CN210974594U - High-efficient distillation plant of cinnamomum micranthum hagata oil - Google Patents
High-efficient distillation plant of cinnamomum micranthum hagata oil Download PDFInfo
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- CN210974594U CN210974594U CN201921340068.9U CN201921340068U CN210974594U CN 210974594 U CN210974594 U CN 210974594U CN 201921340068 U CN201921340068 U CN 201921340068U CN 210974594 U CN210974594 U CN 210974594U
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Abstract
The utility model relates to a fragrant cinnamon oil refines technical field, discloses a high-efficient distillation plant of fragrant cinnamon oil, including distillation plant, distillation plant includes furnace, and furnace is put on the shelf and is equipped with the steamer, is provided with on the steamer and evaporates the steamer tray subassembly, and the steamer outside is provided with water storage box group, and water storage box group is located the furnace top, and water storage box group one end is provided with the comdenstion water import, the other end and steamer intercommunication. The utility model discloses can realize improving the energy utilization rate in the cinnamomum micranthum oil distillation process to increase and refine the purpose of efficiency, through set up the water storage box group in the steamer outside, water storage box group one end is provided with the comdenstion water import, and the other end and steamer intercommunication have solved current cinnamomum micranthum oil distillation plant and have had the temperature reduction in leading to the steamer after the comdenstion water backward flow, thereby influence the problem of distillation efficiency.
Description
Technical Field
The utility model relates to a fragrant cinnamon oil refines technical field, specifically indicates a fragrant cinnamon oil high efficiency distillation plant.
Background
Cinnamon and arbor. The young branches of the current year are densely covered by grayish yellow or faint yellow flat short hair, the shape is close to a quadrangular shape, the hair of the young branches of the second year gradually falls off, and the bud scales are densely covered by grayish yellow flat soft hair. The leaves are in the opposite, near-opposite or alternate growth, and the ventral surface is dark green and glossy. The cinnamon oil exists in the oil cells of the woody structure of the cinnamon, and the content of the cinnamon oil is different according to the biological characteristics, the variety, the conditions of the site and the season of the cinnamon. The main component of the cinnamon oil is safrole, and the safrole can be used for synthesizing various well-known famous flower fragrance type and milk fragrance type spices such as heliotropin, piperonyl acetone, vanillin and the like, so that the cinnamon oil is a foreign trade salable material and is also an important raw material related to light industry. There are many methods for extracting aromatic oil from plants, and three methods, i.e., a squeezing method, a distillation method and an extraction method, are commonly used. Because of the dispersion of raw material resources, the extraction of the cinnamomum subavenium primary oil generally adopts a steam distillation method.
Since the 80 s in the last century, the wild cinnamomum cassia oil grain plants are researched and developed in China, the production scale is gradually enlarged, the oil refining technology is gradually improved, the oil yield of primary processing is improved from about 1% to about 2%, and the following problems exist in the existing cinnamomum cassia oil distillation and extraction process:
the in-process that the cinnamomum micranthum hagata oil refined, cinnamomum micranthum hagata oil gets into condensing equipment along with steam to carry out water oil separating in condensing equipment, the steamer can be refluxed to the comdenstion water after the separation, because the temperature of comdenstion water is lower, can lead to temperature reduction in the steamer in directly flowing into the steamer, then direct influence distillation efficiency, and the cinnamomum micranthum hagata oil refines the in-process and causes a large amount of heat energy extravagant.
SUMMERY OF THE UTILITY MODEL
Based on the above problem, the utility model provides a high-efficient distillation plant of cinnamomum micranthum hagata oil. The utility model discloses can realize improving the energy utilization rate in the cinnamomum micranthum oil distillation process to increase and refine the purpose of efficiency, through set up the water storage box group in the steamer outside, water storage box group one end is provided with the comdenstion water import, and the other end and steamer intercommunication have solved current cinnamomum micranthum oil distillation plant and have had the temperature reduction in leading to the steamer after the comdenstion water backward flow, thereby influence the problem of distillation efficiency.
