CN207175966U - A kind of novel saccharification tank - Google Patents
A kind of novel saccharification tank Download PDFInfo
- Publication number
- CN207175966U CN207175966U CN201721169331.3U CN201721169331U CN207175966U CN 207175966 U CN207175966 U CN 207175966U CN 201721169331 U CN201721169331 U CN 201721169331U CN 207175966 U CN207175966 U CN 207175966U
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- China
- Prior art keywords
- tank body
- coil pipe
- tank
- steam distribution
- steam
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Abstract
The utility model provides a kind of novel saccharification tank, including tank body and agitating device, the agitating device enters in tank body from the bottom oblique cutting of tank body side, the technique mouth of pipe is provided with the top of the tank body, the tank body lower part is provided with steam distribution coil pipe, the steam distribution coil pipe is annular coil pipe, one end of steam distribution coil pipe is horizontally fixed in the side wall of tank body, multiple dispensing orifices are uniformly provided with steam distribution coil pipe, coiled tube supports part is provided with below the steam distribution coil pipe between tank base, the side of tank body is provided with purified liquor outlet and turbid exports.The utility model is simple in construction, reasonable in design, and agitating device is stirred using side, is reduced power consumption, is improved mixing effect, distributes coil pipe using steam, steam is uniformly and quickly entered in tank, reduce sterilization time, improve efficiency.
Description
Technical field
The utility model belongs to starch sugar processing field, specifically a kind of novel saccharification tank.
Background technology
In the production engineering of starch sugar, saccharification is important production process, directly influences quality and the production of final products
Amount.Material needs to carry out steam sterilizing to saccharifying tank before entering saccharifying tank, and liquid glucose needs to carry out liquid glucose during entering saccharifying tank
Stirring, saccharifying tank liquid level reach the process for entering filtrate protein after technological requirement through pump.Traditional saccharifying tank steam is directly over
Pipeline enters saccharifying tank, and distribution of steam is uneven, sterilization time length；Traditional saccharifying tank stirring is top stirring, and power consumption is big, stirs
It is poor to mix effect；For traditional saccharifying tank from bottom discharge, liquid glucose is more containing albumen, removes next filter station filtration difficulty.
The content of the invention
For above-mentioned the deficiencies in the prior art, the utility model provides a kind of novel saccharification tank, and the saccharifying tank is simple in construction,
Side is stirred, and power consumption is small, and sterilizing steam is evenly distributed, and pure and turbid liquid separately discharges, and improves filter station efficiency.
Technical scheme provided by the utility model：A kind of novel saccharification tank, including tank body and agitating device, the stirring dress
Put from the bottom oblique cutting of tank body side to enter in tank body, at least one technique mouth of pipe, the tank body lower part are provided with the top of the tank body
Coil pipe is distributed provided with steam, the steam distribution coil pipe is annular coil pipe, and one end of steam distribution coil pipe import is horizontally fixed on
In the side wall of tank body, multiple dispensing orifices, the steam distribution coil pipe lower section and tank base are uniformly provided with steam distribution coil pipe
Between be provided with coiled tube supports part, the bottom of tank body side exports provided with turbid, and the tank body side of turbid outlet top is provided with clear
Liquid exports.
Further, the agitating device includes blender base, stirring motor, reductor and agitator, the agitator
For arm stirrer.
Further, CIP washers are additionally provided with the top of the tank body.
Further, normal-pressure quick-opening manhole is additionally provided with the top of the tank body, tank body opposite side is provided with lower inner pressed manhole.
The beneficial effects of the utility model：
(1) the utility model is stirred using side, is stirred relative to traditional top, is reduced power consumption, improve and stir
Mix effect.The utility model is provided with steam distribution coil pipe in tank body lower part, by dispensing orifice, steam is uniformly and quickly passed through tank
It is interior, reduce sterilization time, improve efficiency；Tank bottom is equipped with coiled tube supports part, makes more firm in steam course of conveying.
(2) tank body lower part is separately provided with purified liquor outlet and turbid exports, and is advantageous to clear liquid and turbid separation, avoids liquid glucose
In contain excessive protein, protein is separated from turbid outlet, and liquid glucose filters after purified liquor outlet collection, solves
The problem of filtration difficulty, improve filter station efficiency.
(4) CIP washers are provided with the top of tank body, can be simple and convenient with on-line cleaning tank inner chamber.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the structural representation of steam distribution coil pipe in saccharifying tank；
In figure：1-tank body, 2-agitating device, 3-steam distribution coil pipe, 3-1-dispensing orifice, 3-2-coil pipe import,
4-turbid exports, 5-purified liquor outlet, 6-technique mouth of pipe, 7-coiled tube supports part, 8-CIP washers, and 9-normal pressure opens people soon
Hole, 10-lower inner pressed manhole.
Embodiment
The utility model is described further below in conjunction with the accompanying drawings.
Novel saccharification tank as shown in Figure 1, including tank body 1 and agitating device 2, the agitating device 2 is from the side of tank body 1
Middle and lower part oblique cutting enters in tank body 1, and the top of tank body 1 is provided with least one technique mouth of pipe 6, and the bottom of tank body 1 is provided with steam
Coil pipe 3 is distributed, the steam distribution coil pipe 3 is annular coil pipe, and one end of the steam distribution import of coil pipe 3 is horizontally fixed on tank body 1
Side wall on, steam distribute coil pipe 3 coil pipe import 3-2 connection external steam pipelines, steam distribute coil pipe 3 on be uniformly provided with it is more
Individual dispensing orifice 3-1, coiled tube supports part 7, the bottom of the side of tank body 1 are provided between the lower section of steam distribution coil pipe 3 and the bottom of tank body 1
Portion is provided with turbid outlet 4, and the side of tank body 1 of the top of turbid outlet 4 is provided with purified liquor outlet 5.
The agitating device 1 includes stirring motor, reductor and agitator, and the agitator is arm stirrer.Institute
State the top of tank body 1 and be additionally provided with CIP washers 8.The top of tank body 1 is additionally provided with normal-pressure quick-opening manhole 9, and tank body opposite side is provided with down
Inner pressed manhole 10.
When the utility model is specifically used, feed liquid is passed through in tank body from the technique mouth of pipe, after reaching certain liquid level, unlatching is stirred
Motor is mixed, drives reductor to rotate, so as to which agitator starts running, after saccharification terminates in saccharifying tank, opens jet chimney, will
High-temperature steam is passed through steam distribution coil pipe from jet chimney, and by dispensing orifice, high-temperature steam is evenly distributed in tank body, makes tank body
The rapid heat temperature raising of interior saccharified liquid, temperature is set to rise to 75-85 DEG C, after enzyme deactivation is complete, saccharified liquid is discharged from purified liquor outlet, and
Turbid containing protein is exported from turbid and discharged, and is divided into filter progress.
The detailed description of specific embodiment of the present utility model is the foregoing is only, it is new not limit this practicality with this
Type, all any modification, equivalent and improvement made in mentality of designing of the present utility model etc., should be included in this practicality
Within new protection domain.
Claims (4)
1. a kind of novel saccharification tank, including tank body (1) and agitating device (2), it is characterised in that：The agitating device (2) is from tank
The bottom oblique cutting of body (1) side enters in tank body (1), and at least one technique mouth of pipe (6), the tank are provided with the top of the tank body (1)
Body (1) bottom is provided with steam distribution coil pipe (3), and the steam distribution coil pipe (3) is annular coil pipe, and steam distribution coil pipe (3) enters
One end of mouth is horizontally fixed in the side wall of tank body (1), and multiple dispensing orifices (3-1), institute are uniformly provided with steam distribution coil pipe (3)
State and be provided with coiled tube supports part (7) between tank body (1) bottom below steam distribution coil pipe (3), the bottom of tank body (1) side is provided with
Turbid exports (4), and tank body (1) side above turbid outlet (4) is provided with purified liquor outlet (5).
2. novel saccharification tank according to claim 1, it is characterised in that：The agitating device (2) includes blender base, stirred
Motor, reductor and agitator are mixed, the agitator is arm stirrer.
3. novel saccharification tank according to claim 1, it is characterised in that：CIP washers are additionally provided with the top of the tank body (1)
(8)。
4. novel saccharification tank according to claim 1, it is characterised in that：Normal pressure is additionally provided with the top of the tank body (1) to open soon
Manhole (9), tank body opposite side are provided with lower inner pressed manhole (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721169331.3U CN207175966U (en) | 2017-09-08 | 2017-09-08 | A kind of novel saccharification tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721169331.3U CN207175966U (en) | 2017-09-08 | 2017-09-08 | A kind of novel saccharification tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207175966U true CN207175966U (en) | 2018-04-03 |
Family
ID=61747301
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721169331.3U Active CN207175966U (en) | 2017-09-08 | 2017-09-08 | A kind of novel saccharification tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207175966U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108455233A (en) * | 2018-04-11 | 2018-08-28 | 烟台良荣机械精业有限公司 | Be saccharified bed |
| CN110106215A (en) * | 2019-05-10 | 2019-08-09 | 武汉友谊兴泰科技有限公司 | Saccharification, filtering technique and its equipment in a kind of fructose production process |
-
2017
- 2017-09-08 CN CN201721169331.3U patent/CN207175966U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108455233A (en) * | 2018-04-11 | 2018-08-28 | 烟台良荣机械精业有限公司 | Be saccharified bed |
| CN110106215A (en) * | 2019-05-10 | 2019-08-09 | 武汉友谊兴泰科技有限公司 | Saccharification, filtering technique and its equipment in a kind of fructose production process |
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