CN204958929U - Device of single -channel type cell backward flow continuous production high -purity gala oligosaccharide - Google Patents
Device of single -channel type cell backward flow continuous production high -purity gala oligosaccharide Download PDFInfo
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- CN204958929U CN204958929U CN201520682201.4U CN201520682201U CN204958929U CN 204958929 U CN204958929 U CN 204958929U CN 201520682201 U CN201520682201 U CN 201520682201U CN 204958929 U CN204958929 U CN 204958929U
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- galactooligosacchari
- purity
- fermenter
- transfer line
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Abstract
The utility model relates to a device of single -channel type cell backward flow continuous production high -purity gala oligosaccharide, collector unit, agitator, first pump, second pump, third pump and fourth pump including gas control device, fermentation tank, cell settler, raw material tank, high -purity gala oligosaccharide, the utility model discloses a coherency saccharomycete condense the characteristic to and make full use of cell settler flows back by the thallus and the continuous operation of single groove series connection, can carry out the fermentation in highly diluted speed, avoids miscellaneous fungus to grow up, maintains the system stability, reduction in production cost, improvement production efficiency.
Description
Technical field
The utility model relates to a kind of cell refluxing reactor, espespecially a kind of device of single-channel type cell backflow continuous seepage high purity galactooligosacchari(es.
Background technology
Galactooligosacchari(es (Galactooligosaccharides, GOS) be a kind of bifidus factor, there is the propagation that can promote bifidus bacillus in enteron aisle, improve intestinal flora distribution, suppress harmful bacteria breeding in enteron aisle, improve digestion and absorption function, and to make in intestines organic acid concentration increase, promote calcium absorptivity, with the effect such as reduction serum cholesterol, there are many benefits to the health of human body, and become the emphasis of biotechnology research now.
Utility model content
The purpose of this utility model is to provide the device of a kind of single-channel type cell backflow continuous seepage high purity galactooligosacchari(es, utilize the production advantage of this device, realize serialization, automatization transform purity be 57% galactooligosacchari(es GOS-570 and purity be the galactooligosacchari(es GOS-700 of 70%, with production high purity galactooligosacchari(es, such as purity is the galactooligosacchari(es GOS-1000 of 100%.
In order to achieve the above object, the technical scheme that the utility model is taked is:
A kind of device of single-channel type cell backflow continuous seepage high purity galactooligosacchari(es, wherein, the device of this single-channel type cell backflow continuous seepage high purity galactooligosacchari(es comprises a gas control equipment, a fermenter, a cell settlement device, a raw material tank, the collector unit of a high purity galactooligosacchari(es, an agitator, one first pump, one second pump, one the 3rd pump and one the 4th pump, described gas control equipment is communicated with described fermenter with an airline, described fermenter is communicated to the top of described cell settlement device with fermented liquid transfer line, the bottom of described cell settlement device is reclaimed transfer line with yeast and is communicated with described fermenter, the side top of described cell settlement device is communicated with the collector unit of supernatant product transfer line with described high purity galactooligosacchari(es, described fermenter is communicated with described raw material tank with feedstock transportation pipeline, described agitator is installed in described fermenter, described first pump is located on described feedstock transportation pipeline, described second pump is located on described fermented liquid transfer line, described 3rd pump is located at described yeast and is reclaimed on transfer line, described 4th pump is located on described supernatant product transfer line.
Advantage of the present utility model is:
The utility model utilize continuous print mode by by raw material and purity be 57% galactooligosacchari(es GOS-570 or purity be 70% galactooligosacchari(es be automatically converted into high purity galactooligosacchari(es, such as purity is the galactooligosacchari(es GOS-1000 of 100%, there is highly diluted speed ferment, avoid varied bacteria growing, maintain system stability, reduce production cost, the advantage such as to enhance productivity.
Accompanying drawing explanation
The following drawings is only intended to schematically illustrate the utility model and explain, does not limit scope of the present utility model.Wherein:
Fig. 1 is the configuration diagram of the device of single-channel type cell of the present utility model backflow continuous seepage high purity galactooligosacchari(es.
Drawing reference numeral illustrates:
1 gas control equipment 2 fermenter
3 cell settlement device 4 raw material tanks
Collector unit 6 agitator of 5 high purity galactooligosacchari(es
10 first pump 20 second pumps
30 the 3rd pump 40 the 4th pumps
50 airline 60 fermented liquid transfer lines
70 yeast reclaim transfer line 80 supernatant product transfer line
90 feedstock transportation pipelines
Embodiment
In order to have clearer understanding to the technical solution of the utility model, object and effect, existing accompanying drawings embodiment of the present utility model.
Please refer to shown in Fig. 1, it is the configuration diagram of the device of single-channel type cell of the present utility model backflow continuous seepage high purity galactooligosacchari(es.
The utility model provides the device of a kind of single-channel type cell backflow continuous seepage high purity galactooligosacchari(es, wherein, high purity galactooligosacchari(es refers to that purity is the galactooligosacchari(es of 90% ~ 100%, and the device of this single-channel type cell backflow continuous seepage high purity galactooligosacchari(es comprises gas control equipment 1, fermenter 2, cell settlement device 3, raw material tank 4, the collector unit 5 of high purity galactooligosacchari(es, agitator 6, first pump 10, second pump 20, the 3rd pump 30 and the 4th pump 40; Wherein:
Be communicated with airline 50 between gas control equipment 1 with fermenter 2, fermenter 2 is communicated with fermented liquid transfer line 60 with the top of cell settlement device 3, the bottom of cell settlement device 3 with reclaim transfer line 70 with yeast again between fermenter 2 and be communicated with, the side top of cell settlement device 3 is communicated with the collector unit 5 of high purity galactooligosacchari(es with supernatant product transfer line 80, and fermenter 2 is communicated with raw material tank 4 with feedstock transportation pipeline 90; Agitator 6 is installed in fermenter 2, namely agitator 6 is installed on the top of fermenter 2, and the stirring end of agitator 6 stretches into the inside of described fermenter 2, first pump 10 is located on feedstock transportation pipeline 90, second pump 20 is located on fermented liquid transfer line 60,3rd pump 30 is located at yeast and is reclaimed on transfer line 70, and the 4th pump 40 is located on supernatant product transfer line 80.
Single-channel type cell of the present utility model is used to reflux the device production purity of continuous seepage high purity galactooligosacchari(es when being the galactooligosacchari(es GOS-1000 of 100%, by raw material and purity be 57% GOS-570 galactooligosacchari(es or purity be 70% GOS-700 galactooligosacchari(es and yeast liquid be placed in raw material tank 4, again by the start of the first pump 10 make raw material and purity be 57% GOS-570 galactooligosacchari(es or purity be 70% GOS-700 galactooligosacchari(es and yeast liquid be transported to fermenter 2 by raw material tank 4 through feedstock transportation pipeline 90, make air send into fermenter 2 by gas control equipment 1 through airline 50 to ferment simultaneously, when the galactooligosacchari(es purity in fermenter 2 reaches 100%, by the start of the second pump 20, fermentation liquor fermented liquid transfer line 60 is delivered to cell settlement device 3 and carry out yeast sedimentation, the yeast of sedimentation makes the yeast of sedimentation reclaim transfer line 70 via yeast by the start of the 3rd pump 30 and sends fermenter 2 back to, and by the first pump 10 by raw material and purity be 57% GOS-570 galactooligosacchari(es or purity be 70% GOS-700 galactooligosacchari(es add to fermenter 2 by raw material tank 4 through feedstock transportation pipeline 90 and continue fermentation, the collector unit 5 that the supernatant product (purity is the galactooligosacchari(es GOS-1000 of 100%) of cell settlement device 3 delivers to high purity galactooligosacchari(es through the 4th pump 40 start by supernatant product transfer line 80 stores.
The foregoing is only the schematic embodiment of the utility model, and be not used to limit scope of the present utility model.Any those of ordinary skill in the art, equivalent variations done under the prerequisite not departing from design of the present utility model and principle and amendment, all should belong to the scope of the utility model protection.
Claims (1)
1. the device of a single-channel type cell backflow continuous seepage high purity galactooligosacchari(es, it is characterized in that, the device of described single-channel type cell backflow continuous seepage high purity galactooligosacchari(es comprises a gas control equipment, a fermenter, a cell settlement device, a raw material tank, the collector unit of a high purity galactooligosacchari(es, an agitator, one first pump, one second pump, one the 3rd pump and one the 4th pump, described gas control equipment is communicated with described fermenter with an airline, described fermenter is communicated to the top of described cell settlement device with fermented liquid transfer line, the bottom of described cell settlement device is reclaimed transfer line with yeast and is communicated with described fermenter, the side top of described cell settlement device is communicated with the collector unit of supernatant product transfer line with described high purity galactooligosacchari(es, described fermenter is communicated with described raw material tank with feedstock transportation pipeline, described agitator is installed in described fermenter, described first pump is located on described feedstock transportation pipeline, described second pump is located on described fermented liquid transfer line, described 3rd pump is located at described yeast and is reclaimed on transfer line, described 4th pump is located on described supernatant product transfer line.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520682201.4U CN204958929U (en) | 2015-09-02 | 2015-09-02 | Device of single -channel type cell backward flow continuous production high -purity gala oligosaccharide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520682201.4U CN204958929U (en) | 2015-09-02 | 2015-09-02 | Device of single -channel type cell backward flow continuous production high -purity gala oligosaccharide |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204958929U true CN204958929U (en) | 2016-01-13 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520682201.4U Active CN204958929U (en) | 2015-09-02 | 2015-09-02 | Device of single -channel type cell backward flow continuous production high -purity gala oligosaccharide |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204958929U (en) |
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2015
- 2015-09-02 CN CN201520682201.4U patent/CN204958929U/en active Active
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 527343, Guangdong, Yunfu Province peak double pit Bridge Industrial Zone Patentee after: Yunfu Jinshan biological Polytron Technologies Inc Address before: 527343, Guangdong, Yunfu Province peak double pit Bridge Industrial Zone Patentee before: NEW FRANCISCO (YUNFU CITY) BIOTECHNOLOGY CORPORATION |