CN206355973U - A kind of heat exchange type saccharifying tank - Google Patents
A kind of heat exchange type saccharifying tank Download PDFInfo
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- CN206355973U CN206355973U CN201621308239.6U CN201621308239U CN206355973U CN 206355973 U CN206355973 U CN 206355973U CN 201621308239 U CN201621308239 U CN 201621308239U CN 206355973 U CN206355973 U CN 206355973U
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- tank
- saccharifying tank
- heat exchanger
- tubular heat
- saccharifying
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Abstract
The utility model discloses a kind of heat exchange type saccharifying tank, including laminar flow tank, tubular heat exchanger, liquefier flash tank and saccharifying tank；The discharging opening of the laminar flow tank connects the tube-side inlet of tubular heat exchanger, the import of the tube side outlet connection liquefier flash tank of tubular heat exchanger；Liquefier discharging pump is provided between laminar flow tank, tubular heat exchanger, the inlet of liquefier discharging pump connects the discharging opening of laminar flow tank, and liquefier discharging pump liquid outlet connects the tube-side inlet of tubular heat exchanger；The circulation discharging opening of the saccharifying tank connects the shell side inlet of tubular heat exchanger, and the shell-side outlet of tubular heat exchanger connects the charging aperture of saccharifying tank；Saccharified liquid discharging pump, saccharified liquid discharging pump inlet connection circulation discharging opening are provided between the saccharifying tank, tubular heat exchanger；Labour is largely saved in utility model works efficiency high, energy-conserving and environment-protective, can at-once monitor, improve the yield of product.
Description
Technical field
The utility model is related to saccharifying tank, specifically a kind of heat exchange type saccharifying tank.
Background technology
Saccharification is process important during starch sugar is produced, and directly influences the quality and yield of final products, and after being saccharified
High temperature is needed to go out enzyme.It is general to be gone out enzyme, method 1 using two ways in actual production:Directly changed after saccharification with plate and be heated to 80 and take the photograph
Family name's degree, enzyme and membrane filtration condition is met to play to go out；Method 2:Steam is passed directly into saccharifying tank, the temperature of saccharified liquid is reached
To 75 degrees Celsius, to reach enzyme effect of going out；But both approaches have deficiency, according to method 1, then plate is changed in heating process,
Coherency albumen in saccharified liquid can be attached on the inside of plate type heat exchanger in deformation process, not only reduce heat transfer effect, simultaneously
Also reduction flow is, it is necessary to often unpick and wash, increase workload；Steam is passed through into saccharified liquid according to method 2, sugar is not only reduced
It is larger to the impact of tank body when changing the concentration of liquid, the consumption of increase steam raising below, and being passed through steam, produce larger shake
Dynamic, tank body is also easily damaged
Utility model content
The purpose of this utility model is to provide that a kind of operating efficiency is high, and energy-conserving and environment-protective largely save labour, can be
When monitor, improve the heat exchange type saccharifying tank of the yield of product, to solve the problems mentioned in the above background technology.
To achieve the above object, the utility model provides following technical scheme：
A kind of heat exchange type saccharifying tank, including laminar flow tank, tubular heat exchanger, liquefier flash tank and saccharifying tank；The layer
The discharging opening for flowing tank connects the tube-side inlet of tubular heat exchanger, the tube side outlet connection liquefier flash tank of tubular heat exchanger
Import；Liquefier discharging pump, the inlet articulamentum of liquefier discharging pump are provided between the laminar flow tank, tubular heat exchanger
The discharging opening of tank is flowed, liquefier discharging pump liquid outlet connects the tube-side inlet of tubular heat exchanger；The saccharifying tank is recycled
Material mouth connects the shell side inlet of tubular heat exchanger, and the shell-side outlet of tubular heat exchanger connects the charging aperture of saccharifying tank；Institute
State and saccharified liquid discharging pump is provided between saccharifying tank, tubular heat exchanger, saccharified liquid discharging pump inlet connection circulation discharging opening,
Saccharified liquid discharging pump connects the shell side inlet of tubular heat exchanger；Heat-insulation layer is provided with the outside of the saccharifying tank, be saccharified pot bottom bag
Total discharging opening is included, motor is fixedly installed in saccharifying tank screw top；The motor-driven rotatable shaft, rotating shaft passes through saccharifying tank, and rotating shaft
Sealed bearings are fixedly installed between saccharifying tank；Set the spacing between multigroup agitating paddle, agitating paddle equal in the rotating shaft, and
It is arranged in parallel between agitating paddle, wherein, agitating paddle is tilted-spent in the horizontal direction；It is provided with the right side of the saccharifying tank upper end
Check valve is provided with the right side of cleaning pipe, cleaning pipe, cleaning pipe lower end is provided with fountain head, and fountain head is located at saccharifying tank inner upper；Institute
State and be provided with internal provided with temperature sensor and concentration sensor on the right side of liquid level gauge, saccharifying tank on the left of saccharifying tank, wherein, TEMP
Processor is provided with inside device and concentration sensor signal connection controller, controller, and controller surface is provided with display screen；It is described
The pot sidewall that is saccharified is provided with watch window；Saccharified liquid oil film separation withdrawing device is additionally provided with above the saccharifying tank；Saccharified liquid oil
UF membrane withdrawing device includes adjusting nut, screw rod, funnel, wired hose and drain valve, wherein, screw rod is stretched through adjusting nut
Enter inside saccharifying tank, and connection funnel below screw rod；Wired hose, the outlet of wired hose are connected at the funnel lower opening
End is stretched out outside saccharifying tank, and the port of export of wired hose is additionally provided with drain valve.
