CN203593740U - Heat recovery rapid-discharging type flower essential oil separating distillation system - Google Patents
Heat recovery rapid-discharging type flower essential oil separating distillation system Download PDFInfo
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- CN203593740U CN203593740U CN201320846091.1U CN201320846091U CN203593740U CN 203593740 U CN203593740 U CN 203593740U CN 201320846091 U CN201320846091 U CN 201320846091U CN 203593740 U CN203593740 U CN 203593740U
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Abstract
The utility model discloses a heat recovery rapid-discharging type flower essential oil separating distillation system. The heat recovery rapid-discharging type flower essential oil separating distillation system comprises a steam boiler, a distillation tower, a condensing tower and a separating device which are connected in sequence. The separating device comprises an essential oil outlet pipe, a cone tank body and a base tank body which are sequentially arranged from top to bottom. One end of the essential oil outlet pipe is fixed on the small end face of the cone tank body, the base tank body is fixed on the large end face of the cone tank body, a side wall of the cone tank body is provided with a material mixing feeding hopper, the material mixing feeding hopper is communicated with a feeding pipe extending into the inside of the base tank body, a side wall of the essential oil outlet pipe is communicated with an oil outlet pipe, a side wall of the cone tank body is communicated with a hydrolat outlet pipe, the distance between one end of the oil outlet pipe connected with the essential oil outlet pipe and the small end face of the cone tank body is 5-10cm, and the diameter of the hydrolat outlet pipe is smaller than that of the small end face of the cone tank body. The heat recovery rapid-discharging type flower essential oil separating distillation system has the advantages that the system is simple in structure, time for waiting for essential oil removal is shortened, and the essential oil material remaining amount is small.
Description
Technical field
The utility model relates to flowers essential oil and separates, and specifically the fast emission type flowers of recovery of heat essential oil separates Distallation systm.
Background technology
Traditional flowers essential oil tripping device comprises staving, staving upper end is provided with feed pipe, feed pipe inserts staving inside, staving sidewall is provided with 2 pipelines, 1 pipeline is essential oil output channel, 1 pipeline is hydrosol output channel, wherein essential oil output channel position is higher than hydrosol output channel, its operating method is, hydrosol output channel is sealed, essential oil material level is in hydrosol material upper strata, hydrosol material below is water, after conventional way is the sealing of hydrosol output channel, liquid level liquid in staving raises gradually, treat that essential oil material discharge from essential oil output channel, after for some time, when hydrosol material is too much, open hydrosol output channel discharge unit hydrosol material, so reciprocally repeatedly operate, but there is a defect in said structure, due to the essential oil material of layering, hydrosol material, water is all positioned at same staving, while only having isolated essential oil material abundant, could discharge essential oil material, itself is because the amount of essential oil material is few, therefore the time of waiting for out essential oil material is more of a specified duration, and the speed of discharging essential oil material is fast not, for this reason, we need to improve said apparatus, make the essential oil material discharging waiting time short, stay remaining essential oil material in device as far as possible few.
Utility model content
The purpose of this utility model is to provide the fast emission type flowers of a kind of recovery of heat essential oil to separate Distallation systm.
The purpose of this utility model is achieved through the following technical solutions: the fast emission type flowers of recovery of heat essential oil separates Distallation systm, comprise the steam boiler connecting successively, distillation tower, condensing tower, tripping device, the steam-pipe of steam boiler is passed in distillation tower, in distillation tower, be provided with flowers supporter, the lower end of distillation tower is communicated with steam-pipe, the upper end of distillation tower is communicated with condensing tower, the lower end of condensing tower is provided with phlegma relief outlet, phlegma relief outlet is communicated with tripping device, in condensing tower, be provided with interchanger, interchanger one termination cold water pipe, another termination hot-water line of interchanger, tripping device comprises the essential oil outlet pipe setting gradually from top to bottom, vertebra tank body, end tank body, essential oil outlet pipe, essential oil outlet pipe one end is fixed on the small end face of vertebra tank body, end tank body is fixed on the large end face of vertebra tank body, vertebra tank wall is provided with batch mixing hopper, batch mixing hopper is communicated with the feed-pipe that extends into end tank interior, essential oil outlet pipe sidewall is communicated with oil outlet pipe, vertebra tank wall is communicated with hydrosol and goes out pipe, wherein the distance between one end and the vertebra tank body small end face of oil outlet pipe connection essential oil outlet pipe is 5cm to 10cm, the diameter that hydrosol goes out pipe is less than the diameter of vertebra tank body small end face, batch mixing hopper is communicated with phlegma relief outlet, the hot-water line of condensing tower is connected with flow guide heat preservation pipe by transparent plastic bottle, and flow guide heat preservation pipe is communicated in steam boiler.
