CN206447802U - A kind of gibberellin high power enrichment facility - Google Patents
A kind of gibberellin high power enrichment facility Download PDFInfo
- Publication number
- CN206447802U CN206447802U CN201720084608.6U CN201720084608U CN206447802U CN 206447802 U CN206447802 U CN 206447802U CN 201720084608 U CN201720084608 U CN 201720084608U CN 206447802 U CN206447802 U CN 206447802U
- Authority
- CN
- China
- Prior art keywords
- gibberellin
- pump
- high power
- enrichment facility
- high pressure
- 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.)
- Active
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a kind of gibberellin high power enrichment facility, including the head tank being sequentially connected by feed pipe, feed pump, cartridge filter, one-level booster pump, two-stage supercharging pump and high pressure resistant membrane module, there is concentrated solution outlet and dialyzate to export on described high pressure resistant membrane module, the concentrated solution outlet of described high pressure resistant membrane module connects reflux line and concentrate pipeline by pipeline respectively, described concentrate pipeline connection concentration flow container, the feed pipe between described reflux line connection one-level booster pump and two-stage supercharging pump；Described dialyzate outlet connects dialysis fluid container by dialysis pipeline.Gibberellin high power enrichment facility described in the utility model, instead of the group technology of traditional nanofiltration+thin film evaporation using high power enrichment facility, and ton water process expense is at 25 yuans or so, and high degree reduces production cost；One step realizes the high power concentration of gibberellin, and yield lifting is obvious；Product loss caused by evaporation heating is avoided simultaneously.
Description
Technical field
The utility model is related to gibberellin and extracts field, more particularly to a kind of gibberellin high power enrichment facility.
Background technology
Gibberellin, its molecular formula is C19H22O6, molecular weight is 346.37.Gibberellin is that the class plant being widely present swashs
Element；Its chemical constitution belongs to Diterpenes acid, is derived by four ring skeletons and is obtained.The growth of leaf and bud can be stimulated.Known gibberellin
At least 38 kinds of class.Gibberellin is applied to agricultural production, there is better effects in some aspects.Zante currant yield is for example improved,
Break potato dormancy；In beer brewing, promoted to prepare the sprouting of the barley seed of maltose with gibberellin；Work as late rice
When meeting overcast and rainy low temperature and earing slow, heading can be promoted by being handled with gibberellin；Or in breeding of hybrid rice florescence alternation so that
Parent flower synchronization etc..
Current gibberellin is mainly produced by fermentation process.Fermentation primary raw material is starch, peanut cake, corn steep liquor, grape
Sugar etc..Gibberellin strain is first through slant strains culture（27 DEG C, 4-5d), then through seed Spawn incubation（27 DEG C, 4-5d).In seed
The process conditions of tank fermentation are 27 DEG C, 72h.The process conditions of fermentation tank synthesis are 27 DEG C, 160h, dense through filtering after biosynthesis
Contracting produces gibberellin finished product（Concentrate aqueous liquid）.
At present, common method for concentration is high-temperature steam concentration and NF membrane concentration, wherein using the red mould of nanofiltration concentration
The production technology comparative maturity, the basic flow of traditional gibberellin method for concentration of element：Zymotic fluid-plate-frame filtering-nanofiltration
Concentration-thin film evaporation-crystallization.The combination of wherein nanofiltration and thin film evaporation is the key point of concentration, and nanofiltration process is from 2000mg/
L or so is concentrated into 8000mg/L or so, then transfers to thin film evaporation to be concentrated into 18000mg/L or so and is post-processed again.Using
This technique, with following shortcomings：1）Thin film evaporation is due to being that evaporation and concentration energy consumption is high, and ton water evaporation expense is probably at 80 yuan
RMB or so；2）Gibberellin is heat-sensitive substance, and the high temperature that evaporation is produced can make product degrade, and reduce Product Activity.
The content of the invention
In view of the above-mentioned problems, the purpose of this utility model, which is that offer is a kind of, can realize the red mould of gibberellin high power concentration
Plain high power enrichment facility.
To reach above-mentioned purpose, the technical scheme that the utility model is proposed is：A kind of gibberellin high power enrichment facility, its
It is characterised by：Including the head tank being sequentially connected by feed pipe, feed pump, cartridge filter, one-level booster pump, two grades of increasings
There is concentrated solution outlet and dialyzate to export, described resistance to height on press pump and high pressure resistant membrane module, described high pressure resistant membrane module
The concentrated solution outlet of press mold component connects reflux line and concentrate pipeline, described concentrate pipeline connection by pipeline respectively
Concentrate flow container, the feed pipe between described reflux line connection one-level booster pump and two-stage supercharging pump；Described dialyzate goes out
Mouth connects dialysis fluid container by dialysis pipeline.