For solving the above technical problem, the utility model discloses a technical scheme as follows:
the utility model provides a high-efficient distillation plant of cinnamomum micranthum oil, includes distillation plant, distillation plant includes furnace, the furnace is put on the shelf and is equipped with the steamer, be provided with on the steamer and evaporate the steamer tray subassembly, the steamer outside is provided with water storage tank group, water storage tank group is located the furnace top, water storage tank group one end is provided with the comdenstion water import, and the other end communicates with the steamer.
In the utility model, the setting mode of the hearth can refer to the prior sweet osmanthus distilling equipment, if the distilling equipment is built by refractory bricks, and a fuel inlet is arranged on one side, the water storage box group can be built by refractory bricks and arranged above the hearth, when in use, fuel is added into the hearth to burn so as to generate steam in the steamer, the steam passes through the sweet osmanthus branches and leaves in the steamer component and carries out sweet osmanthus oil out and enters a condensing device, the condensing device can adopt the prior condensing device and an oil-water separating device, after condensation and multiple oil-water separation, condensed water flows out from a condensed water outlet of the oil-water separating device and flows into the water storage box group, because the water storage box group is positioned outside the steamer and above the hearth, the flame in the hearth can generate residual fire at the edge of the steamer when heating the steamer and can heat the water storage box group, then the condensed water in the hearth is heated, because the water storage box has a certain water storage function and the volume is far smaller than that of the steamer, the condensed water in the steam boiler can be quickly heated to high temperature, and the heated condensed water flows into the steam boiler again, so that the water temperature in the steam boiler is not reduced basically, the distillation efficiency is improved, and the distillation time is saved.
The utility model discloses can realize improving the energy utilization rate in the cinnamomum micranthum oil distillation process to increase and refine the purpose of efficiency, through set up the water storage box group in the steamer outside, water storage box group one end is provided with the comdenstion water import, and the other end and steamer intercommunication have solved current cinnamomum micranthum oil distillation plant and have had the temperature reduction in leading to the steamer after the comdenstion water backward flow, thereby influence the problem of distillation efficiency.
As a preferred mode, an annular flue is arranged above the hearth, the steam drawer assembly comprises a plurality of stacked steam drawers and a steam cover arranged on the steam drawer at the top end, and the steam cover is provided with an air collecting port.
As a preferred mode, the water storage tank group comprises a first water tank and a second water tank which are respectively arranged on the front side and the rear side of the steamer, one end of the first water tank is provided with a condensate water inlet, the other end of the first water tank is communicated with the second water tank, and the second water tank is communicated with the steamer.
As a preferred mode, the annular flue intercommunication is provided with the flue, it runs through to be provided with water tank three to cross the flue upper wall, three one ends of water tank communicate with water tank one, and the other end communicates with water tank two, the water inlet height of water tank one, water tank two and water tank three all is less than the water outlet height.
As a preferred mode, lifting lugs are arranged on the outer circumferential surfaces of the steaming drawer, the steaming pan and the steaming cover.
As a preferred mode, a ladder step furnace bridge is arranged in the hearth.
As a preferable mode, the ladder step furnace bridge divides the hearth into a combustion part and an ash deposition part, a fire extinguishing pipe penetrates through the side wall of the hearth, one end of the fire extinguishing pipe extends into the ash deposition part, and the other end of the fire extinguishing pipe is communicated with the water supply device.
In a preferred mode, a water distributor is arranged at one end of the fire extinguishing pipe extending into the dust deposition part.
Compared with the prior art, the beneficial effects of the utility model are that:
(1) the utility model discloses can realize improving the energy utilization rate in the cinnamomum micranthum oil distillation process to increase and refine the purpose of efficiency, through set up the water storage box group in the steamer outside, water storage box group one end is provided with the comdenstion water import, and the other end and steamer intercommunication have solved current cinnamomum micranthum oil distillation plant and have had the temperature reduction in leading to the steamer after the comdenstion water backward flow, thereby influence the problem of distillation efficiency.
(2) The utility model discloses well furnace top is provided with annular flue, evaporate the steamer tray subassembly and include that a plurality of superimposed evaporates the steamer tray and set up the lid that evaporates on the steamer tray is evaporated on the top, evaporate and cover and be provided with the gas collection mouth. Here annular flue accessible firebrick builds and establishes in the furnace top, evaporates the steamer tray and sets up to a plurality of back disposable distillations a large amount of cinnamomum subavenium to further improve distillation efficiency, steam carries cinnamomum subavenium oil and flows into condensing equipment through the gas collection mouth.
(3) The utility model discloses well water storage box group is including setting up water tank one and water tank two in the steamer front and back both sides respectively, water tank one end is provided with the comdenstion water import, the other end and two intercommunications of water tank, water tank two and steamer intercommunication. First and second water tank of this place can adopt the better metal of heat conductivility to make, receives the furnace structural constraint, erects the back on furnace when the steamer, and both sides have the excess fire to produce around the steamer, and both sides set up the temperature that first and second water tank of water tank can make full use of excess fire to the comdenstion water around the steamer promptly and heat, and the comdenstion water heats in letting in second water tank after heating in first water tank earlier, and twice heating makes the temperature rise by a wide margin, improves distillation efficiency.
(4) The utility model discloses well annular flue intercommunication is provided with the flue, it runs through to be provided with water tank three to cross the flue upper wall, three one ends of water tank and water tank one intercommunication, the other end and two intercommunications of water tank, the height of intaking of water tank one, water tank two and water tank three all is less than out the water height.
High-temperature smoke dust flows into the flue from the annular flue, and heat a water tank III embedded in the upper end of the flue, the water tank III can be made of metal with better heat conduction performance, condensed water sequentially enters a water tank I, the water tank III, the water tank II and a steamer, the water temperature is basically the same as the water temperature in the steamer after three times of heating, under the condition that energy consumption is not increased, the condensed water is heated by using the temperatures of remaining fire and the high-temperature smoke dust, the water temperature flowing into the steamer meets the use requirement, the distillation efficiency and the energy utilization rate are improved, the water inlet heights of the water tank I, the water tank II and the water tank III are all lower than the water outlet height, certain liquid level height of the condensed water in the water tank is ensured, the heating time is more sufficient, and the joints of the water tanks can adopt bent pipes.
(5) The utility model discloses well evaporate steamer tray, steamer and evaporate the outer periphery that covers and all be provided with the lug, be convenient for load and dismantle steamer tray, steamer and evaporate the lid through the lug.
(6) The utility model discloses well ladder step grate divide into combustion portion and deposition portion with furnace, the furnace lateral wall runs through and is provided with the fire extinguishing pipe, fire extinguishing pipe one end extends into deposition portion, the other end and water supply installation intercommunication. The fuel is packed into to ladder step grate upper portion combustion portion promptly, and the ashes after the fuel burning fall into the grate lower part deposition portion promptly, because contain partial mars in the ashes, the staff is easily scalded by the mars when handling ashes, pours out the mars of ashes in the deposition portion after letting in the cooling water to the fire extinguishing pipe through water supply installation, solves the problem of handling ashes easy dusting simultaneously because of the mars problem of scalding.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
Fig. 2 is a schematic view of the structure of the reclaimed water tank set of the present invention.
The device comprises a lifting lug 1, a distillation device 2, an air collecting port 3, a steam drawer assembly 4, a steam cover 41, a steam drawer 42, a steam boiler 5, a water tank III 6, a condensate water inlet 7, a fire extinguishing pipe 17, a flue 18 passing through, a water distributor 19, an ash deposition part 20, a step grate 21, a hearth 22, a combustion part 23, an annular flue 24, a water tank II 25 and a water tank I26.
Detailed Description
The present invention will be further described with reference to the accompanying drawings. Embodiments of the present invention include, but are not limited to, the following examples.
Example 1:
referring to fig. 1 ~ 2, a high-efficient distillation plant of cinnamomum micranthum oil, including distillation plant 2, distillation plant 2 includes furnace 22, furnace 22 is put on the shelf and is equipped with steamer 5, be provided with steamer tray subassembly 4 on steamer 5, the 5 outsides of steamer are provided with the water storage tank group, the water storage tank group is located furnace 22 top, water storage tank group one end is provided with comdenstion water import 7, and the other end communicates with steamer 5, and the water storage tank group can set up to water tank one 26 and water tank two 25 that distributes both sides around the steamer.
In the utility model, the setting mode of the hearth 22 can refer to the existing sweet osmanthus distilling equipment, if the existing sweet osmanthus distilling equipment is built by refractory bricks, and a fuel inlet is arranged on one side, the water storage box group can be built by refractory bricks and arranged above the hearth 22, when in use, fuel is added into the hearth 22 to burn so as to generate steam in the steamer 5, the steam passes through the sweet osmanthus in the steamer component 4 and then takes out the sweet osmanthus oil and enters the condensing device, the condensing device can adopt the existing condensing equipment and oil-water separating equipment, after condensation and multiple oil-water separation, the condensed water flows out from a condensed water outlet of the oil-water separating equipment and flows into the water storage box group through a condensed water inlet 7, because the water storage box group is positioned outside the steamer 5 and above the hearth 22, the flame in the hearth 22 generates the residual fire at the edge of the steamer 5 when heating the steamer 5 and can heat the water storage box group, and then the condensed water in the inner part is heated, because the water storage tank has a certain water storage function and the volume of the water storage tank is far smaller than that of the steamer 5, the condensed water in the water storage tank can be rapidly heated to high temperature, and the heated condensed water flows into the steamer 5 again, so that the temperature of the water in the steamer 5 is basically not reduced, the distillation efficiency is improved, and the distillation time is saved.
The utility model discloses can realize improving the energy utilization rate in the cinnamomum micranthum oil distillation process to increase and refine the purpose of efficiency, through set up the water storage box group in the steamer outside, water storage box group one end is provided with the comdenstion water import, and the other end and steamer intercommunication have solved current cinnamomum micranthum oil distillation plant and have had the temperature reduction in leading to the steamer after the comdenstion water backward flow, thereby influence the problem of distillation efficiency.
Example 2:
referring to fig. 1-2, a high-efficient distillation plant of cinnamomum micranthum oil, including distillation plant 2, distillation plant 2 includes furnace 22, furnace 22 is put on the shelf and is equipped with steamer 5, be provided with steamer tray subassembly 4 on the steamer 5, the 5 outsides of steamer are provided with water storage tank group, water storage tank group is located furnace 22 top, water storage tank group one end is provided with comdenstion water import 7, the other end and 5 intercommunications of steamer.
An annular flue 24 is arranged above the hearth 22, the steaming drawer assembly 4 comprises a plurality of stacked steaming drawers 42 and a steaming cover 41 arranged on the top steaming drawer 42, and the steaming cover 41 is provided with an air collecting port 3.
In this embodiment, the annular flue 24 can be laid above the hearth 22 by refractory bricks, and the plurality of steaming drawers 42 can be used for distilling a large amount of cinnamomum japonicum at one time, so that the distilling efficiency is further improved, and the steam carrying cinnamomum japonicum oil flows into the condensing device through the air collecting port 3.
