CN2898036Y - Starch sugar liquefier - Google Patents
Starch sugar liquefier Download PDFInfo
- Publication number
- CN2898036Y CN2898036Y CN 200520146821 CN200520146821U CN2898036Y CN 2898036 Y CN2898036 Y CN 2898036Y CN 200520146821 CN200520146821 CN 200520146821 CN 200520146821 U CN200520146821 U CN 200520146821U CN 2898036 Y CN2898036 Y CN 2898036Y
- Authority
- CN
- China
- Prior art keywords
- laminar flow
- fluid inlet
- liquid outlet
- flow jar
- utility
- 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
Images
Landscapes
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
The utility model relates to a liquefying device, substantially that relates to starch sugar production liquefying equipment, comprising a laminar flow tank, the laminar tank is provided with a liquid inlet and a liquid outlet, the liquid inlet is arranged at the lower part of the laminar flow tank, the liquid outlet is arranged at the upper part of the laminar flow tank. The utility model has the advantage of that the utility model can effiectivly make flocculation and dispersion of protein and can prevent the protein from accumulating to result in the block of pipeline and the color of syrup from becoming dark so as to improve the production capacity and quality of syrup, and reduce the consumption of raw materials, so that the liquefication is more thorough and the saccharification is more complete and the conversion ratio is high, so the utility model can be used for large scale continuous production.
Description
Technical field
The utility model relates to a kind of liquefying plant, specifically, relates to a kind of liquefaction device of Dian Fentang.
Background technology
Traditional " laminar flow insulation " equipment, feed liquid be from enterprising under go out, this mode has many shortcomings in practice.
Because after once spraying, it is lighter to solidify the protein floss that in the feed liquid, after the top enters the laminar flow jar, often floating and gathering at tank deck, the very easy pipe blocking that causes is made troubles to operation; Easily aging, the variable color of albumen throw out at tank deck simultaneously causes feed liquid colourity to raise, and brings difficulty for afterwards filtration, decolouring; Influence " saccharification " and the quality of product thereafter.
Summary of the invention
The utility model overcomes above-mentioned defective, provide a kind of feed liquid can be in the laminar flow jar liquefaction device of " low in and high out ".
The technical solution of the utility model is such: it comprises the laminar flow jar, and the laminar flow jar is provided with fluid inlet and liquid outlet, and fluid inlet is arranged on the below of laminar flow jar, and liquid outlet is arranged on the top of laminar flow jar.
The laminar flow jar is set to two or more, and adjacent laminar flow jar fluid inlet links to each other with liquid outlet, and fluid inlet also links to each other with fluid inlet.
Between the fluid inlet of adjacent laminar flow jar and the fluid inlet stopping valve is set, stopping valve also is set between liquid outlet and the fluid inlet.
The liquid outlet setting of last laminar flow jar is connected with temporary storage tank.
Dian Fentang of the present utility model liquefaction equipment can make protein flocculation and dispersion effect good, can prevent that protein accumulation from causing pipeline obstruction and syrup to darken, thereby improve syrupy output and quality, reduce raw materials consumption, make liquefaction more thorough, saccharification is more complete, transformation efficiency height, but large scale continuous prod.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Embodiment
Embodiment 1:
As shown in the figure, Dian Fentang liquefaction equipment of the present utility model comprises 5 laminar flow jars 1, the fluid inlet 4 of laminar flow jar 1 is arranged on the below, liquid outlet 5 is arranged on the top, adjacent laminar flow jar fluid inlet all links to each other with fluid inlet, fluid inlet and liquid outlet and is provided with stopping valve, and in the end the liquid outlet place of a laminar flow jar is provided with a temporary storage tank 6.
Liquefaction device of the present utility model is because fluid inlet 4 is arranged on the below of laminar flow jar 1, liquid outlet 5 is arranged on the top of laminar flow jar 1, adopted " low in and high out " layer flow mode, protein and starch good separating effect, flocculating effect is good, and throw out does not reassociate, but the stable liquid outlet by laminar flow jar 1 top enters next laminar flow jar after overflowing, no longer make pipeline obstruction, throw out is weather stain no longer; Thereby improve syrupy output and quality, reduce raw materials consumption, make liquefaction more thorough; Liquefaction device of the present utility model is provided with 5 laminar flow jars, realized that continuous liquefied mass melts the beginning from a hydrojet and is incubated through laminar flow jar laminar flow, adverse current, contact are uniformly dispersed starch chain repeatedly, fully contact and act on zymin, work continuously, improve the liquefaction effect greatly, guaranteed saccharification quality and transformation efficiency thereafter and can realize scale operation; And connect between the fluid inlet of laminar flow jar and laminar flow jar and be provided with stopping valve 3, the fluid inlet of laminar flow jar and liquid outlet place also are provided with stopping valve 2, even so wherein there is the laminar flow jar to damage, the operation of liquefying of the laminar flow jar that also can avoid damaging can also freely select to carry out several sublayer laminars insulations.
Embodiment 2:
The difference of present embodiment and embodiment 1 is that present embodiment is provided with 4 laminar flow jars, and present embodiment can carry out the laminar flow insulation below four times.
Claims (4)
1, a kind of Dian Fentang is produced liquefaction device, and it comprises laminar flow jar (1), and laminar flow jar (1) is provided with fluid inlet and liquid outlet, it is characterized in that: fluid inlet (4) is arranged on the below of laminar flow jar, and liquid outlet (5) is arranged on the top of laminar flow jar.
2, Dian Fentang according to claim 1 is produced liquefaction device, and it is characterized in that: laminar flow jar (1) is set to two or more, and adjacent laminar flow jar fluid inlet links to each other with liquid outlet, and fluid inlet also links to each other with fluid inlet.
3, Dian Fentang according to claim 2 is produced liquefaction device, it is characterized in that: stopping valve (3) is set between the fluid inlet of adjacent laminar flow jar and the fluid inlet, stopping valve (2) also is set between liquid outlet and the fluid inlet.
4, Dian Fentang according to claim 3 is produced liquefaction device, and it is characterized in that: the liquid outlet setting of last laminar flow jar is connected with temporary storage tank (6).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200520146821 CN2898036Y (en) | 2005-12-23 | 2005-12-23 | Starch sugar liquefier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200520146821 CN2898036Y (en) | 2005-12-23 | 2005-12-23 | Starch sugar liquefier |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2898036Y true CN2898036Y (en) | 2007-05-09 |
Family
ID=38073372
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200520146821 Expired - Fee Related CN2898036Y (en) | 2005-12-23 | 2005-12-23 | Starch sugar liquefier |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2898036Y (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102516354A (en) * | 2011-11-17 | 2012-06-27 | 玉锋实业集团有限公司 | Separation method and equipment of protein from starch sugar liquefied solution |
-
2005
- 2005-12-23 CN CN 200520146821 patent/CN2898036Y/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102516354A (en) * | 2011-11-17 | 2012-06-27 | 玉锋实业集团有限公司 | Separation method and equipment of protein from starch sugar liquefied solution |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN2898036Y (en) | Starch sugar liquefier | |
CN201518692U (en) | Movable nitrogen charging and oxygen reducing device adopting membrane method for granaries | |
CN1899665A (en) | Belt type pressure filter | |
CN102285658B (en) | Multistage fully thermally coupled rectification production device and process method for preparing ultra-pure trichlorosilane | |
CN203227342U (en) | Grading filtration device applied to alcohol production | |
CN201186204Y (en) | Machine for cleaning and testing reverse osmosis membrane | |
CN2794194Y (en) | Pneumatic stone remover for longan | |
CN208232376U (en) | A kind of full-automatic camellia oil filter-pressing device | |
CN203947088U (en) | Coal-seam gas purification system molecular sieve drying tower and drying tower group | |
CN202410342U (en) | Filtering device capable of continuous production | |
CN2566935Y (en) | Modular structure of pressure changing adsorbent air separator | |
CN205152165U (en) | Carbon dioxide separator is deviate from to supersonic speed natural gas | |
CN200957323Y (en) | Belt pressurized filter | |
CN2808809Y (en) | Tank body for transportation tank vehicle | |
CN101100292A (en) | Composite film separation nitrogen-preparing system and method for well drilling technique | |
CN202225418U (en) | Vacuum device for double-screw extruder | |
CN207608539U (en) | A kind of grape wine adjuvant adding device | |
CN206337273U (en) | Liquefied starch continuous conversion equipment | |
CN206375757U (en) | A kind of power-free back washing super-filter purifying device | |
CN2484098Y (en) | Efficient multi-downspout column plate | |
CN102516354A (en) | Separation method and equipment of protein from starch sugar liquefied solution | |
CN2741633Y (en) | Oil-water separator | |
CN115854155A (en) | Improved structure of steam power plant for externally supplying steam main pipeline | |
CN1028304C (en) | Storage and transportation of viscous oil mixture | |
CN217600665U (en) | System for improve coalescence dehydrator water oil separating effect |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |