CN202465672U - Continuous saccharification device for starch sugar production - Google Patents
Continuous saccharification device for starch sugar production Download PDFInfo
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- CN202465672U CN202465672U CN 201220055675 CN201220055675U CN202465672U CN 202465672 U CN202465672 U CN 202465672U CN 201220055675 CN201220055675 CN 201220055675 CN 201220055675 U CN201220055675 U CN 201220055675U CN 202465672 U CN202465672 U CN 202465672U
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- Prior art keywords
- tank
- saccharifying
- feed
- saccharifying tank
- communicated
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- 238000004519 manufacturing process Methods 0.000 title abstract description 6
- 229920002472 Starch Polymers 0.000 title abstract 2
- 235000019698 starch Nutrition 0.000 title abstract 2
- 239000008107 starch Substances 0.000 title abstract 2
- 238000007599 discharging Methods 0.000 claims abstract description 11
- 238000003860 storage Methods 0.000 claims abstract description 9
- 238000006243 chemical reaction Methods 0.000 claims description 12
- 238000009413 insulation Methods 0.000 claims description 3
- 238000004140 cleaning Methods 0.000 abstract description 2
- 230000000694 effects Effects 0.000 abstract description 2
- 102000004190 Enzymes Human genes 0.000 abstract 1
- 108090000790 Enzymes Proteins 0.000 abstract 1
- 230000001954 sterilising effect Effects 0.000 abstract 1
- 239000007788 liquid Substances 0.000 description 8
- 230000002950 deficient Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000005183 environmental health Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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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
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/58—Reaction vessels connected in series or in parallel
-
- 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
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/02—Stirrer or mobile mixing elements
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- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Zoology (AREA)
- Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Organic Chemistry (AREA)
- Chemical & Material Sciences (AREA)
- Wood Science & Technology (AREA)
- Genetics & Genomics (AREA)
- Biomedical Technology (AREA)
- Sustainable Development (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Microbiology (AREA)
- Biotechnology (AREA)
- Molecular Biology (AREA)
- Clinical Laboratory Science (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The utility model relates to a continuous saccharification device for starch sugar production. The continuous saccharification device comprises a plurality of saccharifying tanks which are sequentially communicated, wherein a feed opening and a discharge opening are arranged in each saccharifying tank; an overflow pipeline is communicated between the discharge opening of the previous saccharifying tank and the feed opening of a next saccharifying tank; the feed opening arranged on the first saccharifying tank is communicated with a mixing tank with a stirrer through a feeding pipeline; a sugar feeding pump and an enzyme feeding pump are connected to the mixing tank through a pipeline; the discharge opening arranged at the last saccharifying tank is communicated with a temporary storage tank; the temporary storage tank is communicated with a discharging pipeline; and a discharging pump is arranged on the discharging pipeline. The continuous saccharification device disclosed by the utility model has the advantages that the structure is simple; the yield of products can be increased; the quality of the products can be improved; cleaning and sterilizing steps of the saccharification tanks are omitted; simplicity and convenience in operation are realized; the labor intensity of workers is reduced; the effect of continuous saccharification can be achieved; and the automation is easily realized.
Description
Technical field
The utility model relates to continuous conversion device in a kind of Dian Fentang production, belongs to the sugar mill technical field.
Background technology
In traditional saccharification apparatus; What adopt all is intermittent saccharification apparatus; Intermittent saccharification apparatus has limited production output on the one hand; After certain saccharifying tank is accomplished saccharification, must in time clean, sterilize saccharifying tank on the other hand, not only complex operation, working strength be big, environmental health difference but also cause water resource waste easily.Each saccharifying tank independently carries out saccharification, and the interior front and back charging of each jar is poor if having time, causes sugared composition unstable, and product percent of pass is lower, is unfavorable for guaranteeing quality product, enhances productivity, realizes more robotization.
Summary of the invention
Be technical deficiency more than solving; It is a kind of simple in structure that the utility model provides; Product production be can improve, the cleaning and the sterilisation step of saccharifying tank improved the quality of products, save; Easy and simple to handle, reduced workman labourer's intensity, easily be automated, and the Dian Fentang that reaches the effect of continuous conversion produce in the continuous conversion device.
The utility model is realized through following measure:
Continuous conversion device during a kind of Dian Fentang is produced; It is characterized in that: comprise some saccharifying tanks that are communicated with in order; Each saccharifying tank is provided with opening for feed and discharge port, is communicated with overflow spout between the opening for feed of the discharge port of previous saccharifying tank and a back saccharifying tank, and the opening for feed that is arranged on the first saccharifying tank is connected through feed pipe with the mixing tank that has whisking appliance; Described mixing tank has into sugared pump and enzyme-added pump through pipe connection; The discharge port that is arranged on position, end saccharifying tank is connected with temporary storage tank, and storage tank is connected with discharge pipe temporarily, and discharge pipe is provided with discharging pump.
The opening for feed of said saccharifying tank is arranged on the bottom of saccharifying tank; Discharge port is arranged on the top of saccharifying tank; Feed pipe between the opening for feed of mixing tank and the first saccharifying tank is provided with fresh feed pump, and described feed pipe and overflow spout all adopt the tangential direction charging.The tangential direction charging is meant the plane parallel at the axial of feed-pipe and overflow spout and saccharifying tank pot bottom place; And it is tangent with the edge of saccharifying tank pot bottom; Tangential direction charging, feed liquid are on the circumferential plane when just having got into, and it is defective that feed liquid is mixed the product that causes before and after can preventing.
Preferably, saccharifying tank is the closed container that inwall is provided with thermal insulation layer.
The beneficial effect of the utility model is:
1, the continuous conversion apparatus structure was simple, easy to operate during the Dian Fentang of the utility model was produced; In producing use, only need control advance sugared flow and enzyme-added flow, do not need one jar one jar metering; All be in full state in all saccharifying tank operational processs, needn't clean often and sterilize, greatly reduce labor strength; The continuous discharging of continuous conversion, the feed liquid saccharification result is even, and is best in quality.
2, adopt the continuous conversion device of the utility model can reduce production cost of products, enhance productivity, reduce work load, easily be automated.
Description of drawings
Fig. 1 is the utility model structural representation.
Fig. 2 is feed pipe and saccharifying tank tank base syndeton synoptic diagram.
Among the figure: 1, advance sugared pump; 2, enzyme-added pump; 3, whisking appliance; 4, mixing tank; 5, fresh feed pump; 6, saccharifying tank; 7, overflow spout; 8, temporary storage tank; 9, discharging pump; 10, feed pipe; 11, discharge pipe; 12, saccharifying tank tank base.
Embodiment
Structure is as shown in Figure 1, and continuous conversion device during the Dian Fentang of the utility model is produced comprises some saccharifying tanks 6 that are communicated with in order; Each saccharifying tank is provided with opening for feed and discharge port; The opening for feed of saccharifying tank 6 is arranged on the bottom of saccharifying tank, and discharge port is arranged on the top of saccharifying tank, and the opening for feed of the first saccharifying tank is connected through feed pipe 10 with mixing tank 4; Feed pipe 10 is provided with fresh feed pump 5; The top of saccharifying tank 6 is provided with whisking appliance 3, and the stir shaft of whisking appliance 3 is positioned at mixing tank 4, and mixing tank 4 also is connected with into sugared pump 1 and enzyme-added pump 2 through pipeline.Be communicated with overflow spout 7 between the opening for feed of the discharge port of previous saccharifying tank and a back saccharifying tank.Feed pipe 10 all adopts the tangential direction charging with overflow spout 7.Saccharifying tank adopts the charging of bottom tangent direction; After top overflow discharging, feed liquid were come out from first saccharifying tank top, tangential direction got into next saccharifying tank bottom; The saccharifying tank discharging of position, end is saccharification terminal point feed liquid; The discharge port of position, end saccharifying tank is connected with temporary storage tank 8, and storage tank 8 is connected with discharge pipe 11 temporarily, and discharge pipe 11 is provided with discharging pump 9.The tangential direction charging is meant the plane parallel at the axial of feed pipe 10 and overflow spout 7 and saccharifying tank pot bottom place; And it is tangent with the edge of saccharifying tank pot bottom; The tangential direction charging; Feed liquid is on the circumferential plane when just having got into, and structure is as shown in Figure 2, and it is defective that feed liquid is mixed the product that causes before and after can preventing.
