CN108117923A - A kind of Zanthoxylum essential oil production technology - Google Patents

A kind of Zanthoxylum essential oil production technology Download PDF

Info

Publication number
CN108117923A
CN108117923A CN201711186550.7A CN201711186550A CN108117923A CN 108117923 A CN108117923 A CN 108117923A CN 201711186550 A CN201711186550 A CN 201711186550A CN 108117923 A CN108117923 A CN 108117923A
Authority
CN
China
Prior art keywords
essential oil
chinese prickly
prickly ash
zanthoxylum essential
oil
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.)
Pending
Application number
CN201711186550.7A
Other languages
Chinese (zh)
Inventor
余和春
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.)
Hongya County And Prosperous Development In Agricultural Science And Technology Co Ltd
Original Assignee
Hongya County And Prosperous Development In Agricultural Science And Technology 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 Hongya County And Prosperous Development In Agricultural Science And Technology Co Ltd filed Critical Hongya County And Prosperous Development In Agricultural Science And Technology Co Ltd
Priority to CN201711186550.7A priority Critical patent/CN108117923A/en
Publication of CN108117923A publication Critical patent/CN108117923A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B1/00Production of fats or fatty oils from raw materials
    • C11B1/02Pretreatment
    • C11B1/04Pretreatment of vegetable raw material
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B1/00Production of fats or fatty oils from raw materials
    • C11B1/10Production of fats or fatty oils from raw materials by extracting
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B3/00Refining fats or fatty oils

Abstract

A kind of Zanthoxylum essential oil production technology, is related to Zanthoxylum essential oil production technical field.Including screening Chinese prickly ash, impurity is removed.Chinese prickly ash and edible oil are mixed and added to Zanthoxylum essential oil process units.The mixture of Chinese prickly ash and edible oil is subjected to heating and thermal insulation, heating temperature is 90~160 DEG C, and heating time is 1.5~2.5h, is centrifugally separating to obtain preliminary working Zanthoxylum essential oil.The steam of the spilling when carrying out heating and thermal insulation is collected, and steam is cooled down, collects coolant.Coolant is subjected to water-oil separating, oil is taken, obtains pepper aroma essential oil.And pepper aroma essential oil and preliminary working Zanthoxylum essential oil are pressed 1:500~2000 weight ratio is mixed to get refined Zanthoxylum essential oil.It can be improved in Chinese prickly ash refinement degree, promoted Chinese prickly ash oil quality, substantially improved the mellowness degree of Zanthoxylum essential oil, improve product quality quality and market value.

Description

A kind of Zanthoxylum essential oil production technology
Technical field
The present invention relates to Zanthoxylum essential oil production technical field, in particular to a kind of Zanthoxylum essential oil production technology.
Background technology
Chinese prickly ash oil quality made from existing Zanthoxylum essential oil production technology is general, unknown compared to traditional Zanthoxylum essential oil increased quality Aobvious, with the raising of people’s lives level, existing Zanthoxylum essential oil can not meet pursuit of the people to high-quality food, flower The quality and market value of green pepper oil are difficult to get a promotion.
The content of the invention
It is an object of the invention to provide a kind of Zanthoxylum essential oil production technologies, can greatly improve in Chinese prickly ash oil production process In to the refinement degree of Chinese prickly ash, greatly improve the active constituent content of Zanthoxylum essential oil obtained, promote Chinese prickly ash oil quality;Improve original The utilization rate of material reduces the wasting of resources;The mellowness degree of Zanthoxylum essential oil can be substantially improved simultaneously, greatly improve product quality product Matter and market value.
What the embodiment of the present invention was realized in:
A kind of Zanthoxylum essential oil production technology, including:Chinese prickly ash is screened, removes impurity.Chinese prickly ash and edible oil are mixed and added into To Zanthoxylum essential oil process units.The mixture of Chinese prickly ash and edible oil is subjected to heating and thermal insulation, heating temperature is 90~160 DEG C, heating Time is 1.5~2.5h, is centrifugally separating to obtain preliminary working Zanthoxylum essential oil.The steam of the spilling when carrying out heating and thermal insulation is collected, and it is right Steam is cooled down, and collects coolant.Coolant is subjected to water-oil separating, oil is taken, obtains pepper aroma essential oil.And by Chinese prickly ash Volatile oil presses 1 with preliminary working Zanthoxylum essential oil:500~2000 weight ratio is mixed to get refined Zanthoxylum essential oil.
Further, pepper aroma essential oil is 1 with the weight ratio of preliminary working Zanthoxylum essential oil:800~1500.
Further, it is 2h to the heating time of the mixture of Chinese prickly ash and edible oil.
Further, it is 100~150 DEG C to the heating temperature of the mixture of Chinese prickly ash and edible oil.
Further, Zanthoxylum essential oil process units includes Zanthoxylum essential oil extraction element, cooling device and oily-water seperating equipment.Chinese prickly ash Oil extract device includes heating groove cylinder, conveying mechanism and cover.Conveying mechanism is set up in heating tank cylinder, and conveying mechanism, which has, to be used for To heating groove cylinder conveying Chinese prickly ash and by the Chinese prickly ash by refinement from the foraminous conveyer of heating groove cylinder output, conveying mechanism, which also has, to be used In the power set that power is provided for foraminous conveyer.Cover covers at the one side of the separate heating groove cylinder of conveying mechanism and for sealing Close heating groove cylinder.Heating groove cylinder has heating arrangements, oil inlet and oil outlet, and cover is equipped with for by the steam in heating process Derived steam pipe.The port of export of steam pipe is connected with the input end of cooling device, the same water-oil separating of the port of export of cooling device The input end connection of device.
Further, foraminous conveyer includes charging guipure and discharging guipure.Charging guipure is arranged on feed end and for that will spend Green pepper is delivered to heating groove cylinder.One end of the close charging guipure of discharging guipure is arranged on the close heating tank cylinder bottom portion of charging guipure One side, and for accepting the Chinese prickly ash sent by charging guipure.Discharge guipure the other end towards away from heating tank bottom of chamber portion one side It bends and extends to discharge end.Discharging guipure for carrying Chinese prickly ash to be refined, and for by by the Chinese prickly ash that refines from adding Heat channel cylinder exports.
Further, Zanthoxylum essential oil process units further includes the elevator for conveying mechanism to be taken out from heating groove cylinder.
Further, heating groove cylinder is additionally provided with to filter out the dregs filter of Chinese prickly ash particle, and dregs filter is arranged on heating tank One end of the close oil outlet of cylinder.
Further, the feed end of conveying mechanism is provided with the charging deslagging device to remove the gred to Chinese prickly ash.
The advantageous effect of the embodiment of the present invention is:
Zanthoxylum essential oil production technology provided in an embodiment of the present invention during Chinese prickly ash and edible oil Hybrid Heating by will generate Steam cooled down and carry out water-oil separating, pepper aroma essential oil can be obtained.Pepper aroma essential oil is added in into preliminary working flower The mellowness degree of preliminary working Zanthoxylum essential oil can be substantially improved after in green pepper oil, obtains refined Zanthoxylum essential oil, greatly promotes the quality of product And market value.
By the way that pepper aroma essential oil is added in preliminary working Zanthoxylum essential oil, the mellowness degree of Zanthoxylum essential oil can be substantially improved, is obtained To refined Zanthoxylum essential oil, this has the effect of highly significant for Zanthoxylum essential oil flavoring, increasing alcohol, greatly improves quality and the city of product Field value.
Further, pepper aroma essential oil is 1 with the weight ratio of preliminary working Zanthoxylum essential oil:500~2000.It is added in the ratio Pepper aroma essential oil can not only substantially improve mellowness degree and mouthfeel, and refined Zanthoxylum essential oil obtained is for food process When, will not other flavorings or food be formed with excessive interference, be not in that other condiment or taste of food spy is completely covered The situation of sign can preferably keep the flavor attributes of other flavorings together of food in itself, promote food mouthfeel.
The steaming that Zanthoxylum essential oil production technology provided in an embodiment of the present invention will generate during Chinese prickly ash and edible oil Hybrid Heating Vapour is collected, and is passed through refrigerated separation and obtained pepper aroma essential oil, substantially increases the more of product output rate and product Sample.Multiple product is can obtain by producing Zanthoxylum essential oil, substantially increases the quantum of output of single production procedure so that in Chinese prickly ash Active ingredient can fully be extract and can be fully used, substantially increase in Chinese prickly ash oil production process to flower The refinement degree of green pepper.The utilization rate of raw material is so not only increased, reduces the wasting of resources, and so that production cost is lower It is honest and clean.
In general, Zanthoxylum essential oil production technology provided in an embodiment of the present invention can be greatly improved in Chinese prickly ash oil production process In to the refinement degree of Chinese prickly ash, greatly improve the active constituent content of refined Zanthoxylum essential oil obtained, promote refined Chinese prickly ash oil quality. The utilization rate of raw material is improved, reduces the wasting of resources.And the mellowness degree of refined Zanthoxylum essential oil can be substantially improved, greatly improve production The quality and market value of product.
Description of the drawings
It in order to illustrate the technical solution of the embodiments of the present invention more clearly, below will be to needed in the embodiment attached Figure is briefly described, it should be understood that the following drawings illustrates only certain embodiments of the present invention, therefore is not construed as pair The restriction of scope, for those of ordinary skill in the art, without creative efforts, can also be according to this A little attached drawings obtain other relevant attached drawings.
Fig. 1 is the schematic diagram of Zanthoxylum essential oil process units provided in an embodiment of the present invention.
Icon:1000- Zanthoxylum essential oil process units;100- Zanthoxylum essential oil extraction elements;110- heats groove cylinder;111- heaters Structure;112- oil inlets;113- oil outlets;120- conveying mechanisms;121- feeds guipure;122- discharging guipures;140- covers;141- Steam pipe;150- elevators;160- dregs filters;170- feeds deslagging device;180- universal wheels;190- adjusts lower margin;200- Cooling device;300- oily-water seperating equipments.
Specific embodiment
To make the purpose, technical scheme and advantage of the embodiment of the present invention clearer, below in conjunction with the embodiment of the present invention In attached drawing, the technical solution in the embodiment of the present invention is clearly and completely described, it is clear that described embodiment is Part of the embodiment of the present invention, instead of all the embodiments.The present invention implementation being usually described and illustrated herein in the accompanying drawings The component of example can configure to arrange and design with a variety of.
Therefore, below the detailed description of the embodiment of the present invention to providing in the accompanying drawings be not intended to limit it is claimed The scope of the present invention, but be merely representative of the present invention selected embodiment.Based on the embodiments of the present invention, this field is common Technical staff's all other embodiments obtained without creative efforts belong to the model that the present invention protects It encloses.
It should be noted that:Similar label and letter represents similar terms in following attached drawing, therefore, once a certain Xiang Yi It is defined, then it further need not be defined and explained in subsequent attached drawing in a attached drawing.
In addition, term " vertical " etc. is not offered as requiring component absolute upright, but can be slightly tilted.Such as " vertical " only It is more vertical with respect to for " parallel " to simply mean to its direction, is not to represent that the structure is had to completely vertically, but can be slightly Low dip.
" substantially ", the terms such as " basic " are intended to illustrate that related content is not absolute accurate of requirement, but can have one Fixed deviation.Such as:" being substantially equal to " not merely represents absolute parallel, due in actual production, operating process, it is difficult to do To absolute " equal ", certain deviation is usually present.Therefore, in addition to definitely equal, " being substantially equal to " further includes There is certain deviation in that states.As example, in the case of other, unless otherwise specified, the terms such as " substantially ", " basic " It is meaning similar to the above.
In the description of the present invention, it is also necessary to explanation, unless otherwise clearly defined and limited, term " setting ", " installation ", " connected ", " connection " should be interpreted broadly, for example, it may be being fixedly connected or being detachably connected or one It connects body;It can be directly connected, can also be indirectly connected by intermediary, can be the connection inside two elements. For the ordinary skill in the art, the concrete meaning of above-mentioned term in the present invention can be understood with concrete condition.
Embodiment
Fig. 1 is refer to, the present embodiment provides a kind of Zanthoxylum essential oil production technologies.Zanthoxylum essential oil production technology comprises the following steps:
The first step screens Chinese prickly ash, removes impurity.
Chinese prickly ash and edible oil are mixed and added to Zanthoxylum essential oil process units 1000 by second step.
The mixture of Chinese prickly ash and edible oil is carried out heating and thermal insulation by the 3rd step, and heating temperature is 90~160 DEG C, during heating Between for 1.5~2.5h, be centrifugally separating to obtain preliminary working Zanthoxylum essential oil.
4th step, collects the steam of the spilling when carrying out heating and thermal insulation, and steam is cooled down, and collects coolant.
Coolant is carried out water-oil separating, takes oil, obtain pepper aroma essential oil by the 5th step.
Pepper aroma essential oil and preliminary working Zanthoxylum essential oil are pressed 1 by the 6th step:500~2000 weight ratio is mixed to get refined Zanthoxylum essential oil.
Zanthoxylum essential oil production technology is gone forward side by side by the way that the steam generated during Chinese prickly ash and edible oil Hybrid Heating is carried out cooling Row water-oil separating can obtain pepper aroma essential oil.It can be significantly after pepper aroma essential oil is added in preliminary working Zanthoxylum essential oil Improve the mellowness degree of preliminary working Zanthoxylum essential oil, obtain refined Zanthoxylum essential oil, greatly promote the quality and market value of product.
By the way that pepper aroma essential oil is added in preliminary working Zanthoxylum essential oil, the mellowness degree of Zanthoxylum essential oil can be substantially improved, is obtained To refined Zanthoxylum essential oil, this has the effect of highly significant for Zanthoxylum essential oil flavoring, increasing alcohol, greatly improves quality and the city of product Field value.
Further, pepper aroma essential oil is 1 with the weight ratio of preliminary working Zanthoxylum essential oil:500~2000.It is added in the ratio Pepper aroma essential oil can not only substantially improve mellowness degree and mouthfeel, and refined Zanthoxylum essential oil obtained is for food process When, will not other flavorings or food be formed with excessive interference, be not in that other condiment or taste of food spy is completely covered The situation of sign can preferably keep the flavor attributes of other flavorings together of food in itself, promote food mouthfeel.
Zanthoxylum essential oil production technology is collected the steam generated during Chinese prickly ash and edible oil Hybrid Heating, and is passed through Refrigerated separation has obtained pepper aroma essential oil, substantially increases product output rate and the diversity of product.By producing Zanthoxylum essential oil Multiple product is can obtain, substantially increases the quantum of output of single production procedure so that the active ingredient in Chinese prickly ash can be filled Divide and extract and can be fully used, substantially increase in Chinese prickly ash oil production process to the refinement degree of Chinese prickly ash.So not The utilization rate of raw material is improved only, reduces the wasting of resources, and so that production cost is cheaper.
Wherein, Chinese prickly ash and edible oil are subjected to heat preservation refinement in 90~160 DEG C, can be filled the active ingredient in Chinese prickly ash Divide and refine and be fully discharged into edible oil, so that obtained preliminary working Zanthoxylum essential oil has higher quality.
When being refined using Zanthoxylum essential oil production technology to Chinese prickly ash, due to, there are certain moisture, being refined in Chinese prickly ash In the process, moisture, which is heated, evaporates.In addition, also containing a certain amount of pepper aroma essential oil, pepper aroma essential oil tool in Chinese prickly ash There is certain volatility, with the volatilization of moisture, pepper aroma essential oil is taken out of together with the volatilization of moisture.In the refinement of Chinese prickly ash In the process, pepper aroma essential oil and Chinese prickly ash active water just are contained simultaneously in the gas overflowed at the top of device.
Therefore, in entire extractive process, with the progress of refinement, the active ingredient in Chinese prickly ash constantly enters edible oil In, the active constituent content in edible oil constantly raises, and pepper aroma essential oil is constantly escaped also with the volatilization of moisture.Pass through receipts Collect the steam that is overflowed in extractive process, steam cool down and carries out water-oil separating, can respectively obtain pepper aroma essential oil with Chinese prickly ash active water.Wherein, the pepper aroma essential oil extracted from Chinese prickly ash is the main effective ingredient of Chinese prickly ash fragrance, and per kilogram is spent Green pepper volatile oil is equivalent to fragrance degree possessed by 60~100 kilograms of raw material Chinese prickly ashes.
By collecting the steam overflowed in insulating process, steam is cooled down and carries out water-oil separating, obtains Chinese prickly ash fragrance Essential oil.Pepper aroma essential oil addition preliminary working Zanthoxylum essential oil is obtained into refined Zanthoxylum essential oil again.By the way that pepper aroma essential oil is added to In Zanthoxylum essential oil, the mellowness degree of preliminary working Zanthoxylum essential oil can be substantially improved, obtains refined Zanthoxylum essential oil, this is for Zanthoxylum essential oil flavoring, increasing Alcohol has the effect of highly significant, greatly improves the quality and market value of product.Still optionally further, pepper aroma essential oil Weight ratio with preliminary working Zanthoxylum essential oil is 1:800~1500.
Further, it is 2h to the heating time of the mixture of Chinese prickly ash and edible oil.
Further, it is 100~150 DEG C to the heating temperature of the mixture of Chinese prickly ash and edible oil.
Zanthoxylum essential oil is refined using Zanthoxylum essential oil production technology provided in this embodiment, can disposably obtain three kinds of productions Product are respectively:Preliminary working Zanthoxylum essential oil, pepper aroma essential oil and Chinese prickly ash active water.Substantially increase the production production in production process Extracting rate and product diversity not only facilitate the utilization rate improved to raw material, and can realize product diversification.
During Zanthoxylum essential oil is refined, additionally it is possible to carry out refinement separation to pepper aroma essential oil and Chinese prickly ash active water, no It is only capable of accessing the preliminary working Zanthoxylum essential oil of excellent quality, additionally it is possible to obtain pepper aroma essential oil and Chinese prickly ash active water, and refine Pepper aroma essential oil and active water are carried out at the same time during Zanthoxylum essential oil is refined, and need not carry out additional operation and Processing.In addition, it can also be made with higher mellowness degree, more excellent by the way that pepper aroma essential oil is added in preliminary working Zanthoxylum essential oil The refined Zanthoxylum essential oil of different mouthfeel even more further improves the diversity and market value of Chinese prickly ash oil product.
Zanthoxylum essential oil production technology provided in this embodiment greatly reduces the difficulty and cost of production Zanthoxylum essential oil, and significantly The production time is saved.Preliminary working Zanthoxylum essential oil, pepper aroma essential oil, Chinese prickly ash active water and refined Chinese prickly ash can disposably be made Oil greatly improves product diversity.
The moisture that Zanthoxylum essential oil production technology is contained in itself using Chinese prickly ash raw material refines Japan pepper essential oil and utilizes volatilization The moisture gone out takes Japan pepper essential oil out of together, without additionally adding refinement solvent, greatly reduces and refines pepper aroma essential oil Cost and difficulty significantly improve the extra value in pepper aroma essential oil production process.Pepper aroma essential oil and Chinese prickly ash activity Additional product of the water as Zanthoxylum essential oil extractive process has greatly enriched the output diversity of Chinese prickly ash oil producing method, has widened significantly The scope of application and utility value of Zanthoxylum essential oil production technology.It is mixed in particular with preliminary working Zanthoxylum essential oil and pepper aroma essential oil Refined Zanthoxylum essential oil obtained is even more that the quality of Chinese prickly ash oil product has been refreshed oneself with track one new height.
Further, in order to more easily implement Zanthoxylum essential oil production technology provided in this embodiment, the present embodiment also provides A kind of Zanthoxylum essential oil process units 1000.
Zanthoxylum essential oil process units 1000 includes Zanthoxylum essential oil extraction element 100, cooling device 200 and oily-water seperating equipment 300.
Zanthoxylum essential oil extraction element 100 includes heating groove cylinder 110, conveying mechanism 120 and cover 140.Conveying mechanism 120 is set up In heating groove cylinder 110, conveying mechanism 120 have for heating groove cylinder 110 convey Chinese prickly ash and by by the Chinese prickly ash that refines from adding The foraminous conveyer that heat channel cylinder 110 exports, conveying mechanism 120 also have the power set that power is provided for foraminous conveyer.
Cover 140 covers at the one side of the separate heating groove cylinder 110 of conveying mechanism 120 and for closing heating groove cylinder 110.
Heating groove cylinder 110 has heating arrangements 111, oil inlet 112 and oil outlet 113, and cover 140 is equipped with to heat Steam pipe 141 derived from steam in the process.The port of export of steam pipe 141 is connected with the input end of cooling device 200, cooling dress The input end that 200 port of export is put with oily-water seperating equipment 300 connects.
Chinese prickly ash is delivered to heating groove cylinder 110 by foraminous conveyer, and Chinese prickly ash is made to be contacted with heating the edible oil in groove cylinder 110.It is logical It crosses heating arrangements 111 to heat the mixture of Chinese prickly ash and edible oil, keeps the temperature at 90~160 DEG C and to carry out Chinese prickly ash It refines.In heating process, steam pipe 141 of the steam through cover 140 of generation is exported from heating groove cylinder 110, steam into Enter to cooling device 200 through cooling liquid, obtain coolant, coolant carries out grease point into oily-water seperating equipment 300 immediately From respectively obtaining Chinese prickly ash active water and pepper aroma essential oil.
After 1.5~2.5h is reached to heating time of Chinese prickly ash and the mixture of edible oil, it can stop heating, using dynamic Power apparatus drives foraminous conveyer movement so that the Chinese prickly ash after refining to be exported from heating groove cylinder 110.
Further, after refinement, heat the edible oil in groove cylinder 110 and be converted into preliminary working Zanthoxylum essential oil, it will just Zanthoxylum essential oil unified collection after the releasing of oil outlet 113 is processed, pepper aroma essential oil and preliminary working Zanthoxylum essential oil are pressed 1:500~2000 Weight ratio mixing, refined Zanthoxylum essential oil can be obtained.
So far, a production cycle just completes, when needing to be produced next time, by new edible oil from oil inlet 112 are put into heating groove cylinder 110.
Further, foraminous conveyer includes charging guipure 121 and discharging guipure 122, charging guipure 121 and discharging guipure 122 are sequentially connected with power set.In the present embodiment, power set are the motor for being equipped with reducing gear.
Charging guipure 121 is arranged on feed end and for Chinese prickly ash to be delivered to heating groove cylinder 110.Discharge the close of guipure 122 The one end for feeding guipure 121 is arranged on the one side for close 110 bottom of heating groove cylinder for feeding guipure 121, and for accepting by feeding The Chinese prickly ash that guipure 121 is sent.The other end of discharging guipure 122 bends towards the one side away from heating tank bottom of chamber portion and extends to discharging End.
Groove cylinder 110 is heated in rectangular-shape, vallecular cavity is also in rectangular-shape, axis of the charging guipure 121 along heating groove cylinder 110 Bottom to setting and parallel to groove cylinder 110 is heated, discharging guipure 122 are then arranged on the close heating groove cylinder 110 of charging guipure 121 Bottom one side, and the guipure 122 that discharges also is set approximately along the axial of heating groove cylinder 110.The separate charging of discharging guipure 122 One end of guipure 121 is then bent towards the one side away from heating tank bottom of chamber portion, and the separate charging guipure 121 for the guipure 122 that discharges The distance between end and heating tank bottom of chamber portion are more than charging the distance between guipure 121 and heating tank bottom of chamber portion.
In the prior art, for Zanthoxylum essential oil in extractive process, the easy agglomerate of Chinese prickly ash causes Chinese prickly ash distribution of particles excessively close Collection, causes Chinese prickly ash insufficient contact with oil so that the refinement degree of Chinese prickly ash reduces.This is unfavorable for carrying out effectively, fully Chinese prickly ash Ground refines, and results in the refinement degree of Chinese prickly ash and reduces, is unfavorable for improving the quality of Zanthoxylum essential oil.
In the present embodiment, guipure 122 is discharged for carrying Chinese prickly ash, when Chinese prickly ash is located on discharging guipure 122, due to discharging One end of the close charging guipure 121 of guipure 122 is arranged on the one side of close 110 bottom of heating groove cylinder of charging guipure 121, then Chinese prickly ash can be contacted smoothly with the edible oil in heating groove cylinder 110, in order to be refined to produce preliminary working Chinese prickly ash to Chinese prickly ash Oil.It should be noted that when Chinese prickly ash is located at discharging guipure 122, can be spread apart along discharging guipure 122, in addition edible oil Lubrication, buoyancy and mobilization force can be such that Chinese prickly ash is spread out along discharging guipure 122 so that Chinese prickly ash can fully connect with edible oil It touches, greatly improves the refinement effect to Chinese prickly ash, help to make the active ingredient higher in preliminary working Zanthoxylum essential oil obtained, be promoted just Process the quality of Zanthoxylum essential oil.Further, since the refinement degree of Chinese prickly ash is improved, pepper aroma essential oil and Chinese prickly ash active water carry Refining amount is also improved, and substantially increases the utilization rate to Chinese prickly ash raw material, adds output, reduces cost.
Further, since charging guipure 121 and discharging guipure 122 are independently of each other, it is necessary to when adding in Chinese prickly ash raw material, only need Charging guipure 121 is operated, and since discharging guipure 122 is inoperative, additionally it is possible to Chinese prickly ash raw material is avoided to be anticipated from discharge end Outer output, it is ensured that whole Chinese prickly ash raw materials can be refined.And when needing to export in the Chinese prickly ash after refinement, only it need to make discharging Guipure 122 operates.It feeds guipure 121 and discharging guipure 122 operates independently of each other, energy consumption can not only be reduced, reduction is set Standby production difficulty, additionally it is possible to improve the utilization rate to Chinese prickly ash raw material.
It should be noted that the Chinese prickly ash after the refinement exported by discharging guipure 122 is needed by centrifugal treating, to improve just Process the rate of recovery of Zanthoxylum essential oil.
Further, Zanthoxylum essential oil process units 1000 further includes to take out conveying mechanism 120 from heating groove cylinder 110 Elevator 150.By setting elevator 150, Zanthoxylum essential oil process units 1000 can be made to realize detachable assembling.When being spent During green pepper oil production, conveying mechanism 120 is set up in heating groove cylinder 110 and is placed in the vallecular cavity of heating groove cylinder 110, and cover 140 is then It is covered on the one side of the separate heating groove cylinder 110 of conveying mechanism 120 and closes heating groove cylinder 110.When need to Zanthoxylum essential oil give birth to Production device 1000, which is cleaned or overhauled, to be made, and conveying mechanism 120 and cover 140 are heated groove cylinder 110 relatively using elevator 150 It is promoted, makes conveying mechanism 120 and cover 140 away from heating groove cylinder 110.It is so not only convenient for carrying out whole equipment clear It washes, while convenient for being carried out maintenance to it.
Further, heating groove cylinder 110 is additionally provided with to filter out the dregs filter 160 of Chinese prickly ash particle, and dregs filter 160 is set In one end of the close oil outlet 113 of heating groove cylinder 110.In the present embodiment, dregs filter 160 uses filter plate, and filter plate is arranged on The vallecular cavity of groove cylinder 110 is heated, and filter plate is set perpendicular to the axial line of vallecular cavity, the periphery of filter plate is the same as the inner wall for heating groove cylinder 110 Connection.By setting dregs filter 160 that the Chinese prickly ash particle for residuing in preliminary working Zanthoxylum essential oil can be avoided to be discharged through oil outlet 113, Reduce subsequent processing burden.
Further, the feed end of conveying mechanism 120 is provided with the charging deslagging device to remove the gred to Chinese prickly ash 170, to improve feedstock quality.
Further, the bottom for heating groove cylinder 110 is provided with universal wheel 180 and adjusts lower margin 190, substantially increases Chinese prickly ash The flexibility of oily process units 1000 and practicability.
Further, PLC control flows can also be set to be controlled come the switch to driving device and heating arrangements 111.
Further, in the present embodiment, heating arrangements 111 are heating plate, and heating arrangements 111 are arranged on heating groove cylinder 110 Opposite sides.
In conclusion Zanthoxylum essential oil production technology can be greatly improved in Chinese prickly ash oil production process to the refinement degree of Chinese prickly ash, The active constituent content of refined Zanthoxylum essential oil obtained is greatly improved, promotes refined Chinese prickly ash oil quality.Improve the utilization of raw material Rate reduces the wasting of resources.And the mellowness degree of refined Zanthoxylum essential oil can be substantially improved, greatly improve the quality and market price of product Value.
The foregoing is only a preferred embodiment of the present invention, is not intended to limit the invention, for the skill of this field For art personnel, the invention may be variously modified and varied.Within the spirit and principles of the invention, that is made any repaiies Change, equivalent substitution, improvement etc., should all be included in the protection scope of the present invention.

Claims (9)

1. a kind of Zanthoxylum essential oil production technology, which is characterized in that including:
Chinese prickly ash is screened, removes impurity;
The Chinese prickly ash and edible oil are mixed and added to Zanthoxylum essential oil process units;
The mixture of the Chinese prickly ash and the edible oil is subjected to heating and thermal insulation, heating temperature is 90~160 DEG C, and heating time is 1.5~2.5h is centrifugally separating to obtain preliminary working Zanthoxylum essential oil;
The steam overflowed when carrying out the heating and thermal insulation is collected, and the steam is cooled down, collects coolant;
The coolant is subjected to water-oil separating, oil is taken, obtains pepper aroma essential oil;And
The pepper aroma essential oil and the preliminary working Zanthoxylum essential oil are pressed 1:500~2000 weight ratio is mixed to get refined Chinese prickly ash Oil.
2. Zanthoxylum essential oil production technology according to claim 1, which is characterized in that the pepper aroma essential oil just adds with described The weight ratio of work Zanthoxylum essential oil is 1:800~1500.
3. Zanthoxylum essential oil production technology according to claim 1, which is characterized in that the institute of the Chinese prickly ash and the edible oil The heating time for stating mixture is 2h.
4. Zanthoxylum essential oil production technology according to claim 1, which is characterized in that the institute of the Chinese prickly ash and the edible oil The heating temperature for stating mixture is 100~150 DEG C.
5. Zanthoxylum essential oil production technology according to claim 1, which is characterized in that the Zanthoxylum essential oil process units includes Chinese prickly ash Oil extract device, cooling device and oily-water seperating equipment;The Zanthoxylum essential oil extraction element includes heating groove cylinder, conveying mechanism and lid Body;The conveying mechanism is set up in the heating groove cylinder, and the conveying mechanism has for described in the heating groove cylinder conveying Chinese prickly ash and the foraminous conveyer that will be exported by the Chinese prickly ash refined from the heating groove cylinder, the conveying mechanism, which also has, to be used for The power set of power are provided for the foraminous conveyer;The cover covers at the separate heating groove cylinder of the conveying mechanism One side and for closing the heating groove cylinder;The heating groove cylinder has heating arrangements, oil inlet and oil outlet, the cover Equipped with for by steam pipe derived from the steam in heating process;The port of export of the steam pipe connects with the input end of cooling device Logical, the port of export of the cooling device is connected with the input end of the oily-water seperating equipment.
6. Zanthoxylum essential oil production technology according to claim 5, which is characterized in that the foraminous conveyer include charging guipure and Discharge guipure;The charging guipure is arranged on feed end and for the Chinese prickly ash to be delivered to the heating groove cylinder;The discharging net The one side in the close heating tank cylinder bottom portion that the charging guipure is arranged on close to one end of the charging guipure of band, and be used for Accept the Chinese prickly ash sent by the charging guipure;The other end of the discharging guipure is towards away from heating tank bottom of chamber portion One side bends and extends to discharge end;The discharging guipure carries for carrying the Chinese prickly ash to be refined for that will pass through The Chinese prickly ash of refining is exported from the heating groove cylinder.
7. Zanthoxylum essential oil production technology according to claim 5, which is characterized in that the Zanthoxylum essential oil process units further includes use In the elevator for taking out the conveying mechanism from the heating groove cylinder.
8. Zanthoxylum essential oil production technology according to claim 5, which is characterized in that the heating groove cylinder is additionally provided with to filter out The dregs filter of Chinese prickly ash particle, the dregs filter are arranged on one end of the close oil outlet of the heating groove cylinder.
9. Zanthoxylum essential oil production technology according to claim 5, which is characterized in that the feed end of the conveying mechanism is provided with For the charging deslagging device to remove the gred to the Chinese prickly ash.
CN201711186550.7A 2017-11-23 2017-11-23 A kind of Zanthoxylum essential oil production technology Pending CN108117923A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711186550.7A CN108117923A (en) 2017-11-23 2017-11-23 A kind of Zanthoxylum essential oil production technology

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711186550.7A CN108117923A (en) 2017-11-23 2017-11-23 A kind of Zanthoxylum essential oil production technology

Publications (1)

Publication Number Publication Date
CN108117923A true CN108117923A (en) 2018-06-05

Family

ID=62227861

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711186550.7A Pending CN108117923A (en) 2017-11-23 2017-11-23 A kind of Zanthoxylum essential oil production technology

Country Status (1)

Country Link
CN (1) CN108117923A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108179064A (en) * 2017-12-25 2018-06-19 洪雅县和鑫农业科技发展有限公司 A kind of pepper aroma essential oil production technology
CN113841745A (en) * 2021-01-28 2021-12-28 丰益(上海)生物技术研发中心有限公司 Zanthoxylum oil, preparation method and application thereof, and material using zanthoxylum oil

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1119073A (en) * 1994-09-18 1996-03-27 韩城市农业技术推广站 Chinese prickly ash extract and producing process thereof
CN206143154U (en) * 2016-07-06 2017-05-03 中粮集团有限公司 A device for being directed at fragrant flavor material of flower any of several hot spice plants oil is retrieved

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1119073A (en) * 1994-09-18 1996-03-27 韩城市农业技术推广站 Chinese prickly ash extract and producing process thereof
CN206143154U (en) * 2016-07-06 2017-05-03 中粮集团有限公司 A device for being directed at fragrant flavor material of flower any of several hot spice plants oil is retrieved

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108179064A (en) * 2017-12-25 2018-06-19 洪雅县和鑫农业科技发展有限公司 A kind of pepper aroma essential oil production technology
CN113841745A (en) * 2021-01-28 2021-12-28 丰益(上海)生物技术研发中心有限公司 Zanthoxylum oil, preparation method and application thereof, and material using zanthoxylum oil

Similar Documents

Publication Publication Date Title
CN207567146U (en) A kind of extraction concentrator of vegetable protein
CN206298562U (en) A kind of automatic tea oil pressing device
CN107245373B (en) Preparation process of high unsaturated fatty acid tea oil
CN104152265B (en) A kind of sugar-cane juice maillard reaction product, its preparation method and the application in cigarette
CN103849470B (en) Preparation method of lacquer tree seed wax oil
CN101870918A (en) Method for producing pepper seed oil
CN103992873B (en) A kind of novel Tengjiao oil production technique
CN108117923A (en) A kind of Zanthoxylum essential oil production technology
CN104928011A (en) Production process for producing Acer trunctum Bunge oil and Acer trunctum Bunge protein powder by using Acer trunctum Bunge seed as raw material
CN107384579A (en) A kind of production method of high-quality vegetable oil
CN105969517A (en) Production method of squeezed snake gourd seed oil
CN205653423U (en) Vegetable oil integration refining equipment
CN110801643B (en) Device and method for removing bitter taste of pepper extract
CN106367206B (en) A kind of yam bean essence, preparation method and the application in cigarette
CN109593600A (en) A kind of cold press peanut oil process equipment and its method
CN108085129A (en) A kind of wood wax oil preparation method
CN105132041B (en) A kind of liquid phase dust pelletizing system and method for being pyrolyzed raw coke oven gas
CN203768325U (en) Grease production line
CN208373347U (en) A kind of camellia oil oil residue separating apparatus
CN108179064A (en) A kind of pepper aroma essential oil production technology
CN110373262A (en) A kind of Lai wood fruit oil refinement method of low-cost and high-quality
CN106221901A (en) A kind of oily-water seperating equipment of band chiller
CN103232320B (en) Production technology of octacosanol
CN108094571A (en) A kind of Chinese prickly ash active water production technology
CN107287024B (en) Preparation process of aromatic camellia oil

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20180605