CN205761195U - A kind of liquefaction post with horizontal tangential eddy flow feed end structure - Google Patents
A kind of liquefaction post with horizontal tangential eddy flow feed end structure Download PDFInfo
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- CN205761195U CN205761195U CN201620461581.3U CN201620461581U CN205761195U CN 205761195 U CN205761195 U CN 205761195U CN 201620461581 U CN201620461581 U CN 201620461581U CN 205761195 U CN205761195 U CN 205761195U
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- Prior art keywords
- post
- liquefaction
- pipe
- inner cone
- liquefier
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- 230000000630 rising effect Effects 0.000 claims abstract description 5
- 239000010865 sewage Substances 0.000 claims abstract description 4
- 239000012530 fluid Substances 0.000 abstract description 12
- 239000013078 crystal Substances 0.000 abstract description 2
- 229920002472 Starch Polymers 0.000 description 4
- 235000019698 starch Nutrition 0.000 description 4
- 239000008107 starch Substances 0.000 description 4
- 238000009923 sugaring Methods 0.000 description 4
- 239000007788 liquid Substances 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 239000001058 brown pigment Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Landscapes
- Investigation Of Foundation Soil And Reinforcement Of Foundation Soil By Compacting Or Drainage (AREA)
Abstract
This utility model discloses a kind of liquefaction post with horizontal tangential eddy flow feed end structure；Including liquefaction post, feed pipe, blowoff valve, blow-off pipe；The inversed taper platform of liquefaction column bottom physically, has a post inner cone body；Liquefaction column bottom is inversed taper platform body, and post inner cone physically has helicoid；Feed pipe is connected with inversed taper platform body horizontal tangential；The horizontal feed mouth of pipe is at the initial rising portion of post inner cone physically helicoid；Liquefier tangentially enters liquefaction post, along post inner cone body helicoid spiral；Blow-off pipe connects below the charging aperture being arranged on liquefaction post perpendicular to the ground；Blowoff valve is installed on blow-off pipe；When producing continuously, sewage draining valve is closed.Advantage: the fluid eddy flow in liquefaction post rises, and fluid rotation direction the most quickly flows, first in first out；Do not produce albumen attachment wall built-up liquefaction column wall；Liquefier is as clear as crystal.
Description
Technical field
This utility model belongs to food chemistry technical field, relates to a kind of post and sugar making liquid gasifying device of comprising this liquefaction post of liquefying；Particularly relate to a kind of liquefaction post with horizontal tangential eddy flow feed end structure；It is particularly well-suited to the liquefaction operation of starch sugaring.
Background technology
During sugaring, liquefier is flashed through secondary injection, liquefier, at a temperature of drop to 98 ± 2 ° of C, and continue to 120 minutes in liquefaction post, make DE value be increased to more than 10%.
Liquefaction stage, protein can separate out and condense, and part stops hanging on liquefaction column wall, being in for a long time under such high-temperature, protein gradually becomes brown, during brown pigment is diluted to liquefier simultaneously, namely there occurs Mei Lade phenomenon, affect the transparency of liquefier.
The addition of enzyme preparation and the time maintained in liquefaction post become liquefaction stage and control the key of DE value.In producing continuously, under controlling enzyme preparation low consumption premise, in order to ensure that liquefier is held time and the uniformity of liquefier DE value, it is necessary to meet maintenance stage feed liquid first in first out.
Existing starch sugar manufacturing liquefying process device figure such as Fig. 1
Shown in: include liquefy post 1, feed pipe 2, centrifugal pump 5, two spray flash tank 6, flash tank 7；It is back taper body bottom liquefaction post 1；Feed pipe 2 is axially connected with reverse taper end bottom liquefaction post 1；6 liquefaction post series connection；Two spray flash tank 6 liquefiers after secondary injection enter centrifugal pump 5, are transported to bottom liquefaction post 1, and liquefier is axially into liquefaction post 1；Through liquefaction column bottom, reverse taper is gradually increasing, and overflow enters next one liquefaction column bottom, eventually enters into flash tank 7, as the feed of lower road saccharifying operation.Being observed by the visor on liquefaction post, observe the mobility status of cotton-shaped albumen, flow direction is mixed and disorderly, and turbulent extent is more apparent, and the liquefaction operation feeding manner of existing starch sugaring can not be completely secured liquefier first in first out in liquefaction post；Liquefaction post 1 inner fluid speed is relatively slow, and albumen is easily attached to liquefy on column wall；Liquefier is muddy, color is deep.Original direct current turbulent flow, impurity disperse wall built-up in a liquid.
