CN206746047U - A kind of fir essential oil production oily-water seperating equipment of optimization design - Google Patents

A kind of fir essential oil production oily-water seperating equipment of optimization design Download PDF

Info

Publication number
CN206746047U
CN206746047U CN201720454433.3U CN201720454433U CN206746047U CN 206746047 U CN206746047 U CN 206746047U CN 201720454433 U CN201720454433 U CN 201720454433U CN 206746047 U CN206746047 U CN 206746047U
Authority
CN
China
Prior art keywords
separation container
dividing plate
collecting pipe
feed tube
pipe
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201720454433.3U
Other languages
Chinese (zh)
Inventor
徐春三
邱求金
徐正忠
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fujian Xinlyulin Products Development Co Ltd
Original Assignee
Fujian Xinlyulin Products Development Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fujian Xinlyulin Products Development Co Ltd filed Critical Fujian Xinlyulin Products Development Co Ltd
Priority to CN201720454433.3U priority Critical patent/CN206746047U/en
Application granted granted Critical
Publication of CN206746047U publication Critical patent/CN206746047U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The utility model discloses a kind of fir essential oil production oily-water seperating equipment of optimization design, including separation container;The top of separation container is provided with the condensate line no less than one, and separation container is provided with oil spill pipe by top sidewall, and separation container is provided with drainpipe by bottom sidewall;It is provided with collecting pipe in separation container at center along the vertical direction, the height of collecting pipe bottom face is suitable with position height at the middle waist of separation container;The bottom face of collecting pipe is provided with the internal face seamless connectivity of loop buffer dividing plate, the side face of buffer dividing plate largest contours and the corresponding position of separation container;The bottom week of buffer dividing plate inner ring surface and collecting pipe is along seamless connectivity;Gathered in buffer dividing plate and be provided with multiple through holes;Condensate line quantity is two, is first, second feed tube respectively;First, second feed tube is each provided at the top of collecting pipe, and first feed tube is mutually arranged oppositely with second feed tube.Liquid level stationarity influence of the feed liquor on separation container is small, and oil-water separation is more preferable.

