CN205796577U - A kind of extract Oleum Terebinthinae special recycle distillator - Google Patents
A kind of extract Oleum Terebinthinae special recycle distillator Download PDFInfo
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- CN205796577U CN205796577U CN201620655176.5U CN201620655176U CN205796577U CN 205796577 U CN205796577 U CN 205796577U CN 201620655176 U CN201620655176 U CN 201620655176U CN 205796577 U CN205796577 U CN 205796577U
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- Prior art keywords
- distillator
- extract
- oleum terebinthinae
- water separator
- steam
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Abstract
The utility model discloses a kind of extract Oleum Terebinthinae special recycle distillator, bucket, steam generator and cooler is contained including retinal, described retinal is contained bucket and is arranged on the left side of oil water separator, the extract that is provided above of described oil water separator exports, and the right side of oil water separator is provided with steam (vapor) outlet, the right side of described steam (vapor) outlet is provided with vapour compression machine, and the right side of described extract outlet is provided with admission port, and extract outlet be provided above cool down bucket；Compared with prior art, the beneficial effects of the utility model are: it is scientific and reasonable for structure that what this extraction Oleum Terebinthinae was special recycles distillator, safe and convenient to use, it is provided with on the right side of oil water separator and adds heat pipe and vapour compression machine, the water separating oil water separator is circulated utilization, decreases waste；The steam of low temperature can be pressurizeed and heat up by vapour compression machine, improves steam pressure and makes the purer quality of Oleum Terebinthinae of extraction higher.
Description
Technical field
This utility model belongs to Oleum Terebinthinae distillator technical field, be specifically related to a kind of extract Oleum Terebinthinae special circulation profit
Use distillator.
Background technology
Oleum Terebinthinae, is the one of quintessence oil, and it is a kind of important raw material of industry.Oleum Terebinthinae be by distillation or other
The liquid that method is extracted from the Colophonium of coniferale plant, main component is terpenes.With the pinaster rich in Colophonium as raw material, pass through
The volatility that different processing modes obtains has the terpenes mixed liquor of aromatic odor and is referred to as Oleum Terebinthinae.Terebinthine composition is with tree
Kind, the age of tree and the difference in the place of production and different, with top grade and the one-level Oleum Terebinthinae of Pinus massoniana Lamb pine gum processing, its main component is a-pinane
Alkene, next to that b-pinene, limonene etc..Also have a small amount of sesquiterpene, i.e. longifolene and caryophyllene.Oleum Terebinthinae is a kind of excellent
Organic solvent, is widely used in the industry such as paint, drier, adhesive.In recent years, Oleum Terebinthinae is more for compound probability.With
In alleviating myalgia, arthralgia, neuralgia and spraining.
Distillator is the utensil utilizing way of distillation separate substance.At ancient Chinese, it be generally used for alchemy, liquor processed,
Steam floral water etc..Different purposes has different shape systems and origin.Distillator is the utensil utilizing way of distillation separate substance.In
State ancient times, it is generally used for alchemy, liquor processed, steams floral water etc..Different purposes has different shape systems and origin.Make pills of immortality
Distillator in art is mostly derived from ancients and takes out the practice of sand refining hydrargyrum.Ancient Times in China hydrargyrum refining, be the earliest use the lowest
Temperature oxidizing roasting method, develops into during the Eastern Han Dynasty and airtight takes out hydrargyrum method, container is sealed, and during heating, the hydrargyrum that cinnabar decomposites steams
Vapour is condensate in container inner wall.
There are some defects in existing Oleum Terebinthinae during using, such as, extracts the steam water after Oleum Terebinthinae not
Can recycle, cause waste；Steam pressure is big not, and that extracts Oleum Terebinthinae is abundant not, and the product quality of production is inadequate
Good.
Utility model content
The purpose of this utility model be to provide a kind of extract Oleum Terebinthinae special recycle distillator, above-mentioned to solve
Propose in background technology can not recycle the problem inadequate with steam pressure.
