CN210382583U - Molasses adding system of conditioner - Google Patents
Molasses adding system of conditioner Download PDFInfo
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- CN210382583U CN210382583U CN201921188184.3U CN201921188184U CN210382583U CN 210382583 U CN210382583 U CN 210382583U CN 201921188184 U CN201921188184 U CN 201921188184U CN 210382583 U CN210382583 U CN 210382583U
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- hot water
- molasses
- pump
- tank
- conditioner
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Abstract
The utility model relates to a conditioner molasses adding system, which comprises a feeding system, a stirrer and a conditioning system, wherein the feeding system comprises a raw material tank, a hot water tank, a first molasses pump, a first hot water pump, a second hot water pump and a weighing tank, the raw material tank is provided with a plurality of heating channels, the bottom of the raw material tank is provided with a separation layer, a feeding port of the stirrer is connected with a second molasses pump, a discharging port of the stirrer is connected with a spraying pump, and the second molasses pump is connected with a discharging port of the weighing tank; the quenching and tempering system comprises a low charging bucket, a discharging disc and a quenching and tempering machine which are sequentially connected from top to bottom. The utility model discloses melting earlier molasses, diluting, stirring back, atomizing the spraying to the raw materials alone again, pelletize after the quenching and tempering at last again, can directly reform transform on original mechanical equipment, so low in manufacturing cost, because the temperature is high during the quenching and tempering, can not condense after the molasses atomization, consequently pelletize evenly, be difficult for solidifying, block up.
Description
Technical Field
The utility model relates to a molasses adding system especially relates to a quenching and tempering ware molasses adding system.
Background
The feed is prepared by mixing a plurality of raw materials according to a specific formula, a plurality of small materials are added in the formula in addition to a plurality of raw materials with larger components, in most of the existing feed processing plants, the molasses-containing feed is generally directly filled and added with molasses in a conditioner, but due to higher viscosity of molasses, the molasses is easy to block and is not easy to clean, the material mixing is not uniform, the conditioning and granulating are not uniform, and the modification price of the existing molasses adding system is high.
SUMMERY OF THE UTILITY MODEL
The utility model aims at the defects of the prior art, and provides a conditioner molasses adding system which has the advantages of low manufacturing cost, even granulation, difficult solidification and blockage.
The utility model discloses a realize through following technical scheme: a molasses adding system of a conditioner comprises a feeding system, a stirrer and a conditioning system; the feeding system comprises a raw material tank, a hot water tank, a first molasses pump, a first hot water pump, a second hot water pump and a weighing tank, wherein a backwater outlet, a backwater inlet and a water feeding discharge port are formed in the hot water tank; the feeding hole of the stirrer is connected with a second molasses pump, the discharging hole of the stirrer is connected with a spraying pump, and the second molasses pump is connected with the discharging hole of the weighing tank; the quenching and tempering system comprises a low charging bucket, a discharging tray and a quenching and tempering machine which are sequentially connected from top to bottom, wherein the discharging tray is connected with a discharging port of the stirring machine.
In order to facilitate the water heating interlayer heating channel of the hot water tank, a return water outlet of the hot water tank is provided with a first manual ball valve, and a feeding hole of the interlayer heating channel is provided with a second manual ball valve.
In order to facilitate heating of molasses in the raw material tank, a third manual ball valve is arranged between a return water inlet of the hot water tank and a discharge hole of the interlayer heating channel.
In order to ensure the cleanliness of the discharged molasses water, the discharge end of the raw material tank is connected with a first filter, and a first pneumatic angle valve is arranged between the feed inlet of the weighing tank and the first molasses pump.
In order to facilitate water inlet and water outlet of the hot water tank, a first liquid level meter and a first temperature probe are arranged in the hot water tank, and an air vent, a tap water inlet and a condensate water outlet are formed in the top of the hot water tank.
In order to further filter the diluted molasses water, a fourth manual ball valve and a second filter are arranged between the second hot water pump and the hot water tank.
In order to facilitate the control of the water entering the weighing tank, a second pneumatic angle valve is arranged between the second hot water pump and the weighing tank.
In order to facilitate spraying, a fifth manual ball valve, a flange, a sixth manual ball valve and a third filter are sequentially arranged between the spraying pump and the stirrer.
In order to facilitate spraying, the outlet end of the spraying pump is sequentially connected with an electromagnetic flowmeter, a seventh manual ball valve and a pneumatic ball valve.
The utility model has the advantages that: the utility model discloses melting earlier molasses, diluting, stirring back, atomizing the spraying to the raw materials alone again, pelletize after the quenching and tempering at last again, can directly reform transform on original mechanical equipment, so low in manufacturing cost, because the temperature is high during the quenching and tempering, can not condense after the molasses atomization, consequently pelletize evenly, be difficult for solidifying, block up.
Drawings
Fig. 1 is a schematic structural view of the present invention;
FIG. 2 is a schematic view of the connection between the raw material tank and the hot water tank according to the present invention;
FIG. 3 is a schematic view of the connection of the weighing tank, the stirrer and the tempering system of the present invention;
in the figure: 1. a raw material tank; 11. a barrier heating tunnel; 12. a first filter; 13. a first pneumatic angle valve; 2. a hot water tank; 211. a backwater outlet; 212. a backwater inlet; 213. adding water and discharging; 22. a first manual ball valve; 23. a second manual ball valve; 24. a third manual ball valve; 25. a first liquid level meter; 26. a first temperature probe; 271. air holes are formed; 272. a tap water inlet; 273. a condensed water outlet; 3. a first molasses pump; 4. a first hot water pump; 5. a second hot water pump; 51. a fourth manual ball valve; 52. a second filter; 6. weighing the tank; 61. a second pneumatic angle valve; 7. a blender; 71. a spray pump; 72. a fifth manual ball valve; 73. a flange; 74. a sixth manual ball valve; 75. a third filter; 76. an electromagnetic flow meter; 77. a seventh manual ball valve; 78. a pneumatic ball valve; 8. a second syrup pump; 91. a low charging bucket; 92. a discharging tray; 93. a conditioner.
Detailed Description
The following detailed description of the preferred embodiments of the present invention will be provided in conjunction with the accompanying drawings, so that the advantages and features of the present invention can be more easily understood by those skilled in the art, and the protection scope of the present invention can be clearly and clearly defined.
As shown in figure 1, a conditioner molasses adding system comprises a feeding system, a stirrer 7 and a conditioning system;
the feeding system comprises a raw material tank 1, a hot water tank 2, a first molasses pump 3, a first hot water pump 4, a second hot water pump 5 and a weighing tank 6, wherein a backwater outlet 211, a backwater inlet 212 and a water feeding discharge port 213 are arranged on the hot water tank 2, the raw material tank 1 is provided with a plurality of heating channels 11, the bottom of the raw material tank is provided with a separation heating channel 11, a feed inlet of the separation heating channel 11 is connected with the backwater outlet 211 of the hot water tank 2 through the first hot water pump 4, a discharge port of the separation heating channel 11 is connected with the backwater inlet 212 of the hot water tank 2, the backwater outlet 211 of the hot water tank 2 is provided with a first manual ball valve 22, a feed inlet of the separation heating channel 11 is provided with a second manual ball valve 23, a third manual ball valve 24 is arranged between the backwater inlet 212 of the hot water tank 2 and the discharge port of the separation heating channel 11, a discharge end of the raw material tank 1 is connected with a first filter 12, a first pneumatic angle valve 13, a first liquid level meter 25 and a first temperature probe 26 are arranged in the hot water tank 2, an air hole 271, a tap water inlet 272 and a condensate outlet 273 are formed in the top of the hot water tank 2, the specification of the first temperature probe 26 is PT 1004-20 mA, a fourth manual ball valve 51 and a second filter 52 are arranged between the second hot water pump 5 and the hot water tank 2, a second pneumatic angle valve 61 is arranged between the second hot water pump 5 and the weighing tank 6, and feed inlets of the weighing tank 6 are respectively connected with a discharge outlet of the raw material tank 1 through a first molasses pump 3 and a water adding discharge outlet 213 of the hot water tank 2 through the second hot water pump 5; the feed inlet of mixer 7 is connected with second molasses pump 8 and mixer 7's discharge gate is connected with spraying pump 71, and spraying pump 71 specification is connected with inverter motor, and the specification is NYP3-40/2.2KW, second molasses pump 8 is connected with weighing tank 6's discharge gate, be equipped with fifth manual ball valve 72, flange 73, sixth manual ball valve 74 and third filter 75 between spraying pump 71 and the mixer 7 in proper order, and third filter 75 is the U type filter, and the specification is DN40, spraying pump 71's exit end has connected gradually electromagnetic flow meter 76, seventh manual ball valve 77 and pneumatic ball valve 78, electromagnetic flow meter 76's specification is AC220V 4-20ma, the quenching and tempering system includes from last low material jar 91, play dish 92 and the quenching and tempering machine 93 that connect gradually down, play dish 92 is connected with mixer 7's discharge gate.
It should be noted that the flow of molasses and molasses water among the elements are communicated through DN40 pipeline or DN20 pipeline.
The working principle is as follows: raw material molasses is placed in a raw material tank 1, hot water flows to an interlayer heating channel 11 from a backwater outlet 211 of a hot water tank 2, finally, backflow flows back into the hot water tank 2 from a backwater inlet 212 of the hot water tank 2, so that the raw material molasses in the raw material tank 1 is heated, a discharge port of the raw material tank 1 sequentially passes through a first filter 12, a first molasses pump 3 and a first pneumatic angle valve 13 and flows into a weighing tank 6, hot water in the hot water tank 2 sequentially passes through a fourth manual ball valve 51, a second filter 52, a second hot water pump 5 and a second pneumatic angle valve 61 from a water feeding and discharging port 213 and enters the weighing tank 6, the molasses is diluted in the weighing tank 6, the diluted molasses sequentially passes through the pneumatic angle valve and a second molasses pump 8 from a discharge port of the weighing tank 6 and reaches a stirrer 7, the diluted molasses is uniformly stirred by the stirrer 7 and sequentially flows to a fifth manual ball valve 72, a fifth manual ball valve and a fifth pneumatic, The device comprises a sixth manual ball valve 74, a spraying pump 71, an electromagnetic flowmeter 76, a seventh manual ball valve 77 and a pneumatic ball valve 78, wherein the tail end of the pneumatic ball valve 78 is connected with a spray head, the spray head is aligned with a discharging disc 92 to spray materials in an atomizing mode, meanwhile, raw materials in a low charging bucket 91 fall down and fall into a conditioner 93 after molasses water is sprayed in an atomizing mode to be conditioned, and discharging is finally carried out.
Compared with the prior art, the molasses adding system of the conditioner has the advantages of low manufacturing and modification cost, difficult solidification and blockage of molasses water and uniform granulation.
The above-mentioned embodiments only represent some embodiments of the present invention, and the description thereof is specific and detailed, but not to be construed as limiting the scope of the present invention. It should be noted that, for those skilled in the art, without departing from the spirit of the present invention, several variations and modifications can be made, which are within the scope of the present invention.
