CN101791593A - Horizontal screw centrifugal machine for solid-liquid separation of pectin and use method thereof - Google Patents
Horizontal screw centrifugal machine for solid-liquid separation of pectin and use method thereof Download PDFInfo
- Publication number
- CN101791593A CN101791593A CN201010120737A CN201010120737A CN101791593A CN 101791593 A CN101791593 A CN 101791593A CN 201010120737 A CN201010120737 A CN 201010120737A CN 201010120737 A CN201010120737 A CN 201010120737A CN 101791593 A CN101791593 A CN 101791593A
- Authority
- CN
- China
- Prior art keywords
- pectin
- horizontal screw
- rotary drum
- solid
- screw centrifuge
- 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.)
- Granted
Links
- 229920001277 pectin Polymers 0.000 title claims abstract description 56
- 235000010987 pectin Nutrition 0.000 title claims abstract description 56
- 239000001814 pectin Substances 0.000 title claims abstract description 56
- 239000007788 liquid Substances 0.000 title claims abstract description 43
- 238000000926 separation method Methods 0.000 title claims abstract description 27
- 238000000034 method Methods 0.000 title claims abstract description 13
- 239000007787 solid Substances 0.000 claims abstract description 12
- 238000001035 drying Methods 0.000 claims abstract description 5
- 239000002893 slag Substances 0.000 claims description 13
- 230000001376 precipitating effect Effects 0.000 claims description 11
- 239000000284 extract Substances 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 6
- 230000001476 alcoholic effect Effects 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 5
- RFSUNEUAIZKAJO-ARQDHWQXSA-N Fructose Chemical compound OC[C@H]1O[C@](O)(CO)[C@@H](O)[C@@H]1O RFSUNEUAIZKAJO-ARQDHWQXSA-N 0.000 claims description 3
- 229930091371 Fructose Natural products 0.000 claims description 3
- 239000005715 Fructose Substances 0.000 claims description 3
- 239000012141 concentrate Substances 0.000 claims description 3
- 238000000605 extraction Methods 0.000 claims description 3
- 238000010298 pulverizing process Methods 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 10
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 238000004140 cleaning Methods 0.000 abstract description 3
- KEQXNNJHMWSZHK-UHFFFAOYSA-L 1,3,2,4$l^{2}-dioxathiaplumbetane 2,2-dioxide Chemical compound [Pb+2].[O-]S([O-])(=O)=O KEQXNNJHMWSZHK-UHFFFAOYSA-L 0.000 abstract 1
- 239000004744 fabric Substances 0.000 description 9
- 239000000047 product Substances 0.000 description 8
- 239000000463 material Substances 0.000 description 6
- 239000000725 suspension Substances 0.000 description 5
- 239000013049 sediment Substances 0.000 description 4
- 239000007790 solid phase Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 230000007246 mechanism Effects 0.000 description 3
- 238000004062 sedimentation Methods 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000005352 clarification Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 239000012065 filter cake Substances 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000005457 optimization Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000010178 pectin extract Substances 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 1
- 206010053615 Thermal burn Diseases 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 210000000170 cell membrane Anatomy 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N ferric oxide Chemical compound O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 150000004676 glycans Polymers 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 150000004804 polysaccharides Polymers 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 230000007480 spreading Effects 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Landscapes
- Centrifugal Separators (AREA)
Abstract
The invention belongs to the field of centrifugal machines, in particular to a horizontal screw centrifugal machine for the solid-liquid separation of pectin and a use method thereof. The horizontal screw centrifugal machine comprises a drum, wherein the internal diameter of the bigger end of the drum is 220-430 mm, the length of the drum is 1100-1550 mm, the diameter of the feeding hole of the drum is 40-50mm, and the screw pitch gradient is 8-13 degrees. By adopting the horizontal screw centrifugal machine to carry out pectin separation, firstly, the production cost can be saved, and the labor intensity of workers can be reduced; secondly, the separation effect can be improved, and the effective yield of the pectin can be improved; and thirdly, the separation equipment, the sanitary environment and the cleaning standard all reach the national sanitary standard. In the invention, the pectin obtained by separation has light milk-white appearance, higher effective component content of solid and very obvious solid-liquid separation effect. The moisture content of the separated pectin is about 40 percent, which is convenient for drying in the next step. In addition, the content of the pectin which is taken away is very low so that the wastage is little.
Description
[technical field]
The invention belongs to the centrifuge field, more particularly, is a kind of horizontal screw centrifuge and using method that is used for the pectin Separation of Solid and Liquid.
[background technology]
Pectous extracting method at first is the pectin extraction: pomace is immersed pH value 1-3, temperature 25-100 ℃, react 30min-5h in the deionized water solution of 10-20 umber, make the pectin stripping that is present in pomace cell membrane intermediate layer, carry out Separation of Solid and Liquid by solid-liquid separating equipment then, pectin and pomace are separated, entered into next link again.
Solid-liquid separating equipment commonly used has tripod pendulum type batch centrifugal and plate and frame filter press.Tripod pendulum type batch centrifugal is equivalent to washing machine, at first will be with the open and flat centrifugal basket of spreading out of cotton system/chemical fibre filter bag of certain tolerable temperature and footpath weft density, squeeze into pectin slag liquid mixture material with slush pump then, starter motor, under the action of the centrifugal, liquid sees through filter bag cloth eye and the rotating cylinder mesh throws away, and the solid matter pomace then combines in the filter bag that is attached on the wall of limit.Tripod pendulum type batch centrifugal, its rotating cylinder diameter is big more, and charge is also many more, but rotating speed is low more. and industrial production generally adopts diameter 800/1000/1200mm, and their rotating speed is respectively 1200/1000/800r/min, about the about 200L of maximum volume.
Plate and frame filter press is filtered the dregs of a decoction with cloth after being similar to and having fried in shallow oil Chinese medicine, its operation principle is by the pressure of screw pump slag liquid water slurry to be filtered successively to be squeezed into filter chamber between the deckle board, the filter cloth that makes clear liquid see through deckle board two side suspensions with the pressure of screw pump flows out from deckle board fovea superior projection mortise, treat that chamber is full of stability hydraulic when 6-7kg left and right sides certain hour leaches the clear liquid flow simultaneously and reduces to a certain degree, hydraulic pressure release-close down material pump-return top board-draw back deckle board shake filter cloth filter cake to come off.
Tripod pendulum type batch centrifugal because separate and discharging longer when accounting for, change operation so factory once must drop into the number chaptrel; Filter bag also will in time clean replacement simultaneously, and cleaning filter cloth incessantly also needs industry washer to finish certainly; Be exactly that the little needs of batch processed amount frequently load and unload filter bag in addition, the one, enterprises using the labor many two is that labour intensity is big; Even in the process of so artificial replacing filter bag, often contact high-temperature material employee's scald accident still may take place unless you give your whole attention to it.
Pectin production uses plate and frame filter press to have following problem: one, the deckle board cavity volume is limited, one produce per year 50 tons the pectin line only washery slag extract workshop section, plate width of cloth 600*600/800*800/1000*1000mm, 60-80 square of deckle board filter press quantity is at least more than 4, and filter cake is collected and need be built 120m for convenience simultaneously
2* 1. the 5m platform takes up an area of many 2. investments greatly; Two, pectin solidliquid mixture viscosity is big, and the filter cloth regeneration difficulty is except that needs allied industry washing machine, and cleaning filter cloth 1. is that 2. the increasing of water consumption can cause secondary pollution.Three, chamber cloth and pressurize are filtered consuming time longer, 1. filtrate contacts with air for a long time, and the easy oxidation of aldehydes matter produces brown stain, and the gloomy commodity color of pectin outward appearance is very grave, 2. overtime reaction disconnects the macromolecule polysaccharide side chain, badly influences important quality index such as the gel degree of product and viscosity.
[summary of the invention]
Technical problem to be solved by this invention is horizontal screw centrifuge is applied in the pectous extracting method, a kind of horizontal screw centrifuge that is used for the pectin Separation of Solid and Liquid is provided, compare with existing equipment, can increase separating effect, improve the pectin slag liquid separating method of the effective yield of pectin, save production cost, reduce working strength of workers.
The present invention solves the problems of the technologies described above by the following technical programs: a kind of horizontal screw centrifuge that is used for the pectin Separation of Solid and Liquid, described horizontal screw centrifuge comprises rotary drum, it is characterized in that the big end interior diameter of described rotary drum is 220～430mm, described rotary drum length is 1100～1550mm, described rotary drum charging aperture diameter is 40～50mm, and the pitch gradient is 8～13 °.
The using method of described horizontal screw centrifuge may further comprise the steps:
A. the slag liquid separation phase that extracts of pectin: get 1: 20 pectin stoste of solid-liquid ratio with the big end interior diameter of rotary drum 430mm, length 1400mm, rotary drum charging aperture diameter 50mm, the horizontal screw centrifuge that the pitch gradient is 10～13 ° separates 20min under the 4200-4500r/min rotating speed;
B. the extraction stages extracted of pectin: will use the horizontal screw centrifuge identical under the 2500-2700r/min rotating speed, to separate 60min through the thick product of pectin of slag liquid separation with step a;
C. pectin precipitating stage of extracting: the alcohol that in through the thick product of pectin that concentrates, adds a certain amount of 95% concentration, stir after adding an amount of hydrochloric acid then, make its PH at 3.5-4.0, the limit adds an amount of fructose concentrating liquid limit stirring then, the alcoholic strength that makes mixed liquor is about 60%, solid-liquid ratio reaches 1: 1.5, again with the big end interior diameter of rotary drum 220mm, length 1100mm, rotary drum charging aperture diameter 40mm, the horizontal screw centrifuge that the pitch gradient is 8～11 ° separates 10min under the 3500-3900r/min rotating speed;
D. the rinse stage that extracts of pectin: the alcohol that adds a certain amount of 95% concentration at the thick product of pectin through precipitating, add the pectin for the treatment of rinsing then while stirring, the alcoholic strength of mixed liquor is reached about 65%, solid-liquid ratio reaches 1: 1.1, under the 4000-4200r/min rotating speed, separate 10min with the horizontal screw centrifuge identical with step c, through drying, pulverizing, sieve, mix, promptly obtain the pectin finished product again.
Principle of the present invention is: horizontal screw centrifuge is the density contrast that relies on the solid-liquid two-phase, and under action of centrifugal force, the sinking speed of accelerating solid phase particles realizes Separation of Solid and Liquid.Because the sedimentation of suspension, the conveying of sediment and dehydration are all finished in rotary drum.Therefore the rotary drum parts are critical pieces of horizontal screw centrifuge.The structure of rotary drum, material, shape and parameter have determined the characteristics and the technological effect of centrifuge to a great extent.Not only be related to the safety of structure problem of centrifuge, but also be related to sediment conveying, the separating effect of centrifuge.The seriation of centrifuge is that the maximum inner diameter with rotary drum is that major parameter is formulated.Along with the raising of centrifuge unit production capacity, its design is just higher towards rotating speed, and the direction that diameter is bigger develops.The ess-strain problem of drum structure is more outstanding.Under the preceding topic that solves the ess-strain problem, the rotary drum group is carried out Analysis of Parameters and optimization, improve the separating effect of centrifuge, alleviate quality, reduce cost concerning horizontal screw centrifuge, have the important project practical significance.Adopt existing tripod pendulum type batch centrifugal to carry out pectin with the deckle board filter press and separate the pectin Separation of Solid and Liquid, backward in technique, technology imperfection, separation equipment are unhygienic, and environmental index does not reach the sanitation and hygiene standard; And take the horizontal screw centrifuge isolation technics, one can save production cost, and reduces labor strength; Two can increase separating effect, improve the effective yield of pectin; Three separation equipments, hygienic conditions and cleanliness standard reach state health standards.
The invention has the advantages that: centrifuge parameters of the present invention is through experiment repeatedly, the preferred plan that obtains after the optimization, adopt described horizontal screw centrifuge, the pectin outward appearance that separation is obtained is light ecru, the solid active constituent content is higher, the effect of Separation of Solid and Liquid is very obvious, and isolated pectin water content is about 40%, is convenient to next step bake drying; The content of the pectin of taking away simultaneously is very low, and loss is few.
[description of drawings]
The invention will be further described in conjunction with the embodiments with reference to the accompanying drawings.
Fig. 1 is the process for producing pectin flow chart.
[specific embodiment]
Referring to subordinate list one, horizontal screw centrifuge of the present invention is made up of parts such as rotary drum, auger conveyor, differential mechanism, base bearing, underframe, liquid-solid phase collecting chamber, loam cake, transmission gear for electric motor, frequency converters.The big end interior diameter of described rotary drum is 220～430mm, and described rotary drum length is 1100～1550mm, and described rotary drum charging aperture diameter is 40～50mm, and the pitch gradient is 8～13 °.Rotary drum pattern: cylinder-pyramid type, spiral pattern: single head, left-handed, leading, cone angle: 2 * 8 °, rotary drum rotating speed: 0～4500r/min is stepless adjustable, maximum separation factor: 2678g, rotary drum and spiral difference rotating speed: frequency conversion, stepless adjustable, 6 grades of overflow plate diameter: φ 199～φ 217 minutes are adjustable, disposal ability: in suspension, 2～10m/h is because the material performance difference, under the same conditions, disposal ability can have bigger difference, power of motor: 15kw. complete machine weight: about 1900kg, appearance and size: 2790 * 1300 * 950mm (length * wide * height).
The operation principle of this machine is: the spiral shell that crouches passes through progressively raising speed of frequency converter, and under the drive of primary and secondary belt wheel, the power shaft of rotary drum and differential mechanism reaches rated speed n
1, n
2, owing to the effect of differential mechanism, make the stable poor rotating speed Δ n of a leading rotary drum of spiral generation, to realize the screw unloading function; The design of rotary drum the place ahead has an awl section, according to the difference of material properties, rotates at a high speed according to the speed of setting.Machine rotational speed is stablized rear suspension liquid by head tank or feed pump, flow control valve, feed pipe enters centrifuge, quicken bucket through spiral and quicken to advance in the rotary drum again, under powerful effect of centrifugal force, heavy solid phase particles is got rid of on the sedimentation wall, and deposit to very soon on the inwall of rotary drum, through the promotion of spiral, sediment constantly is pushed to the rotary drum small end, collects case from slag notch through solid phase and discharges.Further clarification is by the rotary drum spout hole through separate blade for clear liquid after the separation, and liquid phase is collected case and discharged.Suspension is constantly imported in whole separation process, and the liquid phase and the sediment of clarification are constantly discharged, and therefore is to separate automatically continuously.
Referring to Fig. 1, extract the stages such as pectin generally comprises raw material processings, the separation of slag liquid, precipitating, smart filter, concentrated, precipitating, rinsing, oven dry, pulverizes, sieves, mixing, below be the embodiment of the application of described horizontal screw centrifuge in pectous extracting method:
Pectin precipitating: the alcohol that in through the thick product of pectin that concentrates, adds a certain amount of 95% concentration, stir after adding an amount of hydrochloric acid then, make its PH at 3.5-4.0, the limit adds an amount of fructose concentrating liquid limit stirring then, the alcoholic strength that makes mixed liquor is about 60%, solid-liquid ratio reaches 1: 1.5, use the big end interior diameter of described rotary drum 220mm then, length 1100mm, described rotary drum charging aperture diameter 40mm, the horizontal screw centrifuge that the pitch gradient is 8～11 ° separates 10min under the 3500-3900r/min rotating speed.
Pectin rinsing: the alcohol that adds a certain amount of 95% concentration at the thick product of pectin through precipitating, add the pectin for the treatment of rinsing then while stirring, the alcoholic strength of mixed liquor is reached about 65%, solid-liquid ratio reaches 1: 1.1, under the 4000-4200r/min rotating speed, separate 10min with identical horizontal screw centrifuge then, through drying, pulverizing, sieve, mix, promptly obtain the pectin finished product again.Detail parameters is referring to subordinate list two.
Although illustrated and described embodiments of the invention, for the ordinary skill in the art, be appreciated that without departing from the principles and spirit of the present invention and can carry out multiple variation, modification, replacement and modification to these embodiment, scope of the present invention is limited by claims and equivalent thereof.
Table one: be used for the horizontal screw centrifuge parameter that pectin extracts:
| Slag liquid separates | Extract | Precipitating | Rinsing | |
| Roller diameter (mm) | ??430 | ??430 | ??220 | ??220 |
| Rotary drum length (mm) | ??1400 | ??1400 | ??1100 | ??1100mm |
| Rotating speed r/min | ??4200-4500 | ??2500-2700 | ??3500-3900 | ??4000-4200 |
| Slag liquid separates | Extract | Precipitating | Rinsing | |
| Charging aperture diameter mm | ??50 | ??50 | ??40 | ??40 |
| Outlet pitch gradient | ??10-13 | ??10-13 | ??8-11 | ??8-11 |
Table two: be used for the horizontal screw centrifuge operational factor that pectin extracts:
| Slag liquid separates | Extract | Precipitating | Rinsing | |
| Time min | ??20 | ??60 | ??10 | ??10 |
| Total treating capacity | ??2.6t | ??2.6t | ??325kg | ??120kg |
| Solid-liquid ratio | ??1∶20 | ??1∶20 | ??1∶1.5 | ??1∶1.1 |
| Unit treating capacity kg/h | ??5000-4000 | ??2600-4000 | ??1200-1500 | ??1500-1800 |
Claims (2)
1. horizontal screw centrifuge that is used for the pectin Separation of Solid and Liquid, described horizontal screw centrifuge comprises rotary drum, it is characterized in that the big end interior diameter of described rotary drum is 220～430mm, and described rotary drum length is 1100～1550mm, described rotary drum charging aperture diameter is 40～50mm, and the pitch gradient is 8～13 °.
2. the using method of the described horizontal screw centrifuge of claim 1 is characterized in that being may further comprise the steps:
A. the slag liquid separation phase that extracts of pectin: get 1: 20 pectin stoste of solid-liquid ratio with the big end interior diameter of rotary drum 430mm, length 1400mm, rotary drum charging aperture diameter 50mm, the horizontal screw centrifuge that the pitch gradient is 10～13 ° separates 20min under the 4200-4500r/min rotating speed;
B. the extraction stages extracted of pectin: will use the horizontal screw centrifuge identical under the 2500-2700r/min rotating speed, to separate 60min through the thick product of pectin of slag liquid separation with step a;
C. pectin precipitating stage of extracting: the alcohol that in through the thick product of pectin that concentrates, adds a certain amount of 95% concentration, stir after adding an amount of hydrochloric acid then, make its PH at 3.5-4.0, the limit adds an amount of fructose concentrating liquid limit stirring then, the alcoholic strength that makes mixed liquor is about 60%, solid-liquid ratio reaches 1: 1.5, again with the big end interior diameter of rotary drum 220mm, length 1100mm, rotary drum charging aperture diameter 40mm, the horizontal screw centrifuge that the pitch gradient is 8～11 ° separates 10min under the 3500-3900r/min rotating speed;
D. the rinse stage that extracts of pectin: the alcohol that adds a certain amount of 95% concentration at the thick product of pectin through precipitating, add the pectin for the treatment of rinsing then while stirring, the alcoholic strength of mixed liquor is reached about 65%, solid-liquid ratio reaches 1: 1.1, under the 4000-4200r/min rotating speed, separate 10min with the horizontal screw centrifuge identical with step c, through drying, pulverizing, sieve, mix, promptly obtain the pectin finished product again.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010120737 CN101791593B (en) | 2010-03-10 | 2010-03-10 | Use method of horizontal screw centrifugal machine for solid-liquid separation of pectin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010120737 CN101791593B (en) | 2010-03-10 | 2010-03-10 | Use method of horizontal screw centrifugal machine for solid-liquid separation of pectin |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101791593A true CN101791593A (en) | 2010-08-04 |
| CN101791593B CN101791593B (en) | 2013-05-29 |
Family
ID=42584639
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201010120737 Active CN101791593B (en) | 2010-03-10 | 2010-03-10 | Use method of horizontal screw centrifugal machine for solid-liquid separation of pectin |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101791593B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102286111A (en) * | 2011-07-06 | 2011-12-21 | 砀山宇宁生物科技有限公司 | Novel process for extracting pectin from pear skin at normal temperature |
| WO2019043035A1 (en) * | 2017-08-31 | 2019-03-07 | Südzucker AG | Method for reducing the sugar loss in the removal of a coagulate from pre-liming juice and for thickening the coagulate, use of a decanter centrifuge, fraction containing protein, and sugar beet pre-liming juice |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1100899A (en) * | 1993-09-28 | 1995-04-05 | 邵梦欣 | Method for continuously extracting fruit juice-fruit pectin-edible fiber |
| CN1526738A (en) * | 2003-09-23 | 2004-09-08 | 武汉化工学院 | Method of preparing pectin with orange peel |
| US20070254795A1 (en) * | 2006-04-26 | 2007-11-01 | Hutchison Hayes L.P. | Liner For a Centrifuge Discharge Port |
-
2010
- 2010-03-10 CN CN 201010120737 patent/CN101791593B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1100899A (en) * | 1993-09-28 | 1995-04-05 | 邵梦欣 | Method for continuously extracting fruit juice-fruit pectin-edible fiber |
| CN1526738A (en) * | 2003-09-23 | 2004-09-08 | 武汉化工学院 | Method of preparing pectin with orange peel |
| US20070254795A1 (en) * | 2006-04-26 | 2007-11-01 | Hutchison Hayes L.P. | Liner For a Centrifuge Discharge Port |
Non-Patent Citations (2)
| Title |
|---|
| 全国化工设备设计技术中心站机泵技术委员会: "《工业离心机选用手册》", 31 March 1999, 化学工业出版社 * |
| 单杨: "《柑橘加工概论》", 30 November 2004, 中国农业出版社 * |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102286111A (en) * | 2011-07-06 | 2011-12-21 | 砀山宇宁生物科技有限公司 | Novel process for extracting pectin from pear skin at normal temperature |
| CN102286111B (en) * | 2011-07-06 | 2014-02-05 | 砀山宇宁生物科技有限公司 | Process for extracting pectin from pear skin at normal temperature |
| WO2019043035A1 (en) * | 2017-08-31 | 2019-03-07 | Südzucker AG | Method for reducing the sugar loss in the removal of a coagulate from pre-liming juice and for thickening the coagulate, use of a decanter centrifuge, fraction containing protein, and sugar beet pre-liming juice |
| JP2020531035A (en) * | 2017-08-31 | 2020-11-05 | ズートツッカー アーゲー | How to reduce sugar loss when separating coagulum from pre-lime treated juice, and how to concentrate coagulated product, use decanter centrifuge, protein-containing fraction and pre-lime treated beet juice |
| US11702710B2 (en) | 2017-08-31 | 2023-07-18 | Sudzucker Ag | Method for reducing the sugar loss in the removal of a coagulate from pre-liming juice and for thickening the coagulate, use of a decanter centrifuge, fraction containing protein, and sugar beet pre-liming juice |
| JP7374080B2 (en) | 2017-08-31 | 2023-11-06 | ズートツッカー アーゲー | Method for reducing sugar loss during separation of coagulum from prelimed juice, as well as method for thickening coagulum, use of decanter centrifuges, protein-containing fractions and prelimed beet juice |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101791593B (en) | 2013-05-29 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US11603507B2 (en) | Methods for producing a high protein corn meal from a whole stillage byproduct and system therefore | |
| CN102071092B (en) | Method for recovering and recycling silicon slice cutting waste mortar | |
| CN108002599B (en) | Solid-liquid separation method and device for multi-material anaerobic fermentation liquid containing kitchen waste | |
| EP0520172A1 (en) | Treatment of waste and waste-like mixtures, particularly of source separated organic waste, the wet waste and the commercial waste for anaerobic digestion of contained biogenic-organic substances | |
| CN102149440A (en) | Apparatus and method for filtering a material from a liquid medium | |
| CN114748889B (en) | Continuous countercurrent extraction desolventizing system and process | |
| CN101791593B (en) | Use method of horizontal screw centrifugal machine for solid-liquid separation of pectin | |
| CN103497777A (en) | Heavy oil and bitumen extraction and separation method from coal-based oil residue | |
| CN111171163B (en) | Potato starch production line and production method thereof | |
| CN210506034U (en) | Continuous deep dehydration equipment with drying function | |
| CN206828868U (en) | A kind of combination unit for separating cellulose, lignin and carbohydrate | |
| CN208008594U (en) | A kind of more material anaerobic fermented liquid equipment for separating liquid from solid containing kitchen garbage | |
| CN108015099A (en) | Kitchen waste preprocessing technology and system based on two-stage extrusion technique | |
| CN212417124U (en) | Salt mud resource utilization processing system | |
| US1826987A (en) | Method of producing olive oil | |
| CN110558584A (en) | Multifunctional mustard processing equipment | |
| CN88101120A (en) | Processed fruit and method for vegetable are particularly produced the method for juice and are implemented the equipment of this method | |
| CN102618338B (en) | Technology and apparatus for producing slurry and solid fuel from garbage and biomasses | |
| CN213965259U (en) | Citrus peel progressive extraction device | |
| CN202989034U (en) | Continuous dehydration device in production of high-molecular polymer | |
| CN220639006U (en) | Novel spiral extrusion dewatering equipment | |
| CN217757306U (en) | Flour slurry separating and refining device | |
| CN107814828A (en) | The unconventional extractive technique of hydrolysate | |
| CN212057963U (en) | Rotational flow energy-saving extrusion dehydrator | |
| CN219848477U (en) | Slag dragging machine with slag pressing and leaching structure for ethanol raw material processing |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: ANHUI YUNING BIOLOGICAL TECHNOLOGY CO., LTD. Free format text: FORMER NAME: DANGSHAN YUNING BIOLOGICAL TECHNOLOGY CO., LTD. |
|
| CP01 | Change in the name or title of a patent holder |
Address after: The 235323 Anhui city of Suzhou province Dangshan County Guan Di Miao Zhen chic company Patentee after: ANHUI YUNING BIO-TECHNOLOGY Co.,Ltd. Address before: The 235323 Anhui city of Suzhou province Dangshan County Guan Di Miao Zhen chic company Patentee before: Dangshan Yuning Bio-Technology Co.,Ltd. |
|
| CP01 | Change in the name or title of a patent holder |
Address after: The 235323 Anhui city of Suzhou province Dangshan County Guan Di Miao Zhen chic company Patentee after: ANHUI YUNING PECTIN CO.,LTD. Address before: The 235323 Anhui city of Suzhou province Dangshan County Guan Di Miao Zhen chic company Patentee before: ANHUI YUNING BIO-TECHNOLOGY Co.,Ltd. |
|
| CP01 | Change in the name or title of a patent holder | ||
| 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 invention: Use method of horizontal screw centrifugal machine for solid-liquid separation of pectin Effective date of registration: 20170418 Granted publication date: 20130529 Pledgee: Suzhou SME financing Company limited by guarantee Pledgor: ANHUI YUNING PECTIN CO.,LTD. Registration number: 2017340000050 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20171204 Granted publication date: 20130529 Pledgee: Suzhou SME financing Company limited by guarantee Pledgor: ANHUI YUNING PECTIN CO.,LTD. Registration number: 2017340000050 |
|
| 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 invention: Use method of horizontal screw centrifugal machine for solid-liquid separation of pectin Effective date of registration: 20171227 Granted publication date: 20130529 Pledgee: Suzhou SME financing Company limited by guarantee Pledgor: ANHUI YUNING PECTIN CO.,LTD. Registration number: 2017340000486 |
|
| PP01 | Preservation of patent right | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20240508 Granted publication date: 20130529 |