Further：The motor is Double-directional rotary motor.
Further：Timer is provided with the motor.
Compared with prior art, the beneficial effects of the utility model are：
In the utility model, saccharifying tank carries out the liquefier of the saccharified liquid of low temperature and high temperature heat in tubular heat exchanger
Exchange, make the saccharified liquid heat temperature raising of low temperature, and liquefier is cooled down；Saccharified liquid after heating is back in saccharifying tank, when
Temperature in saccharifying tank, which reaches degree Celsius, carries out the enzyme that goes out, and after the enzyme that goes out is complete, closes saccharified liquid discharging pump, saccharified liquid is expelled to
Next production link；
In the utility model, heat-insulation layer is conducive to energy-conservation, and agitating paddle is obliquely installed, be beneficial to saccharified liquid to both sides, to
Upper flowing, it is ensured that saccharified liquid is well mixed, improves operating efficiency；Wherein, liquid level gauge, watch window facilitate observing response situation,
Temperature sensor and concentration sensor being capable of at-once monitor saccharifying tank internal temperature, the reaction conditions of concentration, a large amount of saving work
Power, improves operating efficiency；
In the utility model, by the position of lower adjusting screw rod bottom funnel on adjusting nut, the position of funnel is down to
Below oil reservoir liquid level, fluid enters in funnel, and is discharged by wired hose outside saccharifying tank, is conducive to the saccharification of material
Journey, accelerates the rate of filtration of saccharified liquid, improves the yield of product, more time and labour saving.
Brief description of the drawings
Fig. 1 is the structural representation of heat exchange type saccharifying tank.
Fig. 2 is the structural representation of saccharifying tank in heat exchange type saccharifying tank.
Fig. 3 is the structural representation of saccharified liquid oil film separation withdrawing device in heat exchange type saccharifying tank.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment obtained, belongs to the scope of the utility model protection.
Refer in Fig. 1~3, the utility model embodiment, a kind of heat exchange type saccharifying tank, including laminar flow tank 1, shell and tube are changed
Hot device 3, liquefier flash tank 4 and saccharifying tank 6；The discharging opening of the laminar flow tank 1 connects the tube-side inlet of tubular heat exchanger 3,
The import of the tube side outlet connection liquefier flash tank 4 of tubular heat exchanger 3；Between the laminar flow tank 1, tubular heat exchanger 3
Provided with liquefier discharging pump 2, the inlet of liquefier discharging pump 2 connects the discharging opening of laminar flow tank 1, and liquefier discharging pump 2 goes out liquid
The tube-side inlet of mouth connection tubular heat exchanger 3；The circulation discharging opening 12 of the saccharifying tank 6 connects the shell of tubular heat exchanger 3
Journey entrance, the shell-side outlet of tubular heat exchanger 3 connects the charging aperture 11 of saccharifying tank 6；Exchanged heat in the saccharifying tank 6, shell and tube
Saccharified liquid discharging pump 5 is provided between device 3, the inlet of saccharified liquid discharging pump 5 connection circulation discharging opening 12, saccharified liquid discharging pump 5 connects
The shell side inlet of logical tubular heat exchanger 3；In work, after saccharification terminates in saccharifying tank 6, the outlet valve of laminar flow tank 1 is opened, and
Liquefier discharging pump 2 is opened, liquefier discharging pump 2 inputs the liquefier in laminar flow tank 1 in the tube side of tubular heat exchanger 3,
Liquefier is inputted in liquefier flash tank 4 after the tube side of tubular heat exchanger 3 carries out heat exchange, and enters next production
Link；At the same time, the outlet valve of saccharifying tank 6 is opened, and opens saccharified liquid discharging pump 5, saccharified liquid discharging pump 5 is by saccharifying tank 6
In the shell side of interior saccharified liquid input tubular heat exchanger 3, it is back to again in saccharifying tank 6 after heat exchange；In production, saccharification
The liquefier of the saccharified liquid of low temperature and high temperature is carried out heat exchange by tank 6 in tubular heat exchanger 3, heats the saccharified liquid of low temperature
Heating, and liquefier is cooled down；Saccharified liquid after heating is back in saccharifying tank 6, when the temperature in saccharifying tank 6 reaches that 35 take the photograph
Family name's degree carries out the enzyme that goes out, after the enzyme that goes out is complete, closes saccharified liquid discharging pump 5, saccharified liquid is expelled into next production link；The sugar
Change the outside of tank 6 and be provided with heat-insulation layer 14, the bottom of saccharifying tank 6 includes total discharging opening 13, and motor is fixedly installed in the screw top of saccharifying tank 6
16, motor 16 is to be provided with timer on Double-directional rotary motor, and motor 16；The drive shaft 18 of motor 16, rotating shaft 18 is worn
Cross and sealed bearings 17 are fixedly installed between saccharifying tank 6, and rotating shaft 18 and saccharifying tank 6；Multigroup agitating paddle is set in the rotating shaft 18
19, the spacing between agitating paddle 19 is equal and arranged in parallel between agitating paddle 19, wherein, agitating paddle 19 is in the horizontal direction
Upper inclination 0-20 degree；Provided with cleaning pipe 21 on the right side of the upper end of saccharifying tank 6, the right side of cleaning pipe 21 is provided with check valve 22, cleaning pipe
21 lower ends are provided with fountain head 20, and fountain head 20 is located at the inner upper of saccharifying tank 6；The left side of saccharifying tank 6 is provided with liquid level gauge 15, sugar
Change the right side of tank 6 internal provided with temperature sensor 24 and concentration sensor 25, wherein, temperature sensor 24 and concentration sensor 25 are believed
Number connection controller 26, the inside of controller 26 is provided with processor, and the surface of controller 26 is provided with display screen 27；The saccharifying tank 6
Side wall is provided with watch window 23；In work, heat-insulation layer 14 is conducive to energy-conservation, and agitating paddle 19 is obliquely installed, and is beneficial to saccharified liquid
To both sides, flow up, it is ensured that saccharified liquid is well mixed, improve operating efficiency；Wherein, liquid level gauge 15, the convenience of watch window 23
Observing response situation, temperature sensor 24 and concentration sensor 25 being capable of the internal temperature of at-once monitor saccharifying tank 6, the reactions of concentration
Situation, largely saves labour, improves operating efficiency；As shown in figure 3, being additionally provided with saccharified liquid oil film in the top of saccharifying tank 6
Separate withdrawing device 30；The saccharified liquid oil film separation withdrawing device 30 includes adjusting nut 31, screw rod 32, funnel 33, steel wire
Flexible pipe 34 and drain valve 35, wherein, screw rod 32 is stretched into inside saccharifying tank 6 through adjusting nut 31, and the connection leakage of the lower section of screw rod 32
Bucket 33；Wired hose 34 is connected at the lower opening of funnel 33, the port of export of wired hose 34 is stretched out outside saccharifying tank 6, and steel
The port of export of silk flexible pipe 34 is additionally provided with drain valve 35；In work, pass through the bottom funnel 33 of lower adjusting screw rod on adjusting nut 31 32
Position, the position of funnel 33 is down to below the oil reservoir liquid level, fluid enters in funnel 33, and is discharged by wired hose 34
Outside saccharifying tank 6, be conducive to the saccharifying of material, accelerate the rate of filtration of saccharified liquid, improve the yield of product, more save
Shi Shenggong.
It is obvious to a person skilled in the art that the utility model is not limited to the details of above-mentioned one exemplary embodiment, and
And in the case of without departing substantially from spirit or essential attributes of the present utility model, can realize that this practicality is new in other specific forms
Type.Therefore, no matter from the point of view of which point, embodiment all should be regarded as exemplary, and is nonrestrictive, this practicality is new
The scope of type limits by appended claims rather than described above, it is intended that the equivalency fallen in claim is contained
All changes in justice and scope are included in the utility model.Any reference in claim should not be considered as limitation
Involved claim.
Moreover, it will be appreciated that although the present specification is described in terms of embodiments, not each embodiment is only wrapped
Containing an independent technical scheme, this narrating mode of specification is only that for clarity, those skilled in the art should
Using specification as an entirety, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art
It may be appreciated other embodiment.
Claims (3)
1. a kind of heat exchange type saccharifying tank, including laminar flow tank (1), tubular heat exchanger (3), liquefier flash tank (4) and saccharifying tank
(6)；Characterized in that, the tube-side inlet of the discharging opening connection tubular heat exchanger (3) of the laminar flow tank (1), shell and tube heat exchange
The import of the tube side outlet connection liquefier flash tank (4) of device (3)；The laminar flow tank (1), tubular heat exchanger are set between (3)
There are liquefier discharging pump (2), the discharging opening of the inlet connection laminar flow tank (1) of liquefier discharging pump (2), liquefier discharging pump
(2) tube-side inlet of liquid outlet connection tubular heat exchanger (3)；Circulation discharging opening (12) the connection tubulation of the saccharifying tank (6)
The shell side inlet of formula heat exchanger (3), the charging aperture (11) of the shell-side outlet connection saccharifying tank (6) of tubular heat exchanger (3)；Institute
State and saccharified liquid discharging pump (5) is provided between saccharifying tank (6), tubular heat exchanger (3), the connection of saccharified liquid discharging pump (5) inlet
Circulate discharging opening (12), the shell side inlet of saccharified liquid discharging pump (5) connection tubular heat exchanger (3)；On the outside of the saccharifying tank (6)
Provided with heat-insulation layer (14), saccharifying tank (6) bottom includes total discharging opening (13), and motor is fixedly installed in saccharifying tank (6) screw top
(16)；Motor (16) drive shaft (18), rotating shaft (18) is passed through between saccharifying tank (6), and rotating shaft (18) and saccharifying tank (6)
Sealed bearings (17) are fixedly installed；Spacing phase between multigroup agitating paddle (19), agitating paddle (19) is set on the rotating shaft (18)
Deng, and it is arranged in parallel between agitating paddle (19), wherein, agitating paddle (19) tilts 0-20 degree in the horizontal direction；The sugar
Change provided with cleaning provided with check valve (22) on the right side of pipe (21), cleaning pipe (21) on the right side of tank (6) upper end, cleaning pipe (21) lower end is provided with
Fountain head (20), fountain head (20) is located at saccharifying tank (6) inner upper；Liquid level gauge (15), sugar are provided with the left of the saccharifying tank (6)
Change inside on the right side of tank (6) and be provided with temperature sensor (24) and concentration sensor (25), wherein, temperature sensor (24) and concentration are passed
Processor is provided with inside sensor (25) signal connection controller (26), controller (26), and controller (26) surface is provided with display
Shield (27)；Saccharifying tank (6) side wall is provided with watch window (23)；Saccharified liquid oil film is additionally provided with above the saccharifying tank (6)
Separate withdrawing device (30)；Saccharified liquid oil film separation withdrawing device (30) includes adjusting nut (31), screw rod (32), funnel
(33), wired hose (34) and drain valve (35), wherein, screw rod (32) stretches into saccharifying tank (6) inside through adjusting nut (31),
And connection funnel (33) below screw rod (32)；Wired hose (34), wired hose are connected at funnel (33) lower opening
(34) the port of export stretches out saccharifying tank (6) outside, and the port of export of wired hose (34) is additionally provided with drain valve (35).
2. heat exchange type saccharifying tank according to claim 1, it is characterised in that the motor (16) is Double-directional rotary motor.
3. heat exchange type saccharifying tank according to claim 1, it is characterised in that be provided with timer on the motor (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621308239.6U CN206355973U (en) | 2016-12-01 | 2016-12-01 | A kind of heat exchange type saccharifying tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621308239.6U CN206355973U (en) | 2016-12-01 | 2016-12-01 | A kind of heat exchange type saccharifying tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206355973U true CN206355973U (en) | 2017-07-28 |
Family
ID=59373245
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621308239.6U Active CN206355973U (en) | 2016-12-01 | 2016-12-01 | A kind of heat exchange type saccharifying tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206355973U (en) |
-
2016
- 2016-12-01 CN CN201621308239.6U patent/CN206355973U/en active Active
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