CN106889421A - The preparation method and its production line of a kind of natural lycopene pulvis - Google Patents
The preparation method and its production line of a kind of natural lycopene pulvis Download PDFInfo
- Publication number
- CN106889421A CN106889421A CN201710268583.XA CN201710268583A CN106889421A CN 106889421 A CN106889421 A CN 106889421A CN 201710268583 A CN201710268583 A CN 201710268583A CN 106889421 A CN106889421 A CN 106889421A
- Authority
- CN
- China
- Prior art keywords
- box
- mixer
- enrichment facility
- film evaporator
- rotary film
- 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
- UPYKUZBSLRQECL-UKMVMLAPSA-N Lycopene Natural products CC(=C/C=C/C=C(C)/C=C/C=C(C)/C=C/C1C(=C)CCCC1(C)C)C=CC=C(/C)C=CC2C(=C)CCCC2(C)C UPYKUZBSLRQECL-UKMVMLAPSA-N 0.000 title claims abstract description 36
- JEVVKJMRZMXFBT-XWDZUXABSA-N Lycophyll Natural products OC/C(=C/CC/C(=C\C=C\C(=C/C=C/C(=C\C=C\C=C(/C=C/C=C(\C=C\C=C(/CC/C=C(/CO)\C)\C)/C)\C)/C)\C)/C)/C JEVVKJMRZMXFBT-XWDZUXABSA-N 0.000 title claims abstract description 36
- OAIJSZIZWZSQBC-GYZMGTAESA-N lycopene Chemical compound CC(C)=CCC\C(C)=C\C=C\C(\C)=C\C=C\C(\C)=C\C=C\C=C(/C)\C=C\C=C(/C)\C=C\C=C(/C)CCC=C(C)C OAIJSZIZWZSQBC-GYZMGTAESA-N 0.000 title claims abstract description 36
- 235000012661 lycopene Nutrition 0.000 title claims abstract description 36
- 229960004999 lycopene Drugs 0.000 title claims abstract description 36
- 239000001751 lycopene Substances 0.000 title claims abstract description 36
- ZCIHMQAPACOQHT-ZGMPDRQDSA-N trans-isorenieratene Natural products CC(=C/C=C/C=C(C)/C=C/C=C(C)/C=C/c1c(C)ccc(C)c1C)C=CC=C(/C)C=Cc2c(C)ccc(C)c2C ZCIHMQAPACOQHT-ZGMPDRQDSA-N 0.000 title claims abstract description 36
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 31
- 238000002360 preparation method Methods 0.000 title claims abstract description 11
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 47
- 235000019441 ethanol Nutrition 0.000 claims abstract description 30
- 239000007788 liquid Substances 0.000 claims abstract description 28
- 238000000605 extraction Methods 0.000 claims abstract description 27
- 238000003756 stirring Methods 0.000 claims abstract description 21
- 238000001035 drying Methods 0.000 claims abstract description 18
- 241000220317 Rosa Species 0.000 claims abstract description 14
- 239000010408 film Substances 0.000 claims description 30
- 239000013078 crystal Substances 0.000 claims description 17
- 239000000463 material Substances 0.000 claims description 17
- 238000002425 crystallisation Methods 0.000 claims description 14
- 230000008025 crystallization Effects 0.000 claims description 13
- 238000001914 filtration Methods 0.000 claims description 7
- 239000000843 powder Substances 0.000 claims description 7
- 239000006228 supernatant Substances 0.000 claims description 7
- 239000010409 thin film Substances 0.000 claims description 7
- 239000000706 filtrate Substances 0.000 claims description 6
- 239000012141 concentrate Substances 0.000 claims description 5
- 239000000047 product Substances 0.000 claims description 5
- 235000010469 Glycine max Nutrition 0.000 claims description 4
- 244000068988 Glycine max Species 0.000 claims description 4
- 238000001556 precipitation Methods 0.000 claims description 3
- 238000001291 vacuum drying Methods 0.000 claims description 3
- 150000001875 compounds Chemical class 0.000 claims 1
- 240000003768 Solanum lycopersicum Species 0.000 abstract description 12
- 235000007688 Lycopersicon esculentum Nutrition 0.000 abstract description 11
- 238000000034 method Methods 0.000 abstract description 7
- 239000001054 red pigment Substances 0.000 abstract description 7
- GVJHHUAWPYXKBD-UHFFFAOYSA-N (±)-α-Tocopherol Chemical compound OC1=C(C)C(C)=C2OC(CCCC(C)CCCC(C)CCCC(C)C)(C)CCC2=C1C GVJHHUAWPYXKBD-UHFFFAOYSA-N 0.000 description 4
- 241000196324 Embryophyta Species 0.000 description 3
- 239000004519 grease Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- 229930003427 Vitamin E Natural products 0.000 description 2
- 238000013329 compounding Methods 0.000 description 2
- WIGCFUFOHFEKBI-UHFFFAOYSA-N gamma-tocopherol Natural products CC(C)CCCC(C)CCCC(C)CCCC1CCC2C(C)C(O)C(C)C(C)C2O1 WIGCFUFOHFEKBI-UHFFFAOYSA-N 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000008601 oleoresin Substances 0.000 description 2
- 239000007901 soft capsule Substances 0.000 description 2
- 235000019165 vitamin E Nutrition 0.000 description 2
- 229940046009 vitamin E Drugs 0.000 description 2
- 239000011709 vitamin E Substances 0.000 description 2
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 235000006708 antioxidants Nutrition 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000002775 capsule Substances 0.000 description 1
- 235000021466 carotenoid Nutrition 0.000 description 1
- 150000001747 carotenoids Chemical class 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 235000012907 honey Nutrition 0.000 description 1
- 210000000987 immune system Anatomy 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- -1 oxygen radical Chemical class 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000005070 ripening Effects 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
Abstract
The invention discloses the preparation method and its production line of a kind of natural lycopene pulvis, production line includes extraction element, the extraction element includes catch box and separating box, the separating box is fixedly connected on the surface of liquid collecting chamber interior wall, the bottom of the extraction element is connected with rotary film evaporator enrichment facility, the bottom of the rotary film evaporator enrichment facility is connected with mixer, the top of the mixer and it is fixedly connected with stirring motor on the right side of rotary film evaporator enrichment facility, the top of the mixer and ethyl alcohol box is fixedly connected with the left of stirring motor, the bottom of the mixer is connected with filter, the filter includes Rose Box and liquid reserve tank.The cooperation that the present invention passes through extraction element, rotary film evaporator enrichment facility, mixer, ethyl alcohol box, filter and drying box, improves the production efficiency of production line, solves the problems, such as conventional tomato red pigment process units low production efficiency.
Description
Technical field
The present invention relates to lycopene pulvis production technical field, specially a kind of preparation side of natural lycopene pulvis
Method and its production line.
Background technology
Lycopene is contained a kind of natural pigment in plant, is primarily present in the ripening fruits of plant of Solanaceae tomato
In, it is most one of the powerful antioxidant being found in the plant of nature at present, and science is proved, the singlet oxygen in human body
With oxygen radical be encroach on human body self immune system arch-criminal, lycopene remove free radical effect outclass other
Carotenoid and vitamin E, its singlet-oxygen quenching speed constant are 100 times of vitamin E.Natural tomato in the market
The extraction process of red pigment is substantially all as described above, still because in extraction process, tomato contains some greases in itself, finally carries
, just than larger, particularly content is higher, and the state of oleoresin is more viscous for the ratio that grease is accounted in the lycopene oleoresin for taking
It is thick（As very sticky honey）, it is exactly to cause bad making capsule that such product makees soft capsule to client, is easily caused
The phenomenon of leakage.
At present, it is main using slag-drip opening is set in the bottom of tank body when collection lycopene is extracted, by the separator of bottom
Discharge, the existing amount for extracting collection lycopene device discharge bottom separator is difficult control, can not substantially accomplish completely
Effective lycopene is extracted, impurities left is can hardly be avoided, and the splashing of eddy-currents and liquid can be produced when extracting supernatant liquid,
Section bottom liquid is mixed into upper strata, so as to influence the quality extracted, extraction rate is slow and quality cannot be guaranteed.
The content of the invention
It is an object of the invention to provide the preparation method and its production line of a kind of natural lycopene pulvis, possess and carry
Take, crystallize, stirring, filtering and dry function, greatly improving the advantage of production efficiency, solving conventional tomato red pigment production dress
Put the problem of low production efficiency.
To achieve the above object, the present invention provides following technical scheme：A kind of natural lycopene powder production line, including
Extraction element, the extraction element includes catch box and separating box, and the separating box is fixedly connected on the surface of liquid collecting chamber interior wall,
The bottom of the extraction element is connected with rotary film evaporator enrichment facility, the rotary film evaporator enrichment facility
Bottom be connected with mixer, the top of the mixer and fixed positioned at the right side of rotary film evaporator enrichment facility
It is connected with stirring motor, the top of the mixer and ethyl alcohol box is fixedly connected with the left of stirring motor, the stirring
The bottom of machine is connected with filter, and the filter includes Rose Box and liquid reserve tank, and the liquid reserve tank is flexibly connected
Drying box, the output end and Rotational Thin of the extraction element are connected with the right side of the right side of Rose Box, the Rose Box
The input of film evaporator enrichment facility is unidirectionally electrically connected with, the output end of the rotary film evaporator enrichment facility respectively with
The input of mixer and ethyl alcohol box is unidirectionally electrically connected with, and the output end of the mixer and ethyl alcohol box is defeated with filter
Enter the unidirectional electric connection in end, the output end of the filter is unidirectionally electrically connected with the input of drying box.
A kind of preparation method of natural lycopene pulvis adds alcohol and it is stirred in catsup first, stirs
Filtering removal residue of soya is carried out to catsup afterwards, supernatant carries out filtrate and concentrates to form crystallization, and the crystal for obtaining proceeds crystal
Finished product is formed after precipitation.
Further, supernatant carry out filtrate concentrate to form crystallization after continuously add alcohol and be stirred, it is then right again
Crystal and alcohol are filtered, and obtain crystal again, and crystal being taken after be dried in vacuum drying chamber and adds appropriate auxiliary material
Compounding, is fabricated to the natural lycopene pulvis of various contents.
Preferably, the top of the rotary film evaporator enrichment facility is taken over by material inlet and is connected with catch box,
The bottom of the rotary film evaporator enrichment facility is taken over by material outlet and is connected with mixer.
Preferably, the positive top of rotary film evaporator enrichment facility is fixedly connected with visor, the rotation
The front of thin film evaporator enrichment facility and it is fixedly connected with lower visor positioned at the bottom of upper visor.
Preferably, the bottom of the mixer is connected by stirring efferent duct with Rose Box, and the top of the liquid reserve tank is consolidated
Surely it is connected with vavuum pump.
Preferably, the top of the Rose Box is connected by suck-back screen pipe with liquid reserve tank, and the right side of the liquid reserve tank leads to
Discharge nozzle is crossed to be connected with drying box.
Beneficial effects of the present invention are as follows：
1st, the present invention is by being provided with extraction element so that extraction element can be extracted to the lycopene in tomato, be passed through
There is provided rotary film evaporator enrichment facility so that rotary film evaporator enrichment facility can be concentrated crystallization, by setting
Mixer and ethyl alcohol box are put, mixer adds alcohol while being stirred to crystallization, by being provided with filter, filtering
Lycopene can be carried out separation of solid and liquid by device, then be dried treatment by drying box, ultimately produce lycopene pulvis,
By the cooperation of extraction element, rotary film evaporator enrichment facility, mixer, ethyl alcohol box, filter and drying box, improve
The production efficiency of production line, solves the problems, such as conventional tomato red pigment process units low production efficiency.
2nd, the present invention is taken over and material outlet adapter by being provided with material inlet, improves the processing efficiency of material, is led to
Cross and be provided with upper visor and lower visor, facilitate staff to observe condensing crystallizing situation, it is convenient by being provided with stirring efferent duct
Material is delivered to filter by mixer, and by being provided with vavuum pump, vavuum pump can provide pressure, pass through for suck-back screen pipe
There is provided discharge nozzle, facilitates liquid reserve tank that liquid is delivered into drying box.
Brief description of the drawings
Fig. 1 is schematic structural view of the invention.
Fig. 2 is present system schematic diagram.
Specific embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation is described.
Embodiment 1：The preparation method of natural lycopene pulvis, adds alcohol and it is stirred in catsup first
Mix, carry out filtering removal residue of soya after stirring to catsup, supernatant carries out filtrate and concentrate to form crystallization, the crystal for obtaining continue into
Finished product is formed after row crystal precipitation.Just reduced much by the content of grease in this method finished product, be especially suitable for making soft capsule
Raw material.
Embodiment 2：The preparation method of natural lycopene pulvis, adds alcohol and it is stirred in catsup first
Mix, carry out filtering removal residue of soya after stirring to catsup, supernatant carries out filtrate and concentrates to form crystallization, and crystallization is continuously added into wine
Essence is stirred, and crystal and alcohol are filtered again then, and crystal is obtained again, and crystal is done in taking vacuum drying chamber
Appropriate auxiliary material compounding is added after dry, the natural lycopene pulvis of various contents is fabricated to.It is de- in crystal by process optimization
Before molten, appropriate alcohol is added to wash unnecessary grease off in crystal after crystallisation.
Fig. 1-2 is referred to, production line of the present invention includes extraction element 1, and extraction element 1 includes catch box 11 and separating box
12, separating box 12 is fixedly connected on the surface of the inwall of catch box 11, and the bottom of extraction element 1 is connected with rotating thin film evaporation
Device enrichment facility 2, the bottom of rotary film evaporator enrichment facility 2 is connected with mixer 3, the top and position of mixer 3
Stirring motor 31 is fixedly connected with the right side of rotary film evaporator enrichment facility 2, the top of mixer 3 and positioned at stirring electricity
The left side of machine 31 is fixedly connected with ethyl alcohol box 4, and the bottom of mixer 3 is connected with filter 5, and filter 5 included
Filter box 51 and liquid reserve tank 52, liquid reserve tank 52 are movably connected in the right side of Rose Box 51, and the right side of Rose Box 51 is connected with dry
Dry case 6, output end and the input of rotary film evaporator enrichment facility 2 of extraction element 1 are unidirectionally electrically connected with, rotating thin film
Input of the output end of evaporator enrichment facility 2 respectively with mixer 3 and ethyl alcohol box 4 is unidirectionally electrically connected with, mixer 3 and wine
Input of the output end of smart box 4 with filter 5 is unidirectionally electrically connected with, and the output end of filter 5 is defeated with drying box 6
Enter the unidirectional electric connection in end, the top of rotary film evaporator enrichment facility 2 is connected by material inlet adapter 21 with catch box 11
Logical, the bottom of rotary film evaporator enrichment facility 2 is connected by material outlet adapter 22 with mixer 3, by being provided with thing
Material entrance sleeve 21 and material outlet adapter 22, improve the processing efficiency of material, the front of rotary film evaporator enrichment facility 2
Top be fixedly connected with visor 23, the front of rotary film evaporator enrichment facility 2 and consolidate positioned at the bottom of upper visor 23
Surely lower visor 24 is connected with, by being provided with upper visor 23 and lower visor 24, facilitates staff to observe condensing crystallizing situation, stirred
The bottom for mixing machine 3 is connected by stirring efferent duct 32 with Rose Box 51, and the top of liquid reserve tank 52 is fixedly connected with vavuum pump 53, mistake
The top of filter box 51 is connected by suck-back screen pipe 54 with liquid reserve tank 52, and the right side of liquid reserve tank 52 passes through discharge nozzle 55 and drying box
6 connections, by being provided with stirring efferent duct 32, facilitate mixer 3 that material is delivered into filter 5, by being provided with vacuum
Pump 53, vavuum pump 53 can provide pressure for suck-back screen pipe 54, by being provided with discharge nozzle 55, facilitate liquid reserve tank 52 that liquid is defeated
Drying box 6 is delivered to, by being provided with extraction element 1 so that extraction element 1 can be extracted to the lycopene in tomato, is led to
Cross and be provided with rotary film evaporator enrichment facility 2 so that rotary film evaporator enrichment facility 2 can be concentrated crystallization, lead to
Cross and be provided with mixer 3 and ethyl alcohol box 4,3 pairs of crystallizations of mixer add alcohol while being stirred, by being provided with filtering dress
5 are put, lycopene can be carried out separation of solid and liquid by filter 5, then be dried treatment by drying box 6, ultimately produced kind
Lycopene pulvis, by extraction element 1, rotary film evaporator enrichment facility 2, mixer 3, ethyl alcohol box 4, the and of filter 5
The cooperation of drying box 6, improves the production efficiency of production line, solves asking for conventional tomato red pigment process units low production efficiency
Topic.When using, extraction element 1 can be extracted to the lycopene in tomato, be concentrated by being provided with rotary film evaporator
Device 2 so that rotary film evaporator enrichment facility 2 can be concentrated crystallization, by being provided with mixer 3 and ethyl alcohol box 4, stirs
Mix while 3 pairs of crystallizations of machine are stirred and add alcohol, by being provided with filter 5, filter 5 can enter lycopene
Row separation of solid and liquid, is then dried treatment by drying box 6, ultimately produces lycopene pulvis, by extraction element 1, rotation
Turn the cooperation of thin film evaporator enrichment facility 2, mixer 3, ethyl alcohol box 4, filter 5 and drying box 6, improve production line
Production efficiency, solves the problems, such as conventional tomato red pigment process units low production efficiency.
In sum：The natural lycopene powder production line, by extraction element 1, catch box 11, separating box 12, rotation
Turn the cooperation of thin film evaporator enrichment facility 2, mixer 3, ethyl alcohol box 4, filter 5 and drying box 6, solve conventional tomato
The problem of red pigment process units low production efficiency.
Although an embodiment of the present invention has been shown and described, for the ordinary skill in the art, can be with
Understanding can carry out various changes, modification, replacement to these embodiments without departing from the principles and spirit of the present invention
And modification, the scope of the present invention be defined by the appended.
Claims (7)
1. a kind of natural lycopene powder production line, including extraction element（1）, it is characterised in that：The extraction element（1）Bag
Include catch box（11）And separating box（12）, the separating box（12）It is fixedly connected on catch box（11）The surface of inwall, it is described to carry
Take device（1）Bottom be connected with rotary film evaporator enrichment facility（2）, the rotary film evaporator enrichment facility
（2）Bottom be connected with mixer（3）, the mixer（3）Top and positioned at rotary film evaporator enrichment facility
（2）Right side be fixedly connected with stirring motor（31）, the mixer（3）Top and positioned at stirring motor（31）Left side consolidate
Surely it is connected with ethyl alcohol box（4）, the mixer（3）Bottom be connected with filter（5）, the filter（5）Bag
Include Rose Box（51）And liquid reserve tank（52）, the liquid reserve tank（52）It is movably connected in Rose Box（51）Right side, the Rose Box
（51）Right side be connected with drying box（6）, the extraction element（1）Output end and rotary film evaporator enrichment facility
（2）Input be unidirectionally electrically connected with, the rotary film evaporator enrichment facility（2）Output end respectively with mixer（3）
And ethyl alcohol box（4）Input be unidirectionally electrically connected with, the mixer（3）And ethyl alcohol box（4）Output end and filter
（5）Input be unidirectionally electrically connected with, the filter（5）Output end and drying box（6）Input unidirectionally electrically connect
Connect.
2. a kind of natural lycopene powder production line according to claim 1, it is characterised in that：The rotating thin film steams
Hair device enrichment facility（2）Top by material inlet take over（21）With catch box（11）Connection, the rotary film evaporator
Enrichment facility（2）Bottom by material outlet take over（22）With mixer（3）Connection.
3. a kind of natural lycopene powder production line according to claim 1, it is characterised in that：The rotating thin film steams
Hair device enrichment facility（2）Positive top is fixedly connected with visor（23）, the rotary film evaporator enrichment facility（2）'s
Front and positioned at upper visor（23）Bottom be fixedly connected with lower visor（24）.
4. a kind of natural lycopene powder production line according to claim 1, it is characterised in that：The mixer（3）
Bottom by stirring efferent duct（32）With Rose Box（51）Connection, the liquid reserve tank（52）Top be fixedly connected with vavuum pump
（53）.
5. a kind of natural lycopene powder production line according to claim 1 or 4, it is characterised in that：The Rose Box
（51）Top pass through suck-back screen pipe（54）With liquid reserve tank（52）Connection, the liquid reserve tank（52）Right side pass through discharge nozzle
（55）With drying box（6）Connection.
6. a kind of preparation method of natural lycopene pulvis, it is characterised in that：Alcohol is added in catsup and it is entered first
Row stirring, carries out filtering removal residue of soya to catsup after stirring, supernatant carries out filtrate and concentrate to form crystallization, the crystal for obtaining after
Continue and form finished product after carrying out crystal precipitation.
7. the preparation method of a kind of natural lycopene pulvis according to claim 6, it is characterised in that：Enter in supernatant
Row filtrate is concentrated after forming crystallization and continuously adds alcohol and be stirred, and crystal and alcohol are filtered again then, is obtained again
Crystal, crystal being taken after be dried in vacuum drying chamber and adds appropriate auxiliary material to compound, and is fabricated to natural kind of various contents
Lycopene pulvis.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710268583.XA CN106889421A (en) | 2017-04-23 | 2017-04-23 | The preparation method and its production line of a kind of natural lycopene pulvis |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710268583.XA CN106889421A (en) | 2017-04-23 | 2017-04-23 | The preparation method and its production line of a kind of natural lycopene pulvis |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106889421A true CN106889421A (en) | 2017-06-27 |
Family
ID=59196913
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710268583.XA Pending CN106889421A (en) | 2017-04-23 | 2017-04-23 | The preparation method and its production line of a kind of natural lycopene pulvis |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106889421A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1557879A (en) * | 2004-01-15 | 2004-12-29 | 新疆生命红果蔬制品有限公司 | Process and device for extracting natural lycopene oil resin |
| CN1687239A (en) * | 2005-05-25 | 2005-10-26 | 中国科学院新疆理化技术研究所 | Method for preparing crystal of lycopene and concentrate |
| CN101704703A (en) * | 2008-07-21 | 2010-05-12 | 聂希刚 | Method for producing high-purity lycopene powder by utilizing plant products |
| KR101112053B1 (en) * | 2011-06-20 | 2012-02-13 | 신라대학교 산학협력단 | Method for obtaining purified lycopene and water-soluble lycopene from tomato |
| CN202912866U (en) * | 2012-11-28 | 2013-05-01 | 黑龙江八一农垦大学 | Lycopene extraction device |
| CN203976669U (en) * | 2014-06-24 | 2014-12-03 | 新疆西域果宝生物科技有限公司 | A kind of device that extracts high-purity lycopene from tomato |
-
2017
- 2017-04-23 CN CN201710268583.XA patent/CN106889421A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1557879A (en) * | 2004-01-15 | 2004-12-29 | 新疆生命红果蔬制品有限公司 | Process and device for extracting natural lycopene oil resin |
| CN1687239A (en) * | 2005-05-25 | 2005-10-26 | 中国科学院新疆理化技术研究所 | Method for preparing crystal of lycopene and concentrate |
| CN101704703A (en) * | 2008-07-21 | 2010-05-12 | 聂希刚 | Method for producing high-purity lycopene powder by utilizing plant products |
| KR101112053B1 (en) * | 2011-06-20 | 2012-02-13 | 신라대학교 산학협력단 | Method for obtaining purified lycopene and water-soluble lycopene from tomato |
| CN202912866U (en) * | 2012-11-28 | 2013-05-01 | 黑龙江八一农垦大学 | Lycopene extraction device |
| CN203976669U (en) * | 2014-06-24 | 2014-12-03 | 新疆西域果宝生物科技有限公司 | A kind of device that extracts high-purity lycopene from tomato |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN207567146U (en) | A kind of extraction concentrator of vegetable protein | |
| CN105175564B (en) | The industrialization extraction separation method and separator of ganoderma spore polysaccharide | |
| CN102675910B (en) | Preparation method of high-color-value beet root red color | |
| CN105153737B (en) | The extraction degumming tech of pepper extract | |
| CN1043074A (en) | The manufacture method of instant coconut milk powder, coconut slurry powder | |
| CN212246935U (en) | Camellia seed squeezing device convenient for solid-liquid separation | |
| CN206687097U (en) | A kind of natural lycopene powder production line | |
| CN207385000U (en) | Plant extraction liquid filter device | |
| CN102250488B (en) | Method for improving quality of capsanthin product | |
| CN104397193B (en) | The high micro- defibrination of bucket storage slag circulation is divided to produce the Processes and apparatus of Walnut Milk | |
| CN212998514U (en) | Be used for glossy ganoderma composition extraction device | |
| CN106889421A (en) | The preparation method and its production line of a kind of natural lycopene pulvis | |
| CN210645410U (en) | Honeysuckle dregs of a decoction liquid separator | |
| CN108392858A (en) | A kind of thickener | |
| CN109837136A (en) | A kind of method of Dewaxing of Rice Bran degreasing | |
| CN204981708U (en) | Separator that industrialization of glossy ganoderma spore polysaccharide was drawed | |
| CN214763562U (en) | Plant essential oil filter equipment | |
| CN205867781U (en) | Refine device of six -element digitalis chewing tablet extract | |
| CN209476449U (en) | A kind of vegetable protein classification fine processing device | |
| CN208340171U (en) | A kind of feeding device of the molten extraction of lutein | |
| CN206139463U (en) | Shelled peanut soil block separator | |
| CN107839274A (en) | A kind of feeding device of edible oil oil press | |
| CN109338019A (en) | Sugarcane cleans automatically and the method for cane sugar manufacture | |
| CN207493336U (en) | A kind of Xanthophylls from Marigold purification devices | |
| CN217015704U (en) | Concentrated solution extraction element of string leaf gold sparrow flower |
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 |