It is preferred that, described high pressure resistant membrane module is the high pressure resistant organic nanofiltration membrane component that pressure-resistant scope is 0-90bar；Cut
It is 50-200 dalton to stay molecular weight.
It is preferred that, described cartridge filter filtering accuracy is 1-5 μm.
It is preferred that, described one-level booster pump is plunger pump.
It is preferred that, described two-stage supercharging pump is high pressure resistant centrifugal pump.
Using above-mentioned technical proposal, gibberellin high power enrichment facility described in the utility model, have the advantage that for：
1) group technology of traditional nanofiltration+thin film evaporation is instead of using high power enrichment facility, ton water process expense is 25
Yuan or so, high degree reduces production cost；
2) step realizes the high power concentration of gibberellin, and yield lifting is obvious；
3) high power enrichment facility is that physical concentration process avoids product loss caused by evaporation heating.
Brief description of the drawings
Fig. 1 is gibberellin high power enrichment facility schematic diagram described in the utility model.
Embodiment
With reference to the accompanying drawings and detailed description, the utility model is described further.
As shown in figure 1, gibberellin high power enrichment facility described in the utility model, including by feed pipe 102 successively
Connected head tank 101, feed pump 103, cartridge filter 104, one-level booster pump 105, two-stage supercharging pump 106 and high pressure resistant film
Component 107；Wherein the filtering accuracy of cartridge filter 104 is 1-5 microns, one-level booster pump preferred plunger pump, two-stage supercharging pump
It is preferred that centrifugal pump, high pressure resistant membrane module 107 is with trapezoidal flow passage structure, high pressure resistant rolling organic nanofiltration membrane component；Retention point
Son amount is 50-200 dalton, and pressure-resistant scope is 0-90bar.
Further, there is concentrated solution outlet on high pressure resistant membrane module 107（It is not shown）With dialyzate outlet（It is not shown）,
The concentrated solution outlet of described high pressure resistant membrane module 107 connects reflux line 108 and concentrate pipeline 109 by pipeline respectively,
The connection concentration flow container 110 of concentrate pipeline 109；Make the entrance pipeline that concentrate is back to before two-stage supercharging pump 106, through two grades of increasings
Press pump 106 carries out circulation concentration after being pressurized, and improves concentration or reaches after cycles of concentration requirement and flow to concentration through concentrate pipeline 109
Flow container 110 is stored, for subsequent treatment；Described dialyzate outlet connects dialysis fluid container 112 by dialysis pipeline 111.
When specifically used, gibberellin feed liquid to be concentrated（Gibberellin concentration is 2000-3000mg/L in feed liquid）It is stored in
In head tank, feed pipe is inputted by feed pump, is pressurized after cartridge filter filtering removal solid suspension, then through one-level
Pump is pressurized and two-stage supercharging pump is pressurized to after 75bar or so, and gibberellin feed liquid enters to be concentrated in high pressure nanofiltration membrane component, water
Molecule etc. enters in dialysis fluid container through NF membrane is stored back into use；And the gibberellin concentrate liquid containing high concentration is then by NF membrane
Retention, two-stage supercharging pump intake is back to through reflux line, after being pressurized through two-stage supercharging pump, carries out circulation concentration, solution to be concentrated
Middle GA content reaches after 20000mg/L that then concentrated pipeline flow in concentration flow container and stores standby.
Although specifically showing and describing the utility model with reference to preferred embodiment, those skilled in the art should
This is understood, is not departing from the spirit and scope of the present utility model that appended claims are limited, in form and details
On the utility model is made a variety of changes, be protection domain of the present utility model.
Claims (5)
1. a kind of gibberellin high power enrichment facility, it is characterised in that：Including be sequentially connected by feed pipe head tank, charging
Have on pump, cartridge filter, one-level booster pump, two-stage supercharging pump and high pressure resistant membrane module, described high pressure resistant membrane module dense
Contracting liquid is exported and dialyzate outlet, the concentrated solution outlet of described high pressure resistant membrane module connected respectively by pipeline reflux line and
Concentrate pipeline, described concentrate pipeline connection concentration flow container, described reflux line connection one-level booster pump and two grades of increasings
Feed pipe between press pump；Described dialyzate outlet connects dialysis fluid container by dialysis pipeline.
