CN110117535A - The secondary liquefaction maintenance device of starch in a kind of production of crystal glucose - Google Patents
The secondary liquefaction maintenance device of starch in a kind of production of crystal glucose Download PDFInfo
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- CN110117535A CN110117535A CN201910397331.6A CN201910397331A CN110117535A CN 110117535 A CN110117535 A CN 110117535A CN 201910397331 A CN201910397331 A CN 201910397331A CN 110117535 A CN110117535 A CN 110117535A
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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
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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
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
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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
- 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
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Abstract
The invention discloses the secondary liquefaction of starch in a kind of production of crystal glucose to maintain device, including pipe-line system, sample extraction component, regulatory component, steam Jet liquefier and controller, pipe-line system is by level-one pipeline, secondary canalization and three-level pipeline composition, No.1 connecting tube is fixedly connected between the liquid outlet of level-one pipeline and the inlet of secondary canalization, the secondary liquefaction of starch maintains device in a kind of crystal glucose production of the present invention, by being equipped with level-one pipeline, secondary canalization and three-level pipeline, which are segmented secondary liquefaction, to carry out, it can be respectively to level-one pipeline equipped with sample extraction component, liquefier inside secondary canalization and three-level pipeline is sampled, and level-one pipeline is regulated and controled by regulatory component respectively, the flow velocity of liquefier inside secondary canalization and three-level pipeline, guarantee liquefaction quality, traditional disposably cause excessively is avoided simultaneously It liquefies the occurrence of unqualified.
Description
Technical field:
The invention belongs to glucose production equipment field, in particular to the secondary liquefaction of starch in a kind of crystal glucose production
Maintain device.
Background technique:
Liquefaction is exactly to destroy the aquation of starch granules physics structure and the enzyme water of starch at high temperature after adding α-amylase
Solution is acted on while being carried out, and forms viscosity with respect to (dextrin) lower liquid (non-paste) material, that is, liquefier.Want to be sufficiently destroyed
The crumb structure of starch needs 110 DEG C of even higher temperature, produces crystal glucose using corn starch milk, workshop section of liquefying
Using liquefaction process is sprayed twice, wherein needing to maintain thermotonus 90 minutes after second of injection liquefaction, the prior art is to pass through
What the bend pipe for the uniform-caliber nanometre that length is 35 meters was realized, when being flowed in bend pipe due to liquefier, temperature can be gradually lost, and be caused
Secondary liquefaction is insufficient, and since the liquefier inside bend pipe does not carry out segmentation detection, it is easy to cause disposable excessive liquid
Change unqualified, needs to solve.
Summary of the invention:
The object of the invention is that solve the above-mentioned problems and to provide starch in a kind of production of crystal glucose secondary
Liquefaction maintains device, solves the problems, such as existing at present.
To solve the above-mentioned problems, the present invention provides a kind of technical solutions:
The secondary liquefaction of starch maintains device, including pipe-line system, sample extraction component, tune in a kind of production of crystal glucose
Control component, steam Jet liquefier and controller, the pipe-line system are made of level-one pipeline, secondary canalization and three-level pipeline,
No.1 connecting tube is fixedly connected between the liquid outlet of the level-one pipeline and the inlet of secondary canalization, the secondary canalization
No. two connecting tubes are fixedly connected between liquid outlet and the inlet of three-level pipeline, the liquid outlet of the three-level pipeline is fixedly connected
There are No. three connecting tubes, spiral helicine No.1 heating wire, the level-one pipeline are wound with inside the duct wall of the level-one pipeline
Inside is fixedly installed with No.1 temperature inductor, and spiral helicine No. two heating metal is wound with inside the duct wall of the secondary canalization
Thread, No. two temperature inductors are fixedly installed with inside the secondary canalization, are wound with spiral inside the duct wall of the three-level pipeline
No. three heating wires of shape are fixedly installed with No. three temperature inductors, the No.1 connecting tube, two inside the three-level pipeline
It is equipped with channel inside number connecting tube and No. three connecting tubes, the controller, which is fixed by the bracket, to be mounted in No. three connecting tubes,
The controller respectively with No.1 heating wire, No.1 temperature inductor, No. two heating wires, No. two temperature inductors,
No. three heating wires and No. three temperature inductors are electrically connected.
