CN218793986U - High-pressure extraction device is used in blumea balsamifera borneol processing - Google Patents
High-pressure extraction device is used in blumea balsamifera borneol processing Download PDFInfo
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- CN218793986U CN218793986U CN202123168752.3U CN202123168752U CN218793986U CN 218793986 U CN218793986 U CN 218793986U CN 202123168752 U CN202123168752 U CN 202123168752U CN 218793986 U CN218793986 U CN 218793986U
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Abstract
The utility model discloses a high-pressure extraction device for processing blumea balsamifera borneol, which relates to the field of blumea balsamifera borneol processing, and comprises a tank body, an extraction tank, a plurality of first support frames, a first support frame, a second support frame and a third support frame, wherein the first support frames are fixedly arranged outside the extraction tank; the stirring mechanism comprises a second support frame arranged at the top of the extraction tank and a stirring component arranged on the second support frame; the extraction mechanism comprises a connecting pipe and a condensation component, and the connecting pipe is arranged at the top of the extraction tank. The utility model relates to a high-pressure extraction device is used in processing of blumea balsamifera borneol, extraction jar internally mounted has electric heating wire, the motor drive puddler is rotatory, with water and borneol raw materials intensive mixing, start electric heating wire, extract the interior temperature of jar after rising, the evaporation of water forms vapor, through constantly heating, extraction jar internal pressure constantly rises, vapor or ethanol mixed steam pass through in the connecting pipe gets into the spiral condenser pipe, vapor can be in the spiral condenser pipe abundant liquefaction, the device can improve borneol extraction efficiency, and the product quality is improved.
Description
Technical Field
The utility model relates to a blumea balsamifera borneol processing field, in particular to blumea balsamifera borneol processing is with high-pressure extraction device.
Background
Borneolum, named as Borneolum, pericarpium Citri Tangerinae, folium Artemisiae Argyi, borneolum Syntheticum, serissa, borneolum Syntheticum, and Borneolum Syntheticum, is prepared from stems and leaves of blumea balsamifera of Compositae or branches and leaves of Cinnamomum camphora of Lauraceae by steam distillation and recrystallization. The chemical component is 2-sagittanol, and the turpentine is also obtained by a series of chemical method processes. It can be used for treating block pattern of coma, conjunctival congestion with swelling and pain, pharyngitis, aphtha, sore and ulcer with swelling and pain, and unhealed ulcer. Dried resin is collected from the cracks of the trunks of the borneol incense and processed. Or cutting down trunks and branches, cutting into pieces, distilling and sublimating by water vapor, and cooling to obtain crystals. In addition, borneol can be obtained by the following method: mechanical borneol: pinene obtained by distilling turpentine, contact agent metaboric acid and anhydrous oxalic acid are used to directly produce borneol oxalate, then sodium hydroxide is used to heat and hydrolyze to obtain crude borneol, then the crude borneol is recrystallized and refined by gasoline, and the crude borneol is produced in Guangxi, guangdong, jiangsu and Zhejiang provinces. Moxa roll: is prepared from leaves of blumea balsamifera (L.) DC of Compositae by distilling with steam, cooling to obtain crystals, weighing folium Artemisiae Argyi powder, and refining to obtain Borneolum Syntheticum (folium Artemisiae Argyi tablet).
In the blumea balsamifera tablet manufacturing process, the existing manufacturing method is low in efficiency, the dissolving efficiency is low due to the fact that the temperature or pressure is low during dissolving, and the working speed is reduced.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a high-pressure extraction device is used in blumea balsamifera borneol processing has overcome the not enough of prior art, can fully cool off the liquefaction with the mixed steam that gets into in the connecting tube through the condensation subassembly, has work efficiency height, product quality height, operation safety's characteristics.
In order to solve the above problems, the utility model adopts the following technical proposal:
a high-pressure extraction device for processing blumea balsamifera and borneol comprises
The tank body comprises an extraction tank, the extraction tank is an oval pressure-resistant metal pipe, the top of the extraction tank is provided with a plurality of expansion interfaces, and the outer side of the extraction tank is fixedly provided with a plurality of first support frames;
the stirring mechanism comprises a second support frame arranged at the top of the extraction tank and a stirring component arranged on the second support frame;
the extraction mechanism is arranged on the expansion interface at the top of the extraction tank, and comprises a connecting pipe and a condensation assembly, wherein the connecting pipe is arranged at the top of the extraction tank and used for cooling steam containing moxa tablets after distillation.
Further, the jar body still includes intake pipe, lid door and catalyst jar, the intake pipe is installed in extraction tank bottom and is provided with a plurality of valves, the catalyst jar sets up in extraction tank deck portion and is connected with the extraction jar through the pipeline, the lid door is installed in extraction tank deck portion opening part through a plurality of fixing bolt.
Further, temperature transmitter and pressure transmitter that are used for monitoring the inside temperature of extraction jar and pressure are installed respectively to extraction tank deck portion and bottom, extraction tank deck portion is located lid one side and is provided with the relief valve.
Further, the stirring assembly comprises a motor, a driving shaft and a stirring rod, the motor is installed at the top of the second supporting frame, the output end of the motor is vertically arranged and connected with the driving shaft, the driving shaft is installed on one side of the second supporting frame and the inner portion of the extraction tank through a shaft seat, the driving shaft is movably connected with the shaft seat, and the stirring rod is welded on the driving shaft.
Further, the condensation subassembly includes cooling tube and spiral condenser pipe, the connecting pipe is U type tubular metal resonator, the cooling tube is set up in the connecting pipe output through fixed the knot, spiral condenser pipe installs in the cooling tube insidely.
Furthermore, a discharge pipe is obliquely arranged at the bottom of the radiating pipe.
Compared with the prior art, the utility model, following beneficial effect has:
the utility model discloses a condensation subassembly can be with the mixed steam intensive cooling liquefaction that gets into in the connecting tube, improves work efficiency.
The utility model discloses a set up the stirring subassembly and stir when the raw materials mixes, improve raw materials dissolving rate for extraction work.
The utility model has the characteristics of work efficiency is high, product quality is high, operation safety.
Drawings
FIG. 1 is a schematic view of the first-view external overall structure of a high-pressure extraction device for blumea balsamifera and borneol processing of the present invention;
FIG. 2 is a schematic diagram of a side view of the exterior of the high-pressure extraction apparatus for blumea balsamifera borneol processing of the present invention;
FIG. 3 is a schematic view of the second-view external overall structure of the high-pressure extraction device for blumea balsamifera borneol processing of the present invention;
fig. 4 is the schematic view of the internal sectional structure of the high-pressure extraction device for blumea balsamifera and borneol processing of the utility model.
In the figure: 100. a tank body; 101. an extraction tank; 102. a first support frame; 103. an air inlet pipe; 104. covering the door; 105. a pressure transmitter; 106. a catalyst tank; 107. a temperature transmitter; 108. a pressure relief valve; 200. A stirring mechanism; 201. a motor; 202. a shaft seat; 203. a second support frame; 204. a drive shaft; 205. a stirring rod; 300. an extraction mechanism; 301. a connecting pipe; 302. a fixing buckle; 303. a radiating pipe; 304. A spiral condenser tube; 305. and (4) discharging the pipe.
Detailed Description
In order to make the technical means, creation features, achievement purposes and functions of the present invention easy to understand, the present invention is further described below with reference to the following embodiments.
In the description of the present invention, it should be noted that the terms "upper", "lower", "inner", "outer", "front", "rear", "both ends", "one end", "the other end", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplification of the description, but do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first," "second," and the like are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "disposed," "connected," and the like are to be construed broadly, and for example, "connected" may be either fixedly connected or detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.
Referring to fig. 1-4, the present invention relates to a high pressure extraction device for processing blumea balsamifera and borneol, which comprises
The tank body 100 comprises an extraction tank 101, the extraction tank 101 is an oval pressure-resistant metal pipe, the top of the extraction tank 101 is provided with a plurality of expansion interfaces, and the outer side of the extraction tank 101 is fixedly provided with a plurality of first support frames 102;
the stirring mechanism 200 comprises a second support frame 203 arranged at the top of the extraction tank 101 and a stirring component arranged on the second support frame 203;
the extraction mechanism 300, which is installed on the top expansion interface of the extraction tank 101, includes a connection pipe 301 and a condensation component, wherein the connection pipe 301 is installed on the top of the extraction tank 101, and is used for cooling the steam containing the moxa cone after distillation.
When the device is used, the cover door 104 is opened to add borneol raw materials into the extraction tank 101, the air inlet pipe 103 is connected with a water pipe, an ethanol solution is added into the catalyst tank 106, the electric heating wire is installed inside the extraction tank 101, the motor 201 is started, the motor 201 drives the stirring rod 205 to rotate, water and the borneol raw materials are fully mixed, under the condition of low dissolving efficiency, the ethanol solution is added into the extraction tank 101 through the catalyst tank 106, all valves are closed, the electric heating wire of the extraction tank 101 is started, after the temperature in the extraction tank 101 rises, water is evaporated to form water vapor, through continuous heating, the pressure in the extraction tank 101 constantly rises, data in the extraction tank 101 is monitored through the pressure transmitter 105 and the temperature transmitter 107, after a certain degree is reached, the valve at the bottom of the connecting pipe 301 is opened, the water vapor or the mixed steam of the ethanol enters the spiral condensation pipe 304 through the connecting pipe 301, the spiral condensation pipe 304 is of a spiral hollow structure, the water vapor can be fully liquefied in the spiral condensation pipe 304 and is radiated through the radiating pipe 303, and is discharged through the discharging pipe 305, and then crystallization can be performed, the device can improve the borneol extraction efficiency, the product quality and meanwhile, the dissolving speed and the enterprise benefit is improved.
In order to improve the dissolving efficiency, the tank body 100 further comprises an air inlet pipe 103, a cover door 104 and a catalyst tank 106, the air inlet pipe 103 is installed at the bottom of the extraction tank 101 and is provided with a plurality of valves, the catalyst tank 106 is arranged at the top of the extraction tank 101 and is connected with the extraction tank 101 through a pipeline, and the cover door 104 is installed at an opening at the top of the extraction tank 101 through a plurality of fixing bolts.
In order to observe the internal condition of the device conveniently, a temperature transmitter 107 and a pressure transmitter 105 for monitoring the internal temperature and pressure of the extraction tank 101 are respectively installed at the top and the bottom of the extraction tank 101, and a pressure release valve 108 is arranged at one side of the cover door 104 at the top of the extraction tank 101.
In order to improve the principle dissolving efficiency, the stirring assembly comprises a motor 201, a driving shaft 204 and a stirring rod 205, the motor 201 is installed at the top of the second support frame 203, the output end of the motor is vertically arranged and connected with the driving shaft 204, the driving shaft 204 is installed at one side of the second support frame 203 and the inner part of the extraction tank 101 through a shaft seat 202, the driving shaft 204 is movably connected with the shaft seat 202, and the stirring rod 205 is welded on the driving shaft 204.
In order to sufficiently cool the steam, the condensing assembly includes a heat pipe 303 and a spiral condenser pipe 304, the connection pipe 301 is a U-shaped metal pipe, the heat pipe 303 is disposed at an output end of the connection pipe 301 through a fixing buckle 302, and the spiral condenser pipe 304 is installed inside the heat pipe 303.
The bottom of the heat pipe 303 is provided with a discharge pipe 305 in an inclined manner.
In order to conveniently control the equipment, the equipment is also provided with a PLC control system, and the PLC control system respectively controls the forward and reverse rotation and the rotation angle of the motor 201; the circuit structure and the control principle of the PLC control system are prior art, and are not described in detail in this application.