2. a kind of gibberellin high power enrichment facility according to claim 1, it is characterised in that：Described high pressure resistant membrane module
The high pressure resistant organic nanofiltration membrane component for being 0-90bar for pressure-resistant scope；Molecular cut off is 50-200 dalton.
3. a kind of gibberellin high power enrichment facility according to claim 1, it is characterised in that：Described cartridge filter mistake
It is 1-5 μm to filter precision.
4. a kind of gibberellin high power enrichment facility according to claim 1, it is characterised in that：Described one-level booster pump is
Plunger pump.
5. a kind of gibberellin high power enrichment facility according to claim 1, it is characterised in that：Described two-stage supercharging pump is
High pressure resistant centrifugal pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720084608.6U CN206447802U (en) | 2017-01-23 | 2017-01-23 | A kind of gibberellin high power enrichment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720084608.6U CN206447802U (en) | 2017-01-23 | 2017-01-23 | A kind of gibberellin high power enrichment facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206447802U true CN206447802U (en) | 2017-08-29 |
Family
ID=59666988
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720084608.6U Active CN206447802U (en) | 2017-01-23 | 2017-01-23 | A kind of gibberellin high power enrichment facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206447802U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113940398A (en) * | 2021-09-23 | 2022-01-18 | 同舟纵横（厦门）流体技术有限公司 | Method and device for concentrating carrot juice |
-
2017
- 2017-01-23 CN CN201720084608.6U patent/CN206447802U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113940398A (en) * | 2021-09-23 | 2022-01-18 | 同舟纵横（厦门）流体技术有限公司 | Method and device for concentrating carrot juice |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104862348B (en) | A kind of method that production long-chain biatomic acid is coupled with UF membrane of fermenting | |
| CN101215592B (en) | Fermentation method for producing pullulan polysaccharide | |
| CN101487034B (en) | Preparation of beta-poly malic acid and salt thereof | |
| CN101434553B (en) | Method for all-film extraction of valine | |
| CN101838342A (en) | Membrane separation method for microalgae extracellular polysaccharide | |
| CN103525871B (en) | Method for producing lycopene through fermentation | |
| CN1325633C (en) | Glycerol channel protein gene deleted brewing microzyme strain capable of reducing glycerol output and increasing ethanol output and construction method thereof | |
| CN206447802U (en) | A kind of gibberellin high power enrichment facility | |
| CN106220521B (en) | A kind of method of full film extraction L isoleucines | |
| CN102838624B (en) | Method for purifying clavulanic acid from fermentation liquor | |
| CN103130664A (en) | Process method of extracting gamma-aminobutyric acid through membrane separation technique | |
| CN103224960B (en) | Method for producing erythritol by continuously fermenting and extracting Torula.sp strain | |
| CN206418064U (en) | A kind of gibberellin high power concentration systems | |
| CN102643364A (en) | Method for extracting ganoderan from submerged-fermentation mycelia of ganoderma lucidum | |
| CN100529055C (en) | Alcaligenes and application thereof in preparation of welan gum | |
| CN102021212A (en) | Preparation method of ganoderma polysaccharide | |
| CN104031109A (en) | Method for purifying tea saponin by microbial fermentation | |
| CN104046572B (en) | One plant of saccharomyces cerevisiae that can reduce biogenic amine in yellow rice wine and its construction method and application | |
| CN110066737A (en) | Microalgae and the method for obtaining microalgae biomass | |
| CN105349439A (en) | Culture and fermentation method of inonotus obliquus and preparation method of water-soluble polysaccharides of inonotus obliquus | |
| CN104694614A (en) | Novel extraction process of L-tryptophan | |
| CN106749140A (en) | A kind of gibberellin high power concentration technology and concentration systems | |
| CN205874262U (en) | Sour dragon in mother liquor middle ancient times acid recovery device of gu long | |
| CN104189087A (en) | Method for extracting total flavonoid functional substance from folium mori | |
| CN112481315B (en) | Method for preparing citric acid by continuous liquid-changing fermentation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: A high concentration device for gibberellin Effective date of registration: 20210205 Granted publication date: 20170829 Pledgee: Xiamen Huli District Financing Guarantee Co.,Ltd. Pledgor: CROSSFLOW (XIAMEN) FLUID TECHNOLOGY Co.,Ltd. Registration number: Y2021980001060 |