Preferably, the sample extraction component is by No.1 extraction element, No. two extraction elements and No. three extraction element groups
At level-one pipeline is arranged in close to one end of No.1 connecting tube in the No.1 extraction element, and No. two extraction elements setting exists
Three-level pipeline is arranged in close to the one of No. three connecting tubes close to one end of No. two connecting tubes, No. three extraction elements in secondary canalization
End, the No.1 extraction element, No. two extraction elements and No. three extraction elements include sample bottle, and the lower end of the sample bottle is equal
Be fixedly installed with pedestal, one end two sides of three pedestals pass through support rod respectively with level-one pipeline, secondary canalization and three
Grade pipeline be fixedly connected, the inner upper end of three sample bottles pass through sampling pipe respectively with level-one pipeline, secondary canalization
It is connected to the inside of three-level pipeline, sampling valve is equipped on the sampling pipe, liquid level window, institute are equipped on the sample bottle
The side for stating liquid level window is equipped with fluid level scale line, and the bottle mouth position of the sample bottle is equipped with bottle cap, the lower end of the bottle cap
It is fixedly installed with rubber stopper.
Preferably, the regulatory component is made of No.1 controlling valve, No. two controlling valves and No. three controlling valves, the No.1
Controlling valve is arranged in No.1 connecting tube, and No. two controlling valves are arranged in No. two connecting tubes, No. three controlling valves setting
In No. three connecting tubes, the No.1 controlling valve, No. two controlling valves and No. three controlling valves include convex surface, three convex surfaces point
Not Wei Yu on the outside of No.1 connecting tube, No. two connecting tubes and No. three connecting tubes, be installed with valve rod in the middle part of the convex surface and valve rod with it is convex
Face is threadedly coupled, and one end of the valve rod is fixedly connected with the valve body of disc structure, and the valve body is located at channel interior, institute
The other end for stating valve rod is fixedly installed with handwheel, and the periphery on the convex surface is equipped with angle index line, and the outside on the convex surface is equipped with
Pointer and pointer are fixedly mounted on valve rod periphery.
Preferably, the steam Jet liquefier includes liquefier ontology, the side of the liquefier ontology is equipped with one
The other side of secondary liquefier entrance, the liquefier ontology is equipped with steam inlet.
Preferably, one end of the liquefier ontology is equipped with discharge port and the inlet of discharge port and level-one pipeline is fixed
Connection.
Preferably, the level-one pipeline is identical with the length of three-level pipeline, the length of the secondary canalization is level-one pipe
Twice of road length.
Preferably, the valve body is adapted design with the size in channel.
Preferably, the liquid level window is made of pyroceram material.
Beneficial effects of the present invention: the secondary liquefaction of starch maintains device in a kind of crystal glucose production of the present invention, passes through
Secondary liquefaction is segmented equipped with level-one pipeline, secondary canalization and three-level pipeline and is carried out, No.1 temperature inductor, No. two temperature are equipped with
Inductor and No. three temperature inductors are simultaneously equipped with No.1 heating wire, No. two heating wires and No. three heating wires simultaneously
Temperature sense and heating can be carried out to the secondary liquefier inside level-one pipeline, secondary canalization and three-level pipeline respectively, guarantee two
It is secondary liquefaction sufficiently, equipped with sample extraction component can respectively to the liquefier inside level-one pipeline, secondary canalization and three-level pipeline into
Row sampling, and pass through the flow velocity that regulatory component regulates and controls the liquefier inside level-one pipeline, secondary canalization and three-level pipeline respectively, it protects
Card liquefaction quality, while avoiding and traditional disposably causing the occurrence of unqualified of excessively liquefying.
Detailed description of the invention:
Detailed description will be given by the following detailed implementation and drawings by the present invention for ease of explanation,.
Fig. 1 is schematic diagram of internal structure of the invention；
Fig. 2 is No.1 extraction element structural schematic diagram of the invention；
Fig. 3 is No.1 controlling valve cross-sectional plan view structural schematic diagram of the invention；
Fig. 4 is convex configuration schematic diagram of the invention.
In figure: 1, pipe-line system；11, level-one pipeline；12, secondary canalization；13, three-level pipeline；14, No.1 connecting tube；15,
No. two connecting tubes；16, No. three connecting tubes；17, No.1 heats wire；18, No.1 temperature inductor；19, No. two heating metals
Silk；110, No. two temperature inductors；111, No. three heating wires；112, No. three temperature inductors；113, channel；2, sample mentions
Take component；21, No.1 extraction element；22, No. two extraction elements；23, No. three extraction elements；24, sample bottle；25, pedestal；26,
Support rod；27, sampling pipe；28, sampling valve；29, liquid level window；210, fluid level scale line；211, bottle cap；212, rubber stopper；
3, regulatory component；31, No.1 controlling valve；32, No. two controlling valves；33, No. three controlling valves；34, convex surface；35, valve rod；36, handwheel；
37, valve body；38, pointer；39, angle index line；4, steam Jet liquefier；41, liquefier ontology；42, a liquefier enters
Mouthful；43, steam inlet；5, controller.
Specific embodiment:
As shown in Figs 1-4, present embodiment uses following technical scheme: starch two in a kind of production of crystal glucose
Secondary liquefaction maintains device, including pipe-line system 1, sample extraction component 2, regulatory component 3, steam Jet liquefier 4 and controller
5, the pipe-line system 1 is made of level-one pipeline 11, secondary canalization 12 and three-level pipeline 13, the liquid outlet of the level-one pipeline 11
No.1 connecting tube 14, the liquid outlet and triode of the secondary canalization 12 are fixedly connected between the inlet of secondary canalization 12
No. two connecting tubes 15 are fixedly connected between the inlet in road 13, the liquid outlet of the three-level pipeline 13 is fixedly connected with No. three companies
Adapter tube 16 is wound with spiral helicine No.1 heating wire 17, the level-one pipeline 11 inside the duct wall of the level-one pipeline 11
Inside is fixedly installed with No.1 temperature inductor 18, and spiral helicine No. two heating are wound with inside the duct wall of the secondary canalization 12
Wire 19 is fixedly installed with No. two temperature inductors 110, the duct wall of the three-level pipeline 13 inside the secondary canalization 12
Inside is wound with spiral helicine No. three heating wire 111, is fixedly installed with No. three temperature inductors inside the three-level pipeline 13
112, channel 113, the controller 5 are equipped with inside 14, No. two connecting tubes 15 of the No.1 connecting tube and No. three connecting tubes 16
It is fixed by the bracket and is mounted in No. three connecting tubes 16, the controller 5 heats wire 17, No.1 temperature sense with No.1 respectively
Answer 18, No. two heating temperature inductor 110, three of wire 19, two heating wires 111 of device and No. three temperature inductors
112 are electrically connected.
Wherein, the sample extraction component 2 is by 21, No. two extraction elements 22 of No.1 extraction element and No. three extraction elements 23
Level-one pipeline 11 is arranged in close to one end of No.1 connecting tube 14, No. two extractions dress in composition, the No.1 extraction element 21
It sets 22 and secondary canalization 12 is set close to one end of No. two connecting tubes 15, No. three extraction elements 23 are arranged in three-level pipeline 13
Close to one end of No. three connecting tubes 16,21, No. two extraction elements 22 of the No.1 extraction element and No. three extraction elements 23 are wrapped
Sample bottle 24 is included, the lower end of the sample bottle 24 is fixedly installed with pedestal 25, and one end two sides of three pedestals 25 are logical
Support rod 26 is crossed to be fixedly connected with level-one pipeline 11, secondary canalization 12 and three-level pipeline 13 respectively, three sample bottles 24
Inner upper end passes through sampling pipe 27 and is connected to respectively with the inside of level-one pipeline 11, secondary canalization 12 and three-level pipeline 13, institute
It states and is equipped with sampling valve 28 on sampling pipe 27, liquid level window 29 is equipped on the sample bottle 24, the liquid level window 29
Side is equipped with fluid level scale line 210, and the bottle mouth position of the sample bottle 24 is equipped with bottle cap 211, and the lower end of the bottle cap 211 is solid
Dingan County is equipped with rubber stopper 212.
Wherein, the regulatory component 3 is made of 31, No. two controlling valves 32 of No.1 controlling valve and No. three controlling valves 33, described
No.1 controlling valve 31 is arranged in No.1 connecting tube 14, and No. two controlling valves 32 are arranged in No. two connecting tubes 15, and described three
Number controlling valve 33 is arranged in No. three connecting tubes 16, and 31, No. two controlling valves 32 of the No.1 controlling valve and No. three controlling valves 33 are equal
Including convex surface 34, three convex surfaces 34 are located at 14, No. two connecting tubes 15 of No.1 connecting tube and No. three 16 outsides of connecting tube,
The middle part on the convex surface 34 is installed with valve rod 35 and valve rod 35 is threadedly coupled with convex surface 34, and one end of the valve rod 35 is fixedly connected with
The valve body 37 of disc structure, the valve body 37 are located inside channel 113, and the other end of the valve rod 35 is fixedly installed with hand
Wheel 36, the periphery on the convex surface 34 are equipped with angle index line 39, and the outside on the convex surface 34 is equipped with pointer 38 and pointer 38 is fixed
It is mounted on 35 periphery of valve rod.
Wherein, the steam Jet liquefier 4 includes liquefier ontology 41, and the side of the liquefier ontology 41 is equipped with one
Secondary liquefier entrance 42, the other side of the liquefier ontology 41 are equipped with steam inlet 43, and steam Jet liquefier 4 is by a not good liquor
Change liquid to eject.
Wherein, one end of the liquefier ontology 41 is equipped with discharge port and the inlet of discharge port and level-one pipeline 11 is fixed
Connection, a liquefier enter inside level-one pipeline 11 by the discharge port of liquefier ontology 41.
Wherein, the level-one pipeline 11 is identical with the length of three-level pipeline 13, and the length of the secondary canalization 12 is level-one
Twice of 11 length of pipeline facilitates control to liquefy.
Wherein, the valve body 37 is adapted design with the size in channel 113, guarantees the circulation and cut-off of control channel 113.
Wherein, the liquid level window 29 is made of pyroceram material, facilitates observation liquid level.
It is specific: 5 model siemens PLC of controller of the invention, 18, No. two temperature senses of No.1 temperature inductor
Answering the model of device 110 and No. three temperature inductors 112 is PT100, and steam Jet liquefier 4 is SZE type, and one time liquefier is logical
It crosses a liquefier entrance 42 and enters steam Jet liquefier 4, then sequentially enter level-one pipeline 11,12 and of secondary canalization
Three-level pipeline 13 carries out secondary liquefaction, is respectively equipped with No.1 temperature inside level-one pipeline 11, secondary canalization 12 and three-level pipeline 13
The liquefier for spending 112 pairs of inside of 18, No. two temperature inductors 110 of inductor and No. three temperature inductors carries out temperature sense, when
When temperature is relatively low, 17, No. two heating wires 19 of wire are heated using No.1 and No. three heating wires 111 are powered and distinguish
Heating treatment is carried out to the liquefier inside level-one pipeline 11, secondary canalization 12 and three-level pipeline 13, is equipped with No.1 extraction element
21, No. two extraction elements 22 and No. three extraction elements 23 can be respectively in level-one pipeline 11, secondary canalization 12 and three-level pipelines 13
The liquefier in portion samples, and can judge respectively in level-one pipeline 11, secondary canalization 12 and three-level pipeline 13 according to sample detection
Then the Degree of Liquefaction in portion rationally rotates handwheel 36 according to Degree of Liquefaction, utilize the unlatching between application valve body 37 and channel 113
Gap controls the flow velocity of 13 inside liquefier of level-one pipeline 11, secondary canalization 12 and three-level pipeline, guarantees secondary liquefying time
Abundance, the present invention be equipped with by be equipped with level-one pipeline 11, secondary canalization 12 and three-level pipeline 13 to secondary liquefaction be segmented into
Row, and can successively carry out detection Degree of Liquefaction, avoid and traditional disposably cause the occurrence of unqualified of excessively liquefying.
The above shows and describes the basic principles and main features of the present invention and the advantages of the present invention, the technology of the industry
Personnel are it should be appreciated that the present invention is not limited to the above embodiments, and the above embodiments and description only describe this
The principle of invention, without departing from the spirit and scope of the present invention, various changes and improvements may be made to the invention, these changes
Change and improvement all fall within the protetion scope of the claimed invention, the claimed scope of the invention by appended claims and its
Equivalent thereof.
Claims (8)
1. the secondary liquefaction of starch maintains device in a kind of crystal glucose production, it is characterised in that: including pipe-line system (1), sample
Product extraction assembly (2), regulatory component (3), steam Jet liquefier (4) and controller (5), the pipe-line system (1) is by level-one
Pipeline (11), secondary canalization (12) and three-level pipeline (13) composition, the liquid outlet and secondary canalization of the level-one pipeline (11)
(12) it is fixedly connected between inlet No.1 connecting tube (14), the liquid outlet and three-level pipeline of the secondary canalization (12)
(13) No. two connecting tubes (15) are fixedly connected between inlet, the liquid outlet of the three-level pipeline (13) is fixedly connected with three
Number connecting tube (16) is wound with spiral helicine No.1 heating wire (17) inside the duct wall of the level-one pipeline (11), described
It is fixedly installed with No.1 temperature inductor (18) inside level-one pipeline (11), is wound with inside the duct wall of the secondary canalization (12)
Spiral helicine No. two heating wires (19), the secondary canalization (12) is internal to be fixedly installed with No. two temperature inductors (110),
Spiral helicine No. three heating wires (111), the three-level pipeline (13) are wound with inside the duct wall of the three-level pipeline (13)
Inside is fixedly installed with No. three temperature inductors (112), the No.1 connecting tube (14), No. two connecting tubes (15) and No. three connections
It is equipped with channel (113) inside pipe (16), the controller (5), which is fixed by the bracket, to be mounted on No. three connecting tubes (16), institute
It states controller (5) and heats wire (17), No.1 temperature inductor (18), No. two heating wires (19), two with No.1 respectively
Number temperature inductor (110), No. three heating wires (111) and No. three temperature inductors (112) are electrically connected.
2. the secondary liquefaction of starch maintains device in a kind of crystal glucose production according to claim 1, it is characterised in that:
The sample extraction component (2) is made of No.1 extraction element (21), No. two extraction elements (22) and No. three extraction elements (23),
No.1 extraction element (21) setting is in level-one pipeline (11) close to the one end of No.1 connecting tube (14), No. two extractions dress
(22) setting is set in secondary canalization (12) close to one end of No. two connecting tubes (15), No. three extraction elements (23) are arranged three
Grade pipeline (13) is close to one end of No. three connecting tubes (16), the No.1 extraction element (21), No. two extraction elements (22) and three
Number extraction element (23) includes sample bottle (24), and the lower end of the sample bottle (24) is fixedly installed with pedestal (25), and three
One end two sides of the pedestal (25) pass through support rod (26) respectively with level-one pipeline (11), secondary canalization (12) and triode
Road (13) is fixedly connected, the inner upper end of three sample bottles (24) pass through sampling pipe (27) respectively with level-one pipeline
(11), secondary canalization (12) is connected to the inside of three-level pipeline (13), is equipped with sampling valve (28) on the sampling pipe (27),
It is equipped with liquid level window (29) on the sample bottle (24), the side of the liquid level window (29) is equipped with fluid level scale line
(210), the bottle mouth position of the sample bottle (24) is equipped with bottle cap (211), and the lower end of the bottle cap (211) is fixedly installed with rubber
It fills in (212).
3. the secondary liquefaction of starch maintains device in a kind of crystal glucose production according to claim 1, it is characterised in that:
The regulatory component (3) is made of No.1 controlling valve (31), No. two controlling valves (32) and No. three controlling valves (33), the No.1 tune
It controls valve (31) to be arranged on No.1 connecting tube (14), No. two controlling valves (32) are arranged on No. two connecting tubes (15), described
No. three controlling valves (33) are arranged on No. three connecting tubes (16), the No.1 controlling valve (31), No. two controlling valves (32) and No. three
Controlling valve (33) includes convex surface (34), and three convex surfaces (34) are located at No.1 connecting tube (14), No. two connecting tubes
(15) and on the outside of No. three connecting tubes (16), valve rod (35) is installed in the middle part of the convex surface (34) and valve rod (35) and convex surface (34) spiral shell
Line connection, one end of the valve rod (35) are fixedly connected with the valve body (37) of disc structure, and the valve body (37) is located at logical
Road (113) is internal, and the other end of the valve rod (35) is fixedly installed with handwheel (36), and the periphery of the convex surface (34) is equipped with angle
The outside of graduation mark (39), the convex surface (34) is equipped with pointer (38) and pointer (38) is fixedly mounted on valve rod (35) periphery.
4. the secondary liquefaction of starch maintains device in a kind of crystal glucose production according to claim 1, it is characterised in that:
The steam Jet liquefier (4) includes liquefier ontology (41), and the side of the liquefier ontology (41) is equipped with primary liquefaction
The other side of liquid entrance (42), the liquefier ontology (41) is equipped with steam inlet (43).
5. the secondary liquefaction of starch maintains device in a kind of crystal glucose production according to claim 4, it is characterised in that:
One end of the liquefier ontology (41) is equipped with discharge port and discharge port is fixedly connected with the inlet of level-one pipeline (11).
6. the secondary liquefaction of starch maintains device in a kind of crystal glucose production according to claim 1, it is characterised in that:
The level-one pipeline (11) is identical with the length of three-level pipeline (13), and the length of the secondary canalization (12) is level-one pipeline (11)
Twice of length.
7. the secondary liquefaction of starch maintains device in a kind of crystal glucose production according to claim 3, it is characterised in that:
The valve body (37) is adapted design with the size of channel (113).
8. the secondary liquefaction of starch maintains device in a kind of crystal glucose production according to claim 2, it is characterised in that:
The liquid level window (29) is made of pyroceram material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910397331.6A CN110117535A (en) | 2019-05-14 | 2019-05-14 | The secondary liquefaction maintenance device of starch in a kind of production of crystal glucose |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910397331.6A CN110117535A (en) | 2019-05-14 | 2019-05-14 | The secondary liquefaction maintenance device of starch in a kind of production of crystal glucose |
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| CN110117535A true CN110117535A (en) | 2019-08-13 |
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ID=67522285
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| CN201910397331.6A Withdrawn CN110117535A (en) | 2019-05-14 | 2019-05-14 | The secondary liquefaction maintenance device of starch in a kind of production of crystal glucose |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111662822A (en) * | 2020-05-27 | 2020-09-15 | 河北德瑞淀粉有限公司 | Starch secondary liquefaction maintaining device in improved generation crystalline dextrose production |
| CN114410710A (en) * | 2022-01-21 | 2022-04-29 | 路莹 | Continuous amylase conversion equipment and conversion method |
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| GB1067712A (en) * | 1963-07-15 | 1967-05-03 | Kroyer K K K | Process and apparatus for converting starch and other polysaccharides into dextrose and maltose containing products |
| EP0041670A1 (en) * | 1980-06-06 | 1981-12-16 | Hoechst Aktiengesellschaft | Process for the continuous treatment of nutrient fluids by heating during flow-through |
| CN2536052Y (en) * | 2002-03-16 | 2003-02-19 | 刘克新 | Continuous high-efficiency starch sugar makers |
| CN206289257U (en) * | 2016-10-26 | 2017-06-30 | 山东百盛生物科技有限公司 | A kind of full-automatic continuous production Glucose Liquid system |
| CN206970613U (en) * | 2017-07-25 | 2018-02-06 | 昆明佰佳益康生物科技有限公司 | A kind of microorganism fermentation tank sampler |
| CN207435422U (en) * | 2017-11-01 | 2018-06-01 | 山东西王糖业有限公司 | The secondary liquefaction of starch maintains device in a kind of crystal glucose production |
| CN208651788U (en) * | 2018-07-10 | 2019-03-26 | 恒安（重庆）生活用纸有限公司 | Coating mixing channel condensed water valve angle identification mechanism |
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| CN114410710A (en) * | 2022-01-21 | 2022-04-29 | 路莹 | Continuous amylase conversion equipment and conversion method |
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