CN205223216U - Basicity pectase preparation facilities - Google Patents
Basicity pectase preparation facilities Download PDFInfo
- Publication number
- CN205223216U CN205223216U CN201521043839.XU CN201521043839U CN205223216U CN 205223216 U CN205223216 U CN 205223216U CN 201521043839 U CN201521043839 U CN 201521043839U CN 205223216 U CN205223216 U CN 205223216U
- Authority
- CN
- China
- Prior art keywords
- flocculation
- preparation facilities
- drying tower
- cell body
- machine
- 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 - Fee Related
Links
- 238000002360 preparation method Methods 0.000 title claims abstract description 15
- 238000005189 flocculation Methods 0.000 claims abstract description 31
- 230000016615 flocculation Effects 0.000 claims abstract description 31
- 238000001694 spray drying Methods 0.000 claims abstract description 18
- 210000005056 cell body Anatomy 0.000 claims abstract description 13
- 239000012528 membrane Substances 0.000 claims abstract description 10
- 238000003756 stirring Methods 0.000 claims abstract description 10
- 239000002699 waste material Substances 0.000 claims abstract description 10
- 238000002156 mixing Methods 0.000 claims abstract description 9
- 238000007790 scraping Methods 0.000 claims abstract description 8
- 239000002893 slag Substances 0.000 claims abstract description 8
- 239000007788 liquid Substances 0.000 claims description 10
- 238000010899 nucleation Methods 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 238000004140 cleaning Methods 0.000 claims description 4
- 239000011888 foil Substances 0.000 claims description 3
- 239000005022 packaging material Substances 0.000 claims description 3
- 238000011049 filling Methods 0.000 claims description 2
- 238000000746 purification Methods 0.000 abstract description 9
- 238000000855 fermentation Methods 0.000 abstract description 7
- 230000004151 fermentation Effects 0.000 abstract description 7
- WLNBMPZUVDTASE-HXIISURNSA-N (2r,3r,4s,5r)-2-amino-3,4,5,6-tetrahydroxyhexanal;sulfuric acid Chemical compound [O-]S([O-])(=O)=O.O=C[C@H]([NH3+])[C@@H](O)[C@H](O)[C@H](O)CO.O=C[C@H]([NH3+])[C@@H](O)[C@H](O)[C@H](O)CO WLNBMPZUVDTASE-HXIISURNSA-N 0.000 abstract 3
- 239000012530 fluid Substances 0.000 abstract 1
- 238000001035 drying Methods 0.000 description 7
- 108010059820 Polygalacturonase Proteins 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 229920001277 pectin Polymers 0.000 description 3
- 235000010987 pectin Nutrition 0.000 description 3
- 239000001814 pectin Substances 0.000 description 3
- 238000011218 seed culture Methods 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- 239000002912 waste gas Substances 0.000 description 2
- FRXSZNDVFUDTIR-UHFFFAOYSA-N 6-methoxy-1,2,3,4-tetrahydroquinoline Chemical compound N1CCCC2=CC(OC)=CC=C21 FRXSZNDVFUDTIR-UHFFFAOYSA-N 0.000 description 1
- 101100298222 Caenorhabditis elegans pot-1 gene Proteins 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000604 Hydrolases Proteins 0.000 description 1
- 108010029182 Pectin lyase Proteins 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 210000002421 cell wall Anatomy 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 230000003311 flocculating effect Effects 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 239000003262 industrial enzyme Substances 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000007634 remodeling Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model provides a basicity pectase preparation facilities, including dona tub and fermentation cylinder, by the pipe connection between dona tub and the fermentation cylinder, zymotic fluid pipe -line transportation to the flocculation machine of output in the fermentation cylinder, the cell body is drawn together to the flocculation press packed bale, be equipped with the polar plate in the cell body, the polar plate top is the slot scraping transfer unit, a conveyor pulleys of slot scraping transfer unit lies in the top except that the slag chute, still be equipped with delivery port and waste discharge port on the cell body, the waste discharge port of flocculation machine is connected to the pressure filter, clear liquor from the output of flocculation machine is carried to membrane filter, concentrated clear liquor from membrane filter output advances the spray drying tower, obtain the finished product from the spray drying tower, be equipped with the stirring parts in dona tub and the fermentation cylinder, the stirring parts include the (mixing) shaft and install at the epaxial stirring leaf more than two pairs of stirring. This device has purification rate height, finished product advantage of high quality, with low costs.
Description
Technical field
The utility model relates to polysaccharide preparing technical field, especially relates to a kind of alkaline pectase preparation facilities.
Background technology
Polygalacturonase refers to can the catalysis pectin substance general name of multiple enzyme of decomposing, and the substrate specificity of pectin substance-polygalacturonase is extensively present in higher plant, is the important component of vegetable cell interstitial and primary cell wall.Polygalacturonase can be divided three classes according to the character of the reaction property or degraded substrate that decompose glycosidic link: pectin hydrolase, pectin lyase and Rohapect MPE, and polygalacturonase is divided into alkaline pectase and acid pectase by its pH value.Alkaline pectase is the polygalacturonase in alkaline range with greater activity, is a kind of very important industrial enzyme preparation.
In prior art, the preparation method of alkaline pectase is: 1) spawn culture; 2) ferment; 3) filter; 4) ultrafiltration and concentration; 5) atomization drying; 6) pack.Wherein 3) filtering is the diatomite adding 1% in the fermented liquid obtained after fermentation ends, after Homogeneous phase mixing, mixed liquor is squeezed into plate and frame(type)filter press and carries out press filter type filtration.The defect that above-mentioned technique exists is: cause the impurity rejection rates such as tropina low by diatomite in conjunction with the purification mode of pressure filter, and then affect the purity of alkaline pectase finished product.
Summary of the invention
The purpose of this utility model is to overcome the shortcoming existed in prior art, a kind of alkaline pectase preparation facilities is provided, first this device changes purification mode, become alcohol extracting into flocculation purification, decrease ethanol consumption, improve production security, secondly the structure of flocculation machine is also changed, become one-level flocculation into secondary flocculation, the technical scheme adopted is: a kind of alkaline pectase preparation facilities, comprise seeding tank and fermentor tank, connected by pipeline between described seeding tank and fermentor tank, it is characterized in that: the fermented liquid Cemented filling exported in described fermentor tank is to flocculation machine, described flocculation machine comprises cell body, pole plate is provided with in described cell body, it is slot scraping transfer unit above described pole plate, a belt pulley for feeding foil of described slot scraping transfer unit is positioned at the top except slag chute, described cell body is also provided with water outlet and waste discharge mouth, the waste discharge mouth of described flocculation machine is connected to pressure filter, the clear liquor exported from described flocculation machine is delivered to membrane filter, the concentrating clarifying liquid exported from described membrane filter enters spray-drying tower, finished product is obtained from described spray-drying tower, be provided with mixing component in described seeding tank and fermentor tank, described mixing component comprises the stir shaft paddle above with two couple be arranged on described stir shaft.
Technical characteristic of the present utility model also has: the relief outlet of described spray-drying tower is also connected to interchanger, and an outlet of described interchanger is connected with steam boiler, and the air outlet of described steam boiler is connected to the hot-wind inlet of described spray-drying tower.
Technical characteristic of the present utility model also has: described pole plate comprises one-level pole plate and secondary pole plate.
Technical characteristic of the present utility model also has: described seeding tank comprises first class seed pot and the secondary seed tank of series connection.
Technical characteristic of the present utility model also has: described preparation facilities also comprises wrapping machine, and described wrapping machine is arranged in 100,000 grades of cleaning shops, and described wrapping machine also connects interior packaging material sterilizer.
The beneficial effects of the utility model are: purification mode of 1) flocculating improves production security and purification rate, makes suitability for industrialized production alkaline pectase become possibility; 2) secondary flocculation machine carries out secondary flocculation to fermented liquid, thus improves the rejection rate of the impurity such as tropina, further increases final product quality; 3) in drying, in waste gas, waste heat recycling has energy-saving and cost-reducing advantage; 3) this device has the advantage that purification rate is high, quality of finished product good, cost are low.
Accompanying drawing explanation
Accompanying drawing 1 is the utility model structural representation, accompanying drawing 2 is flocculation machine structural representations, wherein 1 is first class seed pot, 2 is secondary seed tanks, 4 is fermentor tanks, 5 is flocculation machines, 51 is one-level pole plates, 52 is secondary pole plates, 53 is cell bodies, 54 is water outlets, 55 is scrape slag transfer unit, 56 is except slag chute, 57 is waste discharge mouths, 7 is membrane filters, 8 is spray-drying towers, 81 is heat exchanger entrances I, 82 is heat exchanger entrances II, 83 is heat exchanger exits I, 84 is heat exchanger exits II, 85 is steam boilers, 9 is wrapping machines, 10 is plate type pressure filters, 11 is sterilizers.
Embodiment
Below in conjunction with accompanying drawing, embodiment of the present utility model is described.The utility model discloses a kind of alkaline pectase production system, first this system adopts flocculence to remove the impurity such as the tropina contained in fermented liquid, and next also improves the structure of flocculation machine, and becoming one-level flocculation is secondary flocculation mode.Be specially: system comprises seed culture part, fermentation part, purification part, drying nest and the packed portion that pipeline is successively connected.
Seed culture part comprises the first class seed pot 1 and secondary seed tank 2 that are connected successively, and the bacterial classification obtained after seed culture enters fermentor tank 4 and ferments.In order to ensure mixing uniformity, in seeding tank and fermentor tank, be provided with mixing component, mixing component comprises the stir shaft paddle above with two couple be arranged on stir shaft.
Purification part comprises flocculation machine 5, flocculation machine 5 comprises cell body 53, pole plate is provided with in cell body 53, pole plate comprises one-level pole plate 51 and secondary pole plate 52, for scraping slag transfer unit 55 above pole plate, the belt pulley for feeding foil scraping slag transfer unit 55 is positioned at the top except slag chute 56, cell body 53 is also provided with water outlet 54 and waste discharge mouth 57, the waste discharge mouth 57 of flocculation machine 5 is connected to plate type pressure filter 10, fermented liquid after such fermentation first carries out one-level flocculation reaction near one-level pole plate 51, then row secondary flocculation reaction near secondary pole plate 52 is delivered to, twice flocculation can effectively improve product purity, feed liquid containing alkaline pectase after flocculation is delivered to membrane filter 7 from water outlet and carries out thickening filtration process, waste liquid containing albumen thalline etc. enters plate type pressure filter 10, filter cake is become after filter-press dehydration.
The water outlet of flocculation machine 5 is connected with membrane filter 7 entrance, and membrane filter 7 filters to remove small molecular weight impurity, inorganic salt and portion of pure water.
Drying nest comprises spray-drying tower 8, and spray-drying tower 8 is upper feeding type drying tower, and the concentrated solution after filtration treatment enters spray-drying tower 8 from top, and the hot blast of 160 DEG C enters spray-drying tower 8 from below, under hot blast effect, obtains alkaline pectase solid.The drying nest of native system also comprises interchanger and steam boiler 85, the freezing air treating preheating is passed in heat exchanger entrance II 82, the heat exchanger exit II 84 of interchanger is connected with the inlet mouth of steam boiler 85, carries out the drying of spray solidification formula after steam boiler 85 heats again, in satisfactory delivery of steam to spray-drying tower 8.Like this, first enter interchanger, carry out heat exchange process by it to freezing air by the waste gas of discharging in spray-drying tower 8, the air after heat exchange is heated to 160 DEG C that specify by steam boiler 85 again, becomes the hot blast needed for spray-drying tower 8.
Packed portion comprises wrapping machine 9, and in order to obtain purer alkaline pectase, packing shop adopts 100,000 grades of cleaning shops, and wrapping machine is arranged in this cleaning shop, and wrapping material are carried out sterilising treatment by the sterilizer 11 of interior packaging material.
Certainly; above-mentioned explanation is not limitation of the utility model; the utility model is also not limited only to above-mentioned citing, the change that those skilled in the art make in essential scope of the present utility model, remodeling, interpolation or replacement, also belongs to protection domain of the present utility model.
Claims (5)
1. an alkaline pectase preparation facilities, comprise seeding tank and fermentor tank, connected by pipeline between described seeding tank and fermentor tank, it is characterized in that: the fermented liquid Cemented filling exported in described fermentor tank is to flocculation machine, described flocculation machine comprises cell body, pole plate is provided with in described cell body, it is slot scraping transfer unit above described pole plate, a belt pulley for feeding foil of described slot scraping transfer unit is positioned at the top except slag chute, described cell body is also provided with water outlet and waste discharge mouth, the waste discharge mouth of described flocculation machine is connected to pressure filter, the clear liquor exported from described flocculation machine is delivered to membrane filter, the concentrating clarifying liquid exported from described membrane filter enters spray-drying tower, finished product is obtained from described spray-drying tower, be provided with mixing component in described seeding tank and fermentor tank, described mixing component comprises the stir shaft paddle above with two couple be arranged on described stir shaft.
2. according to alkaline pectase preparation facilities according to claim 1, it is characterized in that: the relief outlet of described spray-drying tower is also connected to interchanger, an outlet of described interchanger is connected with steam boiler, and the air outlet of described steam boiler is connected to the hot-wind inlet of described spray-drying tower.
3. according to alkaline pectase preparation facilities according to claim 1, it is characterized in that: described pole plate comprises one-level pole plate and secondary pole plate.
4. according to alkaline pectase preparation facilities according to claim 1, it is characterized in that: described seeding tank comprises first class seed pot and the secondary seed tank of series connection.
5. according to alkaline pectase preparation facilities according to claim 1, it is characterized in that: described preparation facilities also comprises wrapping machine, described wrapping machine is arranged in 100,000 grades of cleaning shops, and described wrapping machine also connects interior packaging material sterilizer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521043839.XU CN205223216U (en) | 2015-12-15 | 2015-12-15 | Basicity pectase preparation facilities |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521043839.XU CN205223216U (en) | 2015-12-15 | 2015-12-15 | Basicity pectase preparation facilities |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205223216U true CN205223216U (en) | 2016-05-11 |
Family
ID=55898293
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521043839.XU Expired - Fee Related CN205223216U (en) | 2015-12-15 | 2015-12-15 | Basicity pectase preparation facilities |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205223216U (en) |
-
2015
- 2015-12-15 CN CN201521043839.XU patent/CN205223216U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107874249A (en) | A kind of manufacture method of pectase | |
| CN103243023B (en) | Circulating synchronous straw enzymatic hydrolysis fermentation fuel ethanol reactor and reaction method thereof | |
| CN103215325A (en) | Production method of high-grade maltodextrin | |
| CN103333787A (en) | Packing tower type continuous surface fermentation apparatus and implementation method thereof | |
| CN106348562A (en) | Method for treating active sludge generated by sewage treatment and extracting protein | |
| CN110106067A (en) | A kind of complex micro organism fungicide preparation facilities and method for Discussion On Measures of Rivers Pollution Treatment | |
| CN106220521B (en) | A kind of method of full film extraction L isoleucines | |
| CN205223216U (en) | Basicity pectase preparation facilities | |
| CN202925027U (en) | Large-scale closed type primary cell preparation device | |
| CN205223200U (en) | Pullulan preparation system by decoloration | |
| CN101664141B (en) | Comprehensive utilization and production process of kudzuvine root | |
| CN205223072U (en) | Energy -saving pullulan production system | |
| CN205258449U (en) | Basicity xylanase production system | |
| CN106282248A (en) | A kind of continuous fermentation production method of sodium gluconate | |
| CN205223073U (en) | Pullulan production system | |
| CN207998567U (en) | Solid-state fermentation installation for microbial manure | |
| CN203247263U (en) | Straw synchronized enzymolysis and fermentation fuel alcohol circulation reactor | |
| CN206284303U (en) | A kind of process units of biodiasmin blackberry drink | |
| CN205223203U (en) | Dextran production system | |
| CN1155388A (en) | Method of extracting somatic protein from zymotic liquid or zymotic waste liquid | |
| CN210974619U (en) | A compound microbial inoculant preparation facilities for river pollution administers | |
| CN102776166B (en) | Production method for xylanase | |
| CN104926639A (en) | Citric acid separation method | |
| CN101434644A (en) | Novel method for efficiently extracting mycoprotein by microfiltration membrane | |
| CN214004549U (en) | Sterilization equipment is refine to medicinal coconut oil |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190117 Address after: 2600 No. 20 Dongzhen Road, Dongcheng Street, Linqu County, Weifang City, Shandong Province Patentee after: Shandong Proland Biotechnology Co.,Ltd. Address before: 2600 No. 20 Dongzhen Road, Linqu County, Weifang City, Shandong Province Patentee before: SHANDONG KANGNAXIN BIOTECHNOLOGY Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20201010 Address after: No.1 Yudong Road, Dongcheng Street, Linqu County, Weifang City, Shandong Province Patentee after: Shandong Meimei Biotechnology Co.,Ltd. Address before: 2600 No. 20 Dongzhen Road, Dongcheng Street, Linqu County, Weifang City, Shandong Province Patentee before: Shandong Proland Biotechnology Co.,Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160511 |