Claims (9)
1. A molasses adding system of a conditioner is characterized in that: comprises a charging system, a stirrer (7) and a tempering system;
the feeding system comprises a raw material tank (1), a hot water tank (2), a first molasses pump (3), a first hot water pump (4), a second hot water pump (5) and a weighing tank (6), a backwater outlet (211), a backwater inlet (212) and a water feeding outlet (213) are arranged on the hot water tank (2), the raw material tank (1) is provided with a plurality of heating channels (11) with separating layers at the bottom, the feed inlet of the interlayer heating channel (11) is connected with the return water outlet (211) of the hot water tank (2) through a first hot water pump (4) and the discharge outlet of the interlayer heating channel (11) is connected with the return water inlet (212) of the hot water tank (2), the feed inlet of the weighing tank (6) is respectively connected with the discharge outlet of the raw material tank (1) through a first molasses pump (3) and is connected with the water feeding discharge outlet (213) of the hot water tank (2) through a second hot water pump (5);
a feed inlet of the stirrer (7) is connected with a second molasses pump (8), a discharge outlet of the stirrer (7) is connected with a spraying pump (71), and the second molasses pump (8) is connected with a discharge outlet of the weighing tank (6);
the quenching and tempering system comprises a low charging bucket (91), a discharging disc (92) and a quenching and tempering machine (93) which are sequentially connected from top to bottom, wherein the discharging disc (92) is connected with a discharging hole of the stirring machine (7).
2. A conditioner molasses addition system according to claim 1, characterized by: a backwater outlet (211) of the hot water tank (2) is provided with a first manual ball valve (22) and a feed inlet of the interlayer heating channel (11) is provided with a second manual ball valve (23).
3. A conditioner molasses addition system according to claim 1, characterized by: and a third manual ball valve (24) is arranged between a return water inlet (212) of the hot water tank (2) and a discharge hole of the interlayer heating channel (11).
4. A conditioner molasses addition system according to claim 1, characterized by: the discharge end of head tank (1) is connected with first filter (12), be equipped with first pneumatic angle valve (13) between the feed inlet of weighing tank (6) and first molasses pump (3).
5. A conditioner molasses addition system according to claim 1, characterized by: a first liquid level meter (25) and a first temperature probe (26) are arranged in the hot water tank (2), and an air hole (271), a tap water inlet (272) and a condensed water outlet (273) are formed in the top of the hot water tank (2).
6. A conditioner molasses addition system according to claim 1, characterized by: a fourth manual ball valve (51) and a second filter (52) are arranged between the second hot water pump (5) and the hot water tank (2).
7. A conditioner molasses addition system according to claim 1, characterized by: and a second pneumatic angle valve (61) is arranged between the second hot water pump (5) and the weighing tank (6).
8. A conditioner molasses addition system according to claim 1, characterized by: and a fifth manual ball valve (72), a flange (73), a sixth manual ball valve (74) and a third filter (75) are sequentially arranged between the spraying pump (71) and the stirrer (7).
9. A conditioner molasses addition system according to claim 1, characterized by: the outlet end of the spraying pump (71) is sequentially connected with an electromagnetic flowmeter (76), a seventh manual ball valve (77) and a pneumatic ball valve (78).
Priority Applications (1)
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CN201921188184.3U CN210382583U (en) | 2019-07-25 | 2019-07-25 | Molasses adding system of conditioner |
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CN201921188184.3U CN210382583U (en) | 2019-07-25 | 2019-07-25 | Molasses adding system of conditioner |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115606684A (en) * | 2022-11-04 | 2023-01-17 | 江苏正昌粮机股份有限公司 | Cuttlefish paste adding process and cuttlefish paste adding equipment |
CN115722138A (en) * | 2022-09-22 | 2023-03-03 | 青岛宝恒机械技术有限公司 | Automatic timing and quantifying control system and method for feed in breeding industry |
-
2019
- 2019-07-25 CN CN201921188184.3U patent/CN210382583U/en active Active
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115722138A (en) * | 2022-09-22 | 2023-03-03 | 青岛宝恒机械技术有限公司 | Automatic timing and quantifying control system and method for feed in breeding industry |
CN115722138B (en) * | 2022-09-22 | 2023-06-23 | 青岛宝恒机械技术有限公司 | Automatic timing and quantitative control system and method for feed in breeding industry |
CN115606684A (en) * | 2022-11-04 | 2023-01-17 | 江苏正昌粮机股份有限公司 | Cuttlefish paste adding process and cuttlefish paste adding equipment |
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