CN209702773U - Molasses dilute automatic control system - Google Patents

Molasses dilute automatic control system Download PDF

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Publication number
CN209702773U
CN209702773U CN201920147230.9U CN201920147230U CN209702773U CN 209702773 U CN209702773 U CN 209702773U CN 201920147230 U CN201920147230 U CN 201920147230U CN 209702773 U CN209702773 U CN 209702773U
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sand device
electric
controller
controlled mechanical
molten
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CN201920147230.9U
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王中天
庞业馨
黄宁
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Qinzhou Zhongyu Instrument Co Ltd
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Qinzhou Zhongyu Instrument Co Ltd
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Abstract

The utility model be molasses dilute automatic control system, this system include material box, the molten sand device of the first electric-controlled mechanical, controller and with display/loader;The material box is connected by mother tube with the molten sand device import of the first electric-controlled mechanical, the import of the molten sand device of first electric-controlled mechanical also passes through hot-water line and is connected with external boiler, the outlet of the molten sand device of first electric-controlled mechanical is connected by feed pipe with external boiling pan, and the molten sand device of the first electric-controlled mechanical is also electrically connected with the output end of controller;Concentration meter is installed on feed pipe, the concentration meter is electrically connected with the input terminal of controller, and hot water regulating valve is equipped on hot-water line, and the hot water regulating valve is electrically connected with the output end of controller.Hold sand device be it is mechanical hold sand device, independent of raw material and hold temperature in sand device, high speed can be realized and hold sand, solve the problems, such as to hold sand dependent on high temperature in the prior art, it is not only high-efficient, be also Zhu Tang workshop section all set condition, improve sugared rate.

Description

Molasses dilute automatic control system
Technical field
The utility model, which belongs in the sugaring of sugar refinery, boils sugar honey workshop section technical field, and in particular to molasses dilution automatically controls System.
Background technique
Mechanism sugar refinery handles molasses using division of labor segmented mode in production at this stage.In the sugar that purging workshop section, sub-sieve come out Then honey enters pneumatic transmission tank through piping by being pooled to opening box first, Zhu Tang workshop section is transported to by way of pneumatic transmission Material box storage.When Zhu Tang workshop section needs to use various molasses materials, then by field worker the molasses of material box are put into dilution In case, a certain proportion of hot water is then added, molten sand and the dilution of material are completed by mechanical stirring, when molasses are by next workshop section After being over, worker repeat before work.Four kinds of different molasses can be generated in the daily production of factory, with a kind of sugar Honey is calculated, and needs a set of pneumatic transmission tank, three raw material storage boxes, three dilution tanks;Each class of two people of needs management of factory at this stage Pneumatic transmission tank, four people manage raw material storage box, and four people manage dilution tank, and daily three boats change, and need 30 workers can Production also wants a large amount of equipment to assist.Conveying and dilution belong to different floors, lack timely and effective communication, often result in life The error of production process link.Existing mode cost of human resources is higher, and the obtained molasses of manual operation are often not achieved The index that production process needs, causes factories to waste, increased costs.
In existing, also there are the intelligence control system that serial dilution molasses may be implemented, such as Publication No. The Chinese utility model patent of CN207591645U discloses a kind of sugar refinery molasses serial dilution intelligence control system, including DCS Or PLC control system, molasses case, mixer, boiling pan and connecting pipe;Molasses case is connect by pipeline with mixer, steam Enter mixer by mixer jet chimney, hot water enters mixer by hot water pipeline, mixer outlet pipeline respectively with Boiling pan connection;Temperature sensor and microwave concentration meter are separately mounted on mixer outlet pipeline, pass through cable and DCS respectively Or PLC control system connection;Steam control valve is installed on entering mixer jet chimney, hot water tune is installed on hot water pipeline Valve is saved, is connect respectively by cable with DCS or PLC control system;Electromagnetism is installed respectively on the pipeline of molasses case to mixer Flowmeter and molasses regulating valve are connect by cable with DCS or PLC control system respectively;In the molasses pipeline for entering boiling pan One switch valve of upper each installation of difference is connect by cable with DCS or PLC control system respectively.The program by by hot water, steam Vapour and material (molasses), which are sent into mixer, to be diluted, and the molasses after dilution are then passed through the suction function in boiling pan, Molasses after dilution are transported in boiling pan, into Boiling Process.The place that this scheme has the following disadvantages: first from sugar It is a continuous production process that honey, which is diluted to and boils sugar, and the temperature for being transported to molasses in mixer is 40 DEG C, hot water temperature is 85- 90 DEG C, the temperature of steam be 110-120 DEG C, under this condition, molasses could rapid dilution, achieve the purpose that on-line dilution, The temperature of molasses at 80 DEG C or more, (have to when entering boiling pan than in boiling pan by the molasses temperature diluted after dilution Material (65-70 DEG C) it is 3-4 DEG C high, not above 5 DEG C, otherwise will cause race sugar, and absolutely not allow lower than in boiling pan Otherwise temperature of charge generates pseudo- brilliant.Secondly, boiling pan is by the effect sucking molasses of negative pressure in tank, speed is very fast, and Mixer is limited by the productivity of high temperature dilution molasses, or will cause molasses dilution deficiency, causes crystallite dissolution insufficient; Or the demand of Boiling Process is not achieved, it cannot achieve the diluted purpose of on-line continuous.
Utility model content
The technical problem to be solved by the utility model is to provide it is a kind of can (molasses be dilute independent of the appearance sand of temperature Release) scheme, and hold that sand speed is fast, percent crystallization in massecuite is high, quality of finished product good, the molasses that low energy consumption dilution automatic control system.
In order to solve the above technical problems, the molasses of the utility model design dilute automatic control system, including material box, the The molten sand device of one electric-controlled mechanical, controller and the display/loader being connected with controller;The material box by mother tube with The molten sand device import of first electric-controlled mechanical is connected, and the import of the molten sand device of the first electric-controlled mechanical also passes through hot-water line and outside Boiler is connected, and the outlet of the molten sand device of the first electric-controlled mechanical is connected by feed pipe with external boiling pan, the first electric-controlled mechanical The molten sand device of formula is also electrically connected with the output end of controller;Concentration meter is installed on feed pipe, the concentration meter and controller Input terminal electrical connection, is equipped with hot water regulating valve, the hot water regulating valve is electrically connected with the output end of controller on hot-water line.
Present boiling pan production power is big, in order to alleviate the dilution pressure of system, it is preferred that above scheme can also wrap Dilution memory is included, the dilution memory is set between feed pipe and external boiling pan.
Molasses regelation after diluting in order to prevent more accurately controls molasses brix, avoids because of molasses at crystal settling Storage influences the brix of molasses, it is preferred that dilution memory described in above scheme is equipped with for detecting in dilution memory The liquid level sensor of material liquid level, the liquid level sensor are electrically connected with the input terminal of controller;The dilution memory peripheral hardware There is the molten sand device of the second electric-controlled mechanical, the molten sand device import and export of second electric-controlled mechanical passes through delivery pipe respectively and dilution stores Device connection, the output end of the controller are electrically connected with the molten sand device of the second electric-controlled mechanical.
For the temperature of adjustable dilution memory molasses, to meet the temperature above scheme of Boiling Process requirement molasses Preferably, the temperature sensor for detecting temperature in dilution memory, the temperature can be equipped on the dilution memory Sensor is electrically connected with the input terminal of controller;The dilution memory is connect by jet chimney with external steam generator, The jet chimney is equipped with steam control valve, which is electrically connected with the output end of controller.
In order to meet the requirement in Boiling Process to molasses conveying, preferably, in the above solution, can also include at least a set of The outlet of the spare molten sand device of electric-controlled mechanical, the spare molten sand device of electric-controlled mechanical passes through feed pipe and the external boiling pan It is connected, the spare molten sand device of electric-controlled mechanical is also electrically connected with the output end of controller;Spare hot water is installed on spare hot-water line Regulating valve, the spare hot water regulating valve are electrically connected with the output end of controller.
In order to improve the efficiency of dilution (holding sand), preferably, in the above solution, the molten sand device of first electric-controlled mechanical, second The molten sand device of electric-controlled mechanical, the molten sand device of spare electric-controlled mechanical are preferably gear pump.
Compared with prior art, the advantages of the utility model molasses dilution automatic control system are as follows:
1, the appearance sand device that this system is is mechanical appearance sand device, independent of the temperature in raw material and appearance sand device, Ji Keshi Now high speed holds sand, solves the problems, such as to hold sand dependent on high temperature in the prior art, such appearance sand mode is not only high-efficient, real The automatic control of existing molasses serial dilution is also Zhu Tang workshop section all set condition, improves sugared rate;In addition, further making With gear pump as sand device is held, so that more fully mixed, more efficient, this is trial for the first time in the art.
2, dilution memory can alleviate the dilution pressure of system, and add a set of mechanical appearance on dilution memory Sand device, can more accurate molasses brix, avoid because molasses store influence molasses brix.
3, dynamic heating, dilution mixing and molten sand, high degree of automation may be implemented in the utility model, reduce employment at This, and production capacity and product quality are also improved, low energy consumption, remarkable benefit.
4, the utility model has the advantages of simple structure and easy realization, and equipment cost is low, is conducive to promote.
Detailed description of the invention
Fig. 1 is a kind of pipeline structure schematic diagram of most preferred embodiment of the utility model.
The system block diagram of the position Fig. 2 the utility model.
Figure label: 1, material box;2, the molten sand device of the first electric-controlled mechanical;3, concentration meter;4, hot water regulating valve;5, hot water Check-valves;6, material check-valves;7, memory is diluted;8, the molten sand device of the second electric-controlled mechanical;9, temperature sensor;10, steam Regulating valve;11, steam check-valves;12, liquid level sensor;13, raw material check-valves.
Specific embodiment
The utility model is described in detail with reference to the accompanying drawings and examples.
As shown in Figure 1, the utility model discloses a kind of molasses to dilute automatic control system, including the 1, first electricity of material box Control mechanical molten sand device 2, controller and the display/loader being connected with controller.The controller be DCS or PLC controller, It is installed in cabinet.
The material box 1 is connected by mother tube with molten 2 import of sand device of the first electric-controlled mechanical, is preferably set on mother tube There is raw material check-valves 13.The import of the molten sand device 2 of first electric-controlled mechanical also passes through hot-water line and is connected with external boiler, In Hot water regulating valve 4 is installed on hot-water line, the hot water regulating valve 4 is electrically connected with the output end of controller, in order to avoid flowing back, Hot-water check valve 5 is preferably provided between the hot water regulating valve 4 and external boiler.The molten sand device 2 of first electric-controlled mechanical Outlet is connected by feed pipe with external boiling pan, and the molten sand device 2 of the first electric-controlled mechanical is also electrically connected with the output end of controller; Concentration meter 3 is installed on feed pipe, the best concentration meter 3 is optics concentration meter, and the concentration meter 3 is defeated with controller Enter end electrical connection.In order to avoid reflux, material non-return is preferably provided between concentration meter 3 and the molten sand device 2 of the first electric-controlled mechanical Valve 6.
This preferred embodiment further includes dilution memory 7, and the dilution memory 7 is set to feed pipe and sugar is boiled in outside Between tank, the molten sand device 8 of the second electric-controlled mechanical, the molten sand device 8 of second electric-controlled mechanical are externally provided in the dilution memory 7 Import and export passes through delivery pipe respectively and connect with dilution memory 7.
The dilution memory 7 is equipped with for detect the temperature sensor 9 for diluting temperature in memory 7, in this way can be with The temperature of molasses in memory 7 is constantly diluted, the temperature sensor 9 is electrically connected with the input terminal of controller;The dilution is deposited Reservoir 7 is connect by jet chimney with external steam generator, and the jet chimney is equipped with steam control valve 10, the steam tune Section valve 10 is electrically connected with the output end of controller, is preferably provided with steaming between the steam control valve 10 and external steam generator Vapour check-valves 11.
The sensor for detecting material liquid level in dilution memory 7, the liquid can be equipped on the dilution memory 7 Level sensor 12 is electrically connected with the input terminal of controller.The liquid level in dilution memory 7 can be monitored in this way, according to the effect for boiling sugar Rate controls the dilution power of molasses, guarantees the supply of Boiling Process molasses.
The utility model can also include at least a set of molten sand device of spare electric-controlled mechanical, to meet the needs of production.Institute The outlet for stating the molten sand device of spare electric-controlled mechanical is connected by feed pipe with the external boiling pan, is preferably provided on mother tube Raw material check-valves 13.The spare molten sand device of electric-controlled mechanical is also electrically connected with the output end of controller;It is equipped on spare hot-water line Spare hot water regulating valve 4, hot-water check valve 5 is preferably also installed on hot-water line, and the spare hot water regulating valve 4 is defeated with controller Outlet electrical connection.
In the preferred embodiment, the molten sand device 2 of first electric-controlled mechanical, the molten sand device 8 of the second electric-controlled mechanical, spare The molten sand device of electric-controlled mechanical is gear pump, is conveyed by being formed by swept volume variation and movement between pumping cylinder and meshing gear Hot water and raw material, and sand is quickly held by the mobile of the two.
The utility model also discloses a kind of molasses dilution autocontrol method simultaneously, includes the following steps, the control Device constantly receives the molasses brix that the molten sand device 2 of the first electric-controlled mechanical detected exports by cable, controller by with it is pre- If molasses brix calculate or logic judgment after, output signals to hot water regulating valve 4, control the aperture of hot water regulating valve 4 Size, and then it is constant to control the molten outlet of the sand device 2 molasses brix of the first electric-controlled mechanical;Controller send current molasses brix signal Enter display/loader, display/loader shows current molasses brix.
It is high that the controller also passes through the liquid level that cable constantly receives in the dilution memory 7 that liquid level sensor 12 detects It is low, after controller is by carrying out calculating or logic judgment with preset liquid level, output signals to the molten sand device of the first electric-controlled mechanical 2, it controls it and runs power, and then control whether the molten sand device 2 of the first electric-controlled mechanical starts.
It is high that the controller also passes through the liquid level that cable constantly receives in the dilution memory 7 that liquid level sensor 12 detects It is low, after controller is by carrying out calculating or logic judgment with preset liquid level, the molten sand device of spare electric-controlled mechanical is output signals to, It controls it and runs power, and then control dilution storage box constant liquid level.The controller also passes through cable and constantly receives the temperature The temperature height in the detection dilution memory 7 of sensor 9 is spent, controller is by carrying out calculating or logic judgment with preset temperature Afterwards, steam control valve 10 is output signals to, its opening size is controlled, and then it is constant to control dilution storage box temperature.
When the system works, it opens hot water valve check-valves and dilution hot water is added, open raw material check-valves 13, hot water and raw material Enter in the molten sand device 2 of the first electric-controlled mechanical simultaneously, raw material is mixed by way of with pump, is diluted, dilution is transported to Storage bin.Raw material has the raw material after 3 pairs of concentration meter dilutions to examine before after dilution, into dilution storage bin It surveys, then feeds back 4-20mA current signal to controller receiving module, the numerical value of feedback and system are arranged inside modules program Numerical value be compared, if the brix value of raw material is higher than the numerical value that system is arranged (low), just output control signal, (closing) hot water regulating valve 4 is proportionally opened, (reduction) is increased and enters water, so recycle, until the feedback that concentration meter 3 measures Until numerical value is identical as the numerical value of setting, system will stop adjusting, and keep into 4 apertures of hot water regulating valve, into steady control System.
The temperature control for diluting storage box passes through contact of the temperature sensor 9 with material, feedback 4-20mA signal to control The numerical value of feedback is compared by device, inside modules program with the numerical value that system is arranged, if the temperature of dilution storage box is than system Unite setting numerical value it is high (low), then just output control signal, proportionally opens (closings) steam control valve 10, increasing (reduction) quantity of steam so recycles, and until the fed back values of temperature sensor 9 and the numerical value of setting are identical, system will Stop adjustment, keep 10 aperture of steam control valve, into steady control.
Above-described embodiment is only further described the purpose of this utility model, technical scheme and beneficial effects Specific case, the utility model are not limited to this.All any modifications made within the scope of disclosure of the utility model, Equivalent replacement, improvement etc., are included in the protection scope of the present invention.

Claims (6)

1. molasses dilute automatic control system, it is characterised in that: including material box (1), the molten sand device (2) of the first electric-controlled mechanical, Controller and the display/loader being connected with controller;The material box (1) is molten by mother tube and the first electric-controlled mechanical (2) import of sand device is connected, and the import of the molten sand device (2) of the first electric-controlled mechanical also passes through hot-water line and external boiler phase Even, the outlet of the molten sand device (2) of the first electric-controlled mechanical is connected by feed pipe with external boiling pan, the molten sand of the first electric-controlled mechanical Device (2) is also electrically connected with the output end of controller;It is equipped on feed pipe concentration meter (3), the concentration meter (3) and controller Input terminal electrical connection, be equipped on hot-water line hot water regulating valve (4), the output of hot water regulating valve (4) and controller End electrical connection.
2. molasses according to claim 1 dilute automatic control system, it is characterised in that: it further include dilution memory (7), The dilution memory (7) is set between feed pipe and external boiling pan.
3. molasses according to claim 2 dilute automatic control system, it is characterised in that: on the dilution memory (7) Equipped with the liquid level sensor (12) for detecting dilution memory (7) interior material liquid level, the liquid level sensor (12) and control The input terminal of device is electrically connected;The dilution memory (7) is externally provided with the molten sand device (8) of the second electric-controlled mechanical, the second automatically controlled machine Molten sand device (8) import and export of tool formula passes through delivery pipe respectively and connect with dilution memory (7), the output end of the controller and the Molten sand device (8) electrical connection of two electric-controlled mechanicals.
4. molasses according to claim 2 dilute automatic control system, it is characterised in that: on the dilution memory (7) Equipped with the temperature sensor (9) for detecting dilution memory (7) interior temperature, the temperature sensor (9) is defeated with controller Enter end electrical connection;The dilution memory (7) is connect by jet chimney with external steam generator, is set on the jet chimney There are steam control valve (10), which is electrically connected with the output end of controller.
5. molasses according to claim 1 dilute automatic control system, it is characterised in that: further include at least a set of standby electricity Mechanical molten sand device is controlled, the outlet of the spare molten sand device of electric-controlled mechanical is connected by feed pipe with the external boiling pan, The spare molten sand device of electric-controlled mechanical is also electrically connected with the output end of controller;Spare hot water regulating valve is installed on spare hot-water line (4), the spare hot water regulating valve (4) is electrically connected with the output end of controller.
6. according to claim 1, molasses described in 3 or 5 dilute automatic control system, it is characterised in that: the first automatically controlled machine The molten sand device (2) of tool formula, the molten sand device (8) of the second electric-controlled mechanical, the molten sand device of spare electric-controlled mechanical are gear pump.
CN201920147230.9U 2019-01-23 2019-01-23 Molasses dilute automatic control system Active CN209702773U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109628650A (en) * 2019-01-23 2019-04-16 钦州中誉仪器有限公司 Molasses dilute automatic control system and method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109628650A (en) * 2019-01-23 2019-04-16 钦州中誉仪器有限公司 Molasses dilute automatic control system and method

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