CN211706457U

CN211706457U - Batching apparatus for producing

Info

Publication number: CN211706457U
Application number: CN202020022304.9U
Authority: CN
Inventors: 孙怀庆; 孙云起; 朱振华; 聂艳峰; 郭朝万; 胡露
Original assignee: Guangdong Marubi Biological Technology Co Ltd
Current assignee: Guangdong Marubi Biological Technology Co Ltd
Priority date: 2020-01-06
Filing date: 2020-01-06
Publication date: 2020-10-20
Anticipated expiration: 2030-01-06

Abstract

The utility model provides a batching apparatus for producing relates to cosmetics technical field. The batching production device comprises an emulsifier and at least two groups of batching systems, wherein the at least two groups of batching systems are respectively connected with the emulsifier; the discharge gate department of every group feed proportioning system is provided with the ware of weighing respectively, and the ware of weighing is used for weighing the material, and the material after weighing can be carried to the emulgator to alleviate and consume a large amount of manpower and materials when carrying out cosmetics production among the prior art, and lower to the ratio precision of material, lead to the lower technical problem of off-the-shelf quality.

Description

Batching apparatus for producing

Technical Field

The utility model relates to a cosmetics technical field especially relates to a batching apparatus for producing.

Background

When traditional cosmetics are produced, a dispensing worker needs to get raw materials from a raw material bin according to formula requirements, weigh the raw materials under the supervision of a rechecker according to formula dosage, record raw material dispensing information, place the dispensed materials in an area to be emulsified, and return redundant raw materials to the bin. And (4) feeding the prepared materials by an emulsifier under the supervision of a rechecker according to the production process, operating the emulsifying equipment and recording the production process in time. However, in the production process, a large amount of manpower and material resources are needed, and the material proportioning precision is low, so that the quality of the formed finished product is difficult to guarantee.

In view of the above, there is a need for a batching production device that can solve the above problems.

The information disclosed in this background section is only for enhancement of understanding of the general background of the invention and should not be taken as an acknowledgement or any form of suggestion that this information constitutes prior art already known to a person skilled in the art.

SUMMERY OF THE UTILITY MODEL

The utility model discloses an it provides a batching apparatus for producing to alleviate among the prior art and consume a large amount of manpower and materials when carrying out cosmetics production, and lower to the ratio precision of material, lead to the lower technical problem of off-the-shelf quality.

In order to achieve the above purpose, the utility model adopts the following technical scheme:

the utility model provides a batching production device, which comprises an emulsifier and at least two groups of batching systems, wherein the at least two groups of batching systems are respectively connected with the emulsifier;

and a weighing device is respectively arranged at the discharge port of each group of the batching system and used for weighing the materials, and the weighed materials can be conveyed to the emulsifier.

In any one of the above technical solutions, further, the batching system includes at least one storage tank, the discharge port of the storage tank with the feed inlet of the emulsifier intercommunication, just the discharge port department of the storage tank is provided with a flowmeter.

In any one of the above technical solutions, further, the batching system further includes a material phase pot, a feed inlet of the material phase pot is communicated with a discharge outlet of the storage tank, a discharge outlet of the material phase pot is communicated with a feed inlet of the emulsifier, and the weigher is arranged at a discharge outlet of the material phase pot.

In any one of the above technical solutions, further, a pump is disposed on a passage through which the storage tank and the material phase pot are communicated, and the pump is used for conveying the material in the storage tank to the material phase pot.

In any one of the above technical solutions, further, when the number of the storage tanks is multiple, the storage tanks are arranged in parallel;

the batching system still includes the manifold, and is a plurality of the discharge gate of storage tank respectively with the manifold intercommunication, just the delivery outlet of manifold with the feed inlet intercommunication of material looks pot.

In any one of the above technical solutions, further, the ingredient production apparatus further includes a hot water tank, and the hot water tank is communicated with the input port of the manifold.

In any one of the above technical solutions, further, a valve is disposed at a discharge port of the storage tank, and the valve is used for opening or closing the storage tank.

In any of the above technical solutions, further, the emulsifier has a storage cavity, and a discharge port of the batching system is communicated with the storage cavity;

the storage cavity is provided with presss from both sides the jacket layer, it can fill the coolant liquid to press from both sides the jacket in situ, the coolant liquid be used for right the material in the storage cavity cools down.

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

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

the weighing device arranged on the water material system is a first weighing device arranged at a discharge port of the water material system; the weighing device arranged on the oil system is a second weighing device arranged at a discharge port of the oil system.

The utility model has the advantages that:

the utility model provides a pair of batching apparatus for producing, including emulgator and at least two sets of feed proportioning system, and at least two sets of feed proportioning system are connected with the emulgator respectively. And the discharge port of each group of the batching system is respectively provided with a weigher, and the materials in the batching system are weighed by the weighers and then conveyed into the emulsifier. Compared with the prior art that the materials need to be weighed by a material distributor firstly, and then rechecked by a rechecker, and the materials are found by an emulsifier and fed, the material proportioning production device directly weighs the materials by the weighing device, is simple and convenient to operate, and saves manpower and material resources. Meanwhile, when the weighing machine is used for weighing, the weighing precision is convenient to control, and the quality of a finished product is improved.

Drawings

In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the embodiments or the technical solutions in the prior art will be briefly described below, and it is obvious that the drawings in the following description are some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.

Fig. 1 is the schematic flow diagram of the batching production device provided by the embodiment of the utility model.

Icon: 10-an emulsifier; 21-water material system; 22-oil system; 31-a first hot water tank; 32-a second hot water tank; 41-connecting a pipeline; 42-a third pump; 50-a control unit; 211-a first weigher; 212-water bucket; 213-first flow meter; 214-aqueous phase pan; 215-a first pump; 216-a first valve; 217-first header; 218-a third valve; 221-a second weigher; 222-oil tank; 223-a second flow meter; 224-oil phase pan; 225-a second pump; 226-a second valve; 227-a second header; 228-fourth valve.

Detailed Description

The technical solution of the present invention will be described clearly and completely with reference to the accompanying drawings, and obviously, the described embodiments are some, but not all embodiments of the present invention. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.

In the description of the present invention, it should be noted that the terms "first" and "second" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.

In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.

As shown in fig. 1, the ingredient production apparatus provided in this embodiment includes an emulsifier 10 and at least two sets of ingredient systems, and the at least two sets of ingredient systems are respectively connected to the emulsifier 10; and a weighing device is respectively arranged at the discharge port of each group of the batching system and used for weighing the materials, and the weighed materials can be conveyed to the emulsifier 10.

Specifically, the batching system is provided with the multiunit, and the parallelly connected setting of multiunit batching system is connected with emulgator 10 respectively, and the material in every batching system of group can carry respectively to carry out the emulsification operation in the emulgator 10. Each group of batching systems can be used for storing different materials, or each group of batching systems is used for storing the same material, as long as the materials stored in the batching systems can be conveyed to the emulsifier 10 for emulsification operation.

During the in-service use, the discharge gate department of every group feed proportioning system is provided with the weigher respectively, that is to say when feed proportioning system carried the material to emulsifier 10 in, the material of output in the feed proportioning system can add to emulsifier 10 after weighing through the weigher earlier. Compared with the prior art, the weighing device has the advantages that the weighing device needs to be sequentially weighed by a batching member, rechecked by a rechecker, found by an emulsifier and fed, the weighing device can directly weigh materials output by a batching system, is simple and convenient to operate, can achieve the set material amount only through one-time weighing, does not need to be weighed by at least two workers, and further saves manpower and material resources. Meanwhile, when the material is weighed by the weighing device, the weighing precision is convenient to control, so that the weighing precision is higher, and the quality of a finished product is improved.

The weighing device adopts electronic weighing, is convenient to control and has higher weighing precision.

It should be added that multiple sets of batching systems can also be arranged in series, or several sets of batching systems can be arranged in series, and several other sets of batching systems can be arranged in parallel, or multiple sets of batching systems can have both series and parallel relations. No matter how the plurality of groups of the batching systems are arranged, the emulsifier can be added with materials according to a certain amount by arranging the weigher at the discharge port of each group of the batching systems.