Summary of the invention
The utility model discloses a kind of liquefaction post with horizontal tangential eddy flow feed end structure, to solve liquefier liquefaction post in first in first out is completely secured in prior art；Rate of flow of fluid is the slowest, and albumen is easily attached to liquefy on column wall；The problems such as liquefier is muddy, color is deep.
This utility model includes liquefy post, feed pipe；Liquefaction column bottom is inversed taper platform body, and feed pipe is connected with inversed taper platform body horizontal tangential；Liquefier tangentially enters liquefaction post.
One scheme optimized is: this utility model also includes blowoff valve, blow-off pipe；Blow-off pipe connects below the charging aperture being arranged on liquefaction post perpendicular to the ground；Blowoff valve is installed on blow-off pipe；When producing continuously, sewage draining valve is closed.
One scheme optimized is: the inversed taper platform of liquefaction column bottom physically, has a post inner cone body；Liquefier tangentially enters liquefaction post, along post inner cone body spiral.The liquefier avoiding whirlpool center during tangential admission is detained, and reduces the frictional resistance of whirlpool core flow simultaneously.
One scheme optimized is: the inversed taper platform of liquefaction column bottom physically, has a post inner cone body；Post inner cone physically has helicoid；The horizontal feed mouth of pipe is at the initial rising portion of post inner cone physically helicoid；Liquefier tangentially enters liquefaction post, along post inner cone body helicoid spiral.
The fluid eddy flow having the active effect that in liquefaction post of the present utility model rises, and fluid rotation direction the most quickly flows, first in first out；Impurity, at eddy flow vortex heart portion not wall built-up, does not produce albumen attachment wall built-up liquefaction column wall；Liquefier is as clear as crystal.
Accompanying drawing explanation
Fig. 1 is the liquefaction process device attachment structure schematic diagram of existing starch sugaring；
Fig. 2 is that this utility model first embodiment liquefaction post master regards partial view；
Fig. 3 is this utility model first embodiment liquefaction post left view partial view；
Fig. 4 is that this utility model the second embodiment liquefaction post master regards partial view；
Fig. 5 is this utility model the second embodiment liquefaction post left view partial view；
Fig. 6 is that this utility model the 3rd embodiment liquefaction post master regards partial view；
Fig. 7 is this utility model the 3rd embodiment liquefaction post left view partial view；
In figure: 1 liquefaction post, 2 feed pipes, 3 blowoff valves, 4 blow-off pipes, 5 centrifugal pumps, 6 two spray flash tank, 7 flash tanks, 1a post inner cone body, 1b helicoids.
Detailed description of the invention
Embodiment of the present utility model is described in detail below in conjunction with accompanying drawing.
This utility model first embodiment as shown in Figure 2 and Figure 3, including liquefaction post 1, feed pipe 2；Being inversed taper platform body bottom liquefaction post 1, feed pipe 2 is connected with inversed taper platform body horizontal tangential；Liquefier tangentially enters liquefaction post 1.Originally liquefaction column bottom is inverted cone, cone being removed in transformation, under feed pipe, charging changes horizontal tangent charging into, utilizes centrifugal pump feed kinetic energy to make fluid rotational flow in liquefaction post, produce the flow velocity of fluid and liquefaction column wall orientation, thus reduce cotton-shaped albumen wall cling phenomenon.
This utility model the second embodiment as shown in Figure 4, Figure 5, including liquefaction post 1, feed pipe 2；Inversed taper platform bottom liquefaction post 1 physically, has a post inner cone body 1a；Liquefier tangentially enters liquefaction post 1, along post inner cone body 1a spiral.Endfeed under every liquefaction post is changed into the charging of horizontal tangential eddy flow.Ensure that fluid realizes the order of first in first out, turbulent extent bottom reduction, reduce liquefier to greatest extent and stop dead angle, it is achieved the uniform rising of liquefaction.The liquefier avoiding whirlpool center during tangential admission is detained, and reduces the frictional resistance of whirlpool core flow simultaneously.
This utility model the 3rd embodiment as shown in Figure 6, Figure 7, including liquefaction post 1, feed pipe 2, blowoff valve 3, blow-off pipe 4；Inversed taper platform bottom liquefaction post 1 physically, has a post inner cone body 1a；On post inner cone body 1a, there is helicoid 1b；The horizontal feed mouth of pipe is the initial rising portion of helicoid 1b on post inner cone body 1a；Liquefier tangentially enters liquefaction post 1, along post inner cone body helicoid spiral；Fluid is made to keep spiralling trend in liquefaction column bottom tangential direction, the intermediate cone conical surface, spiral bottom surface.Liquefier starts eddy flow at the small diameter of liquefaction column bottom, and bottom surface has certain lead angle, and eddy flow resistance is little, and fluid curl is gradually dissolved in liquefaction post, also ensure that the first in first out of fluid.Blow-off pipe connects below the charging aperture being arranged on liquefaction post perpendicular to the ground；Blowoff valve is installed on blow-off pipe；When producing continuously, sewage draining valve is closed.
Claims (4)
1. a liquefaction post with horizontal tangential eddy flow feed end structure；Including liquefaction post, feed pipe；It is characterized in that: liquefaction column bottom is inversed taper platform body, and feed pipe is connected with inversed taper platform body horizontal tangential；Liquefier tangentially enters liquefaction post.
A kind of liquefaction post with horizontal tangential eddy flow feed end structure the most according to claim 1；It is characterized in that: the inversed taper platform of liquefaction column bottom physically, has a post inner cone body；Liquefier tangentially enters liquefaction post, along post inner cone body spiral.
A kind of liquefaction post with horizontal tangential eddy flow feed end structure the most according to claim 1；It is characterized in that: post inner cone physically has helicoid；The horizontal feed mouth of pipe is at the initial rising portion of post inner cone physically helicoid；Liquefier tangentially enters liquefaction post, along post inner cone body helicoid spiral.
A kind of liquefaction post with horizontal tangential eddy flow feed end structure the most according to claim 2；It is characterized in that: also include blowoff valve, blow-off pipe；Blow-off pipe connects below the charging aperture being arranged on liquefaction post perpendicular to the ground；Blowoff valve is installed on blow-off pipe；When producing continuously, sewage draining valve is closed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620461581.3U CN205761195U (en) | 2016-05-20 | 2016-05-20 | A kind of liquefaction post with horizontal tangential eddy flow feed end structure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620461581.3U CN205761195U (en) | 2016-05-20 | 2016-05-20 | A kind of liquefaction post with horizontal tangential eddy flow feed end structure |
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| Publication Number | Publication Date |
|---|---|
| CN205761195U true CN205761195U (en) | 2016-12-07 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620461581.3U Expired - Fee Related CN205761195U (en) | 2016-05-20 | 2016-05-20 | A kind of liquefaction post with horizontal tangential eddy flow feed end structure |
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| Country | Link |
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| CN (1) | CN205761195U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108238695A (en) * | 2016-12-23 | 2018-07-03 | 北京有色金属研究总院 | A kind of ultraviolet catalytic water treatment facilities using float type photochemical catalyst |
-
2016
- 2016-05-20 CN CN201620461581.3U patent/CN205761195U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108238695A (en) * | 2016-12-23 | 2018-07-03 | 北京有色金属研究总院 | A kind of ultraviolet catalytic water treatment facilities using float type photochemical catalyst |
| CN108238695B (en) * | 2016-12-23 | 2020-09-15 | 有研工程技术研究院有限公司 | Ultraviolet light catalysis water treatment device applying floating type photocatalyst |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20180717 Address after: No. 2589 Shengxi Road, Hengshui, Hebei Province, Hebei Patentee after: COFCO BIOCHEMICAL ENERGY (HENGSHUI) Co.,Ltd. Address before: No. 113-1, people's street, Changchun, Jilin Province, Jilin Patentee before: HUANGLONG FOOD INDUSTRY Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190409 Address after: No. 113-1, people's street, Changchun, Jilin Province, Jilin Patentee after: HUANGLONG FOOD INDUSTRY Co.,Ltd. Address before: No. 2589 Shengxi Road, Hengshui, Hebei Province, Hebei Patentee before: COFCO BIOCHEMICAL ENERGY (HENGSHUI) Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161207 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |