CN116785749B - Adjustable condensing device for light volatile oil - Google Patents
Adjustable condensing device for light volatile oil Download PDFInfo
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- CN116785749B CN116785749B CN202311084306.5A CN202311084306A CN116785749B CN 116785749 B CN116785749 B CN 116785749B CN 202311084306 A CN202311084306 A CN 202311084306A CN 116785749 B CN116785749 B CN 116785749B
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- 239000000341 volatile oil Substances 0.000 title claims abstract description 64
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 75
- 238000009833 condensation Methods 0.000 claims abstract description 38
- 230000005494 condensation Effects 0.000 claims abstract description 38
- 210000002445 nipple Anatomy 0.000 claims abstract description 25
- 239000000110 cooling liquid Substances 0.000 claims description 21
- 239000000203 mixture Substances 0.000 claims description 7
- 235000019476 oil-water mixture Nutrition 0.000 abstract description 76
- 239000007788 liquid Substances 0.000 abstract description 48
- 230000002829 reductive effect Effects 0.000 abstract description 14
- 230000000903 blocking effect Effects 0.000 description 14
- 230000000694 effects Effects 0.000 description 10
- 239000000463 material Substances 0.000 description 4
- 238000002360 preparation method Methods 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- 230000003266 anti-allergic effect Effects 0.000 description 2
- 230000003110 anti-inflammatory effect Effects 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 2
- 230000002401 inhibitory effect Effects 0.000 description 2
- 230000000670 limiting effect Effects 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 235000019198 oils Nutrition 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 241000208173 Apiaceae Species 0.000 description 1
- 241000208838 Asteraceae Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 241000207923 Lamiaceae Species 0.000 description 1
- 241001093501 Rutaceae Species 0.000 description 1
- 241000607479 Yersinia pestis Species 0.000 description 1
- 241000234299 Zingiberaceae Species 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 230000000507 anthelmentic effect Effects 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 230000001093 anti-cancer Effects 0.000 description 1
- 230000000845 anti-microbial effect Effects 0.000 description 1
- 230000002790 anti-mutagenic effect Effects 0.000 description 1
- 230000000259 anti-tumor effect Effects 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 239000010692 aromatic oil Substances 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 230000004071 biological effect Effects 0.000 description 1
- 210000003169 central nervous system Anatomy 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000036961 partial effect Effects 0.000 description 1
- 239000002304 perfume Substances 0.000 description 1
- 239000000825 pharmaceutical preparation Substances 0.000 description 1
- 230000000144 pharmacologic effect Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 210000002345 respiratory system Anatomy 0.000 description 1
- 150000003505 terpenes Chemical class 0.000 description 1
- 235000007586 terpenes Nutrition 0.000 description 1
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The application provides an adjustable condensing device for light volatile oil, which comprises a condenser and a valve pipe assembly embedded at the top of the condenser, wherein the condenser comprises a condensing pipeline which is arranged inside, the valve pipe assembly is arranged close to the condensing pipeline, the valve pipe assembly comprises a nipple which is embedded at the top of the condenser and is positioned at the inner side of the condensing pipeline, a plurality of short connection guide ports which extend towards the direction of the condensing pipeline, and a valve core which is movably arranged in the nipple and is used for controlling the opening and the closing of the plurality of short connection guide ports, the condensing pipeline comprises a condensing pipe, a plurality of water retaining parts are arranged on the condensing pipe, condensed water can be collected at the position of the condensing pipe through the water retaining parts, so that a liquid oil-water mixture formed by condensation can flow on the water surface in the condensing pipe, and the loss of the light volatile oil in the oil-water mixture due to the fact that the temperature is too low is avoided, the contact between the light volatile oil and the condensing pipe is reduced, the loss of the light volatile oil adhered to the inner wall of the condensing pipe is reduced, and the yield of the volatile oil is improved.
Description
Technical Field
The application relates to the technical field of volatile oil extraction, in particular to an adjustable condensing device for light volatile oil.
Background
The volatile oil is also called essential oil, essential oil or aromatic oil, mainly derived from aromatic Chinese medicinal materials, especially from Asteraceae (folium Artemisiae Argyi, rhizoma Atractylodis, atractylodis rhizoma), umbelliferae (radix Angelicae sinensis, fructus Foeniculi, bupleuri radix), rutaceae (fructus Citri Tangerinae, fructus Zanthoxyli), labiatae (herba Menthae, perillae herba), and Zingiberaceae (such as rhizoma Zingiberis recens, curcumae rhizoma), etc., and mainly composed of chemical molecules such as terpenes, aldehydes, esters, alcohols, etc. Most plant essential oils have various biological activities such as anti-inflammatory, antibacterial, antiallergic, antioxidant, enzyme-inhibiting and antitumor activities, and are widely applied to the aspects of perfume, food industry, pharmacy, medical treatment, cosmetics, agricultural pests and the like at present, and pharmacological experiments show that: the volatile oil has antiinflammatory, antiallergic, antimicrobial, antimutagenic, anticancer, anthelmintic, enzyme inhibiting, central nervous system regulating, and respiratory system regulating effects. The content of the volatile oil in the traditional Chinese medicinal materials is generally 0.12% -10%.
The condenser is commonly used in chemical or pharmaceutical preparations, particularly in the manufacture of volatile oils, and is used for condensing a high-temperature gaseous oil-water mixture into a liquid oil-water mixture through heat exchange, and separating the liquid oil-water mixture in a subsequent process.
However, current condensers suffer from the following drawbacks: the length of the condensing pipe in the condenser is fixed and longer, and the temperature of the oil-water mixture is lower when the oil-water mixture is condensed and leaves, so that the viscosity of the volatile oil in the oil-water mixture is increased.
Disclosure of Invention
Based on the above, the application aims to provide an adjustable condensing device for light volatile oil, which is used for solving the problems of the prior art that the length of a condensing tube inside a condenser is fixed and longer, the temperature of an oil-water mixture is lower when the oil-water mixture is condensed and leaves, and the viscosity of the volatile oil is increased.
The embodiment of the application relates to an adjustable condensing device for light volatile oil, which comprises a condenser and a valve pipe assembly embedded at the top of the condenser;
the condenser comprises a condensation pipeline arranged inside, the valve pipe assembly is arranged close to the condensation pipeline, and the condenser further comprises a cooling liquid inlet with the bottom extending outwards and a cooling liquid outlet with the top extending outwards away from one side of the cooling liquid inlet;
the valve pipe assembly comprises a nipple which is embedded at the top of the condenser and is positioned at the inner side of the condensing pipeline, a plurality of short circuit guide ports which extend out from the nipple towards the direction of the condensing pipeline, and a valve core which is movably arranged in the nipple and is used for controlling the opening and the closing of the short circuit guide ports;
the condenser pipeline includes along the feed inlet that the condenser top was extended, along the discharge gate that the condenser bottom was extended, set up the feed inlet with be used for the intercommunication between the discharge gate the condenser pipe and the condenser pipe inboard towards valve pipe assembly direction extends and a plurality of the short circuit interface that the short circuit guide port is connected, the condenser pipe appearance is the spiral design of multilayer condenser pipe, and every layer spiral pipe all level downward sloping, so that follow in the condenser pipe the short circuit interface flows in the oil-water mixture in the short circuit pipe can directly follow the discharge gate is derived.
Further, a water blocking portion is arranged on each layer of the condensation pipe, so that condensed water is collected on one side of each layer of the condensation pipe, which is higher in level, of the water blocking portion.
Furthermore, the appearance of the water retaining part is of an inverted V-shaped design.
Further, the short circuit interface is arranged at the bottom of the higher side of the water retaining part.
Further, the condenser also comprises a lifting rod arranged close to the condenser.
Further, the output end of the lifting rod is connected with the valve core, so that the valve core can slide along the track of the valve core in the nipple.
Further, a plurality of water retaining parts are arranged on the condensation pipe, and the bottom end of the nipple is communicated with the discharge port.
Compared with the prior art: the application provides an adjustable condensing device for light volatile oil, which comprises the steps that firstly, a preparer can inject cooling liquid into a condenser through a cooling liquid inlet, fill the condenser with the cooling liquid to pre-cool a condensing pipe arranged in the condenser, then connect a feed inlet with an external raw material discharge port, so that a high-temperature gaseous oil-water mixture can be introduced into the condensing pipe along the feed inlet to be condensed into a liquid oil-water mixture, in particular, a large amount of water vapor is generated before the high-temperature gaseous oil-water mixture enters a condensing pipeline in the actual volatile oil extraction process, is preferentially introduced into the condensing pipe through the feed inlet, the water vapor can be condensed in the pipe to form condensed water and pass through the condensing pipe, but as a water blocking part arranged on each layer of condensing pipe can block the condensed water, the condensed water is collected on one side with a higher water blocking part level, when the water collected at the water retaining part at the topmost layer exceeds the highest horizontal position of the water retaining part, the water flows into the next layer of condensing pipe along the uppermost condensing pipe, and is collected again at the water retaining part arranged at the lower layer of condensing pipe until the condensed water is collected at the water retaining part arranged at each layer of condensing pipe, then the gaseous oil-water mixture enters the condensing pipe and is condensed to form a liquid oil-water mixture, the liquid oil-water mixture can flow along the condensing pipe by attaching the water collected at the position of the condensing pipe close to the water retaining part, the contact between the oil-water mixture and the condensing pipe is reduced, the yield of volatile oil is improved, the structure is simple and reliable, the operation energy consumption is lower, the yield loss caused by adhesion of 15% -80% of light volatile oil can be obviously reduced, in addition, the volatile oil in the liquid oil-water mixture can be continuously reduced according to the temperature, the condition of viscosity increase occurs, the liquid oil-water mixture needs to be timely led out, therefore, the preparation personnel can adjust the height of the valve core between the multi-layer condensing pipes upwards, the short connection guide opening at the position of the first-layer condensing pipe with the best condensing effect of the liquid oil-water mixture is opened, so that the liquid oil-water mixture can flow into the short connection guide opening at the position of the first-layer condensing pipe with the best current effect in sequence and flow into the short connection pipe connected with the liquid oil-water mixture to be led out at the position of the discharge opening, the purpose of adjusting the path of the condensing pipe is realized, the condition that the viscosity of volatile oil in the liquid oil-water mixture is increased continuously during condensation is avoided, the condition that the viscosity of the volatile oil in the liquid oil-water mixture is increased when the valve core is increased is then the subsequent leading-out is realized, the temperature of the volatile oil in the liquid oil-water mixture is relatively higher and lower due to short contact time with the cooling liquid, and the premise that the temperature of the volatile oil in the liquid oil-water mixture is completely condensed to the liquid oil-water mixture is ensured, the problem that the current condenser is effectively solved due to the fact that the length of the inside condensing pipe is fixed and longer, the temperature of the liquid oil-water mixture is reduced to a lower level due to the fact that the viscosity of the volatile oil is increased at low temperature, and the whole course is easy to contact with the pipe wall in the condensing pipe, and the volatile oil is more serious influence on the condition that the volatile oil is more serious inner wall of the condensing pipe when passing through the longer condensing pipe, and the volatile oil is unable to separate the subsequent oil.
Drawings
FIG. 1 is a schematic cross-sectional view of an adjustable condensing device for light volatile oil according to an embodiment of the present application;
FIG. 2 is a schematic view in partial cross-section of a valve tube assembly and a condensing tube in an adjustable condensing apparatus for light-weight volatile oils in accordance with an embodiment of the present application;
FIG. 3 is a schematic view showing a part of a condensing pipeline in an adjustable condensing device for light volatile oil according to an embodiment of the present application;
FIG. 4 is a schematic diagram of an established coordinate system in an embodiment of the present application;
FIG. 5 is a schematic view of a cross-sectional coordinate system of a condensing tube during condensation in an embodiment of the present application;
fig. 6 is a schematic cross-sectional view of a condenser tube when a conventional condenser condenses.
Description of main reference numerals:
the following detailed description will further illustrate the application with reference to the above-described drawings.
Detailed Description
In order that the application may be readily understood, a more complete description of the application will be rendered by reference to the appended drawings. Several embodiments of the application are presented in the figures. This application may, however, be embodied in many different forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this application belongs. The terminology used herein in the description of the application is for the purpose of describing particular embodiments only and is not intended to be limiting of the application. The term "and/or" as used herein includes any and all combinations of one or more of the associated listed items.
Examples
Referring to fig. 1 to 6, an adjustable condensing device for light volatile oil in an embodiment of the application is shown, which comprises a condenser 1 and a valve tube assembly 3 embedded at the top of the condenser 1, wherein the condenser 1 comprises a condensing tube 4 arranged inside, the valve tube assembly 3 is arranged close to the condensing tube 4, the valve tube assembly 3 comprises a nipple 31 embedded at the top of the condenser 1 and positioned at the inner side of the condensing tube 4, a plurality of nipple guide ports 33 extending from the nipple 31 towards the condensing tube 4, and a valve core 32 movably arranged in the nipple 31 and used for controlling the opening and closing of the plurality of nipple guide ports 33, the condensing tube 4 comprises a feed port 41 extending from the top of the condenser 1, a discharge port 42 extending from the bottom of the condenser 1, a condensing tube 43 arranged between the feed port 41 and the discharge port 42, and a nipple interface 45 connected with the plurality of nipple guide ports 33 extending from the inner side of the condensing tube 43 towards the direction of the valve tube assembly 3, the shape of the condensing tube 43 is a spiral design of the multi-layer condensing tube, and each layer of the nipple 31 is horizontally inclined downwards, the bottom end of the nipple 31 is communicated with the discharge port 42, so that the oil mixture in the condenser tube 43 can flow into the nipple 42 along the nipple guide ports 42.
In the specific implementation, firstly, a preparation person can inject the cooling liquid into the condenser 1 through the cooling liquid inlet 11 and fill the condenser 1 with the cooling pipe 43 arranged in the condenser for pre-cooling treatment, in some alternative embodiments, liquid pumps can be respectively added at the cooling liquid inlet 11 and the cooling liquid outlet 12, and a liquid pump pipeline is connected with a refrigeration device in an external connection mode to form a cooling liquid pumping cycle in the condenser 1, and then the feed inlet 41 is connected with an external raw material discharge port, so that the high-temperature gaseous oil-water mixture can be introduced into the cooling pipe 43 along the feed inlet 41 for condensing treatment to form a final liquid oil-water mixture, and then the final liquid oil-water mixture is led out through the discharge port 42. Further, the condenser 1 further includes a cooling liquid inlet 11 with a bottom extending outward and a cooling liquid outlet 12 with a top extending outward away from the side of the cooling liquid inlet 11, and the condensation duct 43 has a spiral design with eleven layers, and in some alternative embodiments of the present application, the number of layers of the condensation duct 43 is not limited.
For example, assuming that the condensing tube 43 in a spiral design is provided with eleven layers as shown in fig. 1 of the specification, the number of layers of the condensing tube may be set according to the condensing effect in order to satisfy the condensing condition of the volatile oil. When the gaseous oil-water mixture is completely liquefied to form a liquid oil-water mixture at the seventh layer of condensing tube 43, if the recondensing path is too long, the temperature of the volatile oil is further lowered, which increases the viscosity of the volatile oil, resulting in the volatile oil adhering to the inner wall of the condensing tube. In this regard, in the embodiment of the present application, a preparation person may pull the valve core 32 upwards, so that the valve core 32 is sequentially separated from the short connection guide port 33 at the position from the eleventh layer to the seventh layer of the condensation pipe 43 at the bottom, so that the short connection guide port 33 directly flows into the discharge port 42 along the short connection pipe 31 to be led out, meanwhile, the liquid oil-water mixture originally remained at the position from the eleventh layer to the seventh layer of the condensation pipe 43 can flow into the short connection pipe 31 to the discharge port 42 along the short connection guide port 33 to be discharged, and the shortened oil-water mixture passes through the path of the condensation pipe 43, so as to achieve the effect of adjusting the liquid guiding path of the condensation pipe 43, and simultaneously reduce the contact area between the volatile oil and the pipe wall in the oil-water mixture, and improve the yield of the volatile oil.
In some alternative embodiments of the present application, a temperature sensor may be further disposed at the outlet 42 to obtain the current temperature of the liquid oil-water mixture discharged and observe the current viscosity, and when the temperature sensor detects that the temperature of the discharged oil-water mixture is too low, the current valve core 32 may be further moved to the position of the condensation pipe 43 with the best effect. It will be appreciated that when the elevation of the valve element 32 is higher, the liquid oil-water mixture to be subsequently discharged is shorter in contact time with the cooling liquid, so that the temperature of the volatile oil in the liquid oil-water mixture is relatively higher and the viscosity is lower, provided that the gaseous oil-water mixture is ensured to be completely condensed into the liquid oil-water mixture.
In addition, in order to facilitate the regulation and control of the valve core 32, a lifting rod 2 may be disposed at a side close to the condenser 1, an output end of the lifting rod 2 is connected to the valve core 32, so that the valve core 32 may slide along a track of the lifting rod in the nipple 31, in some alternative embodiments of the present application, the lifting rod 2 may be an electric lifting rod and a hydraulic lifting rod, a preparer may electrically connect the lifting rod 2 with a temperature sensor disposed at the discharge port 42, where the electrical connection may be a wireless connection and a wired connection, where the wireless connection includes but is not limited to a bluetooth connection, a WiFi, an IF radio frequency, and a zigbee, the wired connection includes but is not limited to a USB line connecting the temperature sensor and the lifting rod 2, a specific control may obtain temperature information of the liquid oil-water mixture fed back at the discharge port 42 through the temperature sensor, analyze the temperature information through a controller in the temperature sensor, and store initial control data in the controller. For example, when the temperature of the liquid oil-water mixture is ten degrees celsius, the corresponding valve core 32 is located at the position where the short connection guide port 33 is opened at the position of the ninth layer of the condensation pipe 43, when the temperature of the liquid oil-water mixture is twenty degrees celsius, the corresponding valve core 32 is located at the position where the short connection guide port 33 is opened at the position of the seventh layer of the condensation pipe 43, and the viscosities of the corresponding liquid oil-water mixtures at different temperatures are different, wherein the controller may be an MCU (Microcontroller Unit; micro control unit) chip, so as to control the lifting height of the lifting rod 2 through the MCU chip, and drive the valve core 32 to adjust the height in the shorting pipe 31, the preparer may determine the viscosity thereof according to the temperature of the liquid oil-water mixture, and input control parameters through the controller, so that the lifting rod 2 may drive the valve core 32 to adjust the use height in the shorting pipe 31 in real time according to the feedback temperature, thereby ensuring the quality and the acquisition of the liquid oil-water mixture guided along the discharge port 42, and being convenient for the operation and use of the preparer.
Further, in this embodiment, each layer of condensation pipes 43 is provided with a water blocking portion 44 protruding upwards, so that condensed water is collected at a side of the water blocking portion 44 having a higher level, the water blocking portion 44 is in an inverted V-shaped design, and a shorting connection 45 is provided at the bottom of the side of the water blocking portion 44 having a higher level.
Specifically, in the actual process of extracting volatile oil, steam is preferentially evaporated before the volatile oil, so that a large amount of steam is preferentially introduced into the condensation pipe 43 through the feed inlet 41 before the high-temperature gaseous oil-water mixture enters the condensation pipe 4, the steam is condensed in the pipe to form condensed water and passes through the condensation pipe 43, but because the water blocking part 44 arranged on each layer of condensation pipe 43 can block the condensed water, the condensed water is collected at one side of the water blocking part 44 with higher level, when the water collected at the water blocking part 44 at the topmost layer exceeds the highest level of the water blocking part 44, the water flows into the next layer of condensation pipe 43, and is collected again at the position where the water blocking part 44 is arranged at the lower layer of condensation pipe 43 until the condensed water is collected at the position where the water blocking part 44 is arranged at the topmost layer of condensation pipe 43 in the specification, such as the shadow part of the condensation pipe 43 arranged in the figure 2 of the specification. Meanwhile, after the gaseous oil-water mixture enters the condensing pipe 43, the gaseous oil-water mixture is condensed to form a liquid oil-water mixture, and as the condensing pipe 43 is covered by the collected water near the water retaining part 44, the liquid oil-water mixture can flow along the condensing pipe 43 along the water surface, so that the liquid oil-water mixture formed by condensation flows on the water surface in the condensing pipe, and the loss of the light volatile oil adhered to the inner wall of the condensing pipe is reduced and the yield of the volatile oil is improved by avoiding the contact between the light volatile oil in the oil-water mixture and the condensing pipe due to the rapid increase of the viscosity of the volatile oil in the oil-water mixture caused by too low temperature. The water retaining part 44 arranged at the condensing tube 43 can obviously reduce the yield loss of 15% -80% of light volatile oil caused by adhesion;
specifically, the dam reduces the adhesion of volatile oil as follows: let the inner radius of the condenser tube be R (constant), build as shown in the coordinate system of fig. 4, thereby yielding the formula:0 < y < 2R, shadow cross sectional area:the method comprises the steps of carrying out a first treatment on the surface of the Then->The cross section of the condensing tube in the condensation of the application as shown in fig. 5 is obtained according to the above formula, wherein H is the condensed water height, H2 is the oil-water mixture height, and the oil-water mixture cross section is as follows: />，/>，/>The oil-water mixture contacts the perimeter of the condenser tube: />；
Further, as shown in fig. 6, the section of the condensing tube is a section of a conventional condenser when condensing, wherein h1 is the height of the oil-water mixture, and the sectional area s1=of the oil-water mixture，/>The circumference of the oil-water mixture and the condenser tube are connected>The solution equation set can be obtained: />Thereby obtaining the loss percentage of volatile oil due to adhesion reduction>The loss of the light volatile oil caused by adhesion can be obviously reduced by 15% -80% by combining other factors and combining the above formulas.
The volatile oil in the oil-water mixture in the application is light volatile oil, and the specific characteristic is that the density is less than that of water, so that the effect that the liquid oil-water mixture formed by condensation flows on the water surface in the condensing tube is achieved, and the subsequent liquid oil-water mixture can be fused with water collected at the water retaining part 44 to normally circulate along the condensing tube 43 towards the discharge hole 42, wherein when the temperature is gradually reduced, the light volatile oil in the liquid oil-water mixture formed by condensation can be more easily adhered to the inner wall of the condensing tube 43 due to the increase of the viscosity, so that the loss of the volatile oil in the liquid oil-water mixture is caused, and the yield of the light volatile oil is reduced.
In summary, firstly, the preparation staff can firstly fill the cooling liquid into the condenser 1 through the cooling liquid inlet 11 and fill the condenser 1 with the condensing tube 43 arranged in the condenser 1 for precooling treatment, then connect the feed inlet 41 with the external raw material discharge port, so that the high-temperature gaseous oil-water mixture can be led into the condensing tube 43 along the feed inlet 41 for condensation treatment and converted into liquid oil-water mixture, in particular, a large amount of water vapor is firstly generated before the high-temperature gaseous oil-water mixture enters the condensing tube 4 in the actual essential oil extraction process, and is led into the condensing tube 43 through the feed inlet 41, the water vapor can be condensed in the tube to form condensed water and pass through the condensing tube 43, but because the water retaining part 44 arranged on each layer of condensing tube 43 can block the condensed water, the condensed water is positioned on one side higher than the water retaining part 44, when the water collected at the topmost layer of the water retaining part 44 exceeds the highest horizontal position, the water can flow into the next layer of the condensing tube 43 along the uppermost condensing tube 43, and is collected again at the lower layer of the condensing tube 43 until the water mixture is collected at the position of each layer of condensing tube 43, the water retaining tube 44 is arranged at the position of the liquid layer of the condensing tube 43, the water retaining tube is contacted with the water retaining tube 43, the water-oil-water mixture can continuously flow along the water retaining surface of the liquid oil-water mixture, the liquid oil-water mixture can be reduced, and the water mixture can flow along the water retaining tube is continuously due to the water retaining surface of the condensate, the water-water mixture can be reduced, and the water-water mixture can flow in time, and the condition is reduced due to the condition that the water-saving effect of the water-absorbing effect is reduced, the preparer can adjust the height of the valve core 32 between the multi-layer condensation pipes 43 upwards until the short connection guide opening 33 at the position of the layer condensation pipe 43 with the best condensation effect of the liquid oil-water mixture is opened, so that the liquid oil-water mixture can sequentially flow into the short connection pipe 31 connected with the liquid oil-water mixture along the position of the layer condensation pipe 43 with the best current effect and flow into the discharge hole 42 for guiding out, and the purpose of adjusting the path of the condensation pipe 43 is realized.
In the description of the present specification, a description referring to terms "one embodiment," "some embodiments," "examples," "specific examples," or "some examples," etc., means that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the present application. In this specification, schematic representations of the above terms do not necessarily refer to the same embodiments or examples. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.
The foregoing examples illustrate only a few embodiments of the application and are described in detail herein without thereby limiting the scope of the application. It should be noted that it will be apparent to those skilled in the art that several variations and modifications can be made without departing from the spirit of the application, which are all within the scope of the application. Accordingly, the scope of protection of the present application is to be determined by the appended claims.
Claims (4)
1. An adjustable condensing device for light volatile oil is characterized by comprising a condenser and a valve tube assembly embedded at the top of the condenser;
the condenser comprises a condensation pipeline arranged inside, the valve pipe assembly is arranged close to the condensation pipeline, and the condenser further comprises a cooling liquid inlet with the bottom extending outwards and a cooling liquid outlet with the top extending outwards away from one side of the cooling liquid inlet;
the valve pipe assembly comprises a nipple which is embedded at the top of the condenser and is positioned at the inner side of the condensing pipeline, a plurality of short circuit guide ports which extend out from the nipple towards the direction of the condensing pipeline, and a valve core which is movably arranged in the nipple and is used for controlling the opening and the closing of the short circuit guide ports;
the condenser pipeline includes the edge feed inlet that the condenser top was extended, edge discharge gate that the condenser bottom was extended, set up the feed inlet with be used for the intercommunication between the discharge gate the condenser pipe and the condenser pipe inboard is towards the valve pipe assembly direction is extended and is connected with a plurality of the short circuit interface that the short circuit was led out, the condenser pipe appearance is the spiral design of multilayer condenser pipe, and every layer spiral pipe all level downward sloping, so that follow in the condenser pipe the short circuit interface flows in the oily water mixture in the nipple can be directly followed the discharge gate is derived, every layer be provided with the manger plate portion on the condenser pipe, so that the comdenstion water is in every layer on the higher one side of manger plate portion level on the condenser pipe is collected, the manger plate portion appearance is the design of reverse V style of calligraphy, the short circuit interface is seted up the bottom of the higher one side of manger plate portion.
2. The adjustable condensing device for light-weight volatile oil of claim 1, further comprising a lift rod disposed proximate to the condenser.
3. The adjustable condensing device for light weight essential oils of claim 2, wherein the output end of the lifting rod is connected to the valve core so that the valve core can slide along its trajectory within the nipple.
4. The adjustable condensing device for light volatile oil according to claim 1, wherein a plurality of water retaining parts are arranged on the condensing tube, and the bottom end of the nipple is communicated with the discharge port.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202311084306.5A CN116785749B (en) | 2023-08-28 | 2023-08-28 | Adjustable condensing device for light volatile oil |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202311084306.5A CN116785749B (en) | 2023-08-28 | 2023-08-28 | Adjustable condensing device for light volatile oil |
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| Publication Number | Publication Date |
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| CN116785749A CN116785749A (en) | 2023-09-22 |
| CN116785749B true CN116785749B (en) | 2023-12-01 |
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| CN (1) | CN116785749B (en) |
Citations (8)
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| US11525377B1 (en) * | 2021-07-09 | 2022-12-13 | Hyundai Motor Company | Condensed water drainage device and exhaust system of a vehicle having the same |
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| DE29716538U1 (en) * | 1997-09-11 | 1999-01-28 | Aarcon Prauss Arminius GmbH, 10709 Berlin | Length-adjustable window pane condensate drainage device with integrated collecting container |
| KR20110112684A (en) * | 2010-04-07 | 2011-10-13 | (주)대일아쿠아 | Evaporated water recovery and plume abatement apparatus from the evaporated water vapor using condensing device and method using the same |
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| CN113171627A (en) * | 2021-04-14 | 2021-07-27 | 响水中山生物科技有限公司 | Distillation plant in adjustable bentazone production |
| US11525377B1 (en) * | 2021-07-09 | 2022-12-13 | Hyundai Motor Company | Condensed water drainage device and exhaust system of a vehicle having the same |
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| CN116785749A (en) | 2023-09-22 |
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