As a preferred mode, the water storage tank group comprises a first water tank 26 and a second water tank 25 which are respectively arranged on the front side and the rear side of the steamer 5, one end of the first water tank 26 is provided with a condensed water inlet 7, the other end of the first water tank is communicated with the second water tank 25, and the second water tank 25 is communicated with the steamer 5. In this mode, here water tank 26 and water tank two 25 can adopt the better metal of thermal conductivity to make, receive furnace 22 structural limitation, after 5 erects on furnace 22 of steamer, both sides have the excess fire to produce around 5 of steamer, both sides set up water tank 26 and water tank two 25 around 5 of steamer promptly can make full use of the temperature of excess fire heat the comdenstion water, the comdenstion water heats in letting in water tank two 25 after heating in water tank 26 earlier, twice heating makes the temperature rise by a wide margin, improve distillation efficiency.
As a preferred mode, the annular flue 24 is communicated with the flue 18, the upper wall of the flue 18 penetrates through a third water tank 6, one end of the third water tank 6 is communicated with a first water tank 26, the other end of the third water tank is communicated with a second water tank 25, and the water inlet height of the first water tank 26, the second water tank 25 and the third water tank 6 is lower than the water outlet height.
In the mode, high-temperature smoke dust flows into the flue 18 from the annular flue 24, and heat the water tank III 6 embedded in the upper end of the flue 18, the water tank III 6 can be made of metal with better heat conduction performance, condensed water sequentially enters the water tank I26, the water tank III 6, the water tank II 25 and the steamer 5, the water temperature is basically the same as the water temperature in the steamer 5 after three times of heating, under the condition that energy consumption is not increased, the temperature of the residual fire and the high-temperature smoke dust is utilized to heat the condensed water, the water temperature flowing into the steamer 5 meets the use requirement, the distillation efficiency and the energy utilization rate are improved, the water inlet heights of the water tank I26, the water tank II 25 and the water tank III 6 are all lower than the water outlet height, the condensed water has a certain liquid level height in the water tank, the heating time is more sufficient, and the joint of the water tanks can adopt bent pipes.
In a preferable mode, the steaming drawer 42, the steaming pan 5 and the steaming cover 41 are provided with lifting lugs 1 on the outer circumferential surfaces. In this way, the lifting lugs 1 are convenient for loading and unloading the steaming drawer 42, the steaming pan 5 and the steaming cover 41.
In a preferred mode, a step furnace bridge 21 is arranged in the hearth 22.
In a preferable mode, the step furnace bridge 21 divides the hearth 22 into a combustion part 23 and an ash deposition part 20, a fire extinguishing pipe 17 penetrates through the side wall of the hearth 22, one end of the fire extinguishing pipe 17 extends into the ash deposition part 20, and the other end of the fire extinguishing pipe is communicated with a water supply device. In this mode, the fuel is loaded into the combustion part 23 which is the upper part of the ladder step furnace bridge 21, the ash after the fuel combustion falls into the ash deposition part 20 which is the lower part of the furnace bridge, because the ash contains partial sparks, the worker is easily scalded by the sparks when handling the ash, the sparks of the ash in the ash deposition part 20 are cast out after the cooling water is introduced into the fire extinguishing pipe 17 through the water supply device, and the problem of burning due to the sparks is solved and the problem of easy dusting when handling the ash is solved.
In a preferred manner, a water distributor 19 is provided at the end of the fire extinguishing pipe 17 extending into the dust deposition part. In the mode, the cooling water can be uniformly dispersed on ash through the water distributor 19, and the fire extinguishing area is increased.
The other parts of this embodiment are the same as embodiment 1, and are not described herein again.
The embodiment of the present invention is the above. The specific parameters in the above embodiments and examples are only for the purpose of clearly showing the verification process of the present invention, and are not used to limit the patent protection scope of the present invention, which is still subject to the claims, and all the equivalent structural changes made by using the contents of the specification and the drawings of the present invention should be included in the protection scope of the present invention.
