CN204653726U - A kind of feed molasses adds automatic control system - Google Patents
A kind of feed molasses adds automatic control system Download PDFInfo
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- CN204653726U CN204653726U CN201520335040.1U CN201520335040U CN204653726U CN 204653726 U CN204653726 U CN 204653726U CN 201520335040 U CN201520335040 U CN 201520335040U CN 204653726 U CN204653726 U CN 204653726U
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- Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)
Abstract
The utility model provides a kind of feed molasses and adds automatic control system, and system comprises molasses tank, heating tank, batch box and surge tank, and wherein molasses tank connects heating tank by fluid infusion pump; Heating tank connects batch box by dosing pump, batch box connects surge tank by Liquid spraying pump, surge tank hydrojet pipeline out stretches in feed mixing machine and is connected with stock distributor, hydrojet pipeline is divided into multichannel branch road and sends into spiral nozzle injection by stock distributor, and being also provided with an air pressure distributor in feed mixing machine is that spiral nozzle pressurization forms atomized spray.Native system is equipped with PLC as controller, is also provided with touch-screen or computer as operation interface.Compare with conventional feed molasses add-on system, native system can control the addition of molasses exactly for different types of feed, and molasses hydrojet atomizing effect is better, and automaticity is high, control and regulate all very convenient, can effectively save man power and material's cost.
Description
Technical field
The utility model relates to a kind of automatic control system, and specifically a kind of feed factory is the automatic control system that feed adds molasses.
Background technology
Aquaculture development is rapid in recent years, also more and more higher to the quality requirements of the required feed of cultivation, and in order to effectively improve the nutritional labeling in feed, Europe and some countries of Asia generally add a certain amount of molasses in feed at present.Molasses are byproducts of the sugar industry such as sugarcane, beet, it is a kind of inexpensive nutrients, not only energy is high, and digest and assimilate fast, be added in feed, not only can significantly improve nutritional labeling and the palatability of feed, but also feed granules forming quality can be improved, reduce feed at the dust produced and handling process produces.
The existing feed molasses add-on system of each Feed Manufacturing factory of current China adopts directly to be transported to by the molasses after heating and mixes with feed, complete the interpolation adding molasses, such addition manner can not accurately control for the addition of molasses, the uniformity of mixing is also bad, and the ratio of the required molasses added of different types of feed is different, if molasses add-on system can not add according to quantity accurately, or mixture homogeneity is bad, the quality of producing feed can be affected, and the general automaticity of existing feed molasses add-on system is not high, control and regulate difficulty, larger to the consumption of man power and material, cause Feed Manufacturing cost also higher.
Utility model content
In order to solve the problem, the utility model provides a kind of feed molasses and adds automatic control system, and in Feed Manufacturing, apply this system is that feed adds molasses, automaticity is high, add metering accurately, hydrojet is even, can save a large amount of man power and materials.
The technical scheme that the utility model adopts is as follows:
A kind of feed molasses adds automatic control system, and it is characterized in that: comprise molasses tank, heating tank, batch box and surge tank, wherein molasses tank connects fluid infusion pump and the first filter successively by pipeline, then is connected to heating tank; Heating tank top is provided with the heating stirrer stretched in tank body, heating tank is provided with the liquid-level switch monitoring upper and lower liquid level respectively, the top of heating tank is also provided with water supply line and steam supply pipes, water supply line and steam supply pipes are respectively equipped with priming valve and steam valve, be provided with the V1 pipeline valve for arranging the end bottom heating tank, heating tank two bottom sides is also equipped with Weighing module; Heating tank bottom connects V2 pipeline valve successively by pipeline, the second filter, dosing pump, Pneumatic valve, then is connected to batch box; Described Pneumatic valve is provided with corresponding compressed air supply line and controls it; Batch box top is provided with the metering agitator stretched in staving, and the both sides of batch box are provided with LOAD CELLS, is provided with the V3 pipeline valve for arranging the end bottom batch box; After connecting Liquid spraying pump and check-valves successively by pipeline bottom batch box, then converge mutually with an air-blowing pipeline, common formation hydrojet pipeline; Air-blowing pipeline is provided with air-blowing electrically-controlled valve and check valve controls the compressed air for air-blowing; After hydrojet pipeline connects surge tank and V6 pipeline valve successively, stretch in feed mixing machine and be connected with stock distributor, hydrojet pipeline is divided into the multichannel branch road of laid out in parallel by stock distributor in feed mixing machine, and the end of each branch road is equipped with spiral nozzle; Also be provided with an air pressure distributor in feed mixing machine, be its air feed by compressed air supply line, this supply air line is provided with atomization electrically-controlled valve, and the outlet that air pressure distributor is provided with multichannel branch road is connected to described spiral nozzle respectively for its pressurization formation atomized spray; Native system is also equipped with PLC as controller, described fluid infusion pump, dosing pump, Liquid spraying pump, heating stirrer and metering agitator all control by PLC, described liquid-level switch, Weighing module, LOAD CELLS are all connected with PLC, and described priming valve, steam valve, Pneumatic valve, air-blowing electrically-controlled valve, atomization electrically-controlled valve all control by PLC.
The heating of described heating tank adopts the mode of steam pipe coil indirect and electric-heating belt insulation, and is provided with thermal resistance and temperature control instrument is monitored heating-up temperature.
Also continue to extend one section for the first blow-off line of blowdown after pipeline after described check-valves and air-blowing ducts converge, which is provided with V4 pipeline valve; The part of described hydrojet pipeline between surge tank and V6 pipeline valve is also provided with one section for the second blow-off line of blowdown, which is provided with V5 pipeline valve.
Described feed molasses adds automatic control system and is also provided with touch-screen or computer as operation interface, and touch-screen or computer are connected with PLC and also can arrange its parameter thus control the automatic operation of whole system.
The beneficial effects of the utility model are: compare with conventional feed molasses add-on system, this feed molasses adds automatic control system can control molasses exactly addition for different types of feed, its measuring accuracy can reach ± and more than 0.3%, and the hydrojet pipeline of native system adopts the mode of compressed air air-blowing convey materials, and be provided with hydrojet surge tank, efficiently solve because molasses viscosity is high, the problem of pumping difficulties, native system also introduces pressurized with compressed air atomization branch road at spiral nozzle place in addition, nozzle outlet pressure increases, molasses hydrojet atomizing effect is better, its hydrojet uniformity reaches more than 90%.Native system automaticity is high, and control and regulate all very convenient, can effectively save man power and material's cost, be the more efficient feed molasses add-on system of one.
Accompanying drawing explanation
Fig. 1 is the schematic diagram that feed molasses of the present utility model adds automatic control system.
In figure: 1-molasses tank, 2-fluid infusion pump, 3-first filter, 4-heating stirrer, 5-priming valve, 6-liquid-level switch, 7-Weighing module, 8-V1 pipeline valve, 9-steam valve, 10-heating tank, 11-V2 pipeline valve, 12-second filter, 13-dosing pump, 14-Pneumatic valve, 15-heating stirrer, 16-LOAD CELLS, 17-batch box, 18-V3 pipeline valve, 19-Liquid spraying pump, 20-check-valves, 21-air-blowing electrically-controlled valve, 22-check valve, 23-V4 pipeline valve, 24-V5 pipeline valve, 25-V6 pipeline valve, 26-surge tank, 27-stock distributor, 28-air pressure distributor, 29-is atomized electrically-controlled valve, 30-spiral nozzle, 31-feed mixing machine.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is described further.
As shown in Figure 1, this feed molasses adds automatic control system and comprises molasses tank 1, heating tank 10, batch box 17 and surge tank 26, and wherein molasses tank 1 connects fluid infusion pump 2 and the first filter 3 successively by pipeline, then is connected to heating tank 10; Heating tank 10 top is provided with the heating stirrer 4 stretched in tank body, heating tank 10 is provided with the liquid-level switch 6 monitoring upper and lower liquid level respectively, the top of heating tank 10 is also provided with water supply line and steam supply pipes, water supply line and steam supply pipes are respectively equipped with priming valve 5 and steam valve 9, be provided with the V1 pipeline valve 8 for arranging the end bottom heating tank 10, heating tank 10 two bottom sides is also equipped with Weighing module 7; Heating tank 10 bottom connects V2 pipeline valve 11, second filter 12 successively by pipeline, dosing pump 13, Pneumatic valve 14, then is connected to batch box 17; Described Pneumatic valve 14 is provided with corresponding compressed air supply line and controls it; Batch box 17 top is provided with the metering agitator 15 stretched in staving, and the both sides of batch box 17 are provided with LOAD CELLS 16, is provided with the V3 pipeline valve 18 for arranging the end bottom batch box 17; After connecting Liquid spraying pump 19 and check-valves 20 successively by pipeline bottom batch box 17, then converge mutually with an air-blowing pipeline, common formation hydrojet pipeline; Air-blowing pipeline is provided with air-blowing electrically-controlled valve 21 and check valve 22 controls the compressed air for air-blowing; Also continue to extend one section for the first blow-off line of blowdown after pipeline after described check-valves 20 and air-blowing ducts converge, which is provided with V4 pipeline valve 23.After hydrojet pipeline connects surge tank 26 and V6 pipeline valve 25 successively, stretch in feed mixing machine 31 and be connected with stock distributor 27, the part of hydrojet pipeline between surge tank 26 and V6 pipeline valve 25 is also provided with one section for the second blow-off line of blowdown, which is provided with V5 pipeline valve 24.Hydrojet pipeline is divided into the multichannel branch road of laid out in parallel by stock distributor 27 in feed mixing machine 31, and the end of each branch road is equipped with spiral nozzle 30; An air pressure distributor 28 is also provided with in feed mixing machine 31, be its air feed by compressed air supply line, this supply air line is provided with atomization electrically-controlled valve 29, and the outlet that air pressure distributor 28 is provided with multichannel branch road is connected to described spiral nozzle 30 respectively for its pressurization formation atomized spray; Native system is also equipped with PLC as controller, described fluid infusion pump 2, dosing pump 13, Liquid spraying pump 19, heating stirrer 4 and metering agitator 15 all control by PLC, described liquid-level switch 6, Weighing module 7, LOAD CELLS 16 are all connected with PLC, and described priming valve 5, steam valve 9, Pneumatic valve 14, air-blowing electrically-controlled valve 21, atomization electrically-controlled valve 29 all control by PLC.
The workflow that this feed molasses adds automatic control system is: under normal circumstances, V1, V3, V4, V5 pipeline valve 8, 18, 23, 24 close, V2, V6 pipeline valve 11, 25 open, molasses are sent into heating tank 10 by fluid infusion pump 2 and are heated by molasses tank 1, heating tank 10 is added water by supply channel, as long as set the ratio of water and molasses on operation interface, system can calculate automatically to be needed the weight of water and molasses and is carried out fluid infusion by PLC control fluid infusion pump 2 and priming valve 5 and added water, monitored by Weighing module 7 pairs of weight, the height of heating tank sugar 10 sweet liquid levels is detected to judge the start and stop of fluid infusion pump 2 and priming valve 5 by liquid-level switch 6.After having heated, when system acceptance is to dosing signal, dosing pump 13 works and Pneumatic valve 14 is opened, the molasses heated are carried from heating tank 10 to batch box 17, through LOAD CELLS 16 sense weight of batch box 17, after arriving setting value, dosing pump 13 quits work and Pneumatic valve 14 is closed.After dosing completes, when system acceptance is to hydrojet signal, start Liquid spraying pump 19, molasses are after check-valves 20, surge tank 26 and stock distributor 27, be atomized by spiral nozzle 30 and be evenly injected in feed mixing machine 31 li, after a setting-up time postpones, open air-blowing electrically-controlled valve 21 simultaneously and be atomized electrically-controlled valve 29 and pressurize, guarantee that atomizing effect is better.After hydrojet completes, after postponing a setting-up time, close air-blowing electrically-controlled valve 21 and atomization electrically-controlled valve 29, guarantee that in pipeline, residual liquid is sprayed onto feed mixing machine 31 li completely.After hydrojet completes, system starts dosing work automatically, enters subsequent work recurrent state.
The foregoing is only an exemplary embodiments of the present utility model; be not limited to the utility model; all do within spirit of the present utility model and principle any amendment, equivalent to replace and improvement etc., all should be included within protection domain of the present utility model.
Claims (4)
1. a feed molasses adds automatic control system, it is characterized in that: comprise molasses tank (1), heating tank (10), batch box (17) and surge tank (26), wherein molasses tank (1) connects fluid infusion pump (2) and the first filter (3) successively by pipeline, then is connected to heating tank (10); Heating tank (10) top is provided with the heating stirrer (4) stretched in tank body, heating tank (10) is provided with the liquid-level switch (6) monitoring upper and lower liquid level respectively, the top of heating tank (10) is also provided with water supply line and steam supply pipes, water supply line and steam supply pipes are respectively equipped with priming valve (5) and steam valve (9), heating tank (10) bottom is provided with the V1 pipeline valve (8) for arranging the end, and heating tank (10) two bottom sides is also equipped with Weighing module (7); Heating tank (10) bottom connects V2 pipeline valve (11) successively by pipeline, the second filter (12), dosing pump (13), Pneumatic valve (14), then is connected to batch box (17); Described Pneumatic valve (14) is provided with corresponding compressed air supply line and controls it; Batch box (17) top is provided with the metering agitator (15) stretched in staving, and the both sides of batch box (17) are provided with LOAD CELLS (16), and batch box (17) bottom is provided with the V3 pipeline valve (18) for arranging the end; After batch box (17) bottom connects Liquid spraying pump (19) and check-valves (20) successively by pipeline, then converge mutually with an air-blowing pipeline, common formation hydrojet pipeline; Air-blowing pipeline is provided with air-blowing electrically-controlled valve (21) and check valve (22) controls the compressed air for air-blowing; After hydrojet pipeline connects surge tank (26) and V6 pipeline valve (25) successively, stretch in feed mixing machine (31) and be connected with stock distributor (27), hydrojet pipeline is divided into the multichannel branch road of laid out in parallel by stock distributor (27) in feed mixing machine (31), and the end of each branch road is equipped with spiral nozzle (30); An air pressure distributor (28) is also provided with in feed mixing machine (31), be its air feed by compressed air supply line, this supply air line is provided with atomization electrically-controlled valve (29), and the outlet that air pressure distributor (28) is provided with multichannel branch road is connected to described spiral nozzle (30) respectively for its pressurization formation atomized spray; Native system is also equipped with PLC as controller, described fluid infusion pump (2), dosing pump (13), Liquid spraying pump (19), heating stirrer (4) and metering agitator (15) all control by PLC, described liquid-level switch (6), Weighing module (7), LOAD CELLS (16) are all connected with PLC, and described priming valve (5), steam valve (9), Pneumatic valve (14), air-blowing electrically-controlled valve (21), atomization electrically-controlled valve (29) all control by PLC.
2. feed molasses according to claim 1 adds automatic control system, it is characterized in that: the heating of described heating tank (10) adopts the mode of steam pipe coil indirect and electric-heating belt insulation, and be provided with thermal resistance and temperature control instrument is monitored heating-up temperature.
3. feed molasses according to claim 1 adds automatic control system, it is characterized in that: also continue to extend one section of first blow-off line for blowdown after the pipeline after described check-valves (20) and air-blowing ducts converge, which is provided with V4 pipeline valve (23); The part of described hydrojet pipeline between surge tank (26) and V6 pipeline valve (25) is also provided with one section of second blow-off line for blowdown, which is provided with V5 pipeline valve (24).
4. feed molasses according to claim 1 adds automatic control system, it is characterized in that: described feed molasses adds automatic control system and is also provided with touch-screen or computer as operation interface, touch-screen or computer are connected with PLC and also can arrange its parameter thus control the automatic operation of whole system.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520335040.1U CN204653726U (en) | 2015-05-22 | 2015-05-22 | A kind of feed molasses adds automatic control system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520335040.1U CN204653726U (en) | 2015-05-22 | 2015-05-22 | A kind of feed molasses adds automatic control system |
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| CN204653726U true CN204653726U (en) | 2015-09-23 |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106190772A (en) * | 2016-07-15 | 2016-12-07 | 江苏尚昆生物设备有限公司 | Material distributing system |
| CN108498889A (en) * | 2018-05-09 | 2018-09-07 | 重庆天外天医疗器械有限公司 | The online compounding and controlling system of dialysis machine working solution and dialysis machine |
| CN109588745A (en) * | 2018-12-10 | 2019-04-09 | 顾健健 | A kind of preparation facilities, preparation method and the proportion of sucking pig son feed |
| CN111763776A (en) * | 2020-05-14 | 2020-10-13 | 营口新北方制糖有限公司 | Pneumatic automatic syrup adding and converting system and method for soft white sugar |
| CN111820438A (en) * | 2020-08-10 | 2020-10-27 | 磐石自动化系统（深圳）有限公司 | Molasses adding system and using method thereof |
-
2015
- 2015-05-22 CN CN201520335040.1U patent/CN204653726U/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106190772A (en) * | 2016-07-15 | 2016-12-07 | 江苏尚昆生物设备有限公司 | Material distributing system |
| CN108498889A (en) * | 2018-05-09 | 2018-09-07 | 重庆天外天医疗器械有限公司 | The online compounding and controlling system of dialysis machine working solution and dialysis machine |
| CN109588745A (en) * | 2018-12-10 | 2019-04-09 | 顾健健 | A kind of preparation facilities, preparation method and the proportion of sucking pig son feed |
| CN109588745B (en) * | 2018-12-10 | 2021-11-23 | 沈阳爱瑜饲料有限公司 | Preparation device, preparation method and proportion of piglet feed |
| CN111763776A (en) * | 2020-05-14 | 2020-10-13 | 营口新北方制糖有限公司 | Pneumatic automatic syrup adding and converting system and method for soft white sugar |
| CN111763776B (en) * | 2020-05-14 | 2023-09-08 | 营口新北方制糖有限公司 | System and method for automatically adding invert syrup by pneumatic soft sugar |
| CN111820438A (en) * | 2020-08-10 | 2020-10-27 | 磐石自动化系统（深圳）有限公司 | Molasses adding system and using method thereof |
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