For achieving the above object, this utility model provide following technical scheme: a kind of extract Oleum Terebinthinae special circulation profit
With distillator, containing bucket, steam generator and cooler including retinal, described retinal is contained bucket and is arranged on a left side for oil water separator
Side, the extract that is provided above of described oil water separator exports, and the right side of oil water separator is provided with steam (vapor) outlet, described
The right side of steam (vapor) outlet is provided with vapour compression machine, and the right side of described extract outlet is provided with admission port, and extract outlet
Be provided above cool down bucket, described cooling bucket is provided with connecting tube, described distillator be arranged on cooling bucket right side, and steam
The outside evaporating device is provided with Engergy saving full cover for cooking-vessel, described distillator be internally provided with sieve plate, and distillator be provided above cooler,
The lower section of described sieve plate is provided with ring pipe, and described steam generator is arranged on the right side of distillator, on described steam generator
Being provided with drain valve, the right side of described drain valve is provided with water level detection gauge, and the right side of described water level detection gauge is provided with hydraulic pressure
Table, described vapour compression machine, steam generator, hydralic pressure gauge and water level detection gauge are all electrically connected with external control panel.
Preferably, described ring pipe is provided with intensive spray orifice.
Preferably, described connecting tube is provided with the six roots of sensation altogether.
Preferably, described vapour compression machine is connected by connecting tube with steam generator.
Preferably, described steam generator is square structure.
Compared with prior art, the beneficial effects of the utility model are: what this extraction Oleum Terebinthinae was special recycles distillation
Device is scientific and reasonable for structure, safe and convenient to use, is provided with on the right side of oil water separator and adds heat pipe and vapour compression machine, to profit
The water that separator is separated is circulated utilization, decreases waste；The steam of low temperature can be pressurizeed and heat up by vapour compression machine
Improving steam pressure, the purer quality of Oleum Terebinthinae making extraction is higher.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model；
In figure: 1-Engergy saving full cover for cooking-vessel, 2-cooling bucket, 3-admission port, the outlet of 4-extract, 5-Oleum Terebinthinae contain bucket, 6-oil-water separation
Device, 7-add heat pipe, 8-vapour compression machine, 9-ring pipe, 10-sieve plate, 11-distillator, 12-steam generator, 13-hydralic pressure gauge,
14-water level detection gauge, 15-drain valve, 16-cooler, 17-connecting tube.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of this utility model rather than whole
Embodiment.Based on the embodiment in this utility model, those of ordinary skill in the art are not under making creative work premise
The every other embodiment obtained, broadly falls into the scope of this utility model protection.
Referring to Fig. 1, this utility model provides a kind of technical scheme: a kind of extract Oleum Terebinthinae special recycle distillation
Device, contains bucket 5, steam generator 12 and cooler 16 including Oleum Terebinthinae, and Oleum Terebinthinae is contained bucket 5 and is arranged on the left side of oil water separator 6,
The extract that is provided above of oil water separator 6 exports 4, and the right side of oil water separator 6 is provided with and adds heat pipe 7, adds heat pipe 7
Right side is provided with vapour compression machine 8, and the right side of extract outlet 4 is provided with admission port 3, and being provided above of extract outlet 4
Having cooling bucket 2, cooling bucket 2 is provided with connecting tube 17, distillator 11 is arranged on the right side of cooling bucket 2, and outside distillator 11
Side is provided with Engergy saving full cover for cooking-vessel 1, distillator 11 be internally provided with sieve plate 10, and distillator 11 be provided above cooler 16, sieve
The lower section of plate 10 is provided with ring pipe 9, and steam generator 12 is arranged on the right side of distillator 11, and steam generator 12 is provided with
Drain valve 15, the right side of drain valve 15 is provided with water level detection gauge 14, and the right side of water level detection gauge 14 is provided with hydralic pressure gauge 13, steams
Vapour compressor 8, steam generator 12, hydralic pressure gauge 13 and water level detection gauge 14 are all electrically connected with external control panel.
Intensive spray orifice it is provided with on ring pipe 9.Connecting tube 17 is provided with the six roots of sensation altogether.Vapour compression machine 8 and steam generation
Device 12 is connected by connecting tube.Steam generator 12 is square structure.
Oil water separator 6 in this utility model is to be controlled by filter element, glass fiber filter paper, heater and temperature, pressure
Device, electromagnetic valve and water accumulating cup composition, after the compressed air containing big gauging and water solid impurity enters oil water separator 6, oil
Water separates out and flows downwardly into the bottom of oil water separator 6 from steam flow, is carried out essence filtration by filter element the most again, and water droplet is at gravity
Instill separator bottom under effect, thus reach the effect separated；Vapour compression machine 8 in this utility model by compression is mainly
System, steam cooling device and three unit compositions of lubricating system, vapour compression machine 8 is that the heat recovery system steam to producing is by pressure
Contracting effect and improve the key equipment of vapor (steam) temperature and pressure, effect is that intensification of the steam of low temperature being pressurizeed reaches to fill Oleum Terebinthinae
Divide the requirement extracted；Steam generator 12 in this utility model be by water system, robot control system(RCS), flue and heating system and
Safety systems etc. form, and utilize the heat energy of fuel or other energy water to be heated as the plant equipment of hot water or steam.
