CN108977270A - A kind of method of ultrasonic wave assisted extraction tung oil - Google Patents
A kind of method of ultrasonic wave assisted extraction tung oil Download PDFInfo
- Publication number
- CN108977270A CN108977270A CN201810871050.5A CN201810871050A CN108977270A CN 108977270 A CN108977270 A CN 108977270A CN 201810871050 A CN201810871050 A CN 201810871050A CN 108977270 A CN108977270 A CN 108977270A
- Authority
- CN
- China
- Prior art keywords
- tung oil
- ultrasonic wave
- extraction
- tree seed
- oil tree
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, 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
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/02—Pretreatment
- C11B1/04—Pretreatment of vegetable raw material
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, 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
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
- C11B1/106—Production of fats or fatty oils from raw materials by extracting using ultra-sounds
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, 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
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
- C11B1/108—Production of fats or fatty oils from raw materials by extracting after-treatment, e.g. of miscellae
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, 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
- C11B3/00—Refining fats or fatty oils
- C11B3/001—Refining fats or fatty oils by a combination of two or more of the means hereafter
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, 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
- C11B3/00—Refining fats or fatty oils
- C11B3/008—Refining fats or fatty oils by filtration, e.g. including ultra filtration, dialysis
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, 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
- C11B3/00—Refining fats or fatty oils
- C11B3/12—Refining fats or fatty oils by distillation
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Microbiology (AREA)
- Fats And Perfumes (AREA)
Abstract
The invention discloses a kind of methods of ultrasonic wave assisted extraction tung oil, including sorting, drying, it is broken, single extraction, separation, reextraction, distillation and storing step, structure of the invention is scientific and reasonable, it is safe and convenient to use, the present invention is when carrying out ultrasonic wave assisted extraction tung oil to tung oil tree seed, pass through single extraction, the most of tung oil contained in tung oil tree seed can be subjected to extraction proposition, pass through reextraction, the solid oil tung oil dregs of rice that generated after single extraction can be subjected to reextraction, the recovery rate that tung oil tree seed extracts Oleum Verniciae fordii is high, it is short that the active material tool time in need in tung oil tree seed will not be destroyed, it is not required to high temperature and the high advantage of recovery rate, it is 21kHz by frequency, the ultrasonic wave that temperature is 60.5 DEG C, ultrasonic extraction is carried out to tung oil tree seed, it ensure that the tung oil quality that tung oil tree seed extracts, it will not be because High temperature causes to contain carcinogen in tung oil, reduces the process when extraction of tung oil tree seed, has saved a large amount of energy consumption.
Description
Technical field
The present invention relates to agricultural byproducts processing technical field, specially a kind of method of ultrasonic wave assisted extraction tung oil.
Background technique
Tung oil tree is the distinctive commodity trees in China, is distributed mainly on southern region of China, and tung oil is extracted from bancoul nuts
Grease, be a kind of natural vegetable oil, composition is mainly fatty acid triglycercide mixture, and detectable fatty acid has
It is 9 kinds, main to have 5 kinds, i.e. palmitinic acid, stearic acid, oleic acid, linolenic acid and eleostearic acid, wherein again with tung oil acid content highest, about
It is 80 percent, tung oil has the characteristics that rapid drying, high temperature resistant, corrosion-resistant, and tung oil also has good waterproofness, is system
The primary raw material of paint, ink is made, the production of waterproof, anti-corrosion, rush-resisting material is largely used as, and oilcloth, oilpaper, fertilizer can be made
Soap, pesticide and pharmaceutical nauseant, agrochemical, tung oil can also be used to produce biodiesel, increasingly be expected to rise in energy prices
There to be vast potential for future development using reproducible tung oil resource production biodiesel today;
In the prior art, tung oil tree seed generally mentions oil process using traditional compacting and organic solvent extraction carries out tung oil extraction
It takes, compacting mentions oil process when extracting tung oil, needs to heat tung oil tree seed, generally requires temperature being promoted to 100-150 and take the photograph
Family name's degree, when carrying out extraction to tung oil tree seed and mentioning oil, polymerization work easily occurs for three conjugated double bonds in tung oil main component eleostearic acid
With, and people contains grease about 6 percent to 10 in remaining tung oil tree oil meal, and is easy to cause work in summer
Make personnel and generate heatstroke, be also easy because temperature is excessively high, to generate oil smoke when the extraction of tung oil tree seed mentions oil, influences work
The health of personnel, and high temperature when tung oil tree extraction easily leads to staff and is burned, and is extracted using organic solvent extraction
When tung oil, need using dehydrated alcohol, normal propyl alcohol and ethyl acetate equal solvent, solvent be easy to produce when in use evaporation or its
His chemical change be easy to cause eleostearic acid isomerization in extraction process, there are it is toxic, not environmentally, of poor quality and to mention speed oil slow, molten
The disadvantages of agent consumption is big leads to the tung oil quality irregularity extracted, and raw material oil yield is low, and the big phenomenon of material loss occurs;
With the development of science and technology, ultrasonic technology gradually uses in all trades and professions, and ultrasonic wave has wavelength
Short and beam by force and is easy to concentrate mentioning a little for energy by focusing, thus its effect between coal quality can be divided into calorifics mechanism,
Mechanics of Machinery mechanism and three kinds of cavitation mechanism, from multi-expert to ultrasonic wave assisted extraction grease the experimental results showed that, mentioning oil
Under conditions of rate is essentially identical, ultrasonic wave assisted extraction can reduce Extracting temperature, shorten extraction time, save solvent usage,
But also the quality of grease can be improved, but existing compacting mentions oil process and organic solvent extraction when extracting tung oil, exists
It is toxic, not environmentally, it is of poor quality and mention the disadvantages of speed oil is slow, solvent consumption is big, and there is the tung oil quality irregularity extracted, it is former
Expect that oil yield is low, the big phenomenon of material loss is easy to cause tung oil tree seed material loss excessive, reduces the fuel-displaced of tung oil tree seed
Rate, the quality irregularity of tung oil, is not available, thus benefit when influencing plant produced tung oil.
Summary of the invention
The present invention provides a kind of method of ultrasonic wave assisted extraction tung oil, can effectively solve to propose in above-mentioned background technique
There are it is toxic, not environmentally, it is of poor quality and mention the disadvantages of speed oil is slow, solvent consumption is big, and there is the tung oil quality extracted not
Rule are closed, raw material oil yield is low, and the big phenomenon of material loss is easy to cause tung oil tree seed material loss excessive, reduces tung oil tree kind
The oil yield of seed, the quality irregularity of tung oil, is not available, thus benefit when influencing plant produced tung oil etc. ask
Topic.
To achieve the above object, the invention provides the following technical scheme: a kind of method of ultrasonic wave assisted extraction tung oil,
It is characterized in that, includes the following steps:
S1, sorting: eluriating tung oil tree seed using clear water, and screening proposes that particle is not full, insect bite, goes rotten rotten etc.
Inferior tung oil tree seed removes impurity inside tung oil tree seed;
S2, drying: the tung oil tree seed after elutriation is dried using drying box;
S3, it is crushed: tung oil tree seed being crushed using pulverizer;
S4, single extraction: by the container of the anti-merging sealing of tung oil tree kind powder of seeds and distilled water, persistently made with ultrasonic wave
With progress single extraction;
S5, separation: by sealing container filtrate and solid oil tung oil dregs of rice mixture filter, in extraction mixture
The solid oil tung oil dregs of rice;
S6, reextraction: by the solid oil tung oil dregs of rice and the container of distilled water merging sealing, with ultrasonic wave continuous action,
Carry out reextraction;
S7, distillation: being placed into Rotary Evaporators for gained filtrate, by Rotary Evaporators to filtrate decompression distill to get
The tung oil;
S8, storage: the tung oil after distillation is packed into sealing bucket and is saved.
According to the above technical scheme, the tung oil tree seed after eluriating in the step 1 is screened using oscillating separator, will
The solid impurities such as the stone contained in tung oil tree seed sift out, the alternating current that the power supply of the oscillating separator sieve is 380V.
According to the above technical scheme, dryer is 100 DEG C to the drying temperature of tung oil tree seed in the step 2.
According to the above technical scheme, the revolving speed of pulverizer is 3000r/min, smashed tung oil tree seed in the step 3
Powder is screened, and the sieve fineness is 40 mesh.
According to the above technical scheme, the liquid-to-solid ratio of distilled water and tung oil tree kind powder of seeds is 9.4mL/1g, institute in the step 4
Stating ultrasonic frequency is 21kHz, and the ultrasonic temperature is 60.5 DEG C, and the ultrasonic time is 30.4min.
According to the above technical scheme, double deck screen is used when filtering in the step 5 to filtrate and the solid oil tung oil dregs of rice
Net is filtered, and the fineness of the sieve is respectively 40 mesh and 60 mesh.
According to the above technical scheme, the liquid-to-solid ratio of distilled water and the solid oil tung oil dregs of rice is 9.4mL/1g, institute in the step 6
Stating ultrasonic frequency is 21kHz, and the ultrasonic temperature is 60.5 DEG C, and the ultrasonic time is 25min.
According to the above technical scheme, the tung oil tree oil meal waste residue in the step 6 after reextraction uses double medium filtration sieve
It is filtered, the fineness of the sieve is respectively 60 mesh and 80 mesh, and the filtered tung oil tree oil meal waste residue is put into sealing bucket
Carry out unified recovery processing.
According to the above technical scheme, the power supply of Rotary Evaporators is 380V alternating current, the rotary evaporation in the step 7
The revolving speed of instrument is 140r/min.
According to the above technical scheme, in the step 8 sealing bucket selection do not filled sulphur, salt, realgar, pesticide and
The sealing bucket of chemical fertilizer avoids the tung oil denaturation loss stored in sealing bucket.
Compared with prior art, beneficial effects of the present invention: structure of the invention is scientific and reasonable, safe and convenient to use, this hair
It is bright to tung oil tree seed carry out ultrasonic wave assisted extraction tung oil when, by single extraction, the big portion that can will contain in tung oil tree seed
Divide tung oil to carry out extraction proposition, by reextraction, the solid oil tung oil dregs of rice that generated after single extraction can be subjected to reextraction,
The recovery rate that tung oil tree seed extracts Oleum Verniciae fordii is high, when using ultrasonic wave extraction Oleum Verniciae fordii, has to destroy in tung oil tree seed and live
Property substance the advantages of, have that time in need is short, is not required to the advantages that high temperature using ultrasonic wave extraction bancoul nuts, and relative to tradition
Compacting mention oil process and organic solvent extraction, the recovery rate for extracting Oleum Verniciae fordii to tung oil tree seed is high, and is extracting Oleum Verniciae fordii
In the process, it is 21kHz by frequency, the ultrasonic wave that temperature is 60.5 DEG C, ultrasonic extraction is carried out to tung oil tree seed, can avoid tradition
High-temperature extraction when extraction causes active material inside tung oil tree seed to ensure that tung oil tree seed extracted because high temperature is destroyed
Tung oil quality will not cause to contain carcinogen in tung oil because of high temperature, and the tung oil tree oil meal that tung oil tree seed generates after extracting will not
Reextraction is influenced because of high temperature, is reduced the process when extraction of tung oil tree seed, has been saved a large amount of energy consumption.
Detailed description of the invention
Attached drawing is used to provide further understanding of the present invention, and constitutes part of specification, with reality of the invention
It applies example to be used to explain the present invention together, not be construed as limiting the invention.In the accompanying drawings:
Fig. 1 is step schematic diagram of the invention.
Specific embodiment
Hereinafter, preferred embodiments of the present invention will be described with reference to the accompanying drawings, it should be understood that preferred reality described herein
Apply example only for the purpose of illustrating and explaining the present invention and is not intended to limit the present invention.
Embodiment 1: as shown in Figure 1, the present invention provides a kind of method and technology scheme of ultrasonic wave assisted extraction tung oil, it is a kind of
The method of ultrasonic wave assisted extraction tung oil, which comprises the steps of:
S1, sorting: eluriating tung oil tree seed using clear water, and screening proposes that particle is not full, insect bite, goes rotten rotten etc.
Inferior tung oil tree seed removes impurity inside tung oil tree seed;
S2, drying: the tung oil tree seed after elutriation is dried using drying box;
S3, it is crushed: tung oil tree seed being crushed using pulverizer;
S4, single extraction: by the container of the anti-merging sealing of tung oil tree kind powder of seeds and distilled water, persistently made with ultrasonic wave
With progress single extraction;
S5, separation: by sealing container filtrate and solid oil tung oil dregs of rice mixture filter, in extraction mixture
The solid oil tung oil dregs of rice;
S6, reextraction: by the solid oil tung oil dregs of rice and the container of distilled water merging sealing, with ultrasonic wave continuous action,
Carry out reextraction;
S7, distillation: being placed into Rotary Evaporators for gained filtrate, by Rotary Evaporators to filtrate decompression distill to get
The tung oil;
S8, storage: the tung oil after distillation is packed into sealing bucket and is saved.
According to above scheme, the tung oil tree seed after eluriating in step 1 is screened using oscillating separator, by tung oil tree seed
In the solid impurities such as the stone that contains sift out, the power supply of oscillating separator sieve is the alternating current of 380V.
According to above scheme, dryer is 100 DEG C to the drying temperature of tung oil tree seed in step 2.
According to above scheme, the revolving speed of pulverizer is 3000r/min in step 3, and smashed tung oil tree kind powder of seeds needs
It is screened, sieve fineness is 40 mesh.
According to above scheme, the liquid-to-solid ratio of distilled water and tung oil tree kind powder of seeds is 9.4mL/1g, ultrasonic frequency in step 4
For 21kHz, ultrasonic temperature is 60.5 DEG C, ultrasonic time 30.4min.
According to above scheme, carried out when being filtered in step 5 to filtrate and the solid oil tung oil dregs of rice using Double-layer screen
Filter, the fineness of sieve is respectively 40 mesh and 60 mesh.
According to above scheme, the liquid-to-solid ratio of distilled water and the solid oil tung oil dregs of rice is 9.4mL/1g, ultrasonic frequency in step 6
For 21kHz, ultrasonic temperature is 60.5 DEG C, ultrasonic time 30.4min.
According to above scheme, the tung oil tree oil meal waste residue in step 6 after reextraction is filtered using double medium filtration sieve,
The fineness of sieve is respectively 60 mesh and 80 mesh, and filtered tung oil tree oil meal waste residue, which is put into sealing bucket, carries out unified recovery processing.
According to above scheme, the power supply of Rotary Evaporators is 380V alternating current in step 7, and the revolving speed of Rotary Evaporators is
140r/min。
According to above scheme, the sealing bucket selection in step 8 did not fill the close of sulphur, salt, realgar, pesticide and chemical fertilizer
Feng Tong avoids the tung oil denaturation loss stored in sealing bucket.
Embodiment 2: as shown in Figure 1, the present invention provides a kind of method and technology scheme of ultrasonic wave assisted extraction tung oil, it is a kind of
The method of ultrasonic wave assisted extraction tung oil, which comprises the steps of:
S1, sorting: eluriating tung oil tree seed using clear water, and screening proposes that particle is not full, insect bite, goes rotten rotten etc.
Inferior tung oil tree seed removes impurity inside tung oil tree seed;
S2, drying: the tung oil tree seed after elutriation is dried using drying box;
S3, it is crushed: tung oil tree seed being crushed using pulverizer;
S4, single extraction: by the container of the anti-merging sealing of tung oil tree kind powder of seeds and distilled water, persistently made with ultrasonic wave
With progress single extraction;
S5, separation: by sealing container filtrate and solid oil tung oil dregs of rice mixture filter, in extraction mixture
The solid oil tung oil dregs of rice;
S6, reextraction: by the solid oil tung oil dregs of rice and the container of distilled water merging sealing, with ultrasonic wave continuous action,
Carry out reextraction;
S7, distillation: being placed into Rotary Evaporators for gained filtrate, by Rotary Evaporators to filtrate decompression distill to get
The tung oil;
S8, storage: the tung oil after distillation is packed into sealing bucket and is saved.
According to above scheme, the tung oil tree seed after eluriating in step 1 is screened using oscillating separator, by tung oil tree seed
In the solid impurities such as the stone that contains sift out, the power supply of oscillating separator sieve is the alternating current of 380V.
According to above scheme, dryer is 100 DEG C to the drying temperature of tung oil tree seed in step 2.
According to above scheme, the revolving speed of pulverizer is 3000r/min in step 3, and smashed tung oil tree kind powder of seeds needs
It is screened, sieve fineness is 40 mesh.
According to above scheme, the liquid-to-solid ratio of distilled water and tung oil tree kind powder of seeds is 8.5mL/1g, ultrasonic frequency in step 4
For 20kHz, ultrasonic temperature is 55 DEG C, ultrasonic time 25min.
According to above scheme, carried out when being filtered in step 5 to filtrate and the solid oil tung oil dregs of rice using Double-layer screen
Filter, the fineness of sieve is respectively 40 mesh and 60 mesh.
According to above scheme, the liquid-to-solid ratio of distilled water and the solid oil tung oil dregs of rice is 8.5mL/1g, ultrasonic frequency in step 6
For 20kHz, ultrasonic temperature is 55 DEG C, ultrasonic time 25min.
According to above scheme, the tung oil tree oil meal waste residue in step 6 after reextraction is filtered using double medium filtration sieve,
The fineness of sieve is respectively 60 mesh and 80 mesh, and filtered tung oil tree oil meal waste residue, which is put into sealing bucket, carries out unified recovery processing.
According to above scheme, the power supply of Rotary Evaporators is 380V alternating current in step 7, and the revolving speed of Rotary Evaporators is
140r/min。
According to above scheme, the sealing bucket selection in step 8 did not fill the close of sulphur, salt, realgar, pesticide and chemical fertilizer
Feng Tong avoids the tung oil denaturation loss stored in sealing bucket.
Embodiment 3: as shown in Figure 1, the present invention provides a kind of method and technology scheme of ultrasonic wave assisted extraction tung oil, it is a kind of
The method of ultrasonic wave assisted extraction tung oil, which comprises the steps of:
S1, sorting: eluriating tung oil tree seed using clear water, and screening proposes that particle is not full, insect bite, goes rotten rotten etc.
Inferior tung oil tree seed removes impurity inside tung oil tree seed;
S2, drying: the tung oil tree seed after elutriation is dried using drying box;
S3, it is crushed: tung oil tree seed being crushed using pulverizer;
S4, single extraction: by the container of the anti-merging sealing of tung oil tree kind powder of seeds and distilled water, persistently made with ultrasonic wave
With progress single extraction;
S5, separation: by sealing container filtrate and solid oil tung oil dregs of rice mixture filter, in extraction mixture
The solid oil tung oil dregs of rice;
S6, reextraction: by the solid oil tung oil dregs of rice and the container of distilled water merging sealing, with ultrasonic wave continuous action,
Carry out reextraction;
S7, distillation: being placed into Rotary Evaporators for gained filtrate, by Rotary Evaporators to filtrate decompression distill to get
The tung oil;
S8, storage: the tung oil after distillation is packed into sealing bucket and is saved.
According to above scheme, the tung oil tree seed after eluriating in step 1 is screened using oscillating separator, by tung oil tree seed
In the solid impurities such as the stone that contains sift out, the power supply of oscillating separator sieve is the alternating current of 380V.
According to above scheme, dryer is 100 DEG C to the drying temperature of tung oil tree seed in step 2.
According to above scheme, the revolving speed of pulverizer is 3000r/min in step 3, and smashed tung oil tree kind powder of seeds needs
It is screened, sieve fineness is 40 mesh.
According to above scheme, the liquid-to-solid ratio of distilled water and tung oil tree kind powder of seeds is 10mL/1g, ultrasonic frequency in step 4
For 22kHz, ultrasonic temperature is 65 DEG C, ultrasonic time 35min.
According to above scheme, carried out when being filtered in step 5 to filtrate and the solid oil tung oil dregs of rice using Double-layer screen
Filter, the fineness of sieve is respectively 40 mesh and 60 mesh.
According to above scheme, the liquid-to-solid ratio of distilled water and the solid oil tung oil dregs of rice is 10mL/1g, ultrasonic frequency in step 6
For 22kHz, ultrasonic temperature is 65 DEG C, ultrasonic time 35min.
According to above scheme, the tung oil tree oil meal waste residue in step 6 after reextraction is filtered using double medium filtration sieve,
The fineness of sieve is respectively 60 mesh and 80 mesh, and filtered tung oil tree oil meal waste residue, which is put into sealing bucket, carries out unified recovery processing.
According to above scheme, the power supply of Rotary Evaporators is 380V alternating current in step 7, and the revolving speed of Rotary Evaporators is
140r/min。
According to above scheme, the sealing bucket selection in step 8 did not fill the close of sulphur, salt, realgar, pesticide and chemical fertilizer
Feng Tong avoids the tung oil denaturation loss stored in sealing bucket.
The present invention is detected according to tung oil made from embodiment 1-3, as a result such as table 1,
1 testing result of table
As it can be seen that when using ultrasonic wave assisted extraction tung oil, the liquid-to-solid ratio of distilled water and tung oil tree kind powder of seeds is testing result
9.4mL/1g, ultrasonic frequency 21kHz, ultrasonic temperature is 60.5 DEG C, when ultrasonic time is 30.4min, Oleum Verniciae fordii recovery rate
It can reach 38.5%.
The working principle of the invention and process for using: the present invention is carrying out ultrasonic wave assisted extraction tung oil to tung oil tree seed
When, by single extraction, the most of tung oil contained in tung oil tree seed can be subjected to extraction proposition, by reextraction, can incited somebody to action
The solid oil tung oil dregs of rice generated after single extraction carry out reextraction, and the recovery rate that tung oil tree seed extracts Oleum Verniciae fordii is high, using super
When sound wave extracts Oleum Verniciae fordii, has the advantages that active material in tung oil tree seed will not be destroyed, had using ultrasonic wave extraction bancoul nuts
Time in need is short, is not required to the advantages that high temperature, and mentions oil process and organic solvent extraction relative to traditional compacting, to tung oil tree
The recovery rate that seed extracts Oleum Verniciae fordii is high, and during extracting Oleum Verniciae fordii, by frequency be 21kHz, temperature is 60.5 DEG C
Ultrasonic wave, ultrasonic extraction is carried out to tung oil tree seed, can avoid high-temperature extraction when traditional extraction, is caused living inside tung oil tree seed
Property substance be destroyed because of high temperature, ensure that the tung oil quality that tung oil tree seed extracts, will not cause because of high temperature in tung oil containing causing
Cancer substance, the tung oil tree oil meal that tung oil tree seed generates after extracting will not influence reextraction because of high temperature, reduce tung oil tree seed
Process when extraction has saved a large amount of energy consumption.
Finally, it should be noted that being not intended to restrict the invention the foregoing is merely preferred embodiment of the invention, to the greatest extent
Present invention has been described in detail with reference to the aforementioned embodiments for pipe, for those skilled in the art, still can be with
It modifies the technical solutions described in the foregoing embodiments or equivalent replacement of some of the technical features.It is all
Within the spirit and principles in the present invention, any modification, equivalent replacement, improvement and so on should be included in guarantor of the invention
Within the scope of shield.
Claims (10)
1. a kind of method of ultrasonic wave assisted extraction tung oil, which comprises the steps of:
S1, sorting: eluriating tung oil tree seed using clear water, and screening proposes that particle is not full, insect bite, goes rotten rotten etc. inferior
Tung oil tree seed, remove tung oil tree seed inside impurity;
S2, drying: the tung oil tree seed after elutriation is dried using drying box;
S3, it is crushed: tung oil tree seed being crushed using pulverizer;
S4, single extraction: by the container of the anti-merging sealing of tung oil tree kind powder of seeds and distilled water, with ultrasonic wave continuous action, into
Row single extraction;
S5, separation: by sealing container filtrate and solid oil tung oil dregs of rice mixture filter, the solid-state in extraction mixture
Tung oil tree oil meal;
S6, reextraction: it by the solid oil tung oil dregs of rice and the container of distilled water merging sealing, with ultrasonic wave continuous action, carries out
Reextraction;
S7, distillation: being placed into Rotary Evaporators for gained filtrate, is distilled filtrate decompression to get described by Rotary Evaporators
Tung oil;
S8, storage: the tung oil after distillation is packed into sealing bucket and is saved.
2. a kind of method of ultrasonic wave assisted extraction tung oil according to claim 1, it is characterised in that: in the step 1
Tung oil tree seed after elutriation is screened using oscillating separator, and the solid impurities such as the stone contained in tung oil tree seed are sifted out,
The alternating current that the power supply of the oscillating separator sieve is 380V.
3. a kind of method of ultrasonic wave assisted extraction tung oil according to claim 1, it is characterised in that: in the step 2
Dryer is 100 DEG C to the drying temperature of tung oil tree seed.
4. a kind of method of ultrasonic wave assisted extraction tung oil according to claim 1, it is characterised in that: in the step 3
The revolving speed of pulverizer is 3000r/min, and smashed tung oil tree kind powder of seeds is screened, and the sieve fineness is 40 mesh.
5. a kind of method of ultrasonic wave assisted extraction tung oil according to claim 1, it is characterised in that: in the step 4
The liquid-to-solid ratio of distilled water and tung oil tree kind powder of seeds is 9.4mL/1g, and the ultrasonic frequency is 21kHz, and the ultrasonic temperature is
60.5 DEG C, the ultrasonic time 30.4min.
6. a kind of method of ultrasonic wave assisted extraction tung oil according to claim 1, it is characterised in that: in the step 5
Be filtered when being filtered to filtrate and the solid oil tung oil dregs of rice using Double-layer screen, the fineness of the sieve be respectively 40 mesh and
60 mesh.
7. a kind of method of ultrasonic wave assisted extraction tung oil according to claim 1, it is characterised in that: in the step 6
The liquid-to-solid ratio of distilled water and the solid oil tung oil dregs of rice is 9.4mL/1g, and the ultrasonic frequency is 21kHz, and the ultrasonic temperature is
60.5 DEG C, the ultrasonic time 30.4min.
8. a kind of method of ultrasonic wave assisted extraction tung oil according to claim 1, it is characterised in that: in the step 6
Tung oil tree oil meal waste residue after reextraction is filtered using double medium filtration sieve, and the fineness of the sieve is respectively 60 mesh and 80
Mesh, the filtered tung oil tree oil meal waste residue, which is put into sealing bucket, carries out unified recovery processing.
9. a kind of method of ultrasonic wave assisted extraction tung oil according to claim 1, it is characterised in that: in the step 7
The power supply of Rotary Evaporators is 380V alternating current, and the revolving speed of the Rotary Evaporators is 140r/min.
10. a kind of method of ultrasonic wave assisted extraction tung oil according to claim 1, it is characterised in that: in the step 8
Sealing bucket select and do not filled the sealing bucket of sulphur, salt, realgar, pesticide and chemical fertilizer, avoid the tung oil stored in sealing bucket
Denaturation loss.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810871050.5A CN108977270A (en) | 2018-08-02 | 2018-08-02 | A kind of method of ultrasonic wave assisted extraction tung oil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810871050.5A CN108977270A (en) | 2018-08-02 | 2018-08-02 | A kind of method of ultrasonic wave assisted extraction tung oil |
Publications (1)
Publication Number | Publication Date |
---|---|
CN108977270A true CN108977270A (en) | 2018-12-11 |
Family
ID=64554630
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201810871050.5A Pending CN108977270A (en) | 2018-08-02 | 2018-08-02 | A kind of method of ultrasonic wave assisted extraction tung oil |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN108977270A (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101892123A (en) * | 2010-07-23 | 2010-11-24 | 中国科学院武汉植物园 | Ultrasonic-assisted extraction method for tung oil |
CN103484242A (en) * | 2013-09-30 | 2014-01-01 | 广西科学院 | Method for extracting Tung oil through ultrasonic wave auxiliary low-temperature water |
CN104263504A (en) * | 2014-10-22 | 2015-01-07 | 江西省粮油科学技术研究所 | Swida wilsoniana oil extracting method |
-
2018
- 2018-08-02 CN CN201810871050.5A patent/CN108977270A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101892123A (en) * | 2010-07-23 | 2010-11-24 | 中国科学院武汉植物园 | Ultrasonic-assisted extraction method for tung oil |
CN103484242A (en) * | 2013-09-30 | 2014-01-01 | 广西科学院 | Method for extracting Tung oil through ultrasonic wave auxiliary low-temperature water |
CN104263504A (en) * | 2014-10-22 | 2015-01-07 | 江西省粮油科学技术研究所 | Swida wilsoniana oil extracting method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Sahu | Assessment of sugarcane industry: Suitability for production, consumption, and utilization | |
US8628593B2 (en) | Process to separate lipids from lipid-containing biomass for producing platform chemicals and/or liquid biofuels | |
Moraes et al. | Review of the rice production cycle: by-products and the main applications focusing on rice husk combustion and ash recycling | |
CN102766530B (en) | Method for extracting phospholipid-rich krill oil from Antarctic krill | |
Kumar et al. | Chironji nut (Buchanania lanzan) processing, present practices and scope | |
CN103849470B (en) | Preparation method of lacquer tree seed wax oil | |
WO2013131161A1 (en) | Process and apparatus for in situ production of biodiesel on a small scale | |
DE112010000986T5 (en) | Treatment of low rank coal | |
CN113617792B (en) | Method for treating kitchen garbage by hydrothermal carbonization technology | |
CN103657593A (en) | Sunflower husk biomass carbon adsorbent, preparation method and method for removing methylene blue from water | |
Akhabue et al. | Osamilite (K–Na–Ca–Mg–Fe–Al–S): A derived base catalyst for the synthesis of biodiesel from blends of pumpkin seed oil-goat fat-poultry waste fat | |
Low et al. | Economic analysis of waste minimisation and energy recovery from spent bleaching earth | |
CN108085129B (en) | Preparation method of wood wax oil | |
CN108977270A (en) | A kind of method of ultrasonic wave assisted extraction tung oil | |
CN104726197A (en) | Method for extracting tobacco seed oil from aromatic tobacco waste tobacco seed | |
CN107057707A (en) | A kind of prone soil biomass carbon modifying agent containing spirulina | |
Hamid et al. | Characterization of raw and ripen of banana peel wastes and it’s oils extraction using soxhlet method | |
CN105018212A (en) | Aqueous enzymatic method for extracting zanthoxylum seed oil | |
Ojewumi et al. | Optimization of bleaching of crude palm oil using activated groundnut hull | |
CN101040880B (en) | Method for preparing myrica seed oil capsule | |
CN107841373A (en) | A kind of ultrasonic extracting method of rapeseed oil | |
CN106495151A (en) | The preparation method of cotton stalk based active carbon | |
CN107853552A (en) | The method of cadmium content in lactic acid sodium chloride collaboration extraction abatement rice meal | |
JP2016047513A (en) | Producing method of oil palm stem plant cell wall powder by purifying oil palm stem cell wall particle and vascular bundle structure | |
CN110591811A (en) | Preparation method of cyperus esculentus 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 |
Application publication date: 20181211 |
|
RJ01 | Rejection of invention patent application after publication |