The foregoing shows and describes the basic principles and principal features of the invention, together with the advantages thereof. It should be understood by those skilled in the art that the present invention is not limited to the above embodiments, and the above embodiments and descriptions are only illustrative of the principles of the present invention, and that various changes and modifications may be made without departing from the spirit and scope of the present invention, and all such changes and modifications fall within the scope of the present invention as claimed. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (6)
1. The utility model provides a blumea balsamifera borneol processing is with high-pressure extraction device which characterized in that: comprises that
The tank body (100) comprises an extraction tank (101), the extraction tank (101) is an oval pressure-resistant metal pipe, the top of the extraction tank is provided with a plurality of expansion interfaces, and the outer side of the extraction tank (101) is fixedly provided with a plurality of first support frames (102);
the stirring mechanism (200) comprises a second supporting frame (203) arranged at the top of the extraction tank (101) and a stirring component arranged on the second supporting frame (203);
the extraction mechanism (300) is arranged on the expansion interface at the top of the extraction tank (101) and comprises a connecting pipe (301) and a condensation assembly, wherein the connecting pipe (301) is arranged at the top of the extraction tank (101) and is used for cooling steam containing moxa sheets after distillation.
2. The high-pressure extraction device for blumea balsamifera and borneol processing according to claim 1, which is characterized in that: the jar body (100) still includes intake pipe (103), lid door (104) and catalyst jar (106), intake pipe (103) are installed in extraction jar (101) bottom and are provided with a plurality of valves, catalyst jar (106) set up in extraction jar (101) top and are connected with extraction jar (101) through the pipeline, lid door (104) are installed in extraction jar (101) top opening part through a plurality of fixing bolt.
3. The high-pressure extraction device for blumea balsamifera and borneol processing according to claim 2, which is characterized in that: the temperature transmitter (107) and the pressure transmitter (105) that are used for monitoring the inside temperature and pressure of extraction jar (101) are installed respectively to extraction jar (101) top and bottom, extraction jar (101) top is located lid door (104) one side and is provided with relief valve (108).
4. The high-pressure extraction device for blumea balsamifera and borneol processing according to claim 1, which is characterized in that: the stirring assembly comprises a motor (201), a driving shaft (204) and a stirring rod (205), the motor (201) is installed at the top of the second supporting frame (203), the output end of the motor is vertically arranged and connected with the driving shaft (204), the driving shaft (204) is installed on one side of the inside of the second supporting frame (203) and the extraction tank (101) through a shaft seat (202), the driving shaft (204) is movably connected with the shaft seat (202), and the stirring rod (205) is welded on the driving shaft (204).
5. The high-pressure extraction device for blumea balsamifera and borneol processing according to claim 1, which is characterized in that: the condensation subassembly includes cooling tube (303) and spiral condenser pipe (304), connecting pipe (301) are U type tubular metal resonator, cooling tube (303) set up in connecting pipe (301) output through fixed knot (302), spiral condenser pipe (304) are installed inside cooling tube (303).
6. The high-pressure extraction device for blumea balsamifera and borneol processing according to claim 5, wherein: the bottom of the radiating pipe (303) is obliquely provided with a discharging pipe (305).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123168752.3U CN218793986U (en) | 2021-12-16 | 2021-12-16 | High-pressure extraction device is used in blumea balsamifera borneol processing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123168752.3U CN218793986U (en) | 2021-12-16 | 2021-12-16 | High-pressure extraction device is used in blumea balsamifera borneol processing |
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| Publication Number | Publication Date |
|---|---|
| CN218793986U true CN218793986U (en) | 2023-04-07 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202123168752.3U Active CN218793986U (en) | 2021-12-16 | 2021-12-16 | High-pressure extraction device is used in blumea balsamifera borneol processing |
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| Country | Link |
|---|---|
| CN (1) | CN218793986U (en) |
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2021
- 2021-12-16 CN CN202123168752.3U patent/CN218793986U/en active Active
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