CN204074073U - A kind of heating saccharifying tank - Google Patents
A kind of heating saccharifying tank Download PDFInfo
- Publication number
- CN204074073U CN204074073U CN201420521560.7U CN201420521560U CN204074073U CN 204074073 U CN204074073 U CN 204074073U CN 201420521560 U CN201420521560 U CN 201420521560U CN 204074073 U CN204074073 U CN 204074073U
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- China
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- tank body
- cover
- coil pipe
- temperature water
- funnel
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Abstract
The utility model discloses a kind of heating saccharifying tank, comprise tank body, cover, saccharified liquid oil film be separated withdrawing device, agitator and high-temperature water and steamed coil pipe; Described sealing of tank cover is arranged on the upper end of tank body, is provided with feed pipe on the left of cover, and tank base is provided with discharge nozzle; In the inwall of tank body, be provided with high-temperature water steamed coil pipe, wherein, high-temperature water has steamed coil pipe and has stretched out on the upper left side of tank body, and connects the heating plant of high-temperature vapor, and high-temperature water has steamed coil pipe and stretched out at tank body lower right-hand side, and connects the recovery EGR of steam; Above described cover, centre position is provided with stirring motor, stirring motor drives and connects shaft, and shaft end is fixedly installed agitator, the utility model stirs fully, tool saves the effect of driving force, can be released by saccharified liquid upper strata oil reservoir easily, be conducive to the saccharifying of material by funnel, accelerate the rate of filtration of saccharified liquid, improve the yield of product.
Description
Technical field
The utility model relates to saccharifying tank, specifically a kind of heating saccharifying tank.
Background technology
Saccharifying tank prepares the equipment must used in high fructose corn, malt syrup, and the structure of saccharifying tank directly affects the quality of product.Existing saccharifying tank mainly exists that stirring efficiency is low, heat exchange is insufficient, and the control existing defects of technological parameter, need of production can not be adapted to, and the material such as protein, fat owing to containing in starch, cause in saccharifying, the floating one deck oil film in saccharifying tank liquid level upper strata, had both been unfavorable for the saccharifying of material, had affected again the rate of filtration of saccharified liquid.
Utility model content
It is high that the purpose of this utility model is to provide a kind of production efficiency, and pick up speed is fast, accelerates the heating saccharifying tank of the rate of filtration of saccharified liquid, to solve the problem proposed in above-mentioned background technology.
For achieving the above object, the utility model provides following technical scheme:
A kind of heating saccharifying tank, comprises tank body, cover, saccharified liquid oil film is separated withdrawing device, agitator and high-temperature water and has steamed coil pipe; Described sealing of tank cover is arranged on the upper end of tank body, is provided with feed pipe on the left of cover, and tank base is provided with discharge nozzle; In the inwall of tank body, be provided with high-temperature water steamed coil pipe, wherein, high-temperature water has steamed coil pipe and has stretched out on the upper left side of tank body, and connects the heating plant of high-temperature vapor, and high-temperature water has steamed coil pipe and stretched out at tank body lower right-hand side, and connects the recovery EGR of steam; Above described cover, centre position is provided with stirring motor, and stirring motor drives and connects shaft, and shaft end is fixedly installed agitator, and its opening part is provided with downward-sloping pushing sheet, and agitator madial wall is welded with the stirring vane of downward-sloping setting; The utility model is also provided with saccharified liquid oil film and is separated withdrawing device, saccharified liquid oil film is separated withdrawing device and comprises the support, adjusting nut, screw rod, funnel, wired hose and the drain valve that are positioned at cover outer wall, wherein, adjusting nut is installed in above leg, screw rod is through adjusting nut, support and cover, stretch into tank interior, and connect funnel below screw rod; Funnel lower opening place is communicated with wired hose, the port of export of wired hose stretches out outside tank body, and the port of export of wired hose is also provided with drain valve, in work, by the position of funnel bottom adjusting nut up-down adjustment screw rod, be down to below oil reservoir liquid level the position of funnel, fluid enters in funnel, and external by wired hose drain tank.
Further, described agitator is the rectangular configuration of lower openings.
Further, described stirring vane and vertical direction angle are 30-60 °, agitator be each side provided with staggered two stirring vanes.
Compared with prior art, the beneficial effects of the utility model are:
1, the utility model arranges high-temperature vapor coil pipe, conveniently to saccharifying tank heating, accelerates response speed, enhances productivity;
2, the utility model adopts the agitator stirring frame, change the agitating mode that tradition adopts intermediate rotary shaft, there is the effect stirring fully, save driving force, mixture in saccharifying tank is produced from top to bottom, by the circulation effect of center to both sides, make saccharification react abundant, improve the quality of production efficiency and production product;
3, the utility model is provided with saccharified liquid oil film and is separated withdrawing device, can be released by saccharified liquid upper strata oil reservoir easily, be conducive to the saccharifying of material, accelerate the rate of filtration of saccharified liquid, improve the yield of product by funnel.
Accompanying drawing explanation
Fig. 1 is the structural representation of heating saccharifying tank.
In figure: 1-tank body, 2-cover, 3-feed pipe, 4-discharge nozzle, 5-high-temperature water have steamed coil pipe, 51-heating plant, 52-recovery EGR, 6-stirring motor, the separation of 7-saccharified liquid oil film withdrawing device, 71-adjusting nut, 72-screw rod, 73-funnel, 74-wired hose, 75-drain valve, 76-support, 8-shaft, 9-agitator, 91-stirring vane 92-pushing sheet.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
Refer to Fig. 1, in the utility model embodiment, a kind of heating saccharifying tank, comprises tank body 1, cover 2, saccharified liquid oil film is separated withdrawing device 7, agitator 9 and high-temperature water and has steamed coil pipe 5, described cover 2 sealing is arranged on the upper end of tank body 1, and be provided with feed pipe 3 on the left of cover 2, be provided with discharge nozzle 4 bottom tank body 1, in work, material enters tank body 1 by feed pipe 3, and after reaction terminates, material is by discharge nozzle 4 discharging, in the inwall of tank body 1, be provided with high-temperature water steam coil pipe 5, wherein, high-temperature water has steamed coil pipe 5 and has stretched out on the upper left side of tank body 1, and connect the heating plant 51 of high-temperature vapor, high-temperature water has steamed coil pipe 5 and has stretched out at tank body 1 lower right-hand side, and connect the recovery EGR 52 of steam, in work, heating plant 51 provides the steam of high temperature in coil pipe 5, tank body 1 inside is heated, its efficiency of heating surface is high, firing rate is fast, simple and easy to use, and it is pollution-free, steam after using is by reclaiming EGR 52 recycling, do not cause the waste of resource, economize energy, reduce production cost, above described cover 2, centre position is provided with stirring motor 6, stirring motor 6 drives and connects shaft 8, and shaft 8 end is fixedly installed agitator 9, wherein, agitator 9 is the rectangular configuration of lower openings, and opening part is provided with downward-sloping pushing sheet 92, agitator 9 madial wall is welded with the stirring vane 91 of downward-sloping setting, stirring vane 91 and vertical direction angle are 30-60 °, agitator 9 be each side provided with staggered two stirring vanes 91, in work, indirectly agitator 9 is driven by stirring motor 6, material is fully stirred, the effect of saving driving force can be played, make mixture in saccharifying tank from top to bottom, circulation is carried out to both sides by center, saccharification react is abundant, improve the quality of production efficiency and production product, improve productive rate, the utility model is also provided with saccharified liquid oil film and is separated withdrawing device 7, saccharified liquid oil film is separated withdrawing device 7 and comprises the support 76, adjusting nut 71, screw rod 72, funnel 73, wired hose 74 and the drain valve 75 that are positioned at cover 2 outer wall, wherein, adjusting nut 71 is installed in above leg 76, screw rod 72 is through adjusting nut 71, support 76 and cover 2, stretch into tank body 1 inner, and connect funnel 73 below screw rod 72, funnel 73 lower opening place is communicated with wired hose 74, the port of export of wired hose 74 stretches out outside tank body 1, and the port of export of wired hose 74 is also provided with drain valve 75, in work, by the position of funnel 73 bottom adjusting nut 71 up-down adjustment screw rod 72, the position of funnel 73 is down to below oil reservoir liquid level, fluid enters in funnel 73, and discharge outside tank body 1 by wired hose 74, be conducive to the saccharifying of material, accelerate the rate of filtration of saccharified liquid, improve the yield of product, more time and labour saving.
To those skilled in the art, obvious the utility model is not limited to the details of above-mentioned one exemplary embodiment, and when not deviating from spirit of the present utility model or essential characteristic, can realize the utility model in other specific forms.Therefore, no matter from which point, all should embodiment be regarded as exemplary, and be nonrestrictive, scope of the present utility model is limited by claims instead of above-mentioned explanation, and all changes be therefore intended in the implication of the equivalency by dropping on claim and scope are included in the utility model.Any Reference numeral in claim should be considered as the claim involved by limiting.
In addition, be to be understood that, although this description is described according to embodiment, but not each embodiment only comprises an independently technical scheme, this narrating mode of description is only for clarity sake, those skilled in the art should by description integrally, and the technical scheme in each embodiment also through appropriately combined, can form other embodiments that it will be appreciated by those skilled in the art that.
Claims (3)
1. heat a saccharifying tank, comprise tank body (1), cover (2), saccharified liquid oil film separation withdrawing device (7), agitator (9) and high-temperature water and steamed coil pipe (5), it is characterized in that, described cover (2) sealing is arranged on the upper end of tank body (1), and cover (2) left side is provided with feed pipe (3), and tank body (1) bottom is provided with discharge nozzle (4), in the inwall of tank body (1), be provided with high-temperature water steam coil pipe (5), wherein, high-temperature water has steamed coil pipe (5) and has stretched out on the upper left side of tank body (1), and connect the heating plant (51) of high-temperature vapor, high-temperature water has steamed coil pipe (5) and has stretched out at tank body (1) lower right-hand side, and connects the recovery EGR (52) of steam, stirring motor (6) is provided with in centre position, described cover (2) top, stirring motor (6) drives and connects shaft (8), and shaft (8) end is fixedly installed agitator (9), its opening part is provided with downward-sloping pushing sheet (92), and agitator (9) madial wall is welded with the stirring vane (91) of downward-sloping setting, the utility model is also provided with saccharified liquid oil film and is separated withdrawing device (7), saccharified liquid oil film is separated withdrawing device (7) and comprises the support (76) being positioned at cover (2) outer wall, adjusting nut (71), screw rod (72), funnel (73), wired hose (74) and drain valve (75), wherein, adjusting nut (71) is installed in leg (76) top, screw rod (72) is through adjusting nut (71), support (76) and cover (2), stretch into tank body (1) inner, and screw rod (72) below connects funnel (73), funnel (73) lower opening place is communicated with wired hose (74), the port of export of wired hose (74) stretches out tank body (1) outward, and the port of export of wired hose (74) is also provided with drain valve (75), in work, by the position of adjusting nut (71) up-down adjustment screw rod (72) bottom funnel (73), the position of funnel (73) is down to below oil reservoir liquid level, fluid enters in funnel (73), and discharges tank body (1) outward by wired hose (74).
2. heating saccharifying tank according to claim 1, is characterized in that, the rectangular configuration that described agitator (9) is lower openings.
3. heating saccharifying tank according to claim 1, it is characterized in that, described stirring vane (91) and vertical direction angle are 30-60 °, agitator (9) be each side provided with staggered two stirring vanes (91).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420521560.7U CN204074073U (en) | 2014-09-12 | 2014-09-12 | A kind of heating saccharifying tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420521560.7U CN204074073U (en) | 2014-09-12 | 2014-09-12 | A kind of heating saccharifying tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204074073U true CN204074073U (en) | 2015-01-07 |
Family
ID=52166839
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420521560.7U Expired - Fee Related CN204074073U (en) | 2014-09-12 | 2014-09-12 | A kind of heating saccharifying tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204074073U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106947649A (en) * | 2017-05-22 | 2017-07-14 | 哈尔滨理工大学 | A kind of beer saccharification tank |
-
2014
- 2014-09-12 CN CN201420521560.7U patent/CN204074073U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106947649A (en) * | 2017-05-22 | 2017-07-14 | 哈尔滨理工大学 | A kind of beer saccharification tank |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| DD01 | Delivery of document by public notice |
Addressee: Du Hongmin Document name: Notification of Termination of Patent Right |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150107 Termination date: 20150912 |
|
| EXPY | Termination of patent right or utility model |