Automatic production system for Baoxinning thick paste

Abstract

The utility model discloses an automatic production system of a Baoxinning thick paste, which comprises a salvia miltiorrhiza thick paste preparation subsystem, a fructus aurantii thick paste preparation subsystem, an angelica sinensis thick paste preparation subsystem, a ginger preparation subsystem and a thick paste mixing tank, a thick paste outlet of the radix salviae miltiorrhizae thick paste storage tank, the fructus aurantii thick paste preparation subsystem, the radix angelicae sinensis thick paste preparation subsystem and the fresh ginger preparation subsystem are communicated with a material inlet pipeline of the thick paste mixing tank through pipelines, and the thick paste mixing tank is further provided with a fine powder feeding port used for feeding radix notoginseng fine powder. The fine powder feeding port is connected with a pseudo-ginseng powder storage tank through a metering screw conveyor, and a stirrer is arranged in the thick paste mixing tank. The automation degree and the working efficiency can be improved.

Description

Technical Field

[0001] This utility model relates to the field of pharmaceutical production technology, specifically to an automated production system for Baoxinning thick paste. Background Technology

[0002] Baoxinning Capsules are a medication used to treat angina pectoris, arrhythmia, and improve symptoms of coronary heart disease. Its main ingredients include herbs such as Danshen (Salvia miltiorrhiza), Sanqi (Panax notoginseng), Danggui (Angelica sinensis), and Zhike (Citrus aurantium). Before capsule preparation, a thick paste needs to be made. This paste is dried, sieved, and then filled into capsules to produce Baoxinning Capsules. The preparation of the thick paste is the core step in the production of Baoxinning Capsules. Currently, the preparation process involves pulverizing Sanqi into a fine powder and sieving it; boiling ginger twice with water, 2 hours each time, combining the decoctions, filtering, and concentrating the filtrate to a suitable volume; extracting Danggui with ethanol and then concentrating it to obtain a thick paste; and then mixing the Sanqi powder, ginger decoction, Danggui thick paste, Zhike percolated thick paste, and Danshen percolated thick paste to obtain the desired mixed thick paste. However, after percolation, the residue of Danshen still contains a large amount of active ingredients, which cannot be completely extracted, resulting in waste of the medicinal material. Furthermore, the current thick paste preparation process requires the manual addition of materials, which may cause contamination and is labor-intensive for workers. Utility Model Content

[0003] This utility model aims to solve the technical problems existing in the prior art, and innovatively proposes an automated production system for Baoxinning paste, which can improve the degree of automation and increase work efficiency.

[0004] To achieve the above objectives, this utility model provides an automated production system for Baoxinning thick paste, including a Danshen thick paste preparation subsystem, a Zhi Ke thick paste preparation subsystem, an Dang Gui thick paste preparation subsystem, a Sheng Jiang (ginger) preparation subsystem, and a thick paste mixing tank. The Danshen thick paste preparation subsystem includes a Danshen percolation tank. The Danshen inlet at the top of the Danshen percolation tank is connected to a Danshen powder storage tank via a metering screw conveyor. The ethanol inlet at the top of the Danshen percolation tank is connected to a Danshen ethanol storage tank via a pipeline. The percolation outlet of the Danshen percolation tank is connected to a Danshen percolation liquid storage tank. The filter residue outlet of the Danshen percolation tank is connected to a screw conveyor, which transports the filter residue to a Danshen filter residue cooking tank. The water inlet is connected to a water storage tank via a pipeline. A heating jacket is provided outside the Danshen filter residue cooking tank. The cooking liquid outlet of the Danshen filter residue cooking tank is connected to a Danshen percolate storage tank via a pipeline. The liquid outlet of the Danshen percolate storage tank is connected to a Danshen concentration tank via a pipeline. The ethanol vapor outlet at the top of the Danshen concentration tank is connected to a Danshen ethanol condenser. The ethanol outlet of the Danshen ethanol condenser is connected to a 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 inlet of the Danshen concentration reboiler. The outlet of the Danshen concentration reboiler is connected to the reboiler inlet at the bottom of the Danshen concentration tank. The material outlet of the Danshen concentration tank is connected to a Danshen thick paste storage tank via a pipeline.

[0005] The sludge outlet of the danshen sludge storage tank, the citrus aurantium sludge preparation subsystem, the angelica sinensis sludge preparation subsystem, and the ginger preparation subsystem are respectively connected to the material inlet pipeline of the sludge mixing tank through pipelines. The sludge mixing tank is also equipped with a fine powder inlet for adding sanqi powder. The fine powder inlet is connected to the sanqi powder storage tank through a metering screw conveyor. A stirrer is installed inside the sludge mixing tank.

[0006] In the above scheme: the tanshinone ethanol recovery tank is connected to the tanshinone ethanol storage tank through a pipeline.

[0007] In the above scheme: the bitter orange peel thick paste preparation subsystem includes a bitter orange peel thick paste storage tank and a bitter orange peel percolation tank. The bitter orange peel inlet at the top of the bitter orange peel percolation tank is connected to a bitter orange peel powder storage tank via a metering screw conveyor. The ethanol inlet at the top of the bitter orange peel percolation tank is connected to a bitter orange peel ethanol storage tank via a pipeline. The percolation liquid outlet at the bottom of the bitter orange peel percolation tank is connected to a bitter orange peel percolation liquid storage tank. The liquid outlet of the bitter orange peel percolation liquid storage tank is connected to a bitter orange peel vacuum concentration tank via a pipeline. The ethanol vapor outlet at the top of the bitter orange peel vacuum concentration tank is connected to... The system is equipped with a bitter orange peel ethanol condenser, the ethanol outlet of which is connected to a bitter orange peel ethanol recovery tank. A bitter orange peel concentration reboiler is installed at the bottom of the bitter orange peel concentration tank. The reboiler outlet at the bottom of the concentration tank is connected to the inlet of the reboiler, and the outlet of the reboiler is connected to the reboiler inlet at the bottom of the concentration tank. The material outlet of the concentration tank is connected to a bitter orange peel viscous paste storage tank via a pipeline, and the viscous paste outlet of the storage tank is connected to a viscous paste mixing tank via a pipeline.

[0008] In the above scheme: the ginger preparation subsystem includes a ginger decoction tank, the water inlet at the top of the ginger decoction tank is connected to a water storage tank; the decoction outlet of the ginger decoction tank is connected to a ginger decoction storage tank, and the ginger decoction storage tank is connected to a thick paste mixing tank through a pipeline.

[0009] In the above scheme: the Angelica sinensis thick paste preparation subsystem includes an Angelica sinensis thick paste storage tank and an Angelica sinensis extraction tank. The top of the Angelica sinensis extraction tank is provided with an Angelica sinensis inlet. The ethanol inlet at the top of the Angelica sinensis extraction tank is connected to the Angelica sinensis ethanol storage tank via a pipeline. The extract outlet of the Angelica sinensis extraction tank is connected to the Angelica sinensis vacuum concentration tank. The bottom of the Angelica sinensis vacuum concentration tank is equipped with an Angelica sinensis concentration reboiler. The reboiler outlet at the bottom of the Angelica sinensis vacuum concentration tank is connected to the inlet of the Angelica sinensis concentration reboiler. The outlet of the Angelica sinensis concentration reboiler is connected to the reboiler inlet at the bottom of the Angelica sinensis vacuum concentration tank. The material outlet of the Angelica sinensis vacuum concentration tank is connected to the Angelica sinensis thick paste storage tank via a pipeline. The ethanol vapor outlet at the top of the Angelica sinensis vacuum concentration tank is connected to the Angelica sinensis ethanol condenser. The ethanol outlet of the Angelica sinensis ethanol condenser is connected to the Angelica sinensis ethanol recovery tank. The Angelica sinensis ethanol recovery tank is connected to the Angelica sinensis ethanol storage tank via a pipeline.

[0010] In the above scheme: both the bitter orange peel vacuum concentration tank and the angelica vacuum concentration tank are equipped with vacuum outlets, and the vacuum outlets are equipped with valves and connected to vacuum pumping equipment.

[0011] In the above scheme: metering pumps and automatic control valves are respectively installed on the pipelines connecting the salvia miltiorrhiza viscous paste storage tank to the viscous paste outlet, the citrus aurantium viscous paste preparation subsystem, the angelica sinensis viscous paste preparation subsystem, the ginger preparation subsystem, and the viscous paste mixing tank.

[0012] In the above scheme: metering pumps and automatic control valves are respectively installed on the pipeline connecting the danshen percolation tank and the danshen ethanol storage tank, the pipeline connecting the zhike percolation tank and the zhike ethanol storage tank, and the pipeline connecting the danggui extraction tank and the danggui ethanol storage tank.

[0013] In the above scheme: a ginger metering conveyor is installed at the ginger inlet at the top of the ginger decoction pot.

[0014] In summary, the beneficial effects of this invention are: after percolation extraction, the active ingredients of Salvia miltiorrhiza can be extracted more effectively through decoction, avoiding waste of medicinal materials. This invention uses an automatic metering pump or metering bolt conveyor to meter and transport materials, enabling automated, unmanned production, improving production efficiency, reducing human pollution, and lowering the labor intensity of workers. Attached Figure Description

[0015] Figure 1 This is a system diagram of this utility model. Detailed Implementation

[0016] The present invention will be further described below with reference to embodiments and accompanying drawings:

[0017] like Figure 1 As shown, an automated production system for Baoxinning thick paste includes a Danshen thick paste preparation subsystem, a Zhi Ke thick paste preparation subsystem, an Dang Gui thick paste preparation subsystem, a Sheng Jiang preparation subsystem, and a thick paste mixing tank 43.

[0018] The Danshen (Salvia miltiorrhiza) thick paste preparation subsystem includes a Danshen percolation tank 11, which is existing technology and will not be described in detail here. The Danshen inlet at the top of the Danshen percolation tank 11 is connected to the Danshen powder storage tank 11b via a metering screw conveyor. The ethanol inlet at the top of the Danshen percolation tank 11 is connected to the Danshen ethanol storage tank 12 via a pipeline. The percolate outlet of the Danshen percolation tank 11 is connected to the Danshen percolate storage tank 15. The filter residue outlet of the Danshen percolation tank 11 is connected to a screw conveyor, which transports the filter residue to the Danshen filter residue cooking tank 14. The water inlet of the Danshen filter residue cooking tank 14 is connected to the water storage tank 13 via a pipeline. A heating jacket is installed outside the Danshen filter residue cooking tank 14. The cooking liquid outlet of the Danshen filter residue cooking tank 14 is connected to the Danshen percolate storage tank 15 via a pipeline. The liquid outlet of the Danshen percolate storage tank 15 is connected to the Danshen concentration tank 18 via a pipeline. The ethanol vapor outlet at the top of the Danshen concentration tank 18 is connected to a Danshen ethanol condenser 16. The ethanol outlet of the Danshen ethanol condenser 16 is connected to a Danshen ethanol recovery tank 17, which is connected to the Danshen ethanol storage tank 12 via a pipeline. The Danshen ethanol condenser 16 is existing technology, consisting of a tube layer and a shell layer. Cooling water flows through the shell layer. Ethanol enters the tube layer, is condensed by the cooling water in the shell layer, and then enters the Danshen ethanol recovery tank 17. The ethanol condensers for Citrus aurantium and Angelica sinensis are the same as those for Danshen ethanol and are existing technology.

[0019] 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, and the outlet of the Danshen concentration reboiler 18a is connected to the reboiler inlet at the bottom of the Danshen concentration tank 18. The material outlet of the Danshen concentration tank 18 is connected to the Danshen thick paste storage tank 19 through a pipeline.

[0020] The sludge outlet of the danshen sludge storage tank 19, the citrus aurantium sludge preparation subsystem, the angelica sinensis sludge preparation subsystem, and the ginger preparation subsystem are all connected to the material inlet pipeline of the sludge mixing tank 43 via pipelines. The sludge mixing tank 43 is also equipped with a fine powder inlet 43a for adding Panax notoginseng fine powder. The fine powder inlet 43a is connected to the Panax notoginseng powder storage tank 44 via a metering screw conveyor. An agitator is installed inside the sludge mixing tank 43. The metering screw conveyor is a type of screw conveyor used for continuous weighing and batch feeding of powdery and bulk materials; this is existing technology and will not be described in detail here.

[0021] The subsystem for preparing bitter orange peel extract includes a bitter orange peel extract storage tank 27 and a bitter orange peel percolation tank 21. The bitter orange peel inlet at the top of the percolation tank 21 is connected to a bitter orange peel powder storage tank via a metering screw conveyor. The ethanol inlet at the top of the percolation tank 21 is connected to a bitter orange peel ethanol storage tank 22 via a pipeline. The percolation liquid outlet at the bottom of the percolation tank 21 is connected to a bitter orange peel percolation liquid storage tank 23. The liquid outlet of the bitter orange peel percolation liquid storage tank 23 is connected to a bitter orange peel vacuum concentration tank 24 via a pipeline. The ethanol vapor outlet at the top of the vacuum concentration tank 24 is connected to a bitter orange peel ethanol... The condenser 25, which condenses ethanol, is connected to the ethanol recovery tank 26. The bottom of the ethanol concentration tank 24 is equipped with an ethanol concentration reboiler 28. The reboiler outlet at the bottom of the ethanol concentration tank 24 is connected to the inlet of the ethanol concentration reboiler 28. The outlet of the ethanol concentration reboiler 28 is connected to the reboiler inlet at the bottom of the ethanol concentration tank 24. The material outlet of the ethanol concentration tank 24 is connected to the ethanol paste storage tank 27 through a pipeline. The paste outlet of the ethanol paste storage tank 27 is connected to the paste mixing tank 43 through a pipeline.

[0022] 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 a water storage tank 13; the decoction outlet of the decoction tank 41 is connected to a ginger decoction storage tank 42, which is connected to a thick paste mixing tank 43 via a pipeline.

[0023] The Angelica sinensis thick paste preparation subsystem includes an Angelica sinensis thick paste storage tank 34 and an Angelica sinensis extraction tank 31. The top of the extraction tank 31 has an Angelica sinensis inlet, which is connected to the storage tank via a metering screw conveyor. The ethanol inlet at the top of the extraction tank 31 is connected to an ethanol storage tank 37 via a pipeline. The extract outlet of the extraction tank 31 is connected to a vacuum concentration tank 32. The bottom of the vacuum concentration tank 32 is equipped with an Angelica sinensis concentrator / reboiler 33, and the reboiler outlet at the bottom of the tank is connected to the inlet of the reboiler. The outlet of the reboiler is connected to the reboiler inlet at the bottom of the vacuum concentration tank 32. The material outlet of the vacuum concentration tank 32 is connected to the Angelica sinensis 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 an Angelica sinensis ethanol condenser 35. The ethanol outlet of the Angelica sinensis ethanol condenser 35 is connected to an Angelica sinensis ethanol recovery tank 36. The Angelica sinensis ethanol recovery tank is connected to an Angelica sinensis ethanol storage tank 37 through a pipeline.

[0024] Both the bitter orange peel vacuum concentration tank 24 and the angelica sinensis vacuum concentration tank 32 are equipped with vacuum outlets, and valves are installed at the vacuum outlets, which are connected to vacuum pumping equipment.

[0025] Metering pumps a and automatic control valves b are respectively installed on the pipelines connecting the thick paste outlet of the Salvia miltiorrhiza thick paste storage tank 19, the thick paste preparation subsystem of Citrus aurantium, the thick paste preparation subsystem of Angelica sinensis, the thick paste preparation subsystem of Ginger, and the thick paste mixing tank 43. Metering pumps a and automatic control valves b are respectively installed on the pipelines connecting the Salvia miltiorrhiza percolation tank 11 and the Salvia miltiorrhiza ethanol storage tank 12, the pipelines connecting the Citrus aurantium percolation tank 21 and the Citrus aurantium ethanol storage tank 22, and the pipelines connecting the Angelica sinensis extraction tank 31 and the Angelica sinensis ethanol storage tank 37. Extraction pumps c are installed on all other pipelines.

[0026] Among them, the Salvia miltiorrhiza 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.

Claims

1. An automated production system for Baoxinning thick paste, characterized in that: The system comprises a Danshen thick paste preparation subsystem, a Fructus Aurantii thick paste preparation subsystem, a Angelica sinensis thick paste preparation subsystem, a raw ginger preparation subsystem, and a thick paste mixing tank (43). The Danshen thick paste preparation subsystem comprises a Danshen percolation tank (11), a Danshen inlet at the top end of the Danshen percolation tank (11) connected to a Danshen powder storage tank (11b) through a metering screw conveyor, an ethanol inlet at the top end of the Danshen percolation tank (11) connected to a Danshen ethanol storage tank (12) through a pipeline, a Danshen percolation liquid outlet end of the Danshen percolation tank (11) connected to a Danshen percolation liquid storage tank (15), a Danshen percolation liquid storage tank (15) liquid outlet connected to a Danshen concentration tank (18) through a pipeline, an ethanol vapor outlet at the top end of the Danshen concentration tank (18) connected to a Danshen ethanol condenser (16), a Danshen ethanol condenser (16) condensing ethanol outlet end connected to a Danshen ethanol recovery tank (17), a Danshen concentration reboiler (18a) provided at the bottom of the Danshen concentration tank (18), a reboiling outlet at the bottom of the Danshen concentration tank (18) connected to the Danshen concentration reboiler (18a) inlet, a Danshen concentration reboiler (18a) outlet connected to the reboiling inlet at the bottom of the Danshen concentration tank (18), and a material outlet of the Danshen concentration tank (18) connected to a Danshen thick paste storage tank (19) through a pipeline. The Danshen thick paste storage tank (19) thick paste outlet, the Fructus Aurantii thick paste preparation subsystem, the Angelica sinensis thick paste preparation subsystem, and the raw ginger preparation subsystem are respectively connected to a material inlet pipeline of the thick paste mixing tank (43) through a pipeline, and the thick paste mixing tank (43) is further provided with a fine powder inlet (43a) for placing Panax notoginseng fine powder, the fine powder inlet (43a) is connected to a Panax notoginseng powder storage tank (44) through a metering screw conveyor, and the thick paste mixing tank (43) is provided with a stirrer.

2. The automatic production system of baoshenning thick paste according to claim 1, characterized in that: The Danshen ethanol recovery tank (17) is connected to the Danshen ethanol storage tank (12) through a pipeline.

3. The automatic production system of baoguanning thick paste according to claim 1 or 2, characterized in that: The prepared subsystem of the Fructus Aurantii includes a Fructus Aurantii thick paste storage tank (27) and a Fructus Aurantii percolation tank (21), the Fructus Aurantii inlet at the top end of the Fructus Aurantii percolation tank (21) is connected with the Fructus Aurantii powder storage tank through a metering screw conveyor, the ethanol inlet at the top end of the Fructus Aurantii percolation tank (21) is connected with the Fructus Aurantii ethanol storage tank (22) through a pipeline, the percolation liquid outlet at the bottom end of the Fructus Aurantii percolation tank (21) is connected with the Fructus Aurantii percolation liquid storage tank (23), the liquid outlet of the Fructus Aurantii percolation liquid storage tank (23) is connected with the Fructus Aurantii reduced pressure concentration tank (24) through a pipeline, the ethanol vapor outlet at the top end of the Fructus Aurantii reduced pressure concentration tank (24) is connected with the Fructus Aurantii ethanol condenser (25), the condensed ethanol outlet of the Fructus Aurantii ethanol condenser (25) is connected with the Fructus Aurantii ethanol recovery tank (26), the bottom of the Fructus Aurantii reduced pressure concentration tank (24) is provided with the Fructus Aurantii concentration reboiler (28), the reboiling outlet at the bottom end of the Fructus Aurantii reduced pressure concentration tank (24) is connected with the inlet of the Fructus Aurantii concentration reboiler (28), the outlet of the Fructus Aurantii concentration reboiler (28) is connected with the reboiling inlet at the bottom end of the Fructus Aurantii reduced pressure concentration tank (24), the material outlet of the Fructus Aurantii reduced pressure concentration tank (24) is connected with the Fructus Aurantii thick paste storage tank (27) through a pipeline, and the thick paste outlet of the Fructus Aurantii thick paste storage tank (27) is connected with the thick paste mixing tank (43) through a pipeline.

