CN203960101U - The concentration systems of inulin liquid glucose - Google Patents
The concentration systems of inulin liquid glucose Download PDFInfo
- Publication number
- CN203960101U CN203960101U CN201420105174.XU CN201420105174U CN203960101U CN 203960101 U CN203960101 U CN 203960101U CN 201420105174 U CN201420105174 U CN 201420105174U CN 203960101 U CN203960101 U CN 203960101U
- Authority
- CN
- China
- Prior art keywords
- pump
- input terminus
- output terminal
- upgrading unit
- inulin
- 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.)
- Expired - Lifetime
Links
- JYJIGFIDKWBXDU-MNNPPOADSA-N inulin Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)OC[C@]1(OC[C@]2(OC[C@]3(OC[C@]4(OC[C@]5(OC[C@]6(OC[C@]7(OC[C@]8(OC[C@]9(OC[C@]%10(OC[C@]%11(OC[C@]%12(OC[C@]%13(OC[C@]%14(OC[C@]%15(OC[C@]%16(OC[C@]%17(OC[C@]%18(OC[C@]%19(OC[C@]%20(OC[C@]%21(OC[C@]%22(OC[C@]%23(OC[C@]%24(OC[C@]%25(OC[C@]%26(OC[C@]%27(OC[C@]%28(OC[C@]%29(OC[C@]%30(OC[C@]%31(OC[C@]%32(OC[C@]%33(OC[C@]%34(OC[C@]%35(OC[C@]%36(O[C@@H]%37[C@@H]([C@@H](O)[C@H](O)[C@@H](CO)O%37)O)[C@H]([C@H](O)[C@@H](CO)O%36)O)[C@H]([C@H](O)[C@@H](CO)O%35)O)[C@H]([C@H](O)[C@@H](CO)O%34)O)[C@H]([C@H](O)[C@@H](CO)O%33)O)[C@H]([C@H](O)[C@@H](CO)O%32)O)[C@H]([C@H](O)[C@@H](CO)O%31)O)[C@H]([C@H](O)[C@@H](CO)O%30)O)[C@H]([C@H](O)[C@@H](CO)O%29)O)[C@H]([C@H](O)[C@@H](CO)O%28)O)[C@H]([C@H](O)[C@@H](CO)O%27)O)[C@H]([C@H](O)[C@@H](CO)O%26)O)[C@H]([C@H](O)[C@@H](CO)O%25)O)[C@H]([C@H](O)[C@@H](CO)O%24)O)[C@H]([C@H](O)[C@@H](CO)O%23)O)[C@H]([C@H](O)[C@@H](CO)O%22)O)[C@H]([C@H](O)[C@@H](CO)O%21)O)[C@H]([C@H](O)[C@@H](CO)O%20)O)[C@H]([C@H](O)[C@@H](CO)O%19)O)[C@H]([C@H](O)[C@@H](CO)O%18)O)[C@H]([C@H](O)[C@@H](CO)O%17)O)[C@H]([C@H](O)[C@@H](CO)O%16)O)[C@H]([C@H](O)[C@@H](CO)O%15)O)[C@H]([C@H](O)[C@@H](CO)O%14)O)[C@H]([C@H](O)[C@@H](CO)O%13)O)[C@H]([C@H](O)[C@@H](CO)O%12)O)[C@H]([C@H](O)[C@@H](CO)O%11)O)[C@H]([C@H](O)[C@@H](CO)O%10)O)[C@H]([C@H](O)[C@@H](CO)O9)O)[C@H]([C@H](O)[C@@H](CO)O8)O)[C@H]([C@H](O)[C@@H](CO)O7)O)[C@H]([C@H](O)[C@@H](CO)O6)O)[C@H]([C@H](O)[C@@H](CO)O5)O)[C@H]([C@H](O)[C@@H](CO)O4)O)[C@H]([C@H](O)[C@@H](CO)O3)O)[C@H]([C@H](O)[C@@H](CO)O2)O)[C@@H](O)[C@H](O)[C@@H](CO)O1 JYJIGFIDKWBXDU-MNNPPOADSA-N 0.000 title claims abstract description 34
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 title claims abstract description 17
- 239000008103 glucose Substances 0.000 title claims abstract description 16
- 238000013375 chromatographic separation Methods 0.000 claims abstract description 8
- 239000012528 membrane Substances 0.000 claims description 8
- 239000000706 filtrate Substances 0.000 claims description 7
- 238000001223 reverse osmosis Methods 0.000 claims description 3
- 238000005096 rolling process Methods 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims description 2
- 229920001202 Inulin Polymers 0.000 abstract description 18
- 229940029339 inulin Drugs 0.000 abstract description 18
- 238000011084 recovery Methods 0.000 abstract description 7
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 238000007599 discharging Methods 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000007788 liquid Substances 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000000088 plastic resin Substances 0.000 description 3
- 244000298479 Cichorium intybus Species 0.000 description 2
- 235000007542 Cichorium intybus Nutrition 0.000 description 2
- 240000008892 Helianthus tuberosus Species 0.000 description 2
- 235000003230 Helianthus tuberosus Nutrition 0.000 description 2
- 239000008280 blood Substances 0.000 description 2
