Automatic production working method of Baoxinning thick paste

Abstract

The invention provides an automatic production working method of Baoxinning thick paste. The automatic production working method comprises the following steps: S1, setting production parameters of the Baoxinning thick paste; and S2, realizing production of the Baoxinning thick paste according to the set production parameters of the Baoxinning thick paste in the step S1. The automation degree can be safely improved, and the working efficiency is improved.

Description

Technical Field

[0001] The present invention relates to the technical field of pharmaceutical production, and in particular to an automated production method for Baoxinning thick paste. Background Art

[0002] Baoxinning Capsules are a medication used to treat angina pectoris, arrhythmias, and improve symptoms of coronary heart disease. Its main ingredients include salvia miltiorrhiza, Panax notoginseng, Chinese angelica root, and fructus aurantii. Before capsule preparation, a thick paste must be prepared. This paste is then dried, sieved, and filled into capsules to produce Baoxinning capsules. Preparation of the thick paste is a key step in Baoxinning capsule production. Currently, the preparation of the thick paste involves pulverizing Panax notoginseng into a fine powder and sieving it. Ginger is decocted with water twice, each for two hours. The decoctions are combined, filtered, and the filtrates concentrated to an appropriate amount. The Chinese angelica root is then extracted with ethanol and concentrated to produce a thick paste. The Panax notoginseng powder, ginger decoction, Chinese angelica root paste, fructus aurantii percolated paste, and salvia miltiorrhiza percolated paste are then combined to create the desired mixed thick paste. After percolation, the salvia miltiorrhiza residue still contains a large amount of active ingredients, which cannot be fully extracted, resulting in a waste of medicinal materials. Furthermore, the current thick paste preparation process requires the addition of artificial materials, which can cause contamination and is labor-intensive. Summary of the Invention

[0003] The present invention aims to at least solve the technical problems existing in the prior art, and particularly innovatively proposes an automated production method for Baoxinning thick paste, which can improve the degree of automation and improve work efficiency.

[0004] In order to achieve the above-mentioned object of the present invention, the present invention provides an automated production method of Bao Xin Ning thick paste, comprising the following steps:

[0005] S1, set the production parameters of Baoxinning thick paste;

[0006] S2, producing the Bao Xin Ning thick paste according to the production parameters of the Bao Xin Ning thick paste set in step S1.

[0007] In a preferred embodiment of the present invention, the production control method of the Bao Xin Ning thick paste in step S2 includes the following steps:

[0008] S21, adding the Danshen fine powder generated by the Danshen thick paste preparation subsystem into a mixing tank;

[0009] S22, adding the Fructus Aurantii Immaturus fine powder generated by the Fructus Aurantii Immaturus thick paste preparation subsystem to a mixing tank;

[0010] S23, adding the fine angelica powder produced by the angelica paste preparation subsystem to a mixing tank;

[0011] S24, adding Panax notoginseng powder to a mixing tank;

[0012] S25, adding the ginger liquid generated by the ginger preparation subsystem to the mixing tank;

[0013] S26, mixing the materials added to the mixing tank.

[0014] In a preferred embodiment of the present invention, the control working method of generating Danshen fine powder in the Danshen thick paste preparation subsystem in step S21 includes the following steps:

[0015] S211, adding salvia miltiorrhiza powder to the salvia miltiorrhiza powder storage tank, adding ethanol liquid to the salvia miltiorrhiza ethanol storage tank, and adding water to the water storage tank;

[0016] S212, metering and conveying the salvia miltiorrhiza powder in the salvia miltiorrhiza powder storage tank to the salvia miltiorrhiza percolation tank via a metering screw conveyor provided between the salvia miltiorrhiza percolation tank and the salvia miltiorrhiza powder storage tank, and opening a metering pump and an automatic control valve provided between the salvia miltiorrhiza percolation tank and the salvia miltiorrhiza ethanol storage tank to allow the ethanol in the salvia miltiorrhiza ethanol storage tank to flow into the salvia miltiorrhiza percolation tank;

[0017] S213, passing the percolation liquid in the Danshen percolation tank into the Danshen percolation liquid storage tank, conveying the Danshen residue in the Danshen percolation tank to the Danshen residue boiling tank via a screw conveyor provided between the Danshen percolation tank and the Danshen residue boiling tank, opening the metering pump and automatic control valve provided between the water storage tank and the Danshen residue boiling tank to pass the water in the water storage tank into the Danshen residue boiling tank;

[0018] S214, turning on the extraction pump provided between the Danshen filter residue boiling tank and the Danshen percolation liquid storage tank to pass the Danshen filtrate prepared in the Danshen filter residue boiling tank into the Danshen percolation liquid storage tank;

[0019] S215, turning on the extraction pump provided between the Danshen concentration tank and the Danshen percolation liquid storage tank to pass the Danshen liquid in the Danshen percolation liquid storage tank into the Danshen concentration tank;

[0020] S216, the ethanol vapor evaporated in the Danshen concentration tank enters the Danshen ethanol condenser for condensation, and the condensed ethanol vapor enters the Danshen ethanol recovery tank, and the extraction pump provided between the Danshen ethanol recovery tank and the Danshen ethanol storage tank is turned on to pass the ethanol liquid in the Danshen ethanol recovery tank into the Danshen ethanol storage tank;

[0021] S217, opening the metering pump provided between the Danshen concentration tank and the Danshen thick paste storage tank to pass the Danshen thick paste in the Danshen concentration tank into the Danshen thick paste storage tank;

[0022] S218, opening the metering pump and the automatic control valve provided between the Danshen thick paste storage tank and the mixing tank to pass the Danshen fine powder in the Danshen thick paste storage tank into the mixing tank;

[0023] Or / and the method for controlling the Fructus Aurantii Immaturus fine powder generated by the Fructus Aurantii Immaturus thick paste preparation subsystem in step S22 includes the following steps:

[0024] S221, adding Fructus Aurantii powder to the Fructus Aurantii powder storage tank, and adding ethanol liquid to the Fructus Aurantii ethanol storage tank;

[0025] S222, metering the Fructus Aurantii Immaturus powder in the Fructus Aurantii Immaturus powder storage tank into the Fructus Aurantii Immaturus percolation tank by a metering screw conveyor provided between the Fructus Aurantii Immaturus percolation tank and the Fructus Aurantii Immaturus powder storage tank, and opening the metering pump and automatic control valve provided between the Fructus Aurantii Immaturus percolation tank and the Fructus Aurantii Immaturus ethanol storage tank to pass the ethanol in the Fructus Aurantii Immaturus ethanol storage tank into the Fructus Aurantii Immaturus percolation tank;

[0026] S223, passing the percolation liquid in the Fructus Aurantii Immaturus percolation tank into the Fructus Aurantii Immaturus percolation liquid storage tank;

[0027] S224, turning on the extraction pump provided between the Fructus Aurantii Immaturus vacuum concentration tank and the Fructus Aurantii Immaturus percolate storage tank to pass the Fructus Aurantii Immaturus liquid in the Fructus Aurantii Immaturus percolate storage tank into the Fructus Aurantii Immaturus vacuum concentration tank;

[0028] S225, the ethanol vapor evaporated in the Fructus Aurantii Immaturus vacuum concentration tank enters the Fructus Aurantii Immaturus ethanol condenser for condensation, and the condensed ethanol vapor enters the Fructus Aurantii Immaturus ethanol recovery tank, and the extraction pump provided between the Fructus Aurantii Immaturus ethanol recovery tank and the Fructus Aurantii Immaturus ethanol storage tank is turned on to pass the ethanol liquid in the Fructus Aurantii Immaturus ethanol recovery tank into the Fructus Aurantii Immaturus ethanol storage tank;

[0029] S226, opening the metering pump provided between the Danzhi Fructus decompression concentration tank and the Zhi Fructus decompression concentration thick paste storage tank to pass the Zhi Fructus decompression concentration thick paste in the Zhi Fructus decompression concentration tank into the Zhi Fructus decompression concentration thick paste storage tank;

[0030] S227, opening the metering pump and the automatic control valve provided between the Fructus Aurantii Immaturus thick paste storage tank and the mixing tank to pass the Fructus Aurantii Immaturus fine powder in the Fructus Aurantii Immaturus thick paste storage tank into the mixing tank;

[0031] Or / and the method for controlling the fine angelica powder generated by the angelica paste preparation subsystem in step S23 includes the following steps:

[0032] S231, adding angelica to the angelica storage tank, and adding ethanol to the angelica ethanol storage tank;

[0033] S232, metering the angelica in the angelica storage tank into the angelica extraction tank by a metering screw conveyor provided between the angelica extraction tank and the angelica storage tank, and opening a metering pump and an automatic control valve provided between the angelica extraction tank and the angelica ethanol storage tank to allow the ethanol in the angelica ethanol storage tank to flow into the angelica extraction tank;

[0034] S233, turning on the extraction pump provided between the Angelica sinensis vacuum concentration tank and the Angelica sinensis extraction tank to pass the extract in the Angelica sinensis extraction tank into the Angelica sinensis vacuum concentration tank;

[0035] S234, the ethanol vapor evaporated in the Angelica sinensis vacuum concentration tank enters the Angelica sinensis ethanol condenser for condensation, and the condensed ethanol vapor enters the Angelica sinensis ethanol recovery tank, and the extraction pump provided between the Angelica sinensis ethanol recovery tank and the Angelica sinensis ethanol storage tank is turned on to pass the ethanol liquid in the Angelica sinensis ethanol recovery tank into the Angelica sinensis ethanol storage tank;

[0036] S235, turning on the metering pump provided between the angelica sinensis vacuum concentration tank and the angelica sinensis thick paste storage tank to pass the angelica sinensis thick paste in the angelica sinensis vacuum concentration tank into the angelica sinensis thick paste storage tank;

[0037] S236, opening the metering pump and the automatic control valve provided between the angelica paste storage tank and the mixing tank to pass the angelica powder in the angelica paste storage tank into the mixing tank;

[0038] Or / and the method for controlling the ginger liquor generated by the ginger preparation subsystem in step S25 includes the following steps:

[0039] S251, adding ginger into the ginger storage tank;

[0040] S252, using a ginger metering conveyor provided between the ginger decoction tank and the ginger storage tank to meter the ginger in the ginger storage tank and to open a metering pump and an automatic control valve provided between the ginger decoction tank and the water storage tank to allow the water in the water storage tank to flow into the ginger decoction tank;

[0041] S253, turning on the extraction pump provided between the ginger decoction pot and the ginger decoction liquid storage tank to pass the ginger liquid in the ginger decoction pot into the ginger decoction liquid storage tank;

[0042] S254, open the metering pump and the automatic control valve provided between the ginger decoction liquid storage tank and the mixing tank to pass the ginger liquid in the ginger decoction liquid storage tank into the mixing tank.

[0043] In a preferred embodiment of the present invention, the method for setting the production parameters of the Bao Xin Ning thick paste in step S1 includes the following steps:

[0044] S11, enter the Baoxinning thick paste production parameter setting interface;

[0045] S12, after entering the Bao Xin Ning thick paste production parameter setting interface, set the Bao Xin Ning thick paste production parameters on the Bao Xin Ning thick paste production parameter setting interface.

[0046] In a preferred embodiment of the present invention, in step S11, the production parameter setting interface of the Po Sin Ning thick paste includes:

[0047] One or any combination of the soaking time setting of Danshen powder in the Danshen percolation tank, the percolation flow rate setting of Danshen liquid in the Danshen percolation tank, the decoction time setting of Danshen filter residue in the Danshen filter residue boiling tank, the drying temperature setting of Danshen thick paste in the thick paste storage tank, and the quality setting of Danshen fine powder in the mixing tank;

[0048] One or any combination of parameter settings for soaking time of Citrus aurantium powder in the Citrus aurantium percolation tank, parameter settings for percolation flow rate of Citrus aurantium powder in the Citrus aurantium percolation tank, parameter settings for drying temperature of Citrus aurantium thick paste in the Citrus aurantium thick paste storage tank, and parameter settings for quality of Citrus aurantium fine powder in the mixing tank;

[0049] One or any combination of the drying temperature parameter setting of the angelica paste in the angelica paste storage tank and the quality parameter setting of the angelica powder in the mixing tank;

[0050] One or any combination of the mesh sieve parameter setting of the Panax notoginseng powder in the Panax notoginseng powder storage tank and the quality parameter setting of the Panax notoginseng powder in the mixing tank;

[0051] One or any combination of the parameter settings of the decoction time of ginger in the ginger decoction pot and the parameter settings of the amount of water supplied to the ginger decoction pot.

[0052] In a preferred embodiment of the present invention, the method for setting the production parameters of the Po Sin Ning Thick Cream on the Po Sin Ning Thick Cream production parameter setting interface in step S12 comprises the following steps:

[0053] S121, modify or keep unchanged the parameters required to be set in the Baoxinning Thick Cream production parameter setting interface;

[0054] S122, determine whether to trigger the save control command:

[0055] If the save control command is triggered, a password input box will pop up;

[0056] If the save control command is not triggered, continue waiting and execute step S122;

[0057] S123: After entering the password in the pop-up password input box, save the changed parameter settings or do not save the changed parameter settings.

[0058] In a preferred embodiment of the present invention, after a password is entered in the pop-up password input box in step S123, the working method of saving the changed parameter settings or not saving the changed parameter settings includes the following steps:

[0059] S1231, after each password character is input, rearrange the characters in the character area on the virtual keyboard;

[0060] S1232, obtain all password characters entered;

[0061] S1233, rearrange all the obtained password characters:

[0062] S1234: Determine whether the rearranged password characters are consistent with the password characters stored in the system:

[0063] If the rearranged password characters are consistent with the password characters stored in the system, the changed parameter settings are saved;

[0064] If the rearranged password characters are inconsistent with the password characters stored in the system, re-enter the password characters. After multiple judgments, if the rearranged password characters are still inconsistent with the password characters stored in the system, the changed parameter settings will not be saved.

[0065] The present invention also discloses a computer system, comprising:

[0066] processor;

[0067] a memory for storing processor-executable instructions;

[0068] Wherein, the processor is configured to implement the automated production method of Bao Xin Ning thick paste when executing the executable instructions.

[0069] The present invention also discloses a computer-readable storage medium, comprising:

[0070] a memory having a computer program stored thereon;

[0071] A processor is used to execute the program in the memory to implement the automated production method of Bao Xin Ning thick paste.

[0072] The present invention also discloses an automated production system for Baoxinning thick paste, which includes a salvia miltiorrhiza thick paste preparation subsystem, a fructus aurantii thick paste preparation subsystem, a angelica thick paste preparation subsystem, a ginger preparation subsystem, and a mixing tank. The salvia miltiorrhiza fine powder, fructus aurantii thick paste preparation subsystem, angelica thick paste preparation subsystem, and ginger preparation subsystem are respectively generated by the salvia miltiorrhiza thick paste preparation subsystem, fructus aurantii thick paste preparation subsystem, angelica thick paste preparation subsystem, and ginger preparation subsystem and enter the mixing tank equipped with a stirrer.

[0073] The salvia miltiorrhiza thick paste preparation subsystem includes a salvia miltiorrhiza percolation tank, the salvia miltiorrhiza inlet at the top of the salvia miltiorrhiza percolation tank is connected to the salvia miltiorrhiza powder storage tank through a metering screw conveyor, the ethanol inlet at the top of the salvia miltiorrhiza percolation tank is connected to the salvia miltiorrhiza ethanol storage tank through a pipeline, the percolation liquid outlet of the salvia miltiorrhiza percolation tank is connected to the salvia miltiorrhiza percolation liquid storage tank, the salvia miltiorrhiza percolation tank filter residue outlet is connected to a screw conveyor, and the filter residue is conveyed to the salvia miltiorrhiza filter residue boiling tank through the screw conveyor, the water inlet of the salvia miltiorrhiza filter residue boiling tank is connected to the water storage tank through a pipeline, a heating interlayer is provided on the outside of the salvia miltiorrhiza filter residue boiling tank, and the salvia miltiorrhiza filter residue boiling tank is connected to the water storage tank through a pipeline. The boiling liquid outlet of the cooking pot is connected to the Danshen percolate storage tank through a pipeline, the liquid outlet of the Danshen percolate storage tank is connected to the Danshen concentration tank through a pipeline, the ethanol vapor outlet at the top of the Danshen concentration tank is connected to the Danshen ethanol condenser, the condensed ethanol outlet end of the Danshen ethanol condenser is connected to the Danshen ethanol recovery tank, the bottom of the Danshen concentration tank is equipped with a Danshen concentration reboiler, the reboiler outlet at the bottom of the Danshen concentration tank is connected to the Danshen concentration reboiler inlet, the Danshen concentration reboiler outlet is connected to the reboiler inlet at the bottom of the Danshen concentration tank, and the material outlet of the Danshen concentration tank is connected to the Danshen thick paste storage tank through a pipeline;

[0074] The thick paste outlet of the Danshen thick paste storage tank, the Citrus aurantium thick paste preparation subsystem, the Angelica sinensis thick paste preparation subsystem, and the ginger preparation subsystem are respectively connected to the material inlet pipeline of the mixing tank through pipelines. The mixing tank is also provided with a fine powder inlet for placing Panax notoginseng fine powder. The fine powder inlet is connected to the Panax notoginseng powder storage tank through a metering screw conveyor, and an agitator is provided in the mixing tank.

[0075] In a preferred embodiment of the present invention, the Danshen ethanol recovery tank is connected to the Danshen ethanol storage tank through a pipeline.

[0076] In a preferred embodiment of the present invention, the Fructus Citri Aurantii thick paste preparation subsystem includes a Fructus Citri Aurantii thick paste storage tank and a Fructus Citri Aurantii percolation tank, the Fructus Citri Aurantii inlet at the top of the Fructus Citri Aurantii percolation tank is connected to the Fructus Citri Aurantii powder storage tank through a metering screw conveyor, the ethanol inlet at the top of the Fructus Citri Aurantii percolation tank is connected to the Fructus Citri Aurantii ethanol storage tank through a pipeline, the percolation liquid outlet at the bottom of the Fructus Citri Aurantii percolation tank is connected to the Fructus Citri Aurantii percolation liquid storage tank, the liquid outlet of the Fructus Citri Aurantii percolation liquid storage tank is connected to the Fructus Citri Aurantii decompression concentration tank through a pipeline, and the top of the Fructus Citri Aurantii decompression concentration tank is connected to the Fructus Citri Aurantii decompression concentration tank. The ethanol vapor outlet is connected to the Fructus Aurantii ethanol condenser, the condensed ethanol outlet of the Fructus Aurantii ethanol condenser is connected to the Fructus Aurantii ethanol recovery tank, the bottom of the Fructus Aurantii decompression concentration tank is equipped with a Fructus Aurantii concentrating reboiler, the reboiler outlet at the bottom end of the Fructus Aurantii concentrating tank is connected to the inlet of the Fructus Aurantii concentrating reboiler, the outlet of the Fructus Aurantii concentrating reboiler is connected to the reboiler inlet at the bottom end of the Fructus Aurantii concentrating tank, the material outlet of the Fructus Aurantii concentrating tank is connected to the Fructus Aurantii thick paste storage tank through a pipeline, and the thick paste outlet of the Fructus Aurantii thick paste storage tank is connected to the mixing tank through a pipeline.

[0077] In a preferred embodiment of the present invention, the ginger preparation subsystem includes a ginger decoction pot, the water inlet at the top of the ginger decoction pot is connected to a water storage tank; the decoction liquid outlet of the ginger decoction pot is connected to the ginger decoction liquid storage tank, and the ginger decoction liquid storage tank is connected to a mixing tank through a pipeline.

[0078] In a preferred embodiment of the present invention, the angelica thick paste preparation subsystem includes an angelica thick paste storage tank and an angelica extraction tank, the top of the angelica extraction tank is provided with an angelica inlet, the ethanol inlet at the top of the angelica extraction tank is connected to the angelica ethanol storage tank through a pipeline, the extract outlet of the angelica extraction tank is connected to the angelica vacuum concentration tank, the bottom of the angelica vacuum concentration tank is equipped with an angelica concentration reboiler, the reboiler outlet at the bottom of the angelica vacuum concentration tank is connected to the angelica concentration reboiler inlet, the angelica concentration reboiler outlet is connected to the reboiler inlet at the bottom of the angelica vacuum concentration tank, the material outlet of the angelica vacuum concentration tank is connected to the angelica thick paste storage tank through a pipeline, the ethanol vapor outlet at the top of the angelica vacuum concentration tank is connected to the angelica ethanol condenser, the condensed ethanol outlet of the angelica ethanol condenser is connected to the angelica ethanol recovery tank, and the angelica ethanol recovery tank is connected to the angelica ethanol storage tank through a pipeline.

[0079] In a preferred embodiment of the present invention, the Fructus Aurantii Immaturus decompression concentration tank and the Danggui Sinensis decompression concentration tank are both provided with a vacuum outlet, a valve is provided at the vacuum outlet, and the vacuum outlet is connected to a vacuum pumping device.

[0080] In a preferred embodiment of the present invention, metering pumps and automatic control valves are respectively provided on the pipelines connecting the Danshen thick paste outlet of the storage tank, the Citrus aurantium thick paste preparation subsystem, the Angelica thick paste preparation subsystem, the ginger preparation subsystem and the mixing tank.

[0081] In a preferred embodiment of the present invention, a metering pump and an automatic control valve are respectively provided on the pipeline connecting the Danshen percolation tank and the Danshen ethanol storage tank, the pipeline connecting the Fructus Aurantii percolation tank and the Fructus Aurantii ethanol storage tank, and the pipeline connecting the Angelica sinensis extraction tank and the Angelica sinensis ethanol storage tank.

[0082] In a preferred embodiment of the present invention, a ginger metering conveyor is provided on the ginger inlet at the top of the ginger decoction pot.

[0083] In summary, due to the adoption of the above-mentioned technical solution, the present invention utilizes salvia miltiorrhiza extractor via percolation followed by decoction, enabling more efficient extraction of its active ingredients and avoiding waste of medicinal materials. The present invention utilizes an automatic metering pump or metering bolt conveyor to meter and deliver materials, enabling automated, unmanned production, improving production efficiency, reducing human pollution, and lowering worker labor intensity. Furthermore, production parameter settings can be safely changed, ensuring automated production of Baoxinning thick paste.

[0084] Additional aspects and advantages of the present invention will be set forth in part in the description which follows and, in part, will be obvious from the description which follows, or may be learned by practice of the present invention. BRIEF DESCRIPTION OF THE DRAWINGS

[0085] The above and / or additional aspects and advantages of the present invention will become apparent and readily understood from the following description of the embodiments with reference to the accompanying drawings, in which:

[0086] Figure 1 It is a schematic block diagram of the process of the present invention.

[0087] Figure 2 It is a schematic block diagram of the system connection of the present invention. DETAILED DESCRIPTION

[0088] The following describes embodiments of the present invention in detail. Examples of the embodiments are shown in the accompanying drawings, wherein the same or similar reference numerals throughout represent the same or similar elements or elements having the same or similar functions. The embodiments described below with reference to the accompanying drawings are exemplary and are intended only to explain the present invention and are not to be construed as limiting the present invention.

[0089] The present invention provides a method for automatically producing Baoxinning thick paste. Figure 1 As shown, the following steps are included:

[0090] S1, set the production parameters of Baoxinning thick paste;

[0091] S2, producing the Bao Xin Ning thick paste according to the production parameters of the Bao Xin Ning thick paste set in step S1.

[0092] In a preferred embodiment of the present invention, the production control method of the Bao Xin Ning thick paste in step S2 includes the following steps:

[0093] S21, adding the Danshen fine powder produced by the Danshen thick paste preparation subsystem to the mixing tank 43;

[0094] S22, adding the Fructus Aurantii Immaturus fine powder generated by the Fructus Aurantii Immaturus thick paste preparation subsystem to the mixing tank 43;

[0095] S23, adding the fine angelica powder produced by the angelica paste preparation subsystem to the mixing tank 43;

[0096] S24, adding the notoginseng powder to the mixing tank 43; generally, first adding the notoginseng powder to the notoginseng powder storage tank 44, and then metering the notoginseng powder in the notoginseng powder storage tank 44 to the mixing tank 43 through a metering screw conveyor provided between the notoginseng powder storage tank 44 and the mixing tank 43, wherein the notoginseng powder in the notoginseng powder storage tank 44 is crushed and passed through a 90-100 mesh sieve;

[0097] S25, adding the ginger liquid generated by the ginger preparation subsystem to the mixing tank 43;

[0098] S26, mixing the materials added into the mixing tank 43.

[0099] In a preferred embodiment of the present invention, the control working method of generating Danshen fine powder in the Danshen thick paste preparation subsystem in step S21 includes the following steps:

[0100] S211, adding salvia miltiorrhiza powder to the salvia miltiorrhiza powder storage tank 11b, adding ethanol liquid to the salvia miltiorrhiza ethanol storage tank 12, and adding water to the water storage tank 13;

[0101] S212, the Danshen powder in Danshen powder storage tank 11b is metered and conveyed to Danshen percolation tank 11 by a metering screw conveyor provided between Danshen percolation tank 11 and Danshen powder storage tank 11b, and the metering pump and automatic control valve provided between Danshen percolation tank 11 and Danshen ethanol storage tank 12 are opened to allow the ethanol in Danshen ethanol storage tank 12 to be introduced into Danshen percolation tank 11; the amount of ethanol introduced depends on the amount of Danshen powder. Generally, Danshen powder is soaked in ethanol for 20 to 28 hours, the percolation flow rate is 2.5 to 5.5 ml / min, and 4 times the amount of percolation liquid enters Danshen percolation liquid storage tank 15;

[0102] S213, the percolation liquid in the Danshen percolation tank 11 is passed into the Danshen percolation liquid storage tank 15, and the Danshen residue in the Danshen percolation tank 11 is conveyed to the Danshen residue decoction tank 14 via a screw conveyor provided between the Danshen percolation tank 11 and the Danshen residue decoction tank 14. The metering pump and automatic control valve provided between the water storage tank 13 and the Danshen residue decoction tank 14 are opened to allow water in the water storage tank 13 to pass into the Danshen residue decoction tank 14; the amount of water introduced depends on the amount of Danshen residue; generally, 6 to 8 times the amount of water is used for decoction for 2 to 2.5 hours;

[0103] S214, turning on the extraction pump provided between the Danshen residue boiling tank 14 and the Danshen percolation liquid storage tank 15 to pass the Danshen filtrate prepared in the Danshen residue boiling tank 14 into the Danshen percolation liquid storage tank 15;

[0104] S215, turning on the extraction pump provided between the Danshen concentration tank 18 and the Danshen percolation liquid storage tank 15 to pass the Danshen liquid in the Danshen percolation liquid storage tank 15 into the Danshen concentration tank 18;

[0105] S216, the evaporated ethanol vapor in the Danshen concentration tank 18 enters the Danshen ethanol condenser 16 for condensation, and the condensed ethanol vapor enters the Danshen ethanol recovery tank 17, and the extraction pump provided between the Danshen ethanol recovery tank 17 and the Danshen ethanol storage tank 12 is turned on to pass the ethanol liquid in the Danshen ethanol recovery tank 17 into the Danshen ethanol storage tank 12;

[0106] S217, turning on the metering pump provided between the Danshen concentrate tank 18 and the Danshen paste storage tank 19 to pass the Danshen paste in the Danshen concentrate tank 18 into the Danshen paste storage tank 19; generally, the Danshen paste passed into the Danshen paste storage tank 19 is dried at a temperature below 70° C. to 75° C. and crushed through a 55-60 mesh sieve to form Danshen fine powder;

[0107] S218, open the metering pump and the automatic control valve provided between the Danshen paste storage tank 19 and the mixing tank 43 to pass the Danshen fine powder in the Danshen paste storage tank 19 into the mixing tank 43. Generally, 160g to 170g of Danshen fine powder is passed in.

[0108] In a preferred embodiment of the present invention, the method for controlling the Fructus Aurantii Immaturus fine powder generated by the Fructus Aurantii Immaturus thick paste preparation subsystem in step S22 comprises the following steps:

[0109] S221, adding Fructus Aurantii powder to the Fructus Aurantii powder storage tank, and adding ethanol liquid to the Fructus Aurantii ethanol storage tank 22;

[0110] S222, the Fructus Aurantii Immaturus powder in the Fructus Aurantii Immaturus powder storage tank is metered and transported to the Fructus Aurantii Immaturus percolation tank 21 by a metering screw conveyor provided between the Fructus Aurantii Immaturus percolation tank 21 and the Fructus Aurantii Immaturus powder storage tank, and the metering pump and automatic control valve provided between the Fructus Aurantii Immaturus percolation tank 21 and the Fructus Aurantii Immaturus ethanol storage tank 22 are opened to pass the ethanol in the Fructus Aurantii Immaturus ethanol storage tank 22 into the Fructus Aurantii Immaturus percolation tank 21; the amount of ethanol introduced is related to the amount of Fructus Aurantii Immaturus powder. Generally, the Fructus Aurantii Immaturus powder is soaked in ethanol for 20 h to 28 h, the percolation flow rate is 2.5 to 5.5 ml / min, and 4 times the amount of percolated liquid enters the Fructus Aurantii Immaturus percolation tank 21;

[0111] S223, passing the percolation liquid in the Fructus Aurantii percolation tank 21 into the Fructus Aurantii percolation liquid storage tank 23;

[0112] S224, turning on the extraction pump provided between the Fructus Aurantii Immaturus vacuum concentration tank 24 and the Fructus Aurantii Immaturus percolate storage tank 23 to pass the Fructus Aurantii Immaturus liquid in the Fructus Aurantii Immaturus percolate storage tank 23 into the Fructus Aurantii Immaturus vacuum concentration tank 24;

[0113] S225, the ethanol vapor evaporated in the Fructus Aurantii Immaturus decompression concentration tank 24 enters the Fructus Aurantii Immaturus ethanol condenser 25 for condensation, and the condensed ethanol vapor enters the Fructus Aurantii Immaturus ethanol recovery tank 26, and the extraction pump provided between the Fructus Aurantii Immaturus ethanol recovery tank 26 and the Fructus Aurantii Immaturus ethanol storage tank 22 is turned on to pass the ethanol liquid in the Fructus Aurantii Immaturus ethanol recovery tank 26 into the Fructus Aurantii Immaturus ethanol storage tank 22;

[0114] S226, opening the metering pump provided between the Danzhi Fructus decompression concentration tank 24 and the Zhi Fructus decompression concentration tank 27 to pass the Zhi Fructus decompression concentration tank 24 into the Zhi Fructus decompression concentration tank 27; generally, the Zhi Fructus decompression concentration tank 27 is dried at a temperature below 70° C. to 75° C., crushed through a 55-60 mesh sieve, and formed Zhi Fructus fine powder;

[0115] S227, open the metering pump and the automatic control valve provided between the thick paste storage tank 27 and the mixing tank 43 to pass the Fructus Aurantii Immaturus powder in the thick paste storage tank 27 into the mixing tank 43. Generally, 80g to 90g of the Fructus Aurantii Immaturus powder is passed into the mixing tank 43.

[0116] In a preferred embodiment of the present invention, the method for controlling the fine angelica powder generated by the angelica paste preparation subsystem in step S23 includes the following steps:

[0117] S231, adding angelica to the angelica storage tank, and adding ethanol to the angelica ethanol storage tank 37;

[0118] S232, the angelica in the angelica storage tank is metered and conveyed into the angelica extraction tank 31 by a metering screw conveyor provided between the angelica extraction tank 31 and the angelica storage tank. Furthermore, a metering pump and an automatic control valve provided between the angelica extraction tank 31 and the angelica ethanol storage tank 37 are opened to allow the ethanol in the angelica ethanol storage tank 37 to be introduced into the angelica extraction tank 31. The amount of ethanol introduced depends on the amount of angelica. Generally, reflux extraction (75% ethanol) is performed twice (six times the amount each time, for 6 to 7 hours), and the extracts are combined.

[0119] S233, turning on the extraction pump provided between the Angelica sinensis vacuum concentration tank 32 and the Angelica sinensis extraction tank 31 to pass the extract in the Angelica sinensis extraction tank 31 into the Angelica sinensis vacuum concentration tank 32;

[0120] In step S234, the ethanol vapor evaporated from the Angelica sinensis vacuum concentration tank 32 enters the Angelica sinensis ethanol condenser 35 for condensation, and the condensed ethanol vapor enters the Angelica sinensis ethanol recovery tank 36. The extraction pump provided between the Angelica sinensis ethanol recovery tank 36 and the Angelica sinensis ethanol storage tank 37 is turned on to pass the ethanol liquid in the Angelica sinensis ethanol recovery tank 36 into the Angelica sinensis ethanol storage tank 37.

[0121] S235: Turn on the metering pump provided between the angelica sinensis vacuum concentration tank 32 and the angelica sinensis paste storage tank 34 to pass the angelica sinensis paste in the angelica sinensis vacuum concentration tank 32 into the angelica sinensis paste storage tank 34. Generally, the angelica sinensis paste passed into the angelica sinensis paste storage tank 34 is dried at a temperature below 70° C. to 75° C. and crushed through a 55-60 mesh sieve to form angelica sinensis fine powder.

[0122] S236, open the metering pump and the automatic control valve provided between the angelica paste storage tank 34 and the mixing tank 43 to pass the angelica powder in the angelica paste storage tank 34 into the mixing tank 43. Generally, 80g to 90g of angelica powder is passed into the mixing tank.

[0123] In a preferred embodiment of the present invention, the method for controlling the ginger liquor generated by the ginger preparation subsystem in step S25 includes the following steps:

[0124] S251, adding ginger into the ginger storage tank;

[0125] S252: The ginger in the ginger storage tank is metered and conveyed into the ginger decoction tank 41 via a ginger metering conveyor provided between the ginger decoction tank 41 and the ginger storage tank. Furthermore, the metering pump and the automatic control valve provided between the ginger decoction tank 41 and the water storage tank 13 are opened to allow water in the water storage tank 13 to flow into the ginger decoction tank 41. The amount of water to be introduced depends on the amount of ginger. Generally, six times the amount of water is added, and the ginger is decocted twice, each time for two hours, with a ginger content of 600g to 650g.

[0126] S253, turning on the extraction pump provided between the ginger decoction pot 41 and the ginger decoction liquid storage tank 42 to pass the ginger liquid in the ginger decoction pot 41 into the ginger decoction liquid storage tank 42;

[0127] S254: The metering pump and automatic control valve between the ginger decoction liquid storage tank 42 and the mixing tank 43 are opened to allow the ginger liquid in the ginger decoction liquid storage tank 42 to flow into the mixing tank 43. Generally, the amount of ginger liquid introduced is proportional to the amount of Danshen fine powder, Citrus aurantium fine powder, Angelica sinensis fine powder, and Panax notoginseng powder, which are then mixed uniformly in the mixing tank 43. The Baoxinning in the mixing tank 43 is dried, crushed, sieved, and capsuled to produce 950-1050 capsules, which are then packaged separately.

[0128] In a preferred embodiment of the present invention, the method for setting the production parameters of the Bao Xin Ning thick paste in step S1 includes the following steps:

[0129] S11, enter the Baoxinning thick paste production parameter setting interface;

[0130] S12, after entering the Bao Xin Ning thick paste production parameter setting interface, set the Bao Xin Ning thick paste production parameters on the Bao Xin Ning thick paste production parameter setting interface.

[0131] In a preferred embodiment of the present invention, in step S11, the production parameter setting interface of the Po Sin Ning thick paste includes:

[0132] One or any combination of the soaking time of Danshen powder in Danshen percolation tank 11, the percolation flow rate of Danshen liquid in Danshen percolation tank 11, the decoction time of Danshen filter residue in Danshen filter residue boiling tank 14, the drying temperature of Danshen thick paste in thick paste storage tank 19, and the quality of Danshen fine powder in mixing tank 43;

[0133] One or any combination of the parameters for soaking the Fructus Aurantii Immaturus powder in the Fructus Aurantii Immaturus percolation tank 21, the parameters for percolation flow rate of the Fructus Aurantii Immaturus powder in the Fructus Aurantii Immaturus percolation tank 21, the parameters for drying the Fructus Aurantii Immaturus thick paste in the Fructus Aurantii Immaturus thick paste storage tank 27, and the parameters for quality of the Fructus Aurantii Immaturus fine powder in the mixing tank 43;

[0134] One or any combination of the drying temperature parameter setting of the angelica paste in the angelica paste storage tank 34 and the quality parameter setting of the angelica powder in the mixing tank 43;

[0135] One or any combination of the mesh sieve parameter setting of the Panax notoginseng powder in the Panax notoginseng powder storage tank 44 and the quality parameter setting of the Panax notoginseng powder in the mixing tank 43;

[0136] One or any combination of the parameter settings of the decoction time of ginger in the ginger decoction pot 41 and the parameter settings of the amount of water introduced into the ginger decoction pot 41.

[0137] In a preferred embodiment of the present invention, the method for setting the production parameters of the Po Sin Ning Thick Cream on the Po Sin Ning Thick Cream production parameter setting interface in step S12 comprises the following steps:

[0138] S121, modify or keep unchanged the parameters required to be set in the Baoxinning Thick Cream production parameter setting interface;

[0139] S122, determine whether to trigger the save control command:

[0140] If the save control command is triggered, a password input box will pop up;

[0141] If the save control command is not triggered, continue waiting and execute step S122;

[0142] S123: After entering the password in the pop-up password input box, save the changed parameter settings or do not save the changed parameter settings.

[0143] In a preferred embodiment of the present invention, after a password is entered in the pop-up password input box in step S123, the working method of saving the changed parameter settings or not saving the changed parameter settings includes the following steps:

[0144] S1231, after each password character is input, rearrange the characters in the character area on the virtual keyboard:

[0145] The original character arrangement of the character area is:

[0146] `1234567890-=

[0147] qwertyuiop[]

[0148] asdfghjkl;'\

[0149] zxcvbnm,. /

[0150] After pressing Caps Lock, the original character arrangement of the character area is:

[0151] `1234567890-=

[0152] QWERTYUIOP[]

[0153] ASDFGHJKL;'\

[0154] ZXCVBNM,. /

[0155] After pressing Shift, the original character arrangement in the character area is:

[0156] ~! @#$%^&*()_+

[0157] qwertyuiop{}

[0158] asdfghjkl:”|

[0159] zxcvbnm<>?

[0160] S12311: Obtain the timestamp of each character input. For example, the timestamp of 11:38:43:678 on April 8, 2025 is 1744083523678; the timestamp of 22:48:47:99 on March 9, 2025 is 1741531727099.

[0161] S12312, use the timestamp and each character to calculate the rearrangement value:

[0162] compare j =comvalue(char j time),

[0163] compare j is the rearrangement value of the jth character; j = 1, 2, 3, ..., 45;

[0164] time is the timestamp;

[0165] comvalue() is the calculation method of the rearrangement value, preferably using the SHA-3(64) algorithm;

[0166] char j is the jth character from left to right and from top to bottom in the character area; for example, char 22 is o, which is the 9th character in the second row of the character area; char 29 f, which is the fourth character in the third row of the character area; after pressing Caps Lock, char 22 O, char 29 F, char 35 is;, that is, the 10th character in the third row of the character area; after pressing shift, char 22 For o, char29 f, 3 chars 35 is :, char4 is #, which is the fourth character in the first row of the character area;

[0167] S12313, sort all rearranged values from largest to smallest;

[0168] S12314: Arrange all characters corresponding to the rearranged values from left to right and from top to bottom as rearranged characters.

[0169] Take the character `123 in the character area and the timestamp 1754918907056 as an example:

[0170] The first step is to get the timestamp of inputting a character, which is 1754918907056;

[0171] The second step is to calculate the reordering value using the timestamp and each character:

[0172] compare1=comvalue(char1time)=comvalue(`1754918907056)=1001011001101100111011010110100000111010001000011110101001011000;

[0173] compare2=comvalue(char2time)=comvalue(11754918907056)=0000011011101100111010101010011001000111001111010001011001001001;

[0174] compare3=comvalue(char3time)=comvalue(21754918907056)=0110011010101110111101101011110001000001101011011000001110000100;

[0175] compare4=comvalue(char4time)=comvalue(31754918907056)=0001101100010101101100000010111001011100010000110011011001000111;

[0176] The third step is to arrange all the rearrangement values from large to small:

[0177] compare1>compare3>compare4>compare2;

[0178] In the fourth step, the characters corresponding to all rearranged values are:

[0179] `231;

[0180] Therefore, the characters `123 in the character area are rearranged to `231.

[0181] S1232, obtain all password characters entered;

[0182] S1233, rearrange all the obtained password characters:

[0183] Check whether the last character of the password is 1 to 9:

[0184] If the last password character is one of 1 to 9, the last password character is moved forward by |L1-L2|, where L1 is the number of digits of all password characters obtained; L2 is the last password character;

[0185] If the last character of the password is not one of 1 to 9, move the last character of the password forward. L1 is the number of digits of all password characters obtained; It is the rounding down algorithm;

[0186] For example, if all the password characters obtained are pd2025Wgood, then the rearranged characters are pd202d5Wgoo; if all the password characters obtained are pd2025Wgood3, then the rearranged characters are pd32025Wgood;

[0187] S1234: Determine whether the rearranged password characters are consistent with the password characters stored in the system:

[0188] If the rearranged password characters are consistent with the password characters stored in the system, the changed parameter settings are saved;

[0189] If the rearranged password characters are inconsistent with the password characters stored in the system, re-enter the password characters. After multiple judgments, if the rearranged password characters are still inconsistent with the password characters stored in the system, the changed parameter settings will not be saved.

[0190] The present invention also discloses a computer system, comprising:

[0191] processor;

[0192] a memory for storing processor-executable instructions;

[0193] Wherein, the processor is configured to implement the automated production method of Bao Xin Ning thick paste when executing the executable instructions.

[0194] The present invention also discloses a computer-readable storage medium, comprising:

[0195] a memory having a computer program stored thereon;

[0196] A processor is used to execute the program in the memory to implement the automated production method of Bao Xin Ning thick paste.

[0197] The present invention also discloses an automated production system for Baoxinning thick paste, such as Figure 2 As shown, it includes a Danshen thick paste preparation subsystem, a Citrus aurantium thick paste preparation subsystem, an Angelica thick paste preparation subsystem, a ginger preparation subsystem and a mixing tank 43.

[0198] The Danshen thick paste preparation subsystem includes a Danshen percolation tank 11. This percolation tank 11 is conventional and will not be described in detail here. The Danshen inlet at the top of the Danshen percolation tank 11 is connected to a Danshen powder storage tank 11b via a metering screw conveyor. The ethanol inlet at the top of the Danshen percolation tank 11 is connected via a pipeline to a Danshen ethanol storage tank 12. The percolation liquid outlet of the Danshen percolation tank 11 is connected to a Danshen percolation storage tank 15. The residue outlet of the Danshen percolation tank 11 is connected to a screw conveyor 11a, which conveys the residue to a Danshen residue decoction tank 14. The water inlet of the Danshen residue decoction tank 14 is connected via a pipeline to a water storage tank 13. A heating interlayer is provided outside the Danshen residue decoction tank 14. The decoction liquid outlet of the Danshen residue decoction tank 14 is connected via a pipeline to a Danshen percolation storage tank 15. The liquid outlet of the Danshen percolation storage tank 15 is also connected via a pipeline to a Danshen concentration tank 18. The ethanol vapor outlet at the top of Danshen concentration tank 18 is connected to Danshen ethanol condenser 16. The condensed ethanol outlet of Danshen ethanol condenser 16 is connected to Danshen ethanol recovery tank 17, which is connected to Danshen ethanol storage tank 12 via a pipeline. Danshen ethanol condenser 16 is prior art and includes a tube layer and a shell layer. Condensate is passed through the shell layer, and ethanol enters the tube layer. After condensation of the condensate in the shell layer, ethanol enters Danshen ethanol recovery tank 17. The subsequent Fructus Aurantii Immaturus ethanol condenser and Angelica Sinensis ethanol condenser are similar to the Danshen ethanol condenser and are also prior art.

[0199] The bottom of the Danshen concentration tank 18 is equipped with a Danshen concentration reboiler 18a, the reboiler outlet at the bottom of the Danshen concentration tank 18 is connected to the inlet of the Danshen concentration reboiler 18a, the outlet of the Danshen concentration reboiler 18a is connected to the reboiler inlet at the bottom of the Danshen concentration tank 18, and the material outlet of the Danshen concentration tank 18 is connected to the Danshen thick paste storage tank 19 through a pipeline.

[0200] The thick paste outlet of Danshen thick paste storage tank 19, the Fructus Aurantii thick paste preparation subsystem, the Angelica sinensis thick paste preparation subsystem, and the ginger preparation subsystem are each connected via pipelines to the material inlet pipeline of mixing tank 43. Mixing tank 43 is also provided with a fine powder feed port 43a for adding Panax notoginseng fine powder. Fine powder feed port 43a is connected to Panax notoginseng powder storage tank 44 via a metering screw conveyor. Mixing tank 43 is equipped with an agitator. The metering screw conveyor is a type of screw conveyor used for continuous weighing and batch feeding of powdered or bulk materials. This is a prior art device and will not be described in detail here.

[0201] The Fructus Citri Aurantii thick paste preparation subsystem includes a Fructus Citri Aurantii thick paste storage tank 27 and a Fructus Citri Aurantii percolation tank 21. The Fructus Citri Aurantii inlet at the top of the Fructus Citri Aurantii percolation tank 21 is connected to the Fructus Citri Aurantii powder storage tank through a metering screw conveyor. The ethanol inlet at the top of the Fructus Citri Aurantii percolation tank 21 is connected to the Fructus Citri Aurantii ethanol storage tank 22 through a pipeline. The percolation liquid outlet at the bottom of the Fructus Citri Aurantii percolation tank 21 is connected to the Fructus Citri Aurantii percolation storage tank 23. The liquid outlet of the Fructus Citri Aurantii percolation storage tank 23 is connected to the Fructus Citri Aurantii decompression concentration tank 24 through a pipeline. The ethanol vapor outlet at the top of the Fructus Citri Aurantii decompression concentration tank 24 is connected to the The Fructus Aurantii Immaturus ethanol condenser 25, the condensed ethanol outlet of the Fructus Aurantii Immaturus ethanol condenser 25 is connected to the Fructus Aurantii Immaturus ethanol recovery tank 26, the Fructus Aurantii Immaturus decompression concentration tank 24 is equipped with a Fructus Aurantii Immaturus concentration reboiler 28 at the bottom, the reboiler outlet at the bottom end of the Fructus Aurantii Immaturus concentration tank 28 is connected to the inlet of the Fructus Aurantii Immaturus concentration reboiler 28, the Fructus Aurantii Immaturus concentration reboiler 28 outlet is connected to the reboiler inlet at the bottom end of the Fructus Aurantii Immaturus concentration tank 28, the material outlet of the Fructus Aurantii Immaturus concentration tank 28 is connected to the Fructus Aurantii Immaturus thick paste storage tank 27 through a pipeline, and the thick paste outlet of the Fructus Aurantii Immaturus thick paste storage tank 27 is connected to the mixing tank 43 through a pipeline.

[0202] The ginger preparation subsystem includes a ginger decoction tank 41, with a ginger metering conveyor installed at the ginger inlet at the top of the decoction tank 41. The water inlet at the top of the decoction tank 41 is connected to the water storage tank 13. The decoction liquid outlet of the decoction tank 41 is connected to the ginger decoction liquid storage tank 42, which is connected to the mixing tank 43 via a pipeline.

[0203] The angelica thick paste preparation subsystem includes an angelica thick paste storage tank 34 and an angelica extraction tank 31. The top of the angelica extraction tank 31 is provided with an angelica inlet, which is connected to the angelica storage tank via a metering screw conveyor. The ethanol inlet at the top of the angelica extraction tank 31 is connected to the angelica ethanol storage tank 37 via a pipeline, and the extract outlet of the angelica extraction tank 31 is connected to the angelica vacuum concentration tank 32. The bottom of the angelica vacuum concentration tank 32 is equipped with an angelica concentration reboiler 33, and the reboiler outlet at the bottom of the angelica vacuum concentration tank 32 is connected to the inlet of the angelica concentration reboiler 33. The outlet of the angelica concentration reboiler 33 is connected to the reboiler inlet at the bottom of the angelica vacuum concentration tank 32, and the material outlet of the angelica vacuum concentration tank 32 is connected to the angelica thick paste storage tank 34 via a pipeline. The ethanol vapor outlet at the top of the Angelica sinensis vacuum concentration tank 32 is connected to the Angelica sinensis ethanol condenser 35, and the condensed ethanol outlet of the Angelica sinensis ethanol condenser 35 is connected to the Angelica sinensis ethanol recovery tank 36, and the Angelica sinensis ethanol recovery tank is connected to the Angelica sinensis ethanol storage tank 37 through a pipeline.

[0204] Both the Fructus Aurantii Immaturus decompression concentration tank 24 and the Danggui Sinensis decompression concentration tank 32 are provided with a vacuum outlet, a valve is provided at the vacuum outlet, and the vacuum outlet is connected to a vacuum pumping device.

[0205] Metering pumps a and automatic control valves b are installed on the pipelines connecting the Danshen thick paste outlet of Danshen thick paste storage tank 19, the Fructus Aurantii thick paste preparation subsystem, the Fructus Angelicae Sinensis thick paste preparation subsystem, and the ginger preparation subsystem to mixing tank 43. Metering pumps a and automatic control valves b are installed on the pipelines connecting Danshen percolation tank 11 to Danshen ethanol storage tank 12, the pipelines connecting Fructus Aurantii percolation tank 21 to Fructus Aurantii ethanol storage tank 22, and the pipelines connecting Fructus Angelicae Sinensis extraction tank 31 to Fructus Angelicae Sinensis ethanol storage tank 37. Extraction pumps c are installed on all remaining pipelines.

[0206] Among them, the Danshen concentration tank 18, the Citrus aurantium vacuum concentration tank 24, the Angelica sinensis vacuum concentration tank 32 and the Angelica sinensis extraction tank 31 are all existing technologies and will not be described in detail here.

[0207] While 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 invention, and that the scope of the invention is defined by the claims and their equivalents.

Claims

1. A method for automated production of Baoxinning thick paste, characterized in that: The following steps are involved: S1, set the production parameters of Baoxinning thick paste; S2, producing the Bao Xin Ning thick paste according to the production parameters of the Bao Xin Ning thick paste set in step S1.

2. The automated production method of Bao Xin Ning thick paste according to claim 1, characterized in that: The production control method for the Bao Xin Ning thick paste in step S2 includes the following steps: S21, adding the Danshen fine powder produced by the Danshen thick paste preparation subsystem to the mixing tank (43); S22, adding the Fructus Aurantii Immaturus fine powder generated by the Fructus Aurantii Immaturus thick paste preparation subsystem to a mixing tank (43); S23, adding the fine angelica powder produced by the angelica paste preparation subsystem to the mixing tank (43); S24, adding Panax notoginseng powder to the mixing tank (43); S25, adding the ginger liquid generated by the ginger preparation subsystem to the mixing tank (43); S26, mixing the materials added to the mixing tank (43).

3. The automated production method of Bao Xin Ning thick paste according to claim 1, characterized in that: In step S21, the control working method of the Danshen thick paste preparation subsystem to generate Danshen fine powder includes the following steps: S211, adding salvia miltiorrhiza powder to the salvia miltiorrhiza powder storage tank (11b), adding ethanol liquid to the salvia miltiorrhiza ethanol storage tank (12), and adding water to the water storage tank (13); S212, the Danshen powder in the Danshen powder storage tank (11b) is metered and transported to the Danshen percolation tank (11) through the metering screw conveyor provided between the Danshen percolation tank (11) and the Danshen powder storage tank (11b), and the metering pump and the automatic control valve provided between the Danshen percolation tank (11) and the Danshen ethanol storage tank (12) are opened to allow the ethanol in the Danshen ethanol storage tank (12) to be passed into the Danshen percolation tank (11); S213, the percolation liquid in the Danshen percolation tank (11) is passed into the Danshen percolation liquid storage tank (15), the Danshen filter residue in the Danshen percolation tank (11) is conveyed to the Danshen filter residue boiling tank (14) via a screw conveyor provided between the Danshen percolation tank (11) and the Danshen filter residue boiling tank (14), and the metering pump and automatic control valve provided between the water storage tank (13) and the Danshen filter residue boiling tank (14) are opened to pass the water in the water storage tank (13) into the Danshen filter residue boiling tank (14); S214, turning on the extraction pump provided between the Danshen filter residue boiling tank (14) and the Danshen percolate storage tank (15) to pass the Danshen filtrate prepared in the Danshen filter residue boiling tank (14) into the Danshen percolate storage tank (15); S215, turning on the extraction pump provided between the Danshen concentration tank (18) and the Danshen percolate storage tank (15) to pass the Danshen liquid in the Danshen percolate storage tank (15) into the Danshen concentration tank (18); S216, the ethanol vapor evaporated in the Danshen concentration tank (18) enters the Danshen ethanol condenser (16) for condensation, and the condensed ethanol vapor enters the Danshen ethanol recovery tank (17), and the extraction pump provided between the Danshen ethanol recovery tank (17) and the Danshen ethanol storage tank (12) is turned on to pass the ethanol liquid in the Danshen ethanol recovery tank (17) into the Danshen ethanol storage tank (12); S217, opening the metering pump provided between the Danshen concentration tank (18) and the Danshen thick paste storage tank (19) to pass the Danshen thick paste in the Danshen concentration tank (18) into the Danshen thick paste storage tank (19); S218, opening the metering pump and the automatic control valve provided between the Danshen thick paste storage tank (19) and the mixing tank (43) to pass the Danshen fine powder in the Danshen thick paste storage tank (19) into the mixing tank (43); Or / and the method for controlling the Fructus Aurantii Immaturus fine powder generated by the Fructus Aurantii Immaturus thick paste preparation subsystem in step S22 includes the following steps: S221, adding Fructus Aurantii powder to the Fructus Aurantii powder storage tank, and adding ethanol liquid to the Fructus Aurantii ethanol storage tank (22); S222, the Fructus Aurantii Immaturus powder in the Fructus Aurantii Immaturus powder storage tank is metered and transported to the Fructus Aurantii Immaturus percolation tank (21) by a metering screw conveyor provided between the Fructus Aurantii Immaturus percolation tank (21) and the Fructus Aurantii Immaturus powder storage tank, and the metering pump and the automatic control valve provided between the Fructus Aurantii Immaturus percolation tank (21) and the Fructus Aurantii Immaturus ethanol storage tank (22) are opened to allow the ethanol in the Fructus Aurantii Immaturus ethanol storage tank (22) to be passed into the Fructus Aurantii Immaturus percolation tank (21); S223, passing the percolation liquid in the Fructus Aurantii Immaturus percolation tank (21) into the Fructus Aurantii Immaturus percolation liquid storage tank (23); S224, opening the extraction pump provided between the Fructus Aurantii Immaturus vacuum concentration tank (24) and the Fructus Aurantii Immaturus percolate storage tank (23) to pass the Fructus Aurantii Immaturus liquid in the Fructus Aurantii Immaturus percolate storage tank (23) into the Fructus Aurantii Immaturus vacuum concentration tank (24); S225, the ethanol vapor evaporated in the Fructus Aurantii Immaturus decompression concentration tank (24) enters the Fructus Aurantii Immaturus ethanol condenser (25) for condensation, and the condensed ethanol vapor enters the Fructus Aurantii Immaturus ethanol recovery tank (26), and the extraction pump provided between the Fructus Aurantii Immaturus ethanol recovery tank (26) and the Fructus Aurantii Immaturus ethanol storage tank (22) is turned on to pass the ethanol liquid in the Fructus Aurantii Immaturus ethanol recovery tank (26) into the Fructus Aurantii Immaturus ethanol storage tank (22); S226, opening the metering pump provided between the Fructus Aurantii Immaturus decompression concentration tank (24) and the Fructus Aurantii Immaturus thick paste storage tank (27) to pass the Fructus Aurantii Immaturus thick paste in the Fructus Aurantii Immaturus decompression concentration tank (24) into the Fructus Aurantii Immaturus thick paste storage tank (27); S227, opening the metering pump and the automatic control valve provided between the Fructus Aurantii Immaturus thick paste storage tank (27) and the mixing tank (43) to pass the Fructus Aurantii Immaturus fine powder in the Fructus Aurantii Immaturus thick paste storage tank (27) into the mixing tank (43); Or / and the method for controlling the fine angelica powder generated by the angelica paste preparation subsystem in step S23 includes the following steps: S231, adding angelica to the angelica storage tank, and adding ethanol to the angelica ethanol storage tank (37); S232, the angelica in the angelica storage tank is metered and transported to the angelica extraction tank (31) by a metering screw conveyor provided between the angelica extraction tank (31) and the angelica storage tank, and the metering pump and the automatic control valve provided between the angelica extraction tank (31) and the angelica ethanol storage tank (37) are opened to allow the ethanol in the angelica ethanol storage tank (37) to flow into the angelica extraction tank (31); S233, turning on the extraction pump provided between the angelica sinensis vacuum concentration tank (32) and the angelica sinensis extraction tank (31) to pass the extract in the angelica sinensis extraction tank (31) into the angelica sinensis vacuum concentration tank (32); S234, the ethanol vapor evaporated in the Angelica sinensis vacuum concentration tank (32) enters the Angelica sinensis ethanol condenser (35) for condensation, and the condensed ethanol vapor enters the Angelica sinensis ethanol recovery tank (36), and the extraction pump provided between the Angelica sinensis ethanol recovery tank (36) and the Angelica sinensis ethanol storage tank (37) is turned on to pass the ethanol liquid in the Angelica sinensis ethanol recovery tank (36) into the Angelica sinensis ethanol storage tank (37); S235, opening the metering pump provided between the angelica decompression concentration tank (32) and the angelica thick paste storage tank (34) to pass the angelica thick paste in the angelica decompression concentration tank (32) into the angelica thick paste storage tank (34); S236, opening the metering pump and the automatic control valve provided between the angelica paste storage tank (34) and the mixing tank (43) to pass the angelica powder in the angelica paste storage tank (34) into the mixing tank (43); Or / and the method for controlling the ginger liquor generated by the ginger preparation subsystem in step S25 includes the following steps: S251, adding ginger into the ginger storage tank; S252, the ginger in the ginger storage tank is metered and transported to the ginger decoction pot (41) through the ginger metering conveyor provided between the ginger decoction pot (41) and the ginger storage tank, and the metering pump and the automatic control valve provided between the ginger decoction pot (41) and the water storage tank (13) are opened to allow the water in the water storage tank (13) to flow into the ginger decoction pot (41); S253, turning on the extraction pump provided between the ginger decoction pot (41) and the ginger decoction liquid storage tank (42) to pass the ginger liquid in the ginger decoction pot (41) into the ginger decoction liquid storage tank (42); S254, open the metering pump and automatic control valve provided between the ginger decoction liquid storage tank (42) and the mixing tank (43) to pass the ginger liquid in the ginger decoction liquid storage tank (42) into the mixing tank (43).

4. The automated production method of Bao Xin Ning thick paste according to claim 1, characterized in that: The method for setting the production parameters of the Po Sin Ning thick paste in step S1 includes the following steps: S11, enter the Baoxinning thick paste production parameter setting interface; S12, after entering the Bao Xin Ning thick paste production parameter setting interface, set the Bao Xin Ning thick paste production parameters on the Bao Xin Ning thick paste production parameter setting interface.

5. The automated production method of Bao Xin Ning thick paste according to claim 1, characterized in that: In step S11, the production parameter setting interface of the Po Sin Ning thick paste includes: One or any combination of the soaking time setting of the salvia miltiorrhiza powder in the salvia miltiorrhiza percolation tank (11), the percolation flow rate setting of the salvia miltiorrhiza liquid in the salvia miltiorrhiza percolation tank (11), the decocting time setting of the salvia miltiorrhiza residue in the salvia miltiorrhiza residue boiling tank (14), the drying temperature setting of the salvia miltiorrhiza paste in the ginseng paste storage tank (19), and the quality setting of the salvia miltiorrhiza fine powder in the mixing tank (43); Setting one or any combination of parameters for soaking the Fructus Aurantii Immaturus powder in the Fructus Aurantii Immaturus percolation tank (21), setting a percolation flow rate parameter for the Fructus Aurantii Immaturus powder in the Fructus Aurantii Immaturus percolation tank (21), setting a drying temperature parameter for the Fructus Aurantii Immaturus thick paste in the Fructus Aurantii Immaturus thick paste storage tank (27), and setting a quality parameter for the Fructus Aurantii Immaturus fine powder in the mixing tank (43); One or any combination of the drying temperature parameter setting of the angelica paste in the angelica paste storage tank (34) and the quality parameter setting of the angelica powder in the mixing tank (43); One or any combination of the mesh sieve parameter setting of the Panax notoginseng powder in the Panax notoginseng powder storage tank (44) and the quality parameter setting of the Panax notoginseng powder in the mixing tank (43); One or any combination of a parameter setting of a decoction time length of ginger in the ginger decoction pot (41) and a parameter setting of a water volume introduced into the ginger decoction pot (41).

6. The automated production method of Bao Xin Ning thick paste according to claim 1, characterized in that: In step S12, the method for setting the production parameters of the Po Sin Ning Thick Cream on the Po Sin Ning Thick Cream production parameter setting interface includes the following steps: S121, modify or keep unchanged the parameters required to be set in the Baoxinning Thick Cream production parameter setting interface; S122, determine whether to trigger the save control command: If the save control command is triggered, a password input box will pop up; If the save control command is not triggered, continue waiting and execute step S122; S123: After entering the password in the pop-up password input box, save the changed parameter settings or do not save the changed parameter settings.

7. The automated production method of Bao Xin Ning thick paste according to claim 1, characterized in that: After entering the password in the pop-up password input box in step S123, the working method of saving the changed parameter settings or not saving the changed parameter settings includes the following steps: S1231, after each password character is input, rearrange the characters in the character area on the virtual keyboard; S1232, obtain all password characters entered; S1233, rearrange all the obtained password characters: S1234: Determine whether the rearranged password characters are consistent with the password characters stored in the system: If the rearranged password characters are consistent with the password characters stored in the system, the changed parameter settings are saved; If the rearranged password characters are inconsistent with the password characters stored in the system, re-enter the password characters. After multiple judgments, if the rearranged password characters are still inconsistent with the password characters stored in the system, the changed parameter settings will not be saved.

8. A computer system, characterized in that: include: processor; a memory for storing processor-executable instructions; Wherein, the processor is configured to implement the automated production method of Bao Xin Ning thick paste as described in any one of claims 1 to 7 when executing the executable instructions.

9. A computer-readable storage medium, characterized in that include: a memory having a computer program stored thereon; A processor is used to execute the program in the memory to implement the automated production method of Bao Xin Ning thick paste as described in any one of claims 1 to 7.

10. An automated production system for Baoxinning thick paste, characterized in that: The invention comprises a danshen thick paste preparation subsystem, a zhi fructus aurantii thick paste preparation subsystem, a angelica thick paste preparation subsystem, a ginger preparation subsystem and a mixing tank (43). The danshen fine powder, zhi fructus aurantii fine powder, angelica fine powder, ginger liquid and panax notoginseng powder respectively generated by the danshen thick paste preparation subsystem, the zhi fructus aurantii thick paste preparation subsystem, the angelica thick paste preparation subsystem and the ginger preparation subsystem are put into the mixing tank (43) provided with a stirrer.

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