Description

A kind of fir essential oil production oily-water seperating equipment of optimization design
Technical field
The utility model belongs to the extractive technique field of fir essential oil, and the fir essential oil production for being related to a kind of optimization design is used Oily-water seperating equipment.
Background technology
Contain substantial amounts of fir essential oil in China fir, its main component is cedrene, cedar wood alcohol etc., available for perfume industry In.At present, the extraction processing of fir essential oil is mainly using solvent extraction method, cracking process, steam distillation.Using solvent extraction The oil yield of method extraction fir essential oil is high compared with the oil yield of steam distillation, but needs substantial amounts of solvent, and subsequent treatment is complicated, The problem of high energy consumption, dissolvent residual be present.Oil yield using cracking process extraction fir essential oil is higher, but it is a chemical mistake Journey, obtained essential oil contain the materials such as substantial amounts of tar, phenol, aldehyde and ketone, have a strong impact on the quality of fir essential oil.Steam distillation The fir essential oil quality of method extraction is best, clear, aroma of pure, is best suitable for being used for blending, and its extraction process is pure thing Reason process, it is pollution-free, but oil yield is relatively low.Several techniques compare, and steam distillation is the production work of preferable environment-friendly type Skill, but should also optimize to improve yield and further reduce energy consumption.Steam distillation extracts the step of fir essential oil It is:A, China fir is ground into fir powder;B, dispensing is added into fir powder and is stirred mixing;C, the fir powder mixed is sent Enter in destilling tower, superheated steam is passed through into destilling tower and is distilled, distillation time is 9-11 hours;That is discharged after D, distilling is mixed Close gas be delivered to cooled down in cooling tower after obtain oil mixing with water liquid;E, oil mixing with water liquid obtains after water-oil separating Fir essential oil.
Oily-water seperating equipment is the equipment of whole flow process most terminal, therefore the efficiency of oily-water seperating equipment is related to whole China fir The efficiency of another name for oil production.The effect quality of water-oil separating is heavily dependent on separation container 2 in dynamic continuous production The stationarity of liquid level.
The structure of fir essential oil production oily-water seperating equipment of the prior art is as shown in figure 1, including separation container 2; The top of separation container 2 is provided with the condensate line 1 no less than one, and the side wall by top of separation container 2 is provided with oil spill pipe 3, the side wall by bottom of separation container 2 is provided with drainpipe 4.
Using the oily-water seperating equipment of such technology it is of course possible to use, but due to the feed liquor impact meeting pair of condensate line 1 The stationarity of the liquid level of separation container 2 has relatively large influence, causes the effect of water-oil separating not good enough, using effect is also It is not ideal enough.
Utility model content
For overcome the deficiencies in the prior art, a kind of influence of the feed liquor of the utility model offer to the stationarity of liquid level is small, oil The fir essential oil production oily-water seperating equipment of the more preferable optimization design of effect of water separation, using effect are more preferable.
The utility model is that technical scheme is used by reaching above-mentioned technical purpose:A kind of fir essential oil of optimization design Production oily-water seperating equipment, including separation container;The top of separation container is provided with the condensate line no less than one, and separation is held The side wall by top of device is provided with oil spill pipe, and the side wall by bottom of separation container is provided with drainpipe;In separation container Collecting pipe is inserted with along the vertical direction at center, the position at the position height of the bottom face of collecting pipe and the middle waist of separation container Put height quite;The bottom face of collecting pipe is provided with the buffer dividing plate of annular, and the side face of the largest contours of buffer dividing plate holds with separating The internal face seamless connectivity of the corresponding position of device;The inner ring surface of buffer dividing plate and the bottom week of collecting pipe are along seamless connectivity;It is slow Rush to gather on dividing plate and be provided with multiple through holes;The quantity of condensate line is two, is first feed tube, second feed tube respectively;First is entered Liquid pipe and second feed tube are each provided at the top of collecting pipe, and first feed tube is mutually arranged oppositely with second feed tube.
Described separation container is the separation container of cylinder;Described collecting pipe is columnar collecting pipe;Separation is held Device is coaxially disposed with collecting pipe;Described buffer dividing plate is the buffer dividing plate of annular, and the outer diameter of a circle of buffer dividing plate is with dividing It is equal from the inner peripheral surface diameter of container;The interior diameter of a circle of buffer dividing plate is equal with the outer diameter of a circle of collecting pipe.
The bottom surface of described separation container is provided with funnelform conical bottom, and the lowermost end of conical bottom is provided with blow-off pipe.
Described oil spill pipe, drainpipe, the valve that regulating flow quantity is equipped with blow-off pipe three.
The utility model has the advantage of:Due to being inserted with collecting pipe along the vertical direction at the center in separation container, The position height of the bottom face of collecting pipe is suitable with the position height at the middle waist of separation container;The bottom face of collecting pipe is provided with ring The internal face seamless connectivity of the buffer dividing plate of shape, the side face of the largest contours of buffer dividing plate and the corresponding position of separation container;It is slow The inner ring surface of dividing plate and the bottom week of collecting pipe are rushed along seamless connectivity;Gathered in buffer dividing plate and be provided with multiple through holes;Condensation The quantity of liquid pipe is two, is first feed tube, second feed tube respectively;First feed tube and second feed tube are each provided at the top of collecting pipe Portion, first feed tube are mutually arranged oppositely with second feed tube.
Therefore, the two strands of feed liquors separately flowed into from first feed tube and second feed tube import after first relative eating up part of small impulsive force Collecting pipe is simultaneously flowed out from bottom of the tube of confluxing to surrounding, and water body can be sunk to the bottom, and oil body can float, due to the filtering resiliency of buffer dividing plate Stop, the process that oil body floats more relaxes, and the slag charge in feed liquor can be blocked in the bottom surface of buffer dividing plate and sinking, floating Influence of the oil body to the stationarity of the liquid level of separation container is with regard to very little, and for the effect of water-oil separating with regard to more preferable, using effect is more preferable.
Brief description of the drawings
The utility model is described in further detail with reference to the accompanying drawings and examples.Wherein:
Fig. 1 is the schematic diagram of the oily-water seperating equipment of prior art;
Fig. 2 is subdivision schematic diagram of the present utility model.
Marker number in accompanying drawing is described as follows:Condensate line 1, first feed tube 1A, second feed tube 1B, separation container 2, overflow Oil pipe 3, drainpipe 4, collecting pipe 5, buffer dividing plate 6, conical bottom 7, blow-off pipe 8
Embodiment
Embodiment of the present utility model, as shown in Fig. 2 a kind of fir essential oil production of optimization design is filled with water-oil separating Put, including separation container 2;The top of separation container 2 is provided with no less than the condensate line of one, separation container 2 by top Side wall is provided with oil spill pipe 3, and the side wall by bottom of separation container 2 is provided with drainpipe 4;At center in separation container 2 Collecting pipe 5 is inserted with along the vertical direction, and the position height of the bottom face of collecting pipe 5 and the position at the middle waist of separation container 2 are high Degree is suitable;The bottom face of collecting pipe 5 is provided with the buffer dividing plate 6 of annular, the side face and separation container of the largest contours of buffer dividing plate 6 The internal face seamless connectivity of 2 corresponding position;The inner ring surface of buffer dividing plate 6 and the bottom week of collecting pipe 5 are along seamless connectivity;It is slow Rush to gather on dividing plate 6 and be provided with multiple through holes;The quantity of condensate line is two, is first feed tube 1A, second feed tube 1B respectively; First feed tube 1A and second feed tube 1B is each provided at the top of collecting pipe 5, and first feed tube 1A is mutually to be arranged oppositely with second feed tube 1B 's.
Described separation container 2 is the separation container 2 of cylinder;Described collecting pipe 5 is columnar collecting pipe 5;Point It is coaxially disposed from container 2 and collecting pipe 5;Described buffer dividing plate 6 is the buffer dividing plate 6 of annular, buffer dividing plate 6 it is cylindrical Diameter is equal with the inner peripheral surface diameter of separation container 2;The outer diameter of a circle phase of the interior diameter of a circle of buffer dividing plate 6 and collecting pipe 5 Deng.
The bottom surface of described separation container 2 is provided with funnelform conical bottom 7, and the lowermost end of conical bottom 7 is provided with blow-off pipe 8。
Described oil spill pipe 3, drainpipe 4, the valve that regulating flow quantity is equipped with the three of blow-off pipe 8.

Claims (4)

1. a kind of fir essential oil production oily-water seperating equipment of optimization design, including separation container;Set at the top of separation container There is a condensate line no less than one, the side wall by top of separation container is provided with oil spill pipe, and separation container leans on bottom Side wall is provided with drainpipe;It is characterized in that:Collecting pipe, collecting pipe are inserted with along the vertical direction at center in separation container The position height of bottom face it is suitable with the position height at the middle waist of separation container;The bottom face of collecting pipe is provided with the slow of annular Rush the internal face seamless connectivity of dividing plate, the side face of the largest contours of buffer dividing plate and the corresponding position of separation container;Buffer dividing plate Inner ring surface and collecting pipe bottom week along seamless connectivity;Gathered in buffer dividing plate and be provided with multiple through holes;Condensate line Quantity is two, is first feed tube, second feed tube respectively;First feed tube and second feed tube are each provided at the top of collecting pipe, and first is entered Liquid pipe is mutually arranged oppositely with second feed tube.
A kind of 2. fir essential oil production oily-water seperating equipment of optimization design according to claim 1, it is characterised in that: Described separation container is the separation container of cylinder;Described collecting pipe is columnar collecting pipe;Separation container is with confluxing Pipe is coaxially disposed;Described buffer dividing plate is the buffer dividing plate of annular, the outer diameter of a circle and separation container of buffer dividing plate Inner peripheral surface diameter is equal;The interior diameter of a circle of buffer dividing plate is equal with the outer diameter of a circle of collecting pipe.
A kind of 3. fir essential oil production oily-water seperating equipment of optimization design according to claim 2, it is characterised in that: The bottom surface of described separation container is provided with funnelform conical bottom, and the lowermost end of conical bottom is provided with blow-off pipe.
A kind of 4. fir essential oil production oily-water seperating equipment of optimization design according to claim 3, it is characterised in that: Described oil spill pipe, drainpipe, the valve that regulating flow quantity is equipped with blow-off pipe three.
CN201720454433.3U 2017-04-27 2017-04-27 A kind of fir essential oil production oily-water seperating equipment of optimization design Expired - Fee Related CN206746047U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720454433.3U CN206746047U (en) 2017-04-27 2017-04-27 A kind of fir essential oil production oily-water seperating equipment of optimization design

