CN106479887A - Syrup production jet liquefaction device - Google Patents
Syrup production jet liquefaction device Download PDFInfo
- Publication number
- CN106479887A CN106479887A CN201611088092.9A CN201611088092A CN106479887A CN 106479887 A CN106479887 A CN 106479887A CN 201611088092 A CN201611088092 A CN 201611088092A CN 106479887 A CN106479887 A CN 106479887A
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- China
- Prior art keywords
- laminar flow
- flow tank
- mouth
- temperature
- atomizing steam
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/18—Apparatus specially designed for the use of free, immobilized or carrier-bound enzymes
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/06—Nozzles; Sprayers; Spargers; Diffusers
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/14—Pressurized fluid
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M33/00—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
- C12M33/04—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus by injection or suction, e.g. using pipettes, syringes, needles
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
- C12M41/18—Heat exchange systems, e.g. heat jackets or outer envelopes
- C12M41/20—Heat exchange systems, e.g. heat jackets or outer envelopes the heat transfer medium being a gas
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Organic Chemistry (AREA)
- Zoology (AREA)
- Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Wood Science & Technology (AREA)
- Genetics & Genomics (AREA)
- General Engineering & Computer Science (AREA)
- Sustainable Development (AREA)
- Biochemistry (AREA)
- Biomedical Technology (AREA)
- General Health & Medical Sciences (AREA)
- Microbiology (AREA)
- Biotechnology (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Analytical Chemistry (AREA)
- Molecular Biology (AREA)
- Confectionery (AREA)
Abstract
The present invention relates to a kind of syrup production jet liquefaction device, including laminar flow tank, the top of laminar flow tank is provided with mouth spray, bottom and is provided with slurry outlet and atomizing steam mouth, mouth spray is connected with spray pump, atomizing steam mouth is connected with atomizing steam pump, the top of the laminar flow tank is dome shape, and bottom is circular arc concave shape, and the mouth spray and slurry outlet are respectively arranged at top center position and the lower center position of laminar flow tank；The atomizing steam mouth includes multiple, and symmetrical ring is around being arranged at around the slurry outlet.In the present invention, the upper and lower side of laminar flow tank is arranged to arch shape, is easy to the diffusion of slurry and atomization vapor, and dispersion effect is good；Atomizing steam mouth arranges multiple in the bottom of laminar flow tank, and the steam pressure of laminar flow pot bottom is uniform, beneficial to uniformly mixing with slurry.
Description
Technical field
The present invention relates to syrup production equipment field, more particularly to syrup production jet liquefaction device.
Background technology
Injector is to prepare the equipment that must be used in high fructose corn, malt syrup, and the structure of injector is directly affected produces
The quality of product.Size mixing after stirring, with pump, slurry pumped into Jet liquefier, directly meet in injection wherein slurry and steam,
Drop temperature control is entered laminar flow tank and is incubated 60 minutes to 90 minutes in 110-115 degree, the feed liquid from injector out, temperature
Degree is maintained at 95-97 degree.Then secondary injection is carried out, and feed liquid and steam directly meet in second injector, and temperature rises to
More than 120-145 degree, and maintain or so 3-5 minute that Thermostable α-Amylase is thoroughly killed in high temperature, while starch can enter one
Step dispersion, protein can solidify further.Need during injection to carrying out enforcement control to temperature, liquid level height etc. in tank, existing
Injector slurry and vapor interface is little, heat exchange is insufficient, it is impossible to adapt to production needs, slurry and steam are insufficient contact, no
The uniform course of injection for being both unfavorable for material, the speed of the saccharification after impact is sprayed again and quality.
Content of the invention
The applicant is studied and is improved for the disadvantages mentioned above of prior art, provides a kind of syrup production injection
Liquefying plant, the present invention adopt following scheme：
A kind of syrup production jet liquefaction device, including laminar flow tank, the top of laminar flow tank is provided with mouth spray, bottom and is provided with
Slurry outlet and atomizing steam mouth, mouth spray are connected with spray pump, and atomizing steam mouth is connected with atomizing steam pump, the laminar flow tank
Top be dome shape, bottom is circular arc concave shape, and the mouth spray and slurry outlet are respectively arranged at the top of laminar flow tank
Middle position and lower center position；The atomizing steam mouth includes multiple, and symmetrical ring is around the week for being arranged at the slurry outlet
Enclose.
Improvement further as technique scheme：
The inner chamber of the laminar flow tank is provided with temperature detection bar by proximal wall, and the temperature detection bar is connected with temperature induction unit
Connect, the output end of the temperature induction unit connects the whitewashing controller of spray pump and the automation controller of atomizing steam pump respectively
Connection.
The temperature detection bar is provided with multiple temperature detecting point that arranges up and down, the temperature detecting point and the temperature
Sensing unit connects.
The temperature detecting point can adjust upper-lower height position on the temperature detection bar.
The temperature detecting point can rotate around the temperature detection bar and adjust circumferential position.
The method have technical effect that：
In the present invention, the upper and lower side of laminar flow tank is arranged to arch shape, is easy to the diffusion of slurry and atomization vapor, dispersion effect
Really good；Atomizing steam mouth is multiple in the bottom setting of laminar flow tank, and the steam pressure of laminar flow pot bottom is uniform, beneficial to uniform with slurry
Mixing；Adjusted using linkage of the temperature detection with whitewashing, atomization, the temperature adjusting to atomization process of whitewashing is realized, its regulation and control can
High, timely by property, it is ensured that slurry is mixed with the high-quality of steam.
Description of the drawings
Fig. 1 is the structural representation of the present invention.
In figure：1st, laminar flow tank；2nd, mouth spray；3rd, slurry outlet；4th, atomizing steam mouth；5th, temperature detection bar；6th, temperature sense
Answer unit；7th, spray pump；8th, atomizing steam pump；9th, whitewashing controller；10th, automation controller；11st, temperature detecting point.
Specific embodiment
Specific embodiment to the present invention is described further below in conjunction with the accompanying drawings.
Embodiment 1：As shown in figure 1, the syrup production jet liquefaction device of the present embodiment, including laminar flow tank 1, laminar flow tank
1 top is provided with mouth spray 2, bottom and is provided with slurry outlet 3 and atomizing steam mouth 4, and mouth spray 2 is connected with spray pump 7, and atomization is steamed
Steam ports 4 is connected with atomizing steam pump 8, and the top of laminar flow tank 1 is dome shape, and bottom is circular arc concave shape, mouth spray 2 and slurry
Outlet 3 is respectively arranged at top center position and the lower center position of laminar flow tank 1；Atomizing steam mouth 4 includes multiple, symmetrical ring
Around being arranged at around slurry outlet 3.
In the present invention, the upper and lower side of laminar flow tank 1 is arranged to arch shape, is easy to the diffusion of slurry and atomization vapor, dispersion
Effect is good；Atomizing steam mouth 4 arranges multiple in the bottom of laminar flow tank 1, and the steam pressure of 1 bottom of laminar flow tank is uniform, beneficial to slurry
Material is uniform to be mixed.
Embodiment 2：As shown in figure 1, used as the improvement further of embodiment 1, the inner chamber of laminar flow tank 1 is provided with temperature by proximal wall
Degree detection bar 5, temperature detection bar 5 are connected with temperature induction unit 6, and the output end of temperature induction unit 6 connects spray pump 7 respectively
Whitewashing controller 9 and the automation controller 10 of atomizing steam pump 8 connect.In 6 real-time detection laminar flow tank 1 of temperature induction unit
Mixing temperature, when the temperature of detection is higher than the max-thresholds which sets, sends the signal to whitewash controller 9 and atomization control
Device 10, controller 9 of whitewashing reduce whitewashing flow and the spray pressure of spray pump 7 in time, and automation controller 10 reduces atomizing steam
The atomizing pressure of pump 8 and flow, so as to realize the adjustment to temperature, until temperature is dropped back to zone of reasonableness, set when temperature is less than
During fixed minimum threshold, whitewashing controller 9 and automation controller 10 adjust spray pump 7 and atomizing steam pump 8 respectively so as to be in
Normal whitewashing and spray pattern.
Embodiment 3：As shown in figure 1, used as the improvement further of embodiment 2, temperature detection bar 5 is provided with multiple upper and lower cloth
The temperature detecting point 11 that puts, temperature detecting point 11 are connected with temperature induction unit 6.Temperature detecting point 11 is arranged using multiple spot, can
The temperature of upper, middle and lower position in complete detection laminar flow tank 1, it is to avoid local temperature too high and affect slurry mixed effect.
Embodiment 4：As shown in figure 1, used as the improvement further of embodiment 3, temperature detecting point 11 can be examined in the temperature
Upper-lower height position is adjusted on measuring staff 5, and/or temperature detecting point 11 can rotate around the temperature detection bar 5 and adjust circumferential position.
The regulation of temperature detecting point 11 is simple to operate, it is convenient to adjust height detection position and circumferential test position.
Claims (5)
1. a kind of syrup production jet liquefaction device, including laminar flow tank (1), the top of laminar flow tank (1) be provided with mouth spray (2),
Bottom is provided with slurry outlet (3) and atomizing steam mouth (4), and mouth spray (2) is connected with spray pump (7), atomizing steam mouth (4) and mist
Change steam pump (8) connection, it is characterised in that：The top of laminar flow tank (1) is dome shape, and bottom is circular arc concave shape, institute
State top center position and lower center position that mouth spray (2) and slurry outlet (3) are respectively arranged at laminar flow tank (1)；Described
Atomizing steam mouth (4) includes multiple, and symmetrical ring is around being arranged at around the slurry outlet (3).
2. syrup production jet liquefaction device according to claim 1, it is characterised in that：Laminar flow tank (1) interior
Chamber is provided with temperature detection bar (5) by proximal wall, and temperature detection bar (5) are connected with temperature induction unit (6), the temperature sense
The output end of unit (6) is answered to connect the whitewashing controller (9) of spray pump (7) and the automation controller of atomizing steam pump (8) respectively
(10) connect.
3. syrup production jet liquefaction device according to claim 2, it is characterised in that：Temperature detection bar (5)
Multiple temperature detecting point (11) that arranges up and down are provided with, temperature detecting point (11) are connected with the temperature induction unit (6)
Connect.
4. syrup production jet liquefaction device according to claim 3, it is characterised in that：Temperature detecting point (11)
Can be in described temperature detection bar (5) upper regulation upper-lower height position.
5. syrup production jet liquefaction device according to claim 3, it is characterised in that：Temperature detecting point (11)
Can rotate around described temperature detection bar (5) and adjust circumferential position.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611088092.9A CN106479887A (en) | 2016-11-30 | 2016-11-30 | Syrup production jet liquefaction device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611088092.9A CN106479887A (en) | 2016-11-30 | 2016-11-30 | Syrup production jet liquefaction device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106479887A true CN106479887A (en) | 2017-03-08 |
Family
ID=58275504
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611088092.9A Pending CN106479887A (en) | 2016-11-30 | 2016-11-30 | Syrup production jet liquefaction device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106479887A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100041119A1 (en) * | 2005-07-19 | 2010-02-18 | Holm Christensen Biosystemer Aps | Method and apparatus for conversion of cellulosic material to ethanol |
| CN202954045U (en) * | 2012-12-19 | 2013-05-29 | 山东华义玉米科技有限公司 | Jetting and reacting device for sugar processing |
| CN104498560A (en) * | 2014-12-23 | 2015-04-08 | 开封市四达农产品设备有限公司 | Liquefaction process and liquefaction equipment of glucose syrup |
| CN206232738U (en) * | 2016-11-30 | 2017-06-09 | 无锡甜丰食品有限公司 | Syrup production jet liquefaction device |
-
2016
- 2016-11-30 CN CN201611088092.9A patent/CN106479887A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100041119A1 (en) * | 2005-07-19 | 2010-02-18 | Holm Christensen Biosystemer Aps | Method and apparatus for conversion of cellulosic material to ethanol |
| CN202954045U (en) * | 2012-12-19 | 2013-05-29 | 山东华义玉米科技有限公司 | Jetting and reacting device for sugar processing |
| CN104498560A (en) * | 2014-12-23 | 2015-04-08 | 开封市四达农产品设备有限公司 | Liquefaction process and liquefaction equipment of glucose syrup |
| CN206232738U (en) * | 2016-11-30 | 2017-06-09 | 无锡甜丰食品有限公司 | Syrup production jet liquefaction device |
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| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170308 |