The utility model is preferred, and saccharifying tank 6 is provided with the closed container of thermal insulation layer for inwall.
The quantity of tank body and volume design according to the flow of liquefier in producing, and are 10m if advance sugared flow
3/ h, saccharification time are 50h, can adopt five 100m so
3The volumetrical jar.Feed liquid from just begin to get into saccharifying tank to time of a last saccharifying tank discharging just be 50 hours.
The foregoing description is said to be in order to specify this patent; Though describe through specific term in the literary composition; But can not limit the protection domain of this patent with this; The personage who is familiar with this technical field can change or revise it after the spirit of understanding this patent and principle and reach equivalent purpose, and this equivalence change and modification all should be covered by the claim scope and define in the category.
Claims (3)
1. continuous conversion device during a Dian Fentang is produced; It is characterized in that: comprise some saccharifying tanks that are communicated with in order; Each saccharifying tank is provided with opening for feed and discharge port, is communicated with overflow spout between the opening for feed of the discharge port of previous saccharifying tank and a back saccharifying tank, and the opening for feed that is arranged on the first saccharifying tank is connected through feed pipe with the mixing tank that has whisking appliance; Described mixing tank has into sugared pump and enzyme-added pump through pipe connection; The discharge port that is arranged on position, end saccharifying tank is connected with temporary storage tank, and storage tank is connected with discharge pipe temporarily, and discharge pipe is provided with discharging pump.
2. continuous conversion device during Dian Fentang according to claim 1 is produced; It is characterized in that: the opening for feed of said saccharifying tank is arranged on the bottom of saccharifying tank; Discharge port is arranged on the top of saccharifying tank; Feed pipe between the opening for feed of mixing tank and the first saccharifying tank is provided with fresh feed pump, and described feed pipe and overflow spout all adopt the tangential direction charging.
3. continuous conversion device during Dian Fentang according to claim 1 is produced, it is characterized in that: saccharifying tank is the closed container that inwall is provided with thermal insulation layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220055675 CN202465672U (en) | 2012-02-20 | 2012-02-20 | Continuous saccharification device for starch sugar production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220055675 CN202465672U (en) | 2012-02-20 | 2012-02-20 | Continuous saccharification device for starch sugar production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202465672U true CN202465672U (en) | 2012-10-03 |
Family
ID=46913850
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220055675 Expired - Fee Related CN202465672U (en) | 2012-02-20 | 2012-02-20 | Continuous saccharification device for starch sugar production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202465672U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111893147A (en) * | 2020-07-13 | 2020-11-06 | 南通佳之味食品有限公司 | Preparation method of glucose syrup with low DE value |
-
2012
- 2012-02-20 CN CN 201220055675 patent/CN202465672U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111893147A (en) * | 2020-07-13 | 2020-11-06 | 南通佳之味食品有限公司 | Preparation method of glucose syrup with low DE value |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: LUZHOU BIO-CHEM TECHNOLOGY(SHANGDONG) CO., LTD. Free format text: FORMER OWNER: LUZHOU FOOD PRODUCT GROUP CORP., LTD., SHANDONG PROV. Effective date: 20130418 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20130418 Address after: 276400 Yishui, Shandong Province Lu Chau Road, No. 18, Patentee after: Lu Zhou Biotechnology (Shandong) Co., Ltd. Address before: 276400 Yishui, Shandong Province Lu Chau Road, No. 18, Patentee before: Luzhou Food Product Group Corp., Ltd., Shandong Prov. |
|
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121003 Termination date: 20140220 |