CN203715645U - High-pressure jet continuous liquefier for maltose and glucose syrup processing - Google Patents
High-pressure jet continuous liquefier for maltose and glucose syrup processing Download PDFInfo
- Publication number
- CN203715645U CN203715645U CN201420043390.6U CN201420043390U CN203715645U CN 203715645 U CN203715645 U CN 203715645U CN 201420043390 U CN201420043390 U CN 201420043390U CN 203715645 U CN203715645 U CN 203715645U
- Authority
- CN
- China
- Prior art keywords
- liquefying
- jet
- starch
- pipe
- tank
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Abstract
The utility model discloses a high-pressure jet continuous liquefier for maltose and glucose syrup processing. The high-pressure jet continuous liquefier comprises a liquefying tank and a jet, wherein a feed pipe and an S-shaped discharge pipe are respectively arranged at the upper end and the lower end of the liquefying tank; the liquefying tank is connected to the jet through the feeding pipe; a steam inlet pipe is arranged on the liquefying tank; a high pressure steam pump is connected on the steam inlet pipe; below a material inlet, a distribution drum is arranged in the liquefying tank; the liquefying tank is connected to a liquefied material storage tank through the S-shaped discharge pipe. The continuous liquefier disclosed by the utility model has the following advantages: 1. through the distribution drum, starch milk in which amylase is added from the jet is completely mixed with high pressure steam, insoluble starch particles are avoided, and liquefied liquid is clear and transparent; 2. through the S-shaped discharge pipe, reaction time after jetting starch is delayed, a hydrolysis efficiency of the starch under an enzymatic catalysis action is enhanced, and a liquefying effect is improved.
Description
Technical field
The utility model relates to maltose, is produced from technical equipment field in glucose syrup processing, and what be specifically related to is a kind of continuous liquefier of high pressure spraying for maltose, glucose syrup processing.
Background technology
Rice grinds in process processed can produce cracking rice of 10%-30% conventionally, due to factors such as the hardness of cracking rice is low, the starch of cracking rice is soluble in water and crack rice gelatinization degree height, cracks rice and is seldom used directly to cooking rice.Start to utilize in some countries crack rice exploitation rice starch, rice gluten, β-amylose product at present, realized the abundant increment utilization to the resource of cracking rice.Wherein malt syrup, high fructose syrup are made with rice starch hydrolysis or hydrolysis isomerization.
Cracking rice, it is similar to prepare the technique of malt syrup and glucose syrup, be all crack rice through soaking, mill rice liquefies after sizing mixing, de-slag, saccharification, decolouring, filters, concentrated, finally canned, wherein liquefaction is extremely crucial step.At present, enterprise generally liquefies to malt syrup, glucose syrup with Jet liquefier, but existing Jet liquefier is because of cost-saving, and compacted starch shelf-time in liquefier as far as possible, it is not very desirable causing liquefaction effect.
Utility model content
The deficiency existing in order to overcome above-mentioned technology, technical problem to be solved in the utility model is to provide the continuous liquefier of high pressure spraying for maltose, glucose syrup processing that a kind of mixing of materials is more even, liquefaction effect is good.
The technical solution of the utility model is: a kind of continuous liquefier of high pressure spraying for maltose, glucose syrup processing, comprise liquefied pot, injector, the upper and lower end of described liquefied pot is respectively equipped with feed-pipe, snakelike discharge nozzle, liquefied pot connects injector by feed-pipe, liquefied pot is provided with steam inlet tube, on steam inlet tube, be connected with high pressure steam pump, be provided with material distribution cartridge below being positioned at opening for feed in liquefied pot, liquefied pot connects liquefaction storage tank by snakelike discharge nozzle.
Advantage of the present utility model: 1, material distribution cartridge makes the diastatic starch milk that is added with gushing out from injector, fully mixes with high pressure steam, does not produce insoluble starch particle, and liquefier is limpid transparent; 2, snakelike discharge nozzle has delayed the reaction times after starch injection, has strengthened the hydrolysis efficiency of starch under enzyme catalysis, and liquefaction effect is better.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Embodiment
Now by reference to the accompanying drawings, technology contents of the present utility model is described further.
In Fig. 1, a kind of continuous liquefier of high pressure spraying for maltose, glucose syrup processing, comprise liquefied pot 1, injector 2, the upper and lower end of described liquefied pot 1 is respectively equipped with feed-pipe 3, snakelike discharge nozzle 4, liquefied pot 1 connects injector 2 by feed-pipe 3, and liquefied pot 1 is provided with steam inlet tube 5, is connected with high pressure steam pump 6 on steam inlet tube 5, be positioned at opening for feed in liquefied pot 1 below, be provided with material distribution cartridge 7, liquefied pot 1 connects liquefaction storage tank 8 by snakelike discharge nozzle 4.Material distribution cartridge makes the diastatic starch milk that is added with gushing out from injector, fully mixes with high pressure steam, does not produce insoluble starch particle, and liquefier is limpid transparent; Snakelike discharge nozzle has delayed the reaction times after starch injection, has strengthened the hydrolysis efficiency of starch under enzyme catalysis, and liquefaction effect is better.
Claims (1)
1. one kind for maltose, the continuous liquefier of high pressure spraying of glucose syrup processing, comprise liquefied pot (1), injector (2), described liquefied pot (1) upper, lower end is respectively equipped with feed-pipe (3), snakelike discharge nozzle (4), liquefied pot (1) connects injector (2) by feed-pipe (3), liquefied pot (1) is provided with steam inlet tube (5), on steam inlet tube (5), be connected with high pressure steam pump (6), in liquefied pot (1), be positioned at opening for feed below and be provided with material distribution cartridge (7), liquefied pot (1) connects liquefaction storage tank (8) by snakelike discharge nozzle (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420043390.6U CN203715645U (en) | 2014-01-24 | 2014-01-24 | High-pressure jet continuous liquefier for maltose and glucose syrup processing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420043390.6U CN203715645U (en) | 2014-01-24 | 2014-01-24 | High-pressure jet continuous liquefier for maltose and glucose syrup processing |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203715645U true CN203715645U (en) | 2014-07-16 |
Family
ID=51154813
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420043390.6U Expired - Fee Related CN203715645U (en) | 2014-01-24 | 2014-01-24 | High-pressure jet continuous liquefier for maltose and glucose syrup processing |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203715645U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104498560A (en) * | 2014-12-23 | 2015-04-08 | 开封市四达农产品设备有限公司 | Liquefaction process and liquefaction equipment of glucose syrup |
| CN105543063A (en) * | 2016-03-04 | 2016-05-04 | 新疆笑厨食品有限公司 | Steam ejector for vinegar production |
| CN106399594A (en) * | 2016-11-30 | 2017-02-15 | 无锡甜丰食品有限公司 | Steam atomization ring of spray atomization device for syrup preparation |
-
2014
- 2014-01-24 CN CN201420043390.6U patent/CN203715645U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104498560A (en) * | 2014-12-23 | 2015-04-08 | 开封市四达农产品设备有限公司 | Liquefaction process and liquefaction equipment of glucose syrup |
| CN105543063A (en) * | 2016-03-04 | 2016-05-04 | 新疆笑厨食品有限公司 | Steam ejector for vinegar production |
| CN106399594A (en) * | 2016-11-30 | 2017-02-15 | 无锡甜丰食品有限公司 | Steam atomization ring of spray atomization device for syrup preparation |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203715645U (en) | High-pressure jet continuous liquefier for maltose and glucose syrup processing | |
| CN109694891B (en) | Method for continuously producing starch saccharification product by using high-concentration starch milk | |
| CN205258484U (en) | Preparation glucose syrup in -process of cracking rice sprays continuous liquefier | |
| CN103276021B (en) | Pretreatment method of potato raw materials | |
| CN211771337U (en) | System for utilize starchy material and cellulose raw materials preparation ethanol | |
| CN101948876A (en) | Method for preparing ethanol through fermentation of cassava | |
| CN101693911A (en) | Liquor cleaning process for refining sugar from corns | |
| CN203635187U (en) | High-efficiency reaction kettle | |
| CN105755069A (en) | Method using corn cobs to prepare xylo-oligosaccharide | |
| CN203072835U (en) | Syrup heater | |
| CN101948875A (en) | Method for preparing ethanol by low-temperature digestion and thick mash fermentation of starch as raw material | |
| CN201295553Y (en) | Deep cone thickener | |
| CN101988031B (en) | Device for preparing ethanol | |
| CN210945551U (en) | Jet liquefier | |
| CN210103972U (en) | Starchy raw material liquid saccharification economizer | |
| CN105543063A (en) | Steam ejector for vinegar production | |
| CN105838754B (en) | Enzyme method secondary circulation jet liquefaction process and liquefaction system | |
| CN205616907U (en) | A liquefaction system that is used for enzyme process a lot of jetting fluid chemical industry to plant | |
| CN202497862U (en) | High-pressure feeding reaction kettle | |
| CN204211724U (en) | A kind of feeding unit making yellow rice wine | |
| CN203582870U (en) | Starch liquefaction device | |
| CN203900064U (en) | Water inlet structure of ultrasonic cleaning tank | |
| CN204325326U (en) | Make the device of yellow rice wine | |
| CN204455091U (en) | The liquefaction device of glucose syrup | |
| CN203715649U (en) | Continuous saccharification reactor for preparing high fructose corn syrup and malt syrup from broken rice |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20140716 Termination date: 20170124 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |