CN205133478U - Novel O -fibres draws device - Google Patents
Novel O -fibres draws device Download PDFInfo
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- CN205133478U CN205133478U CN201520856669.0U CN201520856669U CN205133478U CN 205133478 U CN205133478 U CN 205133478U CN 201520856669 U CN201520856669 U CN 201520856669U CN 205133478 U CN205133478 U CN 205133478U
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Abstract
The utility model relates to a novel O -fibres draws device, characterized by: the bent sieve I of pressure connects fibre drying machine, and fibre drying machine connects filtrating storage tank I, and filtrating storage tank I is through the bent sieve II of first delivery pump connection pressure, and the bent sieve I of pressure and the bent sieve II of pressure connect filtrating storage tank II, and filtrating storage tank II passes through the second delivery pump and connects the O -fibres and extract the machine, and the O -fibres extracts the machine and connects dense seitan jar, and the bent sieve II of pressure and O -fibres extract the machine and connect fibre washing system. The utility model discloses drawing the problem that O -fibres concentration is too low to the sieve method, increasing by one O -fibres toper and extract the machine, draw the O -fibres in the bent sieve filtrating of pressure before fibre drying machine and the drying machine, further concentrated O -fibres makes O -fibres dry content reach 8~15%, has thoroughly solved thin fiber recycling problem.
Description
Technical field
The utility model relates to W-Gum manufacture field, is exactly that one relates to fine-fibered extraction element in production of corn starch.
Background technology
In existing production of corn starch, fine-fibered does not generally extract separately, enter fiber extruder and go dehydration together with fibrous residue, the problem caused is that very most of fine-fibered enters again in the filtrate of water extracter, return fiber wash system, long-time running, a lot of fine-fibered can be accumulated in system, one is the washing effect affecting fiber, and two is the dehydrating effects affecting water extracter, and time serious, water extracter only goes out magma paste, and fine-fibered will be reclaimed separately, because filter liquor concentration is too low, fine fiber particulate is too little again, and recycling is a difficult problem always.Several fine-fibered extraction elements of current existence, all by screening plant, macrobead is removed, screen underflow is as fine-fibered, due to the fine-fibered concentration too low (moisture more than 97%) extracted, be difficult to independent recovery, after running for some time, consider economic factors, most producer all abandons.
Summary of the invention
The utility model extracts the too low problem of fine-fibered concentration for sieve method, increase by one fine-fibered taper extracting machine, extract the fine-fibered in bent sieving liquid before fibre drier and squeezing machine, concentrated fine-fibered further, make fine-fibered dry matter content reach 8-15%, thoroughly solve fine-fibered and reclaim problem.
The technical scheme that the utility model provides is:
A kind of novel fine fiber extraction element, it is characterized in that: pressure curved sieve I connects fibre drier, fibre drier connects filtrate tanks I, filtrate tanks I is by the first transferpump Bonding pressure song sieve II, pressure curved sieve I is connected filtrate tanks II with pressure curved sieve II, filtrate tanks II connects fine-fibered extracting machine by the second transferpump, and fine-fibered extracting machine connects dense seitan tank, and pressure curved sieve II is connected fiber wash system with fine-fibered extracting machine.Described fibre drier connects fiber collecting device.The pressure requirements of described pressure curved sieve I and pressure curved sieve II is 0.2 ~ 0.4MPa.Described fine-fibered extracting machine adopts conical centrifuge formula extracting machine.
From the filtrate of fibre drier, enter into filtrate tanks I, by pump delivery to pressure curved sieve, pressure requirements 0.2 ~ the 0.4MPa of pressure curved sieve, bent sieve screen overflow returns fiber wash system, bent sieve screen underflow (i.e. filtrate) mixes with from bent filtrate of sieving that squeezing machine dewaters, enter filtrate tanks II, then by pump delivery to the process of fine-fibered taper extracting machine, the dilute phase of extracting machine returns fiber wash system as process water, the concentrated phase of extracting machine is as fine-fibered, owing to containing higher albumen, dense seitan tank can be entered mix with dense albumen, then subsequent operations unit is removed.
A kind of novel fine fiber of the utility model extraction element has following advantage:
1. ensure that fiber wash effect, the free starch content in fiber is reduced, the wash water consumption of fiber can be reduced.
2. ensure that the long-term normal of fiber extruder runs, reduce discharging moisture, save the steam consumption that tube bank is dry;
3. the fine-fibered extracted directly mixes with dense seitan, can improve protein yield 0.3 ~ 0.5%.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of novel fine fiber of the utility model extraction element.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail.
A kind of novel fine fiber extraction element described in the utility model as shown in Figure 1, it is characterized in that: pressure curved sieve I1 connects fibre drier 2, fibre drier 2 connects filtrate tanks I3, filtrate tanks I3 is by the first transferpump 4 Bonding pressure song sieve II5, pressure curved sieve I1 is connected filtrate tanks II6 with pressure curved sieve II5, filtrate tanks II6 connects fine-fibered extracting machine 8 by the second transferpump 7, fine-fibered extracting machine 8 connects dense seitan tank, and pressure curved sieve II5 is connected fiber wash system with fine-fibered extracting machine 8.Described fibre drier 2 connects fiber collecting device.The pressure requirements of described pressure curved sieve I1 and pressure curved sieve II5 is 0.2 ~ 0.4MPa.Described fine-fibered extracting machine 8 adopts conical centrifuge formula extracting machine.
From the filtrate of fibre drier 2, enter into filtrate tanks I3, pressure curved sieve II5 is transported to transferpump 4, pressure requirements 0.2 ~ the 0.4MPa of pressure curved sieve II5, bent sieve II5 screen overflow returns fiber wash system, the filtrate that bent sieve II5 screen underflow (i.e. filtrate) sieves I1 with the dewatering pressure song from squeezing machine 2 top mixes, enter filtrate tanks II6, then be transported to conical centrifuge formula extracting machine 8 with transferpump 7 to process, the dilute phase of extracting machine 8 returns fiber wash system as process water, the concentrated phase of extracting machine is as fine-fibered, owing to containing higher albumen, dense seitan tank can be entered mix with dense albumen, then subsequent operations unit is removed.
The utility model principal character: when extracting machine 8 runs work, pressure curved sieve I1 mixes filtrate with pressure curved sieve II5's, extracting machine 8 is delivered to by pump 7, under the influence of centrifugal force, material equably along the distribution of taper extracting machine internal surface, and moves to direction, large footpath, fine-fibered enters collecting chamber, send into dense seitan tank by pipeline, filtrate then through internal surface, gets back to fiber wash system after collection.
Novel fine fiber extraction element in the utility model example production of corn starch has following advantage:
1. ensure that fiber wash effect, the free starch content in fiber is reduced, the wash water consumption of fiber can be reduced.
2. ensure that the long-term normal of fiber extruder runs, reduce discharging moisture, save the steam consumption that tube bank is dry;
3. the fine-fibered extracted directly mixes with dense seitan, can improve protein yield 0.3 ~ 0.5%.
The foregoing is only the detailed description of specific embodiments of the present utility model; the utility model is not limited with this; all do in mentality of designing of the present utility model any amendment, equivalent to replace and improvement etc., all should be included within protection domain of the present utility model.
Claims (4)
1. a novel fine fiber extraction element, it is characterized in that: pressure curved sieve I (1) connects fibre drier (2), fibre drier (2) connects filtrate tanks I (3), filtrate tanks I (3) is by the first transferpump (4) Bonding pressure song sieve II (5), pressure curved sieve I (1) is connected filtrate tanks II (6) with pressure curved sieve II (5), filtrate tanks II (6) connects fine-fibered extracting machine (8) by the second transferpump (7), fine-fibered extracting machine (8) connects dense seitan tank, pressure curved sieve II (5) is connected fiber wash system with fine-fibered extracting machine (8).
2. a kind of novel fine fiber extraction element according to claim 1, is characterized in that: the pressure requirements of described pressure curved sieve I (1) and pressure curved sieve II (5) is 0.2 ~ 0.4MPa.
3. a kind of novel fine fiber extraction element according to claim 1, it is characterized in that: described fine-fibered reclaims through two-stage, dry concentration reaches 8 ~ 15%.
4. a kind of novel fine fiber extraction element according to claim 1, is characterized in that: described fine-fibered extracting machine (8) adopts conical centrifuge formula extracting machine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520856669.0U CN205133478U (en) | 2015-10-30 | 2015-10-30 | Novel O -fibres draws device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520856669.0U CN205133478U (en) | 2015-10-30 | 2015-10-30 | Novel O -fibres draws device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205133478U true CN205133478U (en) | 2016-04-06 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520856669.0U Active CN205133478U (en) | 2015-10-30 | 2015-10-30 | Novel O -fibres draws device |
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| CN (1) | CN205133478U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019157784A1 (en) * | 2018-02-13 | 2019-08-22 | 大庆天之草生物新材料科技有限公司 | Automated production line whole-process monitoring method for herb fiber biological refining |
| CN110721954A (en) * | 2019-11-14 | 2020-01-24 | 山东福宽生物工程有限公司 | Fiber extraction system and method in corn starch production |
-
2015
- 2015-10-30 CN CN201520856669.0U patent/CN205133478U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019157784A1 (en) * | 2018-02-13 | 2019-08-22 | 大庆天之草生物新材料科技有限公司 | Automated production line whole-process monitoring method for herb fiber biological refining |
| CN110721954A (en) * | 2019-11-14 | 2020-01-24 | 山东福宽生物工程有限公司 | Fiber extraction system and method in corn starch production |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Ai Yongxue Inventor after: Lou Xinjian Inventor after: Lu Yanqiu Inventor before: Lou Xinjian Inventor before: Lu Yanqiu |