CN204079965U - Saccharifying tank produced by a kind of maltose - Google Patents

Saccharifying tank produced by a kind of maltose Download PDF

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Publication number
CN204079965U
CN204079965U CN201420522152.3U CN201420522152U CN204079965U CN 204079965 U CN204079965 U CN 204079965U CN 201420522152 U CN201420522152 U CN 201420522152U CN 204079965 U CN204079965 U CN 204079965U
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CN
China
Prior art keywords
tank body
cover
tank
valve
circulating line
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Expired - Fee Related
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CN201420522152.3U
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Chinese (zh)
Inventor
袁加平
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Individual
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Individual
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Priority to CN201420522152.3U priority Critical patent/CN204079965U/en
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Anticipated expiration legal-status Critical

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Abstract

The utility model discloses a kind of maltose and produce saccharifying tank, comprise tank body, cover, heating interlayer, saccharified liquid oil film separation withdrawing device and agitator motor; Described sealing of tank cover is arranged at the top of tank body, in the left side of cover, sealing is provided with feed pipe, tank base sealing is provided with discharge pipe, feed pipe and discharge pipe are respectively equipped with feed valve and bleeder valve, simultaneously, at tank body external wall beneath, place is provided with the impeller pump communicated with circulating line, and the pan feeding port of circulating line is sealedly attached to the below of tank body, and the discharging port of circulating line is connected on the sidewall of the feed pipe between feed valve and cover; The utility model mixing effect is strong, and heats is good, more fully mixture, is released by saccharified liquid upper strata oil reservoir easily, accelerates the filtration velocity of saccharified liquid, improve the yield of product, improve working efficiency by funnel.

Description

Saccharifying tank produced by a kind of maltose
Technical field
The utility model relates to saccharifying tank, and specifically saccharifying tank produced by a kind of maltose.
Background technology
Saccharifying tank prepares the equipment must used in high fructose syrup, malt syrup, and the structure of saccharifying tank directly affects the quality of product.
Saccharifying tank during the fermentation, need to carry out heating and cooling according to the needs of microorganism to the saccharifying tank producing maltose, in addition, in order to accelerate fermenting speed, also need to stir fermented liquid, existing saccharifying tank stirring efficiency is low, heat exchange is insufficient, 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 filtration velocity of saccharified liquid.
Utility model content
The purpose of this utility model is to provide that a kind of mixing effect is good, heat exchange efficiency is high, and the maltose effectively improving mashing process produces saccharifying tank, to solve the problem proposed in above-mentioned background technology.
For achieving the above object, the utility model provides following technical scheme:
Saccharifying tank produced by a kind of maltose, comprises tank body, cover, heating interlayer, saccharified liquid oil film separation withdrawing device and agitator motor; Described sealing of tank cover is arranged at the top of tank body, in the left side of cover, sealing is provided with feed pipe, tank base sealing is provided with discharge pipe, feed pipe and discharge pipe are respectively equipped with feed valve and bleeder valve, simultaneously, at tank body external wall beneath, place is provided with the impeller pump communicated with circulating line, and the pan feeding port of circulating line is sealedly attached to the below of tank body, and the discharging port of circulating line is connected on the sidewall of the feed pipe between feed valve and cover; Outside at described tank body, be provided with the heating interlayer for heating, heating interlayer is provided with the high-temperature vapor import be connected with supplying heat source being positioned at position, tank body upper left side; The position that heating interlayer is being positioned at tank base is provided with water port, and wherein, high-temperature vapor import is provided with check valve; Described cover is provided with agitator motor, and agitator motor drives and connects stir shaft, and stir shaft, through cover, stretches into tank interior, and stir shaft is provided with the stirring rake how group tilts, and stirring rake and stir shaft have certain angle; 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, setting nut, screw rod, funnel, wired hose and the drain valve that are positioned at cover outer wall, wherein, setting nut is installed in above leg, screw rod is through setting nut, support and cover, stretch into tank interior, and connect funnel below screw rod; Funnel lower opening place is communicated with wired hose, and the exit end of wired hose stretches out outside tank body, and the exit end of wired hose is also provided with drain valve.
Further, the angle of described stirring rake and stir shaft is acute angle, and angular range is 30-50 °.
Further, described tank body upper inner wall is provided with two ultraviolet germicidal lamps.
Compared with prior art, the beneficial effects of the utility model are:
1, the utility model is provided with stirring rake, stirring rake and the acute angle folded by stir shaft are 30-50 °, strengthen mixing effect, liquid stream is reasonable, make stirring rake become existing radial flow from pure radial flow form and also have axial flow form, better can disperse, mix, mass transfer and heat transfer, effectively improve mashing process, the Matter Transfer pipeline simultaneously arranged, can mixture more fully;
2, the utility model is provided with heating interlayer, is provided with the high-temperature vapor import be connected with supplying heat source above it, and heated saccharifying tank by high-temperature vapor logical in heating interlayer, heating is convenient, and heats is good, improves working efficiency;
3, the utility model is provided with ultraviolet lamp and can opens when needs sterilization, reach decontaminating liquid object, simultaneously, tank interior is provided with saccharified liquid oil film and is separated withdrawing device, easily saccharified liquid upper strata oil reservoir is released by funnel, be conducive to the saccharifying of material, accelerate the filtration velocity of saccharified liquid, improve the yield of product, more time and labour saving.
Accompanying drawing explanation
Fig. 1 is the structural representation that saccharifying tank produced by maltose.
In figure: 1-tank body, 2-cover, 3-feed pipe, 31-feed valve, 32-circulating line, 33-valve, 34-impeller pump, 4-discharge pipe, 41-bleeder valve, 5-heating interlayer, the import of 51-high-temperature vapor, 52-water port, 53-check valve, 6-agitator motor, 7-saccharified liquid oil film are separated withdrawing device, 71-setting nut, 72-screw rod, 73-funnel, 74-wired hose, 75-drain valve, 76-support, 8-stir shaft, 9-stirring rake, 10-ultraviolet germicidal lamp.
Embodiment
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, saccharifying tank produced by a kind of maltose, comprises tank body 1, cover 2, heating interlayer 5, saccharified liquid oil film separation withdrawing device 7 and agitator motor 6, described cover 2 sealing is arranged at the top of tank body 1, in the left side of cover 2, sealing is provided with feed pipe 3, tank body 1 sealed bottom is provided with discharge pipe 4, feed pipe 3 and discharge pipe 4 are respectively equipped with feed valve 31 and bleeder valve 41, simultaneously, the impeller pump 34 communicated with circulating line 32 is provided with at tank body 1 external wall beneath place, and the pan feeding port of circulating line 32 is sealedly attached to the below of tank body 1, the discharging port of circulating line 32 is connected to the sidewall of the feed pipe 3 between feed valve 31 and cover 2, and circulating line 32 is provided with valve 33, during work, material is entered by the feed pipe 3 above tank body 1, during discharging, material is by discharge pipe 4 discharging below tank body 1, in the course of processing, material can also pass through circulating line 32, the material be positioned at bottom tank body 1 is extracted out, and material is fallen in tank body 1 by the feed pipe 3 above tank body 1, material is fully mixed, enhance productivity, outside at described tank body 1, be provided with the heating interlayer 5 for heating, heating