With continued reference to fig. 1, preferably, the number of the batching systems is two, and the two batching systems respectively comprise a water system 21 and an oil system 22; 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 weigher arranged in the oil system 22 is a second weigher 221, and the second weigher 221 is arranged at the discharge port of the oil system 22.

Take this batching apparatus to be applied to the cosmetics preparation field as an example, in this embodiment, the quantity of batching system is two sets of, and two sets of batching systems are water material system 21 and oil system 22 respectively, and water material system 21 is used for carrying the aqueous phase material, and oil system 22 is used for carrying the oil phase material. A first weighing device 211 is arranged at the discharge port of the water material system 21, and the first weighing device 211 is used for weighing the water phase material conveyed by the water material system 21 so as to control the dosage of the water phase material conveyed to the emulsifier 10 by the water material system 21. A second weigher 221 is disposed at the discharge port of the oil system 22, and the second weigher 221 is configured to weigh the oil phase material delivered by the oil system 22 so as to control the amount of the oil phase material delivered by the oil system 22 to the emulsifier 10. The quantity of the materials output by the water material system 21 and the oil material system 22 is controlled respectively, so that the materials conveyed into the emulsifier 10 are controlled within a certain range, and the quality of the product emulsified by the emulsifier 10 is improved.

With continued reference to fig. 1, preferably, the water system 21 includes at least one water tank 212, a discharge port of the water tank 212 is communicated with the feed port of the emulsifier 10, and a first flow meter 213 is disposed at the discharge port of the water tank 212. The oil system 22 comprises at least one oil tank 222, a discharge port of the oil tank 222 is communicated with the feed port of the emulsifier 10, and a second flow meter 223 is arranged at the discharge port of the oil tank 222.

The water tank 212 is used for storing water phase raw materials, and the oil tank 222 is used for storing oil phase raw materials. When the number of the water tanks 212 is multiple, the water tanks 212 are arranged in parallel, and a first flow meter 213 is correspondingly arranged at a discharge port of each water tank 212, and the first flow meter 213 is used for controlling the usage amount of the water phase raw material output from the water tanks 212, that is, the first flow meter 213 can enable the water phase raw material output from the water tanks 212 to the emulsifier 10 to be at a set value. Meanwhile, the number of the oil tanks 222 is provided with a plurality of oil tanks 222, and the plurality of oil tanks 222 are arranged in parallel. A second flow meter 223 is correspondingly arranged at the output port of each oil tank 222, and the second flow meter 223 is used for controlling the usage amount of the oil phase raw material output from the oil tank 222, so that the oil phase raw material input from the oil tank 222 to the emulsifier 10 is at a set value.

The water phase raw material conveyed out by the water tank 212 is subjected to dosage control through the first flowmeter 213, and then is subjected to secondary weighing through the first weighing device 211, the oil phase raw material conveyed out by the oil tank 222 is subjected to dosage control through the second flowmeter 223, and is subjected to secondary weighing through the second weighing device 221, so that the water phase material and the oil phase material conveyed into the emulsifier 10 are ensured to be in set values, and the quality of the product is improved.

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.

It should be added that when there are a plurality of water tanks 212, a plurality of water tanks 212 may also be arranged in series, or a plurality of water tanks 212 may be arranged in series and in parallel. When there are a plurality of oil tanks 222, the oil tanks 222 may be arranged in series or in parallel. It is sufficient to ensure that the water phase material and the oil phase material to be fed to the emulsifier 10 are at the set values.

With continued reference to fig. 1, preferably, the water material system 21 further includes an aqueous phase pan 214, and a feed inlet of the aqueous phase pan 214 is communicated with a discharge outlet of the water material tank 212, and the first weigher 211 is disposed at the discharge outlet of the aqueous phase pan 214. The oil system 22 further comprises an oil phase pan 224, a feed inlet of the oil phase pan 224 is communicated with a discharge outlet of the oil tank 222, and a second weigher 221 is arranged at the discharge outlet of the oil phase pan 224. Specifically, the water phase pot 214 is used for heating the water phase raw material conveyed by the water material tank 212, and the water phase raw material heated by the water phase pot 214 is conveyed to the emulsifier 10 after being weighed by the first weighing device 211. The oil phase pan 224 is used for heating the oil phase raw material conveyed by the oil tank 222, and the oil phase raw material heated by the oil phase pan 224 is conveyed to the emulsifier 10 after being weighed by the second weigher 221.

The water phase pot 214 and the oil phase pot 224 are arranged in parallel, a discharge port of the water phase pot 214 and a discharge port of the oil phase pot 224 are respectively communicated with the connecting pipeline 41, the connecting pipeline 41 is provided with the third pump 42, the connecting pipeline 41 is communicated with the emulsifier 10, and then the water phase raw material in the water phase pot 214 and the oil phase raw material in the oil phase pot 224 are conveyed into the emulsifier 10 by power generated by the third pump 42.

With reference to fig. 1, in actual use, a first valve 216 is disposed at the discharge port of the water tank 212, and the first valve 216 is used for controlling the opening or closing of the discharge port of the water tank 212; a second valve 226 is disposed at the discharge port of the oil tank 222, and the second valve 226 is used for controlling the opening or closing of the discharge port of the oil tank 222. In actual use, the first valve 216 and the first flow meter 213 are often operated simultaneously, and the second valve 226 and the second flow meter 223 are also operated simultaneously. That is, when it is necessary to input the water phase raw material and the oil phase raw material into the emulsifier 10, the first valve 216 is opened, the water phase raw material in the water tank 212 flows to the first flow meter 213 through the first valve 216, and the first flow meter 213 controls the amount of the water phase raw material flowing out to the water phase pot 214. Meanwhile, the second valve 226 is also in an open state, 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 of the oil phase raw material flowing out to the oil phase pot 224.

In actual use, a third valve 218 is provided at the discharge port of the water phase pan 214, and the opening or closing of the discharge port of the water phase pan 214 is controlled by the third valve 218. A fourth valve 228 is arranged at the discharge port of the oil phase pan 224, and the discharge port of the oil phase pan 224 is controlled to be opened or closed by the fourth valve 228.

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

Referring to fig. 1, in actual use, the water system 21 further includes a first manifold 217, and a plurality of water tanks 212 arranged in parallel are respectively communicated with the first manifold 217. Namely: the first collecting pipe 217 is provided with a plurality of first branch pipes, each first branch pipe is connected with the first collecting pipe 217, and each first branch pipe corresponds to one water tank 212. The output port of the first collecting pipe 217 is communicated with the aqueous phase pot 214, so that the aqueous phase raw material in each aqueous phase pot 212 can flow into the aqueous phase pot 214 along the first collecting pipe 217 for heating. The oil system 22 further includes a second collecting pipe 227, and a plurality of oil tanks 222 arranged in parallel are respectively communicated with the second collecting pipe 227. Namely: the second collecting pipe 227 is provided with a plurality of second branch pipes, the plurality of second branch pipes are respectively communicated with the second collecting pipe 227, and each second branch pipe is correspondingly connected with one oil tank 222, so that the connection of the plurality of oil tanks 222 and the second collecting pipe 227 is realized. Meanwhile, the output port of the second manifold 227 is communicated with the oil phase pan 224, so as to ensure that the oil phase raw material in each oil tank 222 can flow into the oil phase pan 224 along the second manifold 227 for heating.

With continued reference to fig. 1, preferably, the first manifold 217 is provided with a first pump 215, and the first pump 215 is used for providing power to convey 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, and the second pump 225 is used for providing power to convey the oil phase raw material in the oil tank 222 to the oil phase pot 224. The arrangement of the first pump 215 and the second pump 225 accelerates the speed of conveying the water phase raw material and the oil phase raw material, thereby improving the working efficiency.

Here, the first pump 215 and the second pump 225 both employ a suction pump, or only one of them employs a suction pump, as long as the conveyance of the water-phase raw material and the oil-phase raw material can be achieved.

With continued reference to fig. 1, preferably, a first hot water tank 31 is connected to the input port of the first manifold 217, and a second hot water tank 32 is connected to the input port of the second manifold 227. In actual use, when cosmetic preparation is required, the water phase pan 214, the oil phase pan 224, and the emulsifier 10 can be sterilized at high temperature using the hot water in the first and second hot water tanks 31 and 32. At this time, the passage connecting the first hot water tank 31 and the first header 217 is opened, so that the hot water in the first hot water tank 31 can flow to the water phase pot 214 along the first header 217 and then flow into the emulsifier 10. Meanwhile, the passage connecting the second hot water tank 32 and the second header 227 is opened, so that the hot water in the second hot water tank 32 can flow to the oil phase pan 224 along the second header 227 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 performing high-temperature cleaning and disinfection of the water phase pot 214, the oil phase pot 224 and the emulsifier 10.

It should be noted that high-temperature steam may be introduced during the preparation and sterilization of the three water phase boiler 214, the oil phase boiler 224, and the emulsifier 10. It is only required to realize the disinfection treatment of the three.

With continued reference to fig. 1, preferably, the emulsifier 10 has a material storage cavity, the material storage cavity is provided with a jacket layer, the jacket layer can be filled with a cooling liquid, and the cooling liquid is used for cooling the material in the material storage cavity. The water phase pot 214 is communicated with the connecting pipeline 41 through a first pipeline, and then is communicated with the storage cavity of the emulsifier 10 through the connecting pipeline 41, and the water phase raw material heated by the water phase pot 214 is conveyed into the storage cavity through the first pipeline and the connecting pipeline 41 in sequence. Meanwhile, the oil phase pan 224 is communicated with the connecting pipeline 41 through a second pipeline, and then is communicated with the storage cavity of the emulsifier 10 through the connecting pipeline 41, and the oil phase raw material heated by the oil phase pan 224 is conveyed into the storage cavity through the second pipeline and the connecting pipeline 41 in sequence. The water phase raw material and the oil phase raw material are mixed and emulsified in the storage cavity of the emulsifier 10, and then cooled.

Wherein, the cooling liquid adopts cooling water. That is to say, be provided with the coil pipe in the jacket layer of storage cavity, coolant liquid passes through in the coil pipe in order to cool off the mixture in the storage cavity. Wherein the coil is not limited to conveying the cooling liquid.

With continued reference to fig. 1, preferably, a filter screen is detachably connected to the discharge port of the emulsifier 10. Specifically, the discharge port of the emulsifier 10 is communicated with the storage cavity so as to discharge the mixture in the storage cavity. The mixture is firstly emulsified in the storage cavity, and then the cooling operation is started after the emulsification. And after the mixture is finished and the detection is qualified, discharging the mixture from a discharge hole of the emulsifier 10. When the mixed material is discharged, the mixed material can be filtered by the filter screen so as to remove the mixed impurities in the mixed material and improve the quality of the product. Wherein, the filter screen can be dismantled and connect in the discharge gate department of emulgator 10, and then be convenient for dismantle the filter screen and wash it, treat after the sanitization install again in the discharge gate of emulgator 10 can.

As shown in fig. 1, the use flow of the ingredient production apparatus is specifically as follows:

the water phase raw material is stored in the water tank 212, and the oil phase raw material is stored in the oil tank 222, and 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 respectively communicated with the corresponding first manifold 217 and the corresponding second manifold 227, hot water in the first hot water tank 31 flows to the water phase pot 214 along the first manifold 217 and then flows to the storage cavity of the emulsifier 10 along the first pipeline and the connecting pipeline 41, hot water in the second hot water tank 32 flows to the oil phase pot 224 along the second manifold 227 and then flows to the storage cavity of the emulsifier 10 along the second pipeline and the connecting pipeline 41, and finally flows out of the discharge hole of the emulsifier 10. Then, the first valve 216 and the first flow meter 213 are opened, so that the water phase raw material in the water tank 212 is output in a certain amount and flows along the first header 217 to the water phase pot 214 to be heated under the action of the first pump 215. Meanwhile, the second valve 226 and the second flow meter 223 are opened, so that the oil-phase raw material in the oil tank 222 is output in a certain amount and is conveyed to the oil-phase pot 224 for heating along the second header 227 under the action of the second pump 225. At this time, third valve 218 and 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 conveyed to the storage cavity of the emulsifier 10 along the first pipeline and the connecting pipeline 41 for cooling; and opening the fourth valve 228, and conveying the heated oil-phase raw materials to the storage cavity of the emulsifier 10 along the second pipeline and the connecting pipeline 41 for mixing and emulsification. And after the emulsification is finished, cooling to a set temperature, adding the low-temperature excess materials left in the water material system 21 and the oil material system 22 into the emulsifier 10, uniformly mixing the low-temperature excess materials with the cooling materials, and discharging the mixture from a discharge hole of the emulsifier 10 after the detection is qualified.

It needs to supplement that, this batching apparatus for producing still includes control unit 50, and weighing device, four valves, pump and flowmeter are equallyd divide and are connected with control unit 50 electricity respectively, and simultaneously, this batching apparatus for producing still has man-machine interface so that the staff regulation and control, and then realizes this batching apparatus for producing's intelligent control.

It should be noted that how the control unit 50 is electrically connected to the weighing device, the valve, the pump and the flowmeter respectively and how to control the weighing device, the valve, the pump and the flowmeter belong to the existing mature technologies, and also do not belong to the utility model of the application, so the description is omitted.

Finally, it should be noted that: the above embodiments are only used to illustrate the technical solution of the present invention, and not to limit it; although the present invention has been described in detail with reference to the foregoing embodiments, it should be understood by those skilled in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some or all of the technical features may be equivalently replaced; such modifications and substitutions do not depart from the spirit and scope of the embodiments of the present invention.

Claims

1. The batching production device is characterized by comprising an emulsifier (10) and at least two groups of batching systems, wherein the at least two groups of batching systems are respectively connected with the emulsifier (10);

and a discharging port of each group of the batching system is respectively provided with a weigher which is used for weighing the materials, and the weighed materials can be conveyed to the emulsifier (10).

2. The ingredient production device according to claim 1, wherein the ingredient system comprises at least one storage tank, the discharge port of the storage tank is communicated with the feed port of the emulsifier (10), and a flow meter is arranged at the discharge port of the storage tank.

3. The ingredient production device according to claim 2, wherein the ingredient system further comprises a material phase pot, a feeding hole of the material phase pot is communicated with a discharging hole of the storage tank, a discharging hole of the material phase pot is communicated with a feeding hole of the emulsifier (10), and the weighing device is arranged at a discharging hole of the material phase pot.

4. The ingredient production device according to claim 3, wherein a pump is disposed on a passage of the storage tank communicating with the material phase pot, and the pump is used for conveying the material in the storage tank to the material phase pot.

5. The ingredient production apparatus according to claim 3, wherein when the number of the storage tanks is plural, the plural storage tanks are arranged in parallel;

6. The ingredient production apparatus of claim 5 further comprising a hot water tank in communication with the input port of the manifold.

7. The ingredient production apparatus according to claim 2, wherein a valve is provided at the discharge port of the storage tank, the valve being used to open or close the storage tank.

8. The ingredient production apparatus according to any one of claims 1 to 7, wherein the emulsifier (10) has a reservoir chamber, the outlet of the ingredient system communicating with the reservoir chamber;

9. Ingredient production arrangement according to any of claims 1-7, wherein a filter screen is detachably connected to the outlet of the emulsifier (10).

10. The ingredient production arrangement according to any of claims 1-7, wherein the number of ingredient systems is two, the two groups of ingredient systems comprising a water system (21) and an oil system (22), respectively;

the weighing device arranged on the water material system (21) is a first weighing device (211), and the first weighing device (211) is arranged at a discharge port of the water material system (21); the weigher arranged on the oil system (22) is a second weigher (221), and the second weigher (221) is arranged at a discharge port of the oil system (22).