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720454433.3U CN206746047U (en) 2017-04-27 2017-04-27 A kind of fir essential oil production oily-water seperating equipment of optimization design

Publications (1)

Publication Number Publication Date
CN206746047U true CN206746047U (en) 2017-12-15

Family

ID=60615758

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720454433.3U Expired - Fee Related CN206746047U (en) 2017-04-27 2017-04-27 A kind of fir essential oil production oily-water seperating equipment of optimization design

Country Status (1)

Country Link
CN (1) CN206746047U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106902550A (en) * 2017-04-27 2017-06-30 福建鑫绿林产品开发有限公司 A kind of fir essential oil production oily-water seperating equipment of optimization design

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106902550A (en) * 2017-04-27 2017-06-30 福建鑫绿林产品开发有限公司 A kind of fir essential oil production oily-water seperating equipment of optimization design

Similar Documents

Publication Publication Date Title
CN206746047U (en) A kind of fir essential oil production oily-water seperating equipment of optimization design
CN101817586A (en) Spiral-flow water-distribution hydrocyclone internal-circulation anaerobic reactor
CN201485442U (en) Energy-saving type white wine distilling device
CN204434326U (en) A kind of dish-style water-and-oil separator
CN106902550A (en) A kind of fir essential oil production oily-water seperating equipment of optimization design
CN201362614Y (en) Internal circulation anaerobic reactor for cyclone water distribution cyclone separation
CN202315444U (en) Multilayer precipitator
CN108905290B (en) Oil-water separator with interception device and volatile oil extraction system
CN209276482U (en) A kind of volatile oil extracting system
CN203508213U (en) Impulse jetting foam flotation machine
CN206700819U (en) A kind of fir essential oil production alembic for facilitating efficiency higher of slagging tap
CN208678442U (en) A kind of oily water separating equipment of san-mou oil
CN206706054U (en) A kind of fir essential oil production alembic of optimization design
CN202942692U (en) Cyclone desander
CN204727863U (en) Improve the volatile oil extractor of distillate pipe
CN206706055U (en) One kind, which is stirred, turns over formula fir essential oil production alembic
CN201940071U (en) Separation and collection device for traditional Chinese medicinevolatile oil
CN204737938U (en) Volatile oil extractor
CN203639196U (en) Annular sectional plug-flow coalescence structure for vertical tank
CN203741094U (en) Multi-effect equipment for removing oil from brine
CN204643960U (en) Boosting type anaerobic jar reaction solution sampling unit
CN205055993U (en) Oil -water phase reation kettle
CN205948417U (en) Laboratory is with plant polysaccharide reaction liquid extraction knockout
CN202778736U (en) Separator used for dewaxing of petroleum microorganism
CN104086622B (en) Extraction production cottonseed protein circulation dephenolize device and its technique

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20171215

Termination date: 20210427

CF01 Termination of patent right due to non-payment of annual fee