interlayer 5 is provided with the high-temperature vapor import 51 be connected with supplying heat source being positioned at position, tank body 1 upper left side, and by high-temperature vapor import 51 logical high-temperature vapor in heating interlayer 5, thus saccharifying tank tank body 1 inside is heated, suitable temperature is provided in reaction process, enhances productivity, accelerate speed of response in tank, heating interlayer 5 is provided with water port 52 being positioned at the position bottom tank body 1, and the water of water vapour liquefaction in heating interlayer 5 can be discharged heating interlayer 5 by water port 52, and wherein, high-temperature vapor import 51 is provided with check valve 53, described cover 2 is provided with agitator motor 6, agitator motor 6 drives and connects stir shaft 8, stir shaft 8 is through cover 2, stretch into tank body 1 inner, and stir shaft 8 is provided with the stirring rake 9 of many group inclinations, stirring rake 9 and stir shaft 8 have certain angle, its angle is acute angle, angular range is 30-50 °, in work, stirring rake 9 rotates, strengthen mixing effect, liquid stream is reasonable, and stirring rake becomes existing radial flow from pure radial flow form also axial flow form, can better disperse, mixing, mass transfer and heat transfer, effectively improve the technological process of saccharification, 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, setting nut 71, screw rod 72, funnel 73, wired hose 74 and the drain valve 75 that are positioned at cover 2 outer wall, wherein, setting nut 71 is installed in above leg 76, screw rod 72 is through setting 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 exit end of wired hose 74 stretches out outside tank body 1, and the exit end of wired hose 74 is also provided with drain valve 75, in work, by the position of funnel 73 bottom setting 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 filtration velocity of saccharified liquid, improve the yield of product, more time and labour saving, described tank body 1 upper inner wall is provided with two ultraviolet germicidal lamps 10, opens, reach decontaminating liquid object when needs sterilization.
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 specification sheets is described according to embodiment, but not each embodiment only comprises an independently technical scheme, this narrating mode of specification sheets is only for clarity sake, those skilled in the art should by specification sheets 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. a saccharifying tank produced by maltose, comprises tank body (1), cover (2), heating interlayer (5), saccharified liquid oil film separation withdrawing device (7) and agitator motor (6), it is characterized in that, described cover (2) sealing is arranged at the top of tank body (1), in the left side of cover (2), sealing is provided with feed pipe (3), tank body (1) sealed bottom is provided with discharge pipe (4), feed pipe (3) and discharge pipe (4) are respectively equipped with feed valve (31) and bleeder valve (41), simultaneously, the impeller pump (34) communicated with circulating line (32) is provided with at tank body (1) external wall beneath place, and the pan feeding port of circulating line (32) is sealedly attached to the below of tank body (1), the discharging port of circulating line (32) is connected on the sidewall of the feed pipe (3) be positioned between feed valve (31) and cover (2), and circulating line (32) is provided with valve 33, outside at described tank body (1), be provided with the heating interlayer (5) for heating, heating interlayer (5) is provided with the high-temperature vapor import (51) be connected with supplying heat source being positioned at tank body (1) position, upper left side, the position that heating interlayer (5) is being positioned at tank body (1) bottom is provided with water port (52), and wherein, high-temperature vapor import (51) is provided with check valve (53), described cover (2) is provided with agitator motor (6), agitator motor (6) drives and connects stir shaft (8), stir shaft (8) is through cover (2), stretch into tank body (1) inner, and stir shaft (8) being provided with the stirring rake (9) of many group inclinations, stirring rake (9) and stir shaft (8) have certain angle, 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, setting nut (71), screw rod (72), funnel (73), wired hose (74) and drain valve (75), wherein, setting nut (71) is installed in leg (76) top, screw rod (72) is through setting 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 exit end of wired hose (74) stretches out tank body (1) outward, and the exit end of wired hose (74) is also provided with drain valve (75).
2. saccharifying tank produced by maltose according to claim 1, it is characterized in that, described stirring rake (9) is acute angle with the angle of stir shaft (8), and angular range is 30-50 °.
3. saccharifying tank produced by maltose according to claim 1, and it is characterized in that, described tank body (1) upper inner wall is provided with two ultraviolet germicidal lamps (10).
CN201420522152.3U 2014-09-12 2014-09-12 Saccharifying tank produced by a kind of maltose Expired - Fee Related CN204079965U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420522152.3U CN204079965U (en) 2014-09-12 2014-09-12 Saccharifying tank produced by a kind of maltose

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420522152.3U CN204079965U (en) 2014-09-12 2014-09-12 Saccharifying tank produced by a kind of maltose

Publications (1)

Publication Number Publication Date
CN204079965U true CN204079965U (en) 2015-01-07

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Family Applications (1)

Application Number Title Priority Date Filing Date
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106362669A (en) * 2016-12-01 2017-02-01 郑州游爱网络技术有限公司 Heat exchange saccharifying tank
CN106544450A (en) * 2016-12-09 2017-03-29 陈彦羽 A kind of circulating sugar mill
CN106754246A (en) * 2016-12-09 2017-05-31 南宁市黑晶信息技术有限公司 A kind of sugar refining technology energy saver
CN106947649A (en) * 2017-05-22 2017-07-14 哈尔滨理工大学 A kind of beer saccharification tank

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106362669A (en) * 2016-12-01 2017-02-01 郑州游爱网络技术有限公司 Heat exchange saccharifying tank
CN106544450A (en) * 2016-12-09 2017-03-29 陈彦羽 A kind of circulating sugar mill
CN106754246A (en) * 2016-12-09 2017-05-31 南宁市黑晶信息技术有限公司 A kind of sugar refining technology energy saver
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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C14 Grant of patent or utility model
GR01 Patent grant
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