CN201678654U - Inclined fermentation stopping tank - Google Patents
Inclined fermentation stopping tank Download PDFInfo
- Publication number
- CN201678654U CN201678654U CN2010201650911U CN201020165091U CN201678654U CN 201678654 U CN201678654 U CN 201678654U CN 2010201650911 U CN2010201650911 U CN 2010201650911U CN 201020165091 U CN201020165091 U CN 201020165091U CN 201678654 U CN201678654 U CN 201678654U
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- CN
- China
- Prior art keywords
- tank body
- tank
- steam
- yeast
- killing
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- 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
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Abstract
The utility model discloses an inclined fermentation stopping tank, which comprises a tank body. The top and bottom of the tank body are respectively provided with a feeding port and a discharging port, and the tank body is obliquely arranged on a bracket and is provided with a steam feeding pipe communicated with the inside of the tank body. Since the outer surface of the tank body obliquely arranged on the bracket is provided with the steam feeding pipe communicated with the inside of the tank body, the steam feeding pipe is used for feeding steam into the tank body, and the sprayed steam is uniform, the utility model not only ensures the amount of the steam for fermentation stopping of raw materials, thereby ensuring the uniformity of the fermentation stopping of the raw materials, but also effectively improves the automatic flow of the raw materials so that the raw materials can fall down slowly, thereby preventing the bridging of the raw materials, making the material discharging smooth and uniform, greatly lowering the labor intensity of workers, and improving the production efficiency.
Description
Technical field
The utility model belongs to the oily equipment technical field of system, particularly a kind of inclined yeast-killing tank.
Background technology
At present, the yeast-killing tank that the oil mill uses adopts the one-sided discharging form of bottom level, the raw material ratio that ferment is crossed owing to stop is softer, the denser of piling up mutually, pushing, self drainage is poor, is easy to generate the bridging phenomenon, cause the blanking difficulty, material must be manually taken off in perhaps not blanking, and continuing of could guaranteeing to produce carries out.There is following defective in above-mentioned yeast-killing tank: labour intensity is big, and blanking is inhomogeneous, and production process is intermittent, and what be difficult to guarantee to produce normally carries out, and production efficiency is low.
The utility model content
The purpose of this utility model provides the inclined yeast-killing tank that a kind of labour intensity is low, blanking is even, production efficiency is high.
For achieving the above object, the technical solution of the utility model is: a kind of inclined yeast-killing tank, comprise tank body, and tank body top and bottom are respectively equipped with opening for feed, discharge port, and described tank body is obliquely installed on support, and tank body is provided with the steam inlet pipe that communicates with its inside.
Described tank body is made of tank body epimere and tank body hypomere, and the upper edge of the lower edge of tank body epimere and tank body hypomere is tightly connected, and the angle α of the axis of tank body epimere and horizontal plane is 45 °-80 °, and the axis angle β of tank body epimere and tank body hypomere is 90 °-175 °.
Described discharge port is arranged on the bottom of tank body hypomere, and the discharge port outer end is provided with quick operating valve.
Described quick operating valve inside is filled with light filler, and light filler top is provided with cover plate.
The downside of described tank body hypomere is provided with liquid collecting bucket, and the tank body hypomere corresponding with liquid collecting bucket partly offers filter opening or be provided with filter screen.
Described steam inlet pipe axially is provided with, and many steam inlet pipes are distributed on the tank wall, and the steam coils of encircling tank body is between the upper and lower every setting, and steam inlet pipe is connected with steam coils.
The radian of described steam coils increases from top to bottom gradually.
Described tank body epimere and tank body hypomere intersection are provided with a plurality of steam jets that tilt to the tank interior below, and the steam jet outer end links to each other with steam coils.
Compared with prior art, the utility model has the advantages that:
1, the tank body outside surface that is obliquely installed on support is provided with the steam inlet pipe that communicates with its inside, in tank body, feed steam by steam inlet pipe, the steam uniformity that sprays into had both guaranteed the stop quantity of steam of ferment of raw material, made the raw material ferment of stopping even, effectively improve the raw material self drainage again, raw material is slowly fallen, avoid occurring raw material bridging phenomenon, blanking is smooth and easy, even, greatly reduce working strength of workers, improved production efficiency.
2, tank body is made of tank body epimere and tank body hypomere, the axis angle β of tank body epimere and tank body hypomere is 90 °-175 °, the height of drop of material is reduced, reduced the impact of material tank body, blanking is even, smooth and easy, accumulation, the caking of avoiding raw material to fall to causing simultaneously reduce the blanking difficulty.
3, at the inner light filling stopping composition of quick operating valve and add a cover cover plate, when raw material fell on the quick operating valve, light filler and cover plate played shock absorption to raw material, and the protection quick operating valve is avoided damaging, and prolongs its work-ing life.
4, corresponding with liquid collecting bucket tank body part offers filter opening or is provided with filter screen, can effectively prevent that raw material from falling in the liquid collecting bucket effective the discharge in the tank body in the liquid.
5, steam inlet pipe is connected with the steam coils of encircling tank body, by the steam coils unification to steam inlet pipe for steam, spray into a jar intravital steam uniformity, guarantee the stop quantity of steam of ferment of raw material, make the raw material ferment of stopping even, improved production efficiency; Because a jar intravital feed distribution is last few many down, steam coils extends from top to bottom gradually along the tank body axis, and steam is fully used, and has both saved steam and has supplied with, and alleviates the discharge opeing burden of liquid collecting bucket again.