Claims (8)
1. The utility model provides a high-efficient distillation plant of cinnamomum micranthum oil, includes distillation plant (2), distillation plant (2) include furnace (22), furnace (22) are put on the shelf and are equipped with steamer (5), be provided with on steamer (5) and evaporate steamer tray subassembly (4), its characterized in that: steamer (5) outside is provided with water storage tank group, water storage tank group is located furnace (22) top, water storage tank group one end is provided with comdenstion water import (7), the other end and steamer (5) intercommunication.
2. The efficient cinnamomum cassia oil distillation equipment according to claim 1, which is characterized in that: the annular flue (24) is arranged above the hearth (22), the steam drawer assembly (4) comprises a plurality of stacked steam drawers (42) and steam covers (41) arranged on the steam drawers (42) at the top ends, and the steam covers (41) are provided with air collecting ports (3).
3. The efficient cinnamomum cassia oil distillation equipment according to claim 1, which is characterized in that: the water storage tank set comprises a first water tank (26) and a second water tank (25) which are arranged on the front side and the rear side of the steamer (5) respectively, one end of the first water tank (26) is provided with a condensate water inlet (7), the other end of the first water tank is communicated with the second water tank (25), and the second water tank (25) is communicated with the steamer (5).
4. The efficient cinnamomum cassia oil distillation equipment according to claim 2, wherein the efficient cinnamomum cassia oil distillation equipment comprises: the annular flue (24) intercommunication is provided with crosses flue (18), it runs through on flue (18) upper wall and is provided with water tank three (6), water tank three (6) one end and water tank one (26) intercommunication, the other end and water tank two (25) intercommunication, the water inlet height of water tank one (26), water tank two (25) and water tank three (6) all is less than the delivery port height.
5. The efficient cinnamomum cassia oil distillation equipment according to claim 1, which is characterized in that: lifting lugs (1) are arranged on the outer circumferential surfaces of the steaming drawer (42), the steaming pan (5) and the steaming cover (41).
6. The efficient cinnamomum cassia oil distillation equipment according to claim 5, wherein the efficient cinnamomum cassia oil distillation equipment comprises: a step furnace bridge (21) is arranged in the hearth (22).
7. The efficient cinnamomum cassia oil distillation equipment according to claim 6, wherein the efficient cinnamomum cassia oil distillation equipment comprises: the furnace hearth (22) is divided into a combustion part (23) and an ash deposition part (20) by the ladder step furnace bridge (21), a fire extinguishing pipe (17) penetrates through the side wall of the furnace hearth (22), one end of the fire extinguishing pipe (17) extends into the ash deposition part (20), and the other end of the fire extinguishing pipe is communicated with a water supply device.
8. The efficient cinnamomum cassia oil distillation equipment according to claim 7, wherein the efficient cinnamomum cassia oil distillation equipment comprises: one end of the fire extinguishing pipe (17) extending into the dust deposition part is provided with a water distributor (19).
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| Application Number | Priority Date | Filing Date | Title |
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| CN201921340068.9U CN210974594U (en) | 2019-08-16 | 2019-08-16 | High-efficient distillation plant of cinnamomum micranthum hagata oil |
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| CN201921340068.9U CN210974594U (en) | 2019-08-16 | 2019-08-16 | High-efficient distillation plant of cinnamomum micranthum hagata oil |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110358634A (en) * | 2019-08-16 | 2019-10-22 | 蓬溪县民欣香桂有限责任公司 | A kind of efficient distillation equipment of fragrant cassia oil |
| CN113425155A (en) * | 2021-07-30 | 2021-09-24 | 李胜 | Steamer capable of recycling steam and control method thereof |
-
2019
- 2019-08-16 CN CN201921340068.9U patent/CN210974594U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110358634A (en) * | 2019-08-16 | 2019-10-22 | 蓬溪县民欣香桂有限责任公司 | A kind of efficient distillation equipment of fragrant cassia oil |
| CN113425155A (en) * | 2021-07-30 | 2021-09-24 | 李胜 | Steamer capable of recycling steam and control method thereof |
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