4. The automatic production system of baixinning thick paste according to claim 3, characterized in that: The prepared subsystem of the ginger includes the ginger decocting tank (41), the water inlet at the top end of the ginger decocting tank (41) is connected with the water storage tank (13), and the decocting liquid outlet of the ginger decocting tank (41) is connected with the ginger decocting liquid storage tank (42) through a pipeline.

5. The automatic production system of baixinning thick paste according to claim 4, characterized in that: The prepared subsystem of the Angelica includes the Angelica thick paste storage tank (34) and the Angelica extraction tank (31), the top of the Angelica extraction tank (31) is provided with the Angelica inlet, the ethanol inlet at the top end of the Angelica extraction tank (31) is connected with the Angelica ethanol storage tank (37) through a pipeline, the extraction liquid outlet of the Angelica extraction tank (31) is connected with the Angelica reduced pressure concentration tank (32), the bottom of the Angelica reduced pressure concentration tank (32) is provided with the Angelica concentration reboiler (33), the reboiling outlet at the bottom end of the Angelica reduced pressure concentration tank (32) is connected with the inlet of the Angelica concentration reboiler (33), the outlet of the Angelica concentration reboiler (33) is connected with the reboiling inlet at the bottom end of the Angelica reduced pressure concentration tank (32), the material outlet of the Angelica reduced pressure concentration tank (32) is connected with the Angelica thick paste storage tank (34) through a pipeline, the ethanol vapor outlet at the top end of the Angelica reduced pressure concentration tank (32) is connected with the Angelica ethanol condenser (35), the condensed ethanol outlet of the Angelica ethanol condenser (35) is connected with the Angelica ethanol recovery tank (36), and the Angelica ethanol recovery tank is connected with the Angelica ethanol storage tank (37) through a pipeline.

6. The automatic production system of Baoxinyin thick paste according to claim 4, characterized in that: The vacuum outlets are arranged on the Fructus Aurantii reduced pressure concentration tank (24) and the Angelica reduced pressure concentration tank (32), valves are arranged at the vacuum outlets, and the vacuum outlets are connected with vacuumizing equipment.

7. The automatic production system of Baoxinyin thick paste according to claim 6, characterized in that: The pipeline, which is communicated between the thick paste outlet of the Danshen thick paste storage tank (19), the thick paste preparation subsystem of the Jujube, the thick paste preparation subsystem of the Angelica, and the thick paste mixing tank (43), is respectively provided with a metering pump (a) and an automatic control valve (b).

8. The automatic production system of Baoxinning thick paste according to claim 5, characterized in that: The pipeline, which is communicated between the Danshen percolation tank (11) and the Danshen ethanol storage tank (12), the pipeline, which is communicated between the Jujube percolation tank (21) and the Jujube ethanol storage tank (22), and the pipeline, which is communicated between the Angelica extraction tank (31) and the Angelica ethanol storage tank (37), is respectively provided with a metering pump (a) and an automatic control valve (b).

9. The automatic production system of Baoxinning thick paste according to claim 4, characterized in that: The ginger metering conveyor is arranged on the ginger inlet at the top end of the ginger decoction tank (41).

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