6, be provided with a plurality of steam jets that below tank interior, tilt at tank body epimere and tank body hypomere intersection, both can guarantee the stop quantity of steam of ferment of raw material, bonding and the raw material that is deposited on the tank body hypomere inwall in time can be washed out again, effectively prevent raw material be deposited in jar at the bottom of and on the plate that connects material, guarantee the continuity of blanking.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Embodiment
Inclined yeast-killing tank as shown in Figure 1, it comprises tank body, and described tank body is made of tank body epimere 1 and tank body hypomere 2, and tank body epimere 1 top and tank body hypomere 2 bottoms are respectively equipped with opening for feed 3 and discharge port 4, and tank body is obliquely installed on support 5.The upper edge of the lower edge of tank body epimere 1 and tank body hypomere 2 is tightly connected, and the angle α of the axis of tank body epimere 1 and horizontal plane is 45 °-80 °, and tank body epimere 1 is 90 °-175 ° with the axis angle β of tank body hypomere 2.
Tank body epimere 1 and tank body hypomere 2 are provided with steam inlet pipe 6, and steam inlet pipe 6 axially is provided with, and many steam inlet pipes 6 are distributed on the tank wall, and the steam coils 7 of encircling tank body is between the upper and lower every setting, and steam inlet pipe 6 is connected with steam coils 7.Because it is many more that the downward more raw material of tank interior is piled up, the radian of steam coils 7 increases from top to bottom gradually, guarantee the stop quantity of steam of ferment of raw material, improve the raw material self drainage, make raw material landing downwards smoothly, particular case is: tank body epimere 1 outer wall is provided with four steam coilss 7, and its radian is respectively 209 °, 239 °, 269 ° and 350 °; Be provided with a steam coils 7 in the middle and lower part of tank body hypomere 2, the radian of steam coils 7 is 350 °.
For preventing that raw material is deposited in tank body epimere 1 and tank body hypomere 2 intersections, be provided with a plurality of steam jets that below tank interior, tilt 8 at tank body epimere 1 and tank body hypomere 2 intersections, steam jet 8 outer ends are connected with steam coils 9.
On the discharge port 4 of tank body hypomere 2 bottoms, be provided with quick operating valve 10; be filled with light filler 11 in quick operating valve 10 inside; light filler 11 tops are provided with cover plate 12; when raw material falls on the quick operating valve 10; 12 pairs of raw materials of light filler 11 and cover plate play shock absorption, and protection quick operating valve 10 is avoided damaging.
The downside of tank body hypomere 2 and the discharge port 4 adjacent liquid collecting buckets 13 that are provided with, liquid collecting bucket 13 bottoms are provided with leakage fluid dram 14, the tank body part corresponding with liquid collecting bucket 13 offers filter opening or is provided with filter screen 15, fall in the liquid collecting bucket 13 to prevent raw material, and the effective intravital liquid of drain tank.
In the present embodiment, the angle α of the axis of tank body epimere 1 and horizontal plane is 60 °, and tank body epimere 1 is 165 ° with the axis angle β of tank body hypomere 2.
Claims (8)
1. an inclined yeast-killing tank comprises tank body, and tank body top and bottom are respectively equipped with opening for feed, discharge port, it is characterized in that: described tank body is obliquely installed on support, and tank body is provided with the steam inlet pipe that communicates with its inside.
2. inclined yeast-killing tank as claimed in claim 1, it is characterized in that: described tank body is made of tank body epimere and tank body hypomere, the upper edge of the lower edge of tank body epimere and tank body hypomere is tightly connected, the angle α of the axis of tank body epimere and horizontal plane is 45 °-80 °, and the axis angle β of tank body epimere and tank body hypomere is 90 °-175 °.
3. inclined yeast-killing tank as claimed in claim 2 is characterized in that: described discharge port is arranged on the bottom of tank body hypomere, and the discharge port outer end is provided with quick operating valve.
4. inclined yeast-killing tank as claimed in claim 3 is characterized in that: described quick operating valve inside is filled with light filler, and light filler top is provided with cover plate.
5. inclined yeast-killing tank as claimed in claim 4 is characterized in that: the downside of described tank body hypomere is provided with liquid collecting bucket, and the tank body hypomere corresponding with liquid collecting bucket partly offers filter opening or be provided with filter screen.
6. as arbitrary described inclined yeast-killing tank among the claim 1-5, it is characterized in that: described steam inlet pipe axially is provided with, and many steam inlet pipes are distributed on the tank wall, and the steam coils of encircling tank body is between the upper and lower every setting, and steam inlet pipe is connected with steam coils.
7. inclined yeast-killing tank as claimed in claim 6 is characterized in that: the radian of described steam coils increases from top to bottom gradually.
8. inclined yeast-killing tank as claimed in claim 7 is characterized in that: described tank body epimere and tank body hypomere intersection are provided with a plurality of steam jets that tilt to the tank interior below, and the steam jet outer end links to each other with steam coils.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201650911U CN201678654U (en) | 2010-04-21 | 2010-04-21 | Inclined fermentation stopping tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201650911U CN201678654U (en) | 2010-04-21 | 2010-04-21 | Inclined fermentation stopping tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201678654U true CN201678654U (en) | 2010-12-22 |
Family
ID=43343706
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201650911U Expired - Fee Related CN201678654U (en) | 2010-04-21 | 2010-04-21 | Inclined fermentation stopping tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201678654U (en) |
-
2010
- 2010-04-21 CN CN2010201650911U patent/CN201678654U/en not_active Expired - Fee Related
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20101222 Termination date: 20190421 |