CN208465363U - A kind of membranous system device of high magnification numbe concentration pectin - Google Patents
A kind of membranous system device of high magnification numbe concentration pectin Download PDFInfo
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- CN208465363U CN208465363U CN201820810826.8U CN201820810826U CN208465363U CN 208465363 U CN208465363 U CN 208465363U CN 201820810826 U CN201820810826 U CN 201820810826U CN 208465363 U CN208465363 U CN 208465363U
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- China
- Prior art keywords
- membranous system
- filter
- pectin
- filtration membrane
- membrane
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Abstract
The utility model provides a kind of membranous system device of high magnification numbe concentration pectin, including primary filter membranous system and ultimate filtration membrane systems, and the primary filter membranous system includes tank body, liquid material entrance, cylindrical ceramic membrane filter, waste liquid outlet and liquid material outlet；The ultimate filtration membrane systems include: motor, outer housing, inner chamber body, feeding inlet and discharge port；User of service is by the way that crude pectin solution is added into device, device for opening, adjust the revolving speed of machine in ultimate filtration membrane systems, crude pectin solution is allowed to obtain high purity pectin after primary filter membranous system and ultimate filtration membrane systems, utility model device has many advantages, such as that easy to operate, high-efficient, product purity is high.
Description
Technical field
The utility model relates to pectin processing equipment technical fields, and in particular to a kind of membranous system of high magnification numbe concentration pectin
Device.
Background technique
Pectin substance is one of plant cell wall component, is present in the intercellular layer between flanking cell wall, is played cell
Coherent effect.Different vegetables, fruit mouthfeel are had any different, the pectin content and pectin point mainly contained by them
What the difference of son determined.Pectin is a kind of natural polymer, has good gelatine and stable emulsifying effect, extensively
It is general to be used for food, medicine, daily use chemicals and textile industry.
Since impurity content is more in the pectin of extraction, concentration is low to be generally required for extract refining to be concentrated.Simultaneously as hot
In concentration process, no dedoping step, therefore will cause the impurity in extracting solution, especially small molecular weight impurity and inorganic salt content increase
Height, and then influence the quality of product.Mostly use membrane separation process greatly now to purify pectin, membrane separation concentration purification technique is one
The kind other filtering of molecular level can select suitable separation pore size grades according to specific requirement, achieve the purpose that separation, impurity removal.It is solely
Special cross-flow filtration mode can effectively prevent film blocking pollution, prolong the service life, and reduce operating cost.
Utility model content
(1) the technical issues of solving
In view of the deficiencies of the prior art, the utility model provides a kind of membranous system device of high magnification numbe concentration pectin, gram
The deficiency of traditional technology is taken, design is rationally, compact-sized, and user of service beats by the way that crude pectin solution is added into device
Opening apparatus adjusts the revolving speed of machine in ultimate filtration membrane systems, allows crude pectin solution by primary filter membranous system and ultimate
Obtain high purity pectin after filtration membrane systems, it is excellent that utility model device has that easy to operate, high-efficient, product purity is high etc.
Point.
(2) technical solution
In order to achieve the above object, the utility model is achieved by the following technical programs:
A kind of membranous system device of high magnification numbe concentration pectin, including primary filter membranous system and ultimate filtration membrane systems, institute
Stating primary filter membranous system includes tank body, liquid material entrance, cylindrical ceramic membrane filter, waste liquid outlet and liquid material outlet；The column
For the setting of shape purpose ceramic-film filter in tank interior, liquid material entrance merges connection company after passing through pipeline parallel connection cylindricality purpose ceramic-film filter
Logical tank base liquid liquid material outlet, waste liquid outlet are set to tank base side；The ultimate filtration membrane systems include: motor,
Outer housing, inner chamber body, feeding inlet and discharge port；The motor is mounted at the top of outer housing, is fixed by the rotation axis on motor
Cylindrical inner chamber body inside connected with outer casing body, the surrounding and bottom outer wall of inner chamber body are provided with ceramic filter membrane, outer housing top
Equipped with feeding inlet, bottom is equipped with waste liquid outlet and the discharge port that is connected to inner chamber body.
High-pressure circulation pump is equipped between the primary filter membranous system and ultimate filtration membrane systems at connecting pipe.
The cylindrical ceramic membrane filter is equipped with multiple hollow round hole, and circular hole wall is equipped with ceramic filter membrane.
Ceramic filter membrane on the ultimate filtration membrane systems inner lumen body is 4-5 layers.
(3) beneficial effect
The utility model embodiment provides a kind of membranous system device of high magnification numbe concentration pectin.Have following beneficial to effect
Fruit: user of service conveys crude pectin solution into device in advance, and solution is allowed to pass through the column in parallel in primary filter membranous system
Shape purpose ceramic-film filter filters out the impurity such as certain small molecule pectin and ash content and carries out preliminary mention to crude pectin solution
It is pure, and three cylindrical ceramic membrane filters in parallel can increase the efficiency of primary filtration to a certain extent, reduce the operating time；
Pectin solution after preliminary purification is transported in ultimate filtration membrane systems by high-pressure circulation pump, runs machine, allowing is motor
Output shaft drive inner chamber body rotation, by rotation generate centrifugal force and inner cavity body wall on ceramic filter membrane it is further
Impurity is filtered out, this process time is short, high-efficient, and resulting pectin has high concentration and high-quality.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor
Under, it is also possible to obtain other drawings based on these drawings.
Fig. 1 the utility model schematic perspective view；
Fig. 2 the utility model cylindrical ceramic membrane filter top view；
Fig. 3 the utility model cylindrical ceramic membrane filter Structure of cross section schematic diagram；
In figure, 1 tank body, 2 liquid material entrances, 3 cylindrical ceramic membrane filters, 4 waste liquid outlets, the outlet of 5 liquid materials, 6 motors, 7 turns
Moving axis, 8 feeding inlets, 9 outer housings, 10 inner chamber bodies, 11 ceramic filter membranes, 12 discharge ports, 13 high-pressure circulation pumps.
Specific embodiment
It is practical new below in conjunction with this to keep the objectives, technical solutions, and advantages of the embodiments of the present invention clearer
Attached drawing in type embodiment, the technical scheme in the utility model embodiment is clearly and completely described, it is clear that is retouched
The embodiment stated is the utility model a part of the embodiment, instead of all the embodiments.Based on the implementation in the utility model
Example, every other embodiment obtained by those of ordinary skill in the art without making creative efforts belong to
The range of the utility model protection.
A kind of membranous system device of high magnification numbe concentration pectin, including primary filter membranous system and ultimate filtration membrane systems, institute
Stating primary filter membranous system includes tank body 1, liquid material entrance 2, cylindrical ceramic membrane filter 3, waste liquid outlet 4 and liquid material outlet 5；Institute
It states cylindrical ceramic membrane filter 3 to be arranged inside tank body 1, after liquid material entrance 2 passes through pipeline parallel connection cylindricality purpose ceramic-film filter 3
Merging connects 1 bottom liquid liquid material of tank body outlet 5, and waste liquid outlet 4 is set to 1 bottom portion side end of tank body；The ultimate filter membrane
System includes: motor 6, outer housing 9, inner chamber body 10, feeding inlet 8 and discharge port 12；The motor 6 is mounted on 9 top of outer housing,
The cylindrical inner chamber body 10 inside outer housing 9 is fixedly connected with by the rotation axis 7 on motor 6, outside the surrounding of inner chamber body 10 and bottom
Wall is provided with ceramic filter membrane 11, is equipped with feeding inlet 8 at the top of outer housing 9, bottom be equipped with waste liquid outlet 4 be connected to inner chamber body 10
Discharge port 12.
High-pressure circulation pump 13 is equipped between the primary filter membranous system and ultimate filtration membrane systems at connecting pipe.
The cylindrical ceramic membrane filter 3 is equipped with multiple hollow round hole 301, and 301 wall of circular hole is equipped with ceramic filter membrane 302.
Ceramic filter membrane 11 on the ultimate filtration membrane systems inner lumen body 10 is 4-5 layers.
User of service conveys crude pectin solution into device in advance, and solution is allowed to pass through the parallel connection in primary filter membranous system
Cylindrical ceramic membrane filter 3, filter out the impurity such as certain small molecule pectin and ash content crude pectin solution is carried out it is preliminary
Purification, and the efficiency of three cylindrical ceramic membrane filter primary filtrations in parallel reduces the operating time；After preliminary purification
Pectin solution be transported in ultimate filtration membrane systems by high-pressure circulation pump 13, run machine, allow be motor 6 output shaft 7
Inner chamber body 10 is driven to rotate, the further mistake of ceramic filter membrane 11 on 10 wall of centrifugal force and inner chamber body generated by rotation
Impurity is filtered to get high-quality, high purity pectin is arrived.
It should be noted that, in this document, relational terms such as first and second and the like are used merely to a reality
Body or operation are distinguished with another entity or operation, are deposited without necessarily requiring or implying between these entities or operation
In any actual relationship or order or sequence.Moreover, the terms "include", "comprise" or its any other variant are intended to
Non-exclusive inclusion, so that the process, method, article or equipment including a series of elements is not only wanted including those
Element, but also including other elements that are not explicitly listed, or further include for this process, method, article or equipment
Intrinsic element.In the absence of more restrictions, the element limited by sentence "including a ...", it is not excluded that
There is also other identical elements in process, method, article or equipment including the element.
Above embodiments are only to illustrate the technical solution of the utility model, rather than its limitations；Although referring to aforementioned reality
Example is applied the utility model is described in detail, those skilled in the art should understand that: it still can be to preceding
Technical solution documented by each embodiment is stated to modify or equivalent replacement of some of the technical features；And these
It modifies or replaces, the spirit and model of various embodiments of the utility model technical solution that it does not separate the essence of the corresponding technical solution
It encloses.
Claims (4)
1. a kind of membranous system device of high magnification numbe concentration pectin, including primary filter membranous system and ultimate filtration membrane systems, special
Sign is: the primary filter membranous system includes tank body (1), liquid material entrance (2), cylindrical ceramic membrane filter (3), waste liquid outlet
(4) and liquid material exports (5)；Cylindrical ceramic membrane filter (3) setting is internal in tank body (1), and liquid material entrance (2) passes through pipeline
Cylindricality purpose ceramic-film filter (3) in parallel merges afterwards connects tank body (1) bottom liquid material outlet (5), and waste liquid outlet (4) is set to
Tank body (1) bottom portion side end；The ultimate filtration membrane systems include: motor (6), outer housing (9), inner chamber body (10), feeding inlet (8)
With discharge port (12)；The motor (6) is mounted at the top of outer housing (9), is fixedly connected by the rotation axis (7) on motor (6)
The internal cylindrical inner chamber body (10) of outer housing (9), the surrounding and bottom outer wall of inner chamber body (10) are provided with ceramic filter membrane (11),
Feeding inlet (8) are equipped at the top of outer housing (9), bottom is equipped with waste liquid outlet (4) and the discharge port (12) that is connected to inner chamber body (10).
2. a kind of membranous system device of high magnification numbe concentration pectin as described in claim 1, it is characterised in that: the primary filter
High-pressure circulation pump (13) are equipped at connecting pipe between membranous system and ultimate filtration membrane systems.
3. a kind of membranous system device of high magnification numbe concentration pectin as described in claim 1, it is characterised in that: the cylindrical ceramic
Membrane filter (3) is equipped with multiple hollow round hole (301), and circular hole (301) wall is equipped with ceramic filter membrane (302).
4. a kind of membranous system device of high magnification numbe concentration pectin as described in claim 1, it is characterised in that: the ultimate filtering
Ceramic filter membrane (11) on membranous system inner lumen body (10) is 4-5 layers.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820810826.8U CN208465363U (en) | 2018-05-29 | 2018-05-29 | A kind of membranous system device of high magnification numbe concentration pectin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820810826.8U CN208465363U (en) | 2018-05-29 | 2018-05-29 | A kind of membranous system device of high magnification numbe concentration pectin |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208465363U true CN208465363U (en) | 2019-02-05 |
Family
ID=65218974
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820810826.8U Expired - Fee Related CN208465363U (en) | 2018-05-29 | 2018-05-29 | A kind of membranous system device of high magnification numbe concentration pectin |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208465363U (en) |
-
2018
- 2018-05-29 CN CN201820810826.8U patent/CN208465363U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190205 |
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| CF01 | Termination of patent right due to non-payment of annual fee |