Steam boiler produces high temperature and high pressure steam, high temperature and high pressure steam is passed in distillation tower by steam-pipe, flowers are placed on flowers supporter, under the effect of steam, distill, and the essential oil material in flowers is liquid compound with discharge of steam to condensing tower internal conversion; Compound is discharged in tripping device from the phlegma relief outlet of the lower end of condensing tower, carries out the separating treatment of essential oil material by tripping device.Hot water in hot-water line is input in steam boiler by flow guide heat preservation pipe, completes recovery of heat, adopts transparent plastic bottle as interconnecting piece simultaneously, is convenient to observe aquifer yield.
The mode that said structure is dealt with problems is: utilize the essential oil outlet pipe of minor diameter as essential oil material parking space, utilize the vertebra tank body of taper as the parking space of hydrosol material, utilize the parking space of end tank body as water.According to essential oil material, hydrosol material, the shared capacity distribution of water of output and the space that oneself matches, reach with this object that goes out fast essential oil material, thereby shorten the time of waiting for essential oil discharging, reduce residue and leave the essential oil material in device in.This device operation logic is: essential oil material, hydrosol material, the compound that water forms enters end tank interior by batch mixing hopper through feed-pipe, due to essential oil material, hydrosol material, water active layered, essential oil material is to floating, be positioned at end tank body topmost, hydrosol material level is in essential oil material lower region, water level is in bottom region, so, ceaselessly slowly enter after compound, essential oil material, hydrosol material, water increases gradually, through calculating, when essential oil material is full of behind the region between one end and the vertebra tank body small end face that oil outlet pipe connects essential oil outlet pipe, hydrosol material side group originally overflows the space of vertebra tank body, water overflows end tank body.Now along with compound continue splash into, can start essential oil material.Along with compound continue splash into, after liquid level on hydrosol material arrives oil outlet pipe lower zone, now, essential oil material is got rid of completely, can open the hydrosol material that hydrosol goes out tube drainage part, so repeatedly, can rack up the container of replacing splendid attire essential oil material after essential oil material at every turn, and because the material space that holds of each material changes, can cause the waiting time of essential oil material to shorten.In like manner, can discharge port be set at end tank body, overflow while going out to manage to hydrosol until water, can open the discharge port of end tank body, the water of discharge unit.Judge that the water method that goes out pipe to hydrosol of overflowing is, when opening hydrosol and going out the water that pipe flows out, can think that water overflows to hydrosol and go out pipe.
Through calculating, one end that general hydrosol goes out pipe connection vertebra tank body is end A, and end A is 4 cm to 8cm to vertebra tank body small end face distance in the vertical direction.
For despumation, oil outlet pipe is provided with filter screen device to the essential oil outlet pipe region between vertebra tank body small end face.
For despumation, in batch mixing hopper, be provided with filter cloth.
Oil outlet pipe connects one end of essential oil outlet pipe lower than oil outlet pipe away from one end of essential oil outlet pipe.
Hydrosol goes out pipe and goes out lower than hydrosol one end that pipe connects vertebra tank body away from one end of vertebra tank body.
Hydrosol goes out pipe and is provided with valve.
The utility model has the advantage of: simple in structure, shorten and wait for the essential oil eliminating time, the essential oil material amount of leaving over is few.
Accompanying drawing explanation
Fig. 1 is the structural representation of tripping device.
Fig. 2 is the planing surface structural representation of Fig. 1.
Fig. 3 is structural representation of the present utility model.
Fig. 4 is the structural representation of condensing tower.
Reference numeral in figure is expressed as: 1, essential oil outlet pipe; 2, vertebra tank body; 3, end tank body; 4, oil outlet pipe; 5, hydrosol goes out pipe; 6, batch mixing hopper; 7, feed-pipe; 11, steam boiler; 12, distillation tower; 13, condensing tower; 14, tripping device; 15, cold water pipe; 16, hot-water line; 17, transparent plastic bottle; 18, flow guide heat preservation pipe; 19, support platform.
Embodiment
Below in conjunction with embodiment and accompanying drawing, the utility model is described in further detail, but embodiment of the present utility model is not limited to this.
Embodiment 1:
As shown in Figure 1.
The fast emission type flowers of recovery of heat essential oil separates Distallation systm, comprise the steam boiler 11 connecting successively, distillation tower 12, condensing tower 13, tripping device 14, the steam-pipe of steam boiler 11 is passed in distillation tower 12, in distillation tower 12, be provided with flowers supporter, the lower end of distillation tower 12 is communicated with steam-pipe, the upper end of distillation tower 12 is communicated with condensing tower 13, the lower end of condensing tower 13 is provided with phlegma relief outlet, phlegma relief outlet is communicated with tripping device, in condensing tower 13, be provided with interchanger, interchanger one termination cold water pipe 15, another termination hot-water line 16 of interchanger, tripping device comprises the essential oil outlet pipe 1 setting gradually from top to bottom, vertebra tank body 2, end tank body 3, essential oil outlet pipe 1, essential oil outlet pipe 1 one end is fixed on the small end face of vertebra tank body 2, end tank body 3 is fixed on the large end face of vertebra tank body 2, vertebra tank body 2 sidewalls are provided with batch mixing hopper 6, batch mixing hopper 6 is communicated with the feed-pipe 7 that extends into end tank body 3 inside, essential oil outlet pipe 1 sidewall is communicated with oil outlet pipe 4, vertebra tank body 2 sidewalls are communicated with hydrosol and go out pipe 5, wherein to connect the distance between one end and the vertebra tank body small end face of essential oil outlet pipe 1 be 5cm to 10cm to oil outlet pipe 4, hydrosol goes out the diameter that pipe 5 diameter is less than vertebra tank body 2 small end faces, batch mixing hopper 6 is communicated with phlegma relief outlet.The hot-water line 16 of condensing tower 13 is connected with flow guide heat preservation pipe 18 by transparent plastic bottle 17, and flow guide heat preservation pipe 18 is communicated in steam boiler 11.Steam boiler 11 produces high temperature and high pressure steam, high temperature and high pressure steam is passed in distillation tower 12 by steam-pipe, flowers are placed on flowers supporter, under the effect of steam, distill, and the essential oil material in flowers is liquid compound with discharge of steam to condensing tower 13 internal conversions; Compound is discharged in tripping device from the phlegma relief outlet of the lower end of condensing tower 13, carries out the separating treatment of essential oil material by tripping device.Hot water in hot-water line 16 is input in steam boiler by flow guide heat preservation pipe 18, completes recovery of heat, adopts transparent plastic bottle 17 as interconnecting piece simultaneously, is convenient to observe aquifer yield.
The mode that said structure is dealt with problems is: utilize the essential oil outlet pipe 1 of minor diameter as essential oil material parking space, utilize the vertebra tank body 2 of taper as the parking space of hydrosol material, utilize the parking space of end tank body 3 as water.According to essential oil material, hydrosol material, the shared capacity distribution of water of output and the space that oneself matches, reach with this object that goes out fast essential oil material, thereby shorten the time of waiting for essential oil discharging, reduce residue and leave the essential oil material in device in.This device operation logic is: essential oil material, hydrosol material, the compound that water forms enters tank body 3 inside in the end by batch mixing hopper 6 through feed-pipe 7, due to essential oil material, hydrosol material, water active layered, essential oil material is to floating, be positioned at end tank body 3 topmosts, hydrosol material level is in essential oil material lower region, water level is in bottom region, so, ceaselessly slowly enter after compound, essential oil material, hydrosol material, water increases gradually, through calculating, when essential oil material is full of behind the region between one end and the vertebra tank body small end face that oil outlet pipe 4 connects essential oil outlet pipe 1, hydrosol material side group originally overflows the space of vertebra tank body 2, water overflows end tank body 3.Now along with compound continue splash into, can start essential oil material.Along with compound continue splash into, after liquid level on hydrosol material arrives oil outlet pipe 4 lower zones, now, essential oil material is got rid of completely, can open the hydrosol material that hydrosol goes out pipe 5 discharge units, so repeatedly, can rack up the container of replacing splendid attire essential oil material after essential oil material at every turn, and because the material space that holds of each material changes, can cause the waiting time of essential oil material to shorten.In like manner, can discharge port be set at end tank body 3, overflow to hydrosol and go out pipe at 5 o'clock until water, can open the discharge port of end tank body 3, the water of discharge unit.Judging that water overflows goes out pipe 5 method to hydrosol and is, when opening hydrosol and going out the water that pipe 5 flows out, can think that water overflows to hydrosol and go out pipe 5.
Through calculating, one end that general hydrosol goes out pipe 5 connection vertebra tank bodies is end A, and end A is 4 cm to 8cm to vertebra tank body small end face distance in the vertical direction.
For despumation, oil outlet pipe 4 is provided with filter screen device to essential oil outlet pipe 1 region between vertebra tank body 2 small end faces.
For despumation, in batch mixing hopper 6, be provided with filter cloth.
Hydrosol goes out pipe 5 one end away from vertebra tank body 2 and goes out lower than hydrosol one end that pipe 5 connects vertebra tank body 2.
Hydrosol goes out pipe 5 and is provided with valve.
As mentioned above, can well realize the utility model.
Claims (8)
1. the fast emission type flowers of recovery of heat essential oil separates Distallation systm, it is characterized in that: comprise the steam boiler (11) connecting successively, distillation tower (12), condensing tower (13), tripping device (14), the steam-pipe of steam boiler (11) is passed in distillation tower (12), distillation tower is provided with flowers supporter in (12), the lower end of distillation tower (12) is communicated with steam-pipe, the upper end of distillation tower (12) is communicated with condensing tower (13), the lower end of condensing tower (13) is provided with phlegma relief outlet, phlegma relief outlet is communicated with tripping device, condensing tower is provided with interchanger in (13), interchanger one termination cold water pipe (15), another termination hot-water line (16) of interchanger, tripping device comprises the essential oil outlet pipe (1) setting gradually from top to bottom, vertebra tank body (2), end tank body (3), essential oil outlet pipe (1), essential oil outlet pipe (1) one end is fixed on the small end face of vertebra tank body (2), end tank body (3) is fixed on the large end face of vertebra tank body (2), vertebra tank body (2) sidewall is provided with batch mixing hopper (6), batch mixing hopper (6) is communicated with and extends into the inner feed-pipe (7) of end tank body (3), essential oil outlet pipe (1) sidewall is communicated with oil outlet pipe (4), vertebra tank body (2) sidewall is communicated with hydrosol and goes out pipe (5), wherein the distance between one end and the vertebra tank body small end face of oil outlet pipe (4) connection essential oil outlet pipe (1) is 5cm to 10cm, the diameter that hydrosol goes out pipe (5) is less than the diameter of vertebra tank body (2) small end face, batch mixing hopper (6) is communicated with phlegma relief outlet, the hot-water line (16) of condensing tower (13) is connected with flow guide heat preservation pipe (18) by transparent plastic bottle (17), and flow guide heat preservation pipe (18) is communicated in steam boiler (11).
2. the fast emission type flowers of recovery of heat according to claim 1 essential oil separates Distallation systm, it is characterized in that: one end that hydrosol goes out pipe (5) connection vertebra tank body is end A, and end A is 4 cm to 8cm to vertebra tank body small end face distance in the vertical direction.
3. the fast emission type flowers of recovery of heat according to claim 1 essential oil separates Distallation systm, it is characterized in that: oil outlet pipe (4) is provided with filter screen device to essential oil outlet pipe (1) region between vertebra tank body (2) small end face.
4. the fast emission type flowers of recovery of heat according to claim 1 essential oil separates Distallation systm, it is characterized in that: batch mixing hopper is provided with filter cloth in (6).
5. the fast emission type flowers of recovery of heat according to claim 1 essential oil separates Distallation systm, it is characterized in that: oil outlet pipe (4) connects one end of essential oil outlet pipe (1) lower than oil outlet pipe (4) away from one end of essential oil outlet pipe (1).
6. the fast emission type flowers of recovery of heat according to claim 1 essential oil separates Distallation systm, it is characterized in that: hydrosol goes out pipe (5) and goes out lower than hydrosol one end that pipe (5) connects vertebra tank body (2) away from one end of vertebra tank body (2).
7. the fast emission type flowers of recovery of heat according to claim 1 essential oil separates Distallation systm, it is characterized in that: hydrosol goes out pipe (5) and is provided with valve.
8. the fast emission type flowers of recovery of heat according to claim 1 essential oil separates Distallation systm, it is characterized in that: condensing tower (13) is fixed in support platform (19).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320846091.1U CN203593740U (en) | 2013-12-20 | 2013-12-20 | Heat recovery rapid-discharging type flower essential oil separating distillation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320846091.1U CN203593740U (en) | 2013-12-20 | 2013-12-20 | Heat recovery rapid-discharging type flower essential oil separating distillation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203593740U true CN203593740U (en) | 2014-05-14 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320846091.1U Expired - Fee Related CN203593740U (en) | 2013-12-20 | 2013-12-20 | Heat recovery rapid-discharging type flower essential oil separating distillation system |
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| Country | Link |
|---|---|
| CN (1) | CN203593740U (en) |
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2013
- 2013-12-20 CN CN201320846091.1U patent/CN203593740U/en not_active Expired - Fee Related
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140514 Termination date: 20141220 |
|
| EXPY | Termination of patent right or utility model |