 is provided at the discharge port of the water system 21, and the first weighing device 211 is used to weigh the water phase materials transported by the water system 21, so as to control the amount of the water phase materials transported by the water system 21 to the emulsifier 10. A second weighing device 221 is provided at the discharge port of the oil system 22, and the second weighing device 221 is used to weigh the oil phase materials transported by the oil system 22, so as to control the amount of the oil phase materials transported by the oil system 22 to the emulsifier 10. By controlling the amount of materials output by the water system 21 and the oil system 22 respectively, it is ensured that the materials delivered to the emulsifier 10 are controlled within a certain range, thereby improving the quality of the product emulsified by the emulsifier 10.

[0036] Please continue to refer to Figure 1 Preferably, the water system 21 includes at least one water tank 212, the outlet of the water tank 212 is connected to the feed inlet of the emulsifier 10, and a first flow meter 213 is provided at the outlet of the water tank 212. The oil system 22 includes at least one oil tank 222, the outlet of the oil tank 222 is connected to the feed inlet of the emulsifier 10, and a second flow meter 223 is provided at the outlet of the oil tank 222.

[0037] Among them, the water tank 212 is used to store water-phase raw materials, and the oil tank 222 is used to store oil-phase raw materials. When there are multiple water tanks 212, multiple water tanks 212 are arranged in parallel, and a first flow meter 213 is respectively arranged at the outlet of each water tank 212. The first flow meter 213 is used to control the amount of water-phase raw materials output through the water tank 212, that is, the first flow meter 213 can make the water-phase raw materials output from the water tank 212 to the emulsifier 10 at a set value. At the same time, there are multiple oil tanks 222, and multiple oil tanks 222 are arranged in parallel. A second flow meter 223 is respectively arranged at the outlet of each oil tank 222. The second flow meter 223 is used to control the amount of oil-phase raw materials output through the oil tank 222, so that the oil-phase raw materials input from the oil tank 222 to the emulsifier 10 are at a set value.

[0038] The amount of the water phase raw material delivered from the water tank 212 is controlled by the first flow meter 213, and then it is weighed twice by the first weighing device 211. The amount of the oil phase raw material delivered from the oil tank 222 is controlled by the second flow meter 223, and then it is weighed twice by the second weighing device 221, thereby ensuring that the water phase material and the oil phase material delivered to the emulsifier 10 are within the set values, thereby improving the quality of the product.

[0039] In this embodiment, two water tanks 212 are provided, and the two water tanks 212 are arranged in parallel; two oil tanks 222 are also provided, and the two oil tanks 222 are arranged in parallel.

[0040] It should be added that when there are multiple water tanks 212, the multiple water tanks 212 can also be arranged in series, or the multiple water tanks 212 can be arranged in series and in parallel at the same time. When there are multiple oil tanks 222, the multiple oil tanks 222 can also be arranged in series, or in series and in parallel at the same time. It only needs to ensure that the water phase material and the oil phase material delivered to the emulsifier 10 are within the set values.

[0041] Please continue to refer to Figure 1 Preferably, the water material system 21 further includes a water phase pot 214, and the feed port of the water phase pot 214 is connected to the discharge port of the water material tank 212, and the first weighing device 211 is arranged at the discharge port of the water phase pot 214. The oil material system 22 further includes an oil phase pot 224, and the feed port of the oil phase pot 224 is connected to the discharge port of the oil material tank 222, and the second weighing device 221 is arranged at the discharge port of the oil phase pot 224. Specifically, the water phase pot 214 is used to heat the water phase raw material conveyed through the water material tank 212, and the water phase raw material heated by the water phase pot 214 is weighed by the first weighing device 211 and then conveyed to the emulsifier 10. The oil phase pot 224 is used to heat the oil phase raw material conveyed through the oil material tank 222, and the oil phase raw material heated by the oil phase pot 224 is weighed by the second weighing device 221 and then conveyed to the emulsifier 10.

[0042] Among them, the water phase pot 214 and the oil phase pot 224 are arranged in parallel, and the discharge port of the water phase pot 214 and the discharge port of the oil phase pot 224 are respectively connected to the connecting pipe 41, and a third pump 42 is arranged on the connecting pipe 41, and the connecting pipe 41 is connected to the emulsifier 10, and then the third pump 42 generates power to transport the water phase raw material in the water phase pot 214 and the oil phase raw material in the oil phase pot 224 to the emulsifier 10.

[0043] Please continue to refer to Figure 1In actual use, a first valve 216 is provided at the outlet of the water tank 212, and the first valve 216 is used to control the opening or closing of the outlet of the water tank 212; a second valve 226 is provided at the outlet of the oil tank 222, and the second valve 226 is used to control the opening or closing of the outlet of the oil tank 222. In actual use, the first valve 216 and the first flow meter 213 often work at the same time, and the second valve 226 and the second flow meter 223 also work at the same time. That is to say, when it is necessary to input water phase raw materials and oil phase raw materials into the emulsifier 10, the first valve 216 is opened, and the water phase raw materials in the water tank 212 flow to the first flow meter 213 through the first valve 216, and the first flow meter 213 controls the amount flowing out to the water phase pot 214. At the same time, the second valve 226 is also in an open state, and the oil phase raw material in the oil tank 222 flows to the second flow meter 223 through the second valve 226 , and the second flow meter 223 controls the amount flowing out to the oil phase pot 224 .

[0044] In actual use, a third valve 218 is provided at the outlet of the water phase pot 214, and the third valve 218 controls the opening or closing of the outlet of the water phase pot 214. A fourth valve 228 is provided at the outlet of the oil phase pot 224, and the fourth valve 228 controls the opening or closing of the outlet of the oil phase pot 224.

[0045] The first valve 216 , the second valve 226 , the third valve 218 and the fourth valve 228 are all solenoid valves for easy control.

[0046] Please continue to refer to Figure 1 In actual use, the water material system 21 also includes a first manifold 217, and a plurality of water material tanks 212 arranged in parallel are respectively connected to the first manifold 217. That is, the first manifold 217 is provided with a plurality of first branches, each of which is connected to the first manifold 217, and each first branch corresponds to a water material tank 212. The output port of the first manifold 217 is connected to the water phase pot 214, thereby ensuring that the water phase raw materials in each water material tank 212 can flow along the first manifold 217 to the water phase pot 214 for heating. The oil material system 22 also includes a second manifold 227, and a plurality of oil material tanks 222 arranged in parallel are respectively connected to the second manifold 227. That is, the second manifold 227 is provided with a plurality of second branches, each of which is connected to the second manifold 227, and each second branch is correspondingly connected to an oil material tank 222, thereby realizing the connection of a plurality of oil material tanks 222 with the second manifold 227. At the same time, the output port of the second manifold 227 is connected to the oil phase pot 224, thereby ensuring that the oil phase raw materials in each oil tank 222 can flow along the second manifold 227 to the oil phase pot 224 for heating.

[0047] Please continue to refer to Figure 1Preferably, the first manifold 217 is provided with a first pump 215, which is used to provide power to transport the water-phase raw material output from the water tank 212 to the water-phase pot 214. The second manifold 227 is provided with a second pump 225, which is used to provide power to transport the oil-phase raw material in the oil tank 222 to the oil-phase pot 224. The provision of the first pump 215 and the second pump 225 speeds up the rate of transporting the water-phase raw material and the oil-phase raw material, thereby improving the work efficiency.

[0048] The first pump 215 and the second pump 225 are both suction pumps, or only one of them is a suction pump, as long as they can achieve the transportation of water-phase raw materials and oil-phase raw materials.

[0049] Please continue to refer to Figure 1 Preferably, the first hot water tank 31 is connected to the input port of the first manifold 217, and the second hot water tank 32 is connected to the input port of the second manifold 227. In actual use, when cosmetics need to be prepared, the hot water in the first hot water tank 31 and the second hot water tank 32 can be used to sterilize the water phase pot 214, the oil phase pot 224 and the emulsifier 10 at high temperature. At this time, the first hot water tank 31 is connected to the passage connecting the first manifold 217, so that the hot water in the first hot water tank 31 can flow along the first manifold 217 to the water phase pot 214, and then flow into the emulsifier 10. At the same time, the second hot water tank 32 is connected to the passage connecting the second manifold 227, so that the hot water in the second hot water tank 32 can flow along the second manifold 227 to the oil phase pot 224, and then flow into the emulsifier 10. Then the hot water flowing into the emulsifier 10 is discharged from the discharge port of the emulsifier 10, thereby achieving high-temperature cleaning and sterilization of the water phase pot 214, the oil phase pot 224 and the emulsifier 10.

[0050] It should be added that, when the water phase pot 214, the oil phase pot 224 and the emulsifier 10 are being prepared for sterilization, high temperature steam may also be introduced, as long as the sterilization of the above three can be achieved.

[0051] Please continue to refer to Figure 1Preferably, the emulsifier 10 has a storage cavity, and the storage cavity is provided with a jacket layer, and the jacket layer can be filled with a coolant, and the coolant is used to cool the material in the storage cavity. The water phase pot 214 is connected to the connecting pipe 41 through a first pipe, and then connected to the storage cavity of the emulsifier 10 through the connecting pipe 41. The water phase raw material heated by the water phase pot 214 is sequentially transported to the storage cavity through the first pipe and the connecting pipe 41. At the same time, the oil phase pot 224 is connected to the connecting pipe 41 through a second pipe, and then connected to the storage cavity of the emulsifier 10 through the connecting pipe 41. The oil phase raw material heated by the oil phase pot 224 is sequentially transported to the storage cavity through the second pipe and the connecting pipe 41. After the water phase raw material and the oil phase raw material are mixed and emulsified in the storage cavity of the emulsifier 10, a cooling treatment is performed.

[0052] The cooling liquid is cooling water. That is, a coil is provided in the jacket layer of the storage cavity, and the cooling liquid passes through the coil to cool the mixed material in the storage cavity. The cooling liquid is not limited to the coil.

[0053] Please continue to refer to Figure 1 Preferably, a filter is detachably connected to the discharge port of the emulsifier 10. Specifically, the discharge port of the emulsifier 10 is connected to the storage chamber to facilitate the discharge of the mixture in the storage chamber. The mixture is first emulsified in the storage chamber, and the cooling operation begins after emulsification. After the mixture is completed and tested to be qualified, it is discharged from the discharge port of the emulsifier 10. During discharge, the mixture can be filtered through the filter to remove impurities mixed in the mixture and improve the quality of the product. Among them, the filter is detachably connected to the discharge port of the emulsifier 10, which makes it easy to disassemble the filter for cleaning, and reinstall it at the discharge port of the emulsifier 10 after cleaning.

[0054] like Figure 1 As shown, the specific use process of the batching production device is as follows:

[0055] The water phase raw material is stored in the water material tank 212, and the oil phase raw material is stored in the oil material tank 222. At this time, the first valve 216 and the second valve 226 are in a closed state. The first hot water tank 31 and the second hot water tank 32 are opened, so that the first hot water tank 31 and the second hot water tank 32 are connected to the corresponding first manifold 217 and the second manifold 227 respectively, and then the hot water in the first hot water tank 31 flows along the first manifold 217 to the water phase pot 214, and then flows along the first pipeline and the connecting pipeline 41 to the storage chamber of the emulsifier 10, and the hot water in the second hot water tank 32 flows along the second manifold 227 to the oil phase pot 224, and then flows along the second pipeline and the connecting pipeline 41 to the storage chamber of the emulsifier 10, and finally flows out from the discharge port of the emulsifier 10. Then, the first valve 216 and the first flowmeter 213 are opened, so that the water phase raw material in the water material tank 212 is output according to a certain amount, and under the action of the first pump 215, it flows along the first manifold 217 to the water phase pot 214 for heating. At the same time, the second valve 226 and the second flowmeter 223 are opened, so that the oil phase raw material in the oil material tank 222 is output according to a certain amount, and under the action of the second pump 225, it is transported to the oil phase pot 224 along the second manifold 227 for heating. At this time, the third valve 218 and the fourth valve 228 are both in a closed state. After the water phase raw material and the oil phase raw material are heated, the third valve 218 is opened, and the heated water phase raw material is transported to the storage chamber of the emulsifier 10 along the first pipeline and the connecting pipeline 41 for cooling; the fourth valve 228 is opened, and the heated oil phase raw material is transported to the storage chamber of the emulsifier 10 along the second pipeline and the connecting pipeline 41 for mixing and emulsification. After the emulsification is completed, the mixture is cooled to the set temperature, and then the remaining low-temperature residue in the water system 21 and the oil system 22 is added to the emulsifier 10. After the low-temperature residue is evenly mixed with the above-mentioned cooling material and tested to be qualified, the mixture is discharged from the discharge port of the emulsifier 10.

[0056] It should be added that the batching production device also includes a control unit 50, and the weighing device, four valves, pump and flow meter are electrically connected to the control unit 50 respectively. At the same time, the batching production device also has a human-computer interaction interface to facilitate staff adjustment, thereby realizing intelligent control of the batching production device.

[0057] It should be noted that how the control unit 50 is electrically connected to the weighing device, valve, pump and flow meter respectively and how it is controlled are all existing mature technologies and are not the invention of this application, so they are not elaborated here.

[0058] Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention, rather than to limit it. Although the present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should understand that they can still modify the technical solutions described in the aforementioned embodiments, or replace some or all of the technical features therein with equivalents. However, these modifications or replacements do not cause the essence of the corresponding technical solutions to deviate from the scope of the technical solutions of the embodiments of the present invention.

Claims

1. A batching production device, characterized in that: It comprises an emulsifier (10) and two groups of batching systems, wherein the two groups of batching systems are respectively connected to the emulsifier (10); the two groups of batching systems respectively comprise a water system (21) and an oil system (22); A weighing device is provided at the discharge port of each batching system, and the weighing device is used to weigh the material, and the weighed material can be conveyed to the emulsifier (10); the batching system comprises at least one storage tank; the batching system also comprises a material phase pot, the feed port of the material phase pot is connected to the discharge port of the storage tank, the discharge port of the material phase pot is connected to the feed port of the emulsifier (10), and the weighing device is provided at the discharge port of the material phase pot; There are multiple material storage tanks, which are arranged in parallel; the batching system further includes a manifold, the discharge ports of the multiple material storage tanks are respectively connected to the manifold, and the output port of the manifold is connected to the feed port of the material phase pot; a valve is provided at the discharge port of the material storage tank, and the valve is used to open or close the material storage tank; The batching production device further comprises a hot water tank, which is connected to the input port of the manifold; The use process of the batching production device is as follows: the raw materials are stored in the material storage tank, the valve provided at the material outlet of the material storage tank is in a closed state, the hot water tank is opened so that the hot water tank is connected to the manifold, and then the hot water in the hot water tank flows along the manifold to the material phase pot, and then flows to the emulsifier (10), and finally flows out from the material outlet of the emulsifier (10) to preheat the material phase pot and the emulsifier (10) for high-temperature cleaning and disinfection; then the valve is opened so that the raw materials in the material storage tank are discharged and flow along the manifold to the material phase pot for heating.

2. The batching production device according to claim 1, characterized in that: The material outlet of the material storage tank is communicated with the material inlet of the emulsifier (10), and a flow meter is provided at the material outlet of the material storage tank.

3. The batching production device according to claim 1, characterized in that: A pump is provided on the passage connecting the material storage tank and the material phase pot, and the pump is used to transport the material in the material storage tank to the material phase pot.

4. The batching production device according to any one of claims 1 to 3, characterized in that: The emulsifier (10) has a material storage chamber, and the material outlet of the batching system is in communication with the material storage chamber; The material storage cavity is provided with a jacket layer, and the jacket layer can be filled with a coolant, and the coolant is used to cool the material in the material storage cavity.

5. The batching production device according to any one of claims 1 to 3, characterized in that: A filter screen is detachably connected to the discharge port of the emulsifier (10).

6. The batching production device according to any one of claims 1 to 3, characterized in that: The weighing device arranged in the water material system (21) is a first weighing device (211), and the first weighing device (211) is arranged at the discharge port of the water material system (21); the weighing device arranged in the oil material system (22) is a second weighing device (221), and the second weighing device (221) is arranged at the discharge port of the oil material system (22).

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