- 210000004369 blood Anatomy 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 150000003384 small molecules Chemical class 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 241000193830 Bacillus <bacterium> Species 0.000 description 1
- 206010010774 Constipation Diseases 0.000 description 1
- 244000115658 Dahlia pinnata Species 0.000 description 1
- 235000012040 Dahlia pinnata Nutrition 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 229930091371 Fructose Natural products 0.000 description 1
- RFSUNEUAIZKAJO-ARQDHWQXSA-N Fructose Chemical compound OC[C@H]1O[C@](O)(CO)[C@@H](O)[C@@H]1O RFSUNEUAIZKAJO-ARQDHWQXSA-N 0.000 description 1
- 239000005715 Fructose Substances 0.000 description 1
- 208000008589 Obesity Diseases 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000020824 obesity Nutrition 0.000 description 1
- 230000035790 physiological processes and functions Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- -1 water molecules Chemical class 0.000 description 1
- 230000003245 working effect Effects 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model relates to inulin production field, be specifically related to a kind of concentration systems of inulin liquid glucose, comprise batch can, the first pump and cartridge filter, the input terminus of the first described pump connects the output terminal of batch can, the first delivery side of pump connects the input terminus of cartridge filter, the output terminal of described cartridge filter connects the input terminus of upgrading unit group, described upgrading unit group at least consists of two upgrading units, the concentrated solution outlet of last step upgrading unit connects the input terminus of chromatographic separation device, the utility model adopts this continuously feeding, the operating mode of discharging, not only reduced the hot concentrated energy consumption bringing, and improved the rate of recovery of inulin, simultaneously, effectively save concentration time, enhance productivity, make system stability and high efficiency more.
Description
Technical field
The utility model relates to inulin production field, is specifically related to a kind of concentration systems of inulin liquid glucose.
Background technology
Inulin has another name called synanthrin, it is vegetable meal fiber, derive from the plants such as jerusalem artichoke, witloof Dahlia root, a kind of functional fructose, also be the most diffluent food fibre of finding at present, have and control blood fat, reduce blood sugar, promote mineral absorption, make in enteron aisle bifidus bacillus increase and the effect such as anti-constipation and treatment of obesity, due to physico-chemical property and the physiological function of inulin uniqueness, in food, beverage, healthcare products, medicine and other fields, there is widespread use.In production process, inulin extracting solution, after plastic resin treatment, still needs to slough the reducing sugar in feed liquid, the small molecules such as water molecules, the rate of recovery of raising inulin.At present, in traditional technology, be mainly to adopt hot concentration systems, inulin liquid glucose being carried out to dehydration by evaporation concentrates, and then by the dry powdery inulin that makes of spraying, while adopting this technique, power consumption is large, the process time is long, efficiency is low, and redox reaction easily occurs inulin feed liquid, causes in feed liquid the rate of recovery of inulin low.
Utility model content
The purpose of this utility model is to provide the concentration systems of a kind of less energy-consumption, high-recovery, high-level efficiency and reliable and stable inulin liquid glucose.
For realizing above object, the technical solution adopted in the utility model is: a kind of concentration systems of inulin liquid glucose, comprise batch can, the first pump and cartridge filter, the input terminus of the first described pump connects the output terminal of batch can, the first delivery side of pump connects the input terminus of cartridge filter, the output terminal of described cartridge filter connects the input terminus of upgrading unit group, described upgrading unit group at least consists of two upgrading units, and the concentrated solution outlet of last step upgrading unit connects the input terminus of chromatographic separation device.
The utility model has the advantage of: inulin extracting solution enters upgrading unit group and directly carries out multistage concentrated after plastic resin treatment, the small molecules such as reducing sugar in inulin liquid glucose, water molecules have been removed, finally through chromatographic separation device, obtaining the inulin liquid glucose that the polymerization degree meets the demands, adopt the operating mode of this continuously feeding, discharging, not only reduced the hot concentrated energy consumption bringing, and improved the rate of recovery of inulin, simultaneously, effectively save concentration time, enhance productivity, make system stability and high efficiency more.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Embodiment
A kind of concentration systems of inulin liquid glucose, comprise batch can 10, the first pump 20 and cartridge filter 30, the input terminus of the first described pump 20 connects the output terminal of batch can 10, the output terminal of the first pump 20 connects the input terminus of cartridge filter 30, the output terminal of described cartridge filter 30 connects the input terminus of upgrading unit group, described upgrading unit group at least consists of two upgrading units, and the concentrated solution outlet of last step upgrading unit connects the input terminus of chromatographic separation device 70.Principle of work of the present utility model is: inulin extracting solution in dropping into batch can 10 after plastic resin treatment, through the first pump 20, be delivered to cartridge filter 30 and carry out primary filter, to hold back Lou the resin particle crossed and larger suspended substance, guarantee the safe operation of the concentrated film unit group of postorder, the inulin leaching through cartridge filter 30 enters concentrated film unit group and directly carries out multistage concentrated, then from the concentrated solution outlet of last step upgrading unit, enter chromatographic separation device 70, obtain the inulin liquid glucose that the polymerization degree meets the demands.In actually operating, can in batch can 10, add continuously fresh inulin according to certain speed, with guarantee serialization concentration technology continue carry out.Compared with prior art, the utility model adopts the operating mode of continuously feeding, discharging, feed liquid reaches constant temperature, concentrated effect simultaneously, reduced the hot concentrated energy consumption bringing, effectively saved concentration time, enhanced productivity, simultaneously, for serialization liquid glucose concentration systems, supplied with stable charging, the pollution of inulin to membrane module while having alleviated work, has effectively improved stability and the reliability of system operation.
As preferred version: as shown in Figure 1, described upgrading unit group comprises elementary upgrading unit 40, secondary upgrading unit 50 and three grades of upgrading units 60, elementary upgrading unit 40 comprises the second pump 41 and elementary concentrated film device 42, secondary upgrading unit 50 comprises the 3rd pump 51 and the concentrated film device 52 of secondary, three grades of upgrading units 60 comprise the 4th pump 61 and three grades of concentrated film devices 62, the input terminus of the second described pump 41 is connected with the output terminal of cartridge filter 30, the output terminal of the second pump 41 is connected with the input terminus of elementary concentrated film device 42, the input terminus of the 3rd described pump 51 is connected with the elementary concentrated solution output terminal 421 of elementary concentrated film device 42, the output terminal of the 3rd pump 51 is connected with the input terminus of the concentrated film device 52 of secondary, the input terminus of the 4th described pump 61 is connected with the secondary concentrated solution output terminal 521 of the concentrated film device 52 of secondary, the output terminal of the 4th pump 61 is connected with the input terminus of three grades of concentrated film devices 62, three grades of concentrated solution output terminals 621 of three grades of described concentrated film devices 62 are connected with chromatographic separation device 70 input terminuss, that is to say at each upgrading unit and comprise pump and concentrated film device, delivery side of pump is connected with the input terminus of concentrated film device, while making inulin enter concentrated film device, there is certain pressure, guarantee the concentrated speed of inulin and the steady running of concentration systems.
Further, the filtrate output terminal 622 of three described upgrading units leads to collection processing system implementing, as shown in Figure 1, elementary filtrate, secondary filtrate and three grades flow to same pipeline filtrate collecting, facilitate like this centralized recovery of filtrate to use, improve process efficiency, the filtrate of recovery can be for cleaning witloof or Jerusalem artichoke raw material.
Further, the filtering accuracy of described cartridge filter 30 is 50～100 μ m, suspended particle in feed liquid, colloid, microorganism etc. can be trapped in the cartridge surface and hole of cartridge filter 30 like this, for the steady running of postorder upgrading unit group is given security, avoid the membrane element in upgrading unit group to stop up simultaneously, be conducive to extend the work-ing life of membrane element.
Further, the reverse osmosis membrane that the membrane element in described upgrading unit group is rolling, the reverse osmosis membrane of rolling is directly bought on market, convenient realization.
Claims (5)
1. the concentration systems of an inulin liquid glucose, it is characterized in that: comprise batch can (10), the first pump (20) and cartridge filter (30), the input terminus of described the first pump (20) connects the output terminal of batch can (10), the output terminal of the first pump (20) connects the input terminus of cartridge filter (30), the output terminal of described cartridge filter (30) connects the input terminus of upgrading unit group, described upgrading unit group at least consists of two upgrading units, and the concentrated solution outlet of last step upgrading unit connects the input terminus of chromatographic separation device (70).
2. the concentration systems of inulin liquid glucose according to claim 1, it is characterized in that: described upgrading unit group comprises elementary upgrading unit (40), secondary upgrading unit (50) and three grades of upgrading units (60), elementary upgrading unit (40) comprises the second pump (41) and elementary concentrated film device (42), secondary upgrading unit (50) comprises the 3rd pump (51) and the concentrated film device (52) of secondary, three grades of upgrading units (60) comprise the 4th pump (61) and three grades of concentrated film devices (62), the input terminus of described the second pump (41) is connected with the output terminal of cartridge filter (30), the output terminal of the second pump (41) is connected with the input terminus of elementary concentrated film device (42), the input terminus of the 3rd described pump (51) is connected with the elementary concentrated solution output terminal (421) of elementary concentrated film device (42), the output terminal of the 3rd pump (51) is connected with the input terminus of the concentrated film device (52) of secondary, the input terminus of the 4th described pump (61) is connected with the secondary concentrated solution output terminal (521) of the concentrated film device (52) of secondary, the output terminal of the 4th pump (61) is connected with the input terminus of three grades of concentrated film devices (62), three grades of concentrated solution output terminals (621) of described three grades of concentrated film devices (62) are connected with chromatographic separation device (70) input terminus.
3. the concentration systems of inulin liquid glucose according to claim 2, is characterized in that: the filtrate output terminal (622) of three described upgrading units leads to collection processing system implementing.
4. the concentration systems of inulin liquid glucose according to claim 1 and 2, is characterized in that: the filtering accuracy of described cartridge filter (30) is 50～100 μ m.
5. the concentration systems of inulin liquid glucose according to claim 1 and 2, is characterized in that: the reverse osmosis membrane that the membrane element in described upgrading unit group is rolling.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420105174.XU CN203960101U (en) | 2014-03-07 | 2014-03-07 | The concentration systems of inulin liquid glucose |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420105174.XU CN203960101U (en) | 2014-03-07 | 2014-03-07 | The concentration systems of inulin liquid glucose |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203960101U true CN203960101U (en) | 2014-11-26 |
Family
ID=51920710
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420105174.XU Expired - Lifetime CN203960101U (en) | 2014-03-07 | 2014-03-07 | The concentration systems of inulin liquid glucose |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203960101U (en) |
-
2014
- 2014-03-07 CN CN201420105174.XU patent/CN203960101U/en not_active Expired - Lifetime
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20141126 |
|
| CX01 | Expiry of patent term |