Operation principle of the present utility model and use flow process: the special distillator that recycles of this extraction Oleum Terebinthinae installs
Later, being placed on by Colophonium on sieve plate 10, heated by the water in steam generator 12 and become water vapour, water vapour enters into distillator
In 11, when steam pressure is equal with ambient pressure, the Colophonium on sieve plate 10 will seethe with excitement, distill out together then as steam
Coming, the Oleum Terebinthinae distilled cools down in entering into cooler 16 and cooling bucket 2, and the Oleum Terebinthinae after cooling enters back into oil
Oleum Terebinthinae is separated by water separator 6 with water, and Oleum Terebinthinae flows into Oleum Terebinthinae by connecting tube and contains in bucket 5, and water can heat from adding heat pipe 7
Rear entrance vapour compression machine 8, vapour compression machine 8 is connected with steam generator 12 and recycles steam.
Embodiment the most of the present utility model, for the ordinary skill in the art,
It is appreciated that in the case of without departing from principle of the present utility model and spirit and these embodiments can be carried out multiple change, repair
Changing, replace and modification, scope of the present utility model is defined by the appended claims and the equivalents thereof.
Claims (5)
1. extract Oleum Terebinthinae special recycle a distillator, contain bucket (5), steam generator (12) and cold including Oleum Terebinthinae
But device (16), it is characterised in that: described Oleum Terebinthinae is contained bucket (5) and is arranged on the left side of oil water separator (6), described oil water separator
(6) be provided above extract outlet (4), and the right side of oil water separator (6) is provided with and adds heat pipe (7), described in add heat pipe
(7) right side is provided with vapour compression machine (8), and the right side of described extract outlet (4) is provided with admission port (3), and extract
Export (4) is provided above cooling bucket (2), and described cooling bucket (2) is provided with connecting tube (17), and described distillator (11) is pacified
Being contained in the right side of cooling bucket (2), and the outside of distillator (11) is provided with Engergy saving full cover for cooking-vessel (1), the inside of described distillator (11) sets
Be equipped with sieve plate (10), and distillator (11) be provided above cooler (16), the lower section of described sieve plate (10) is provided with annular
Pipe (9), described steam generator (12) is arranged on the right side of distillator (11), and described steam generator is provided with sluicing on (12)
Valve (15), the right side of described drain valve (15) is provided with water level detection gauge (14), and the right side of described water level detection gauge (14) is arranged
Have hydralic pressure gauge (13), described vapour compression machine (8), steam generator (12), hydralic pressure gauge (13) and water level detection gauge (14) all with
External control panel is electrically connected with.
The most according to claim 1 a kind of extract Oleum Terebinthinae special recycle distillator, it is characterised in that: described ring
Shape pipe is provided with intensive spray orifice on (9).
The most according to claim 1 a kind of extract Oleum Terebinthinae special recycle distillator, it is characterised in that: described company
Adapter (17) is provided with the six roots of sensation altogether.
The most according to claim 1 a kind of extract Oleum Terebinthinae special recycle distillator, it is characterised in that: described steaming
Vapour compressor (8) is connected by connecting tube with steam generator (12).
The most according to claim 1 a kind of extract Oleum Terebinthinae special recycle distillator, it is characterised in that: described steaming
Vapour generator (12) is square structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620655176.5U CN205796577U (en) | 2016-06-28 | 2016-06-28 | A kind of extract Oleum Terebinthinae special recycle distillator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620655176.5U CN205796577U (en) | 2016-06-28 | 2016-06-28 | A kind of extract Oleum Terebinthinae special recycle distillator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205796577U true CN205796577U (en) | 2016-12-14 |
Family
ID=57505823
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620655176.5U Expired - Fee Related CN205796577U (en) | 2016-06-28 | 2016-06-28 | A kind of extract Oleum Terebinthinae special recycle distillator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205796577U (en) |
-
2016
- 2016-06-28 CN CN201620655176.5U patent/CN205796577U/en not_active Expired - Fee Related
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Legal Events
| 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: 20161214 Termination date: 20170628 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |