CN2713461Y - On-line autocontrol detector for syrup brix - Google Patents

On-line autocontrol detector for syrup brix Download PDF

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Publication number
CN2713461Y
CN2713461Y CN 200420065068 CN200420065068U CN2713461Y CN 2713461 Y CN2713461 Y CN 2713461Y CN 200420065068 CN200420065068 CN 200420065068 CN 200420065068 U CN200420065068 U CN 200420065068U CN 2713461 Y CN2713461 Y CN 2713461Y
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China
Prior art keywords
syrup
weighing
pipe
container
brix
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Expired - Fee Related
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CN 200420065068
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Chinese (zh)
Inventor
温武才
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Individual
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Individual
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Priority to CN 200420065068 priority Critical patent/CN2713461Y/en
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Publication of CN2713461Y publication Critical patent/CN2713461Y/en
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Abstract

The utility model discloses an on-line automatic detector for syrup brix, compising a control box which controls the brix detection of a plurality of syrup evaporating pots, and a computer. Each evaporating pot is connected by input/output pipelines. The on-line automatic detector for syrup brix is characterized in that the on-line automatic detector for syrup brix also is composed of a feed pipe which is mutually communicated with the output pipe of the evaporating pot, a bucket weighing container, the overflow pipe and the outlet pipe of the bucket weighing container, and the fixed capacity weighting devices of a weighing sensor. Wherein, the feed pipe and the overflow pipe are positioned at the upper part of the weighing container and are mutually communicated with the weighing container; the controlled box of an electromagnetic valve and the control of the computer are arranged in the feed pipe and the outlet pipe; one fixed capacity weighting device is configured on the output pipeline of each evaporating pot. The syrup weight signal in the container is measured through the weighing sensor mutually communicated with the weighing container, and the weight signal are transferred to the control box and the computer; the syrup brix can be displayed on a display by the signal amplifying, the A/D signal converting and the data analyzing and processing of the computer. The on-line automatic detector for syrup brix is suitable for the brix detection of sugar industry.

Description

The on-line automatic control detection device of syrup hammer degree
Technical field
The utility model relates to a kind of measurement mechanism of strength of fluid, especially the measurement mechanism of syrup hammer degree.
Background technology
At present sugar industry detects syrup density on producing, and promptly the mode of degree of hammer into shape has two kinds, a kind ofly detects for traditional artificial glass concentration meter; This detection mode hand labor intensity is big, is difficult to frequent detection.Another kind of for utilizing the characteristic that signal can weaken behind the syrup in the gamma rays piping, along with the different principle of the unlike signal attenuation degree of syrup concentration detects.This pick-up unit has the defective of several aspects: 1, belong to radioactive product, human body is had certain injury; When 2, detecting, if pipeline syrup instability of flow or syrup bubble are more, testing result is untrue; 3, sensing range is narrow, can only detect point of terminal steam tank at present.
Summary of the invention
The purpose of this utility model provides a kind of syrup hammer degree on-line automatic detection device, and it should be able to conveniently detect, and reduces labour intensity, and is harmless, and, the wide and precision height of sensing range.
The utility model comprises control box and the computing machine that several syrup evaporator hammer degree of control detect, and connects with importing/go out pipeline between each evaporator, it is characterized in that also comprising:
Feed pipe communicates with described evaporator efferent duct, contain bucket type weigh container and run-down pipe and vent pipe, and the constant volume weighing apparatus of LOAD CELLS, wherein, feed pipe and run-down pipe communicate with it in the upper end of the container of weighing, and are provided with the control of controlled case of solenoid valve and computing machine in feed pipe and the vent pipe;
Constant volume weighing apparatus of configuration on the output channel of each evaporator.
The syrup hammer degree on-line automatic detection device of said structure, the container of weighing in the constant volume weighing apparatus is known volume, open the electromagnetic valve on the feed pipe, add syrup, syrup is discharged by run-down pipe after being full of the container of weighing, and closes inlet valve, allows extra syrup be continued to discharge by run-down pipe, until the capacity of setting, assert that promptly the syrup volume in the container of weighing is known volume; Measure syrup weight signal in this container by the LOAD CELLS that interrelates with the container of weighing, this weight signal is passed to control box, through signal amplification, A/D conversion of signals, send data-signal to computing machine again, carry out data analysis by computing machine and handle, contrast corresponding syrup standard, on display, demonstrate the syrup hammer degree of being surveyed, the hammer degree is the professional term of sugar industry, and the density of expression syrup is represented with BX, below continues to use.The advantage of this device is: 1, can measure syrup density 5~80BX, syrup density general range is 20~80BX, and measurement range is wide; 2, measuring accuracy height, nominal error are ± 0.2BX that production requirement is ± 0.5BX; Measuring speed is fast, measures once, and satisfies production requirement far away in per 3 minutes; 3, be not subjected to pipeline syrup flow size and the contained influence of air bubbles of syrup; 4, but a cover pick-up unit multiple spot detects, and forms a monitoring system, can be the further full-automatic computer supervisory control system of a whole set of syrup evaporation and concentration of exploitation of basis according to this, realizes automated production management, replaces traditional manually-operated production at present.
Description of drawings
Shown in Figure 1, be structural representation of the present utility model.
Shown in Figure 2, be the weigh structural representation of container 6 of constant volume among Fig. 1.
Embodiment
By in the utility model structural representation of Fig. 1 as can be known, general sugar refinery produces the syrup that needs sugarcane juice evaporation and concentration to 60~65BX of 14BX because the continuity in sugar refinery is uninterruptedly produced, turnout is big, will work without cessation with five large-scale evaporators 1 usually.Step by step through becoming the syrup of high concentration behind five evaporators 1, each evaporator 1 all evaporates the syrup of a certain concentration to the syrup evaporation process by the syrup of low concentration.Syrup is from input pipe 2 input of first evaporator 1, and by 4 outputs of the 5th jar efferent duct, per two pipelines 3 between adjacent promptly are the efferent ducts of last evaporator, also are the input pipes of back one evaporator.Feed pipe 5 one ends of the present utility model communicate with pipeline 3 between per two evaporators 1, and the other end communicates with the container of weighing of constant volume weighing apparatus 6, and the syrup of introducing corresponding evaporator 1 detects.Five evaporators 1 are corresponding to be provided with five constant volume weighing apparatus 6.Electrical equipment in each quantitative weighing device and signal are by the control of control line 7 controlled casees 8 and computing machine 9, wherein, the signal of weighing is passed in control box 8 and the computing machine 9, through signal amplification, mould/processing such as number conversion of signals, after computing machine carries out corresponding data analysis processing, can on display, demonstrate the syrup hammer degree of each evaporator 1 and place on record, may be implemented in line and detect automatically.Described control box 8 and computing machine 9 can be bought or assemble on present market, and those skilled in the art also realize easily, so belong to prior art.
Shown in Figure 2, be the weigh structural representation of container of constant volume in the utility model, it comprise base 10, down solenoid valve 11, run-down pipe 12, shell 13, go up solenoid valve 14, LOAD CELLS 15, bucket type weigh container 16, vent pipe 18 and shell recirculatory pipe 17.Wherein, last solenoid valve 14 is controlled ending and conducting of feed pipes 5, and the mouth of pipe of feed pipe 5 is located at container 16 places suitable for reading of weighing.The weigh lower end of container 16 is a bucket shape, the end opening of bucket be provided with vent pipe 18 and down solenoid valve 11 controls its by and conducting.Container 16 upper ends one side of weighing that is located at suitable for reading of run-down pipe 12 communicates with it, and set this overflow mouth of pipe and the following vessel space of weighing of end surface level that container 16 inboards hand over of weighing, known volume for the container of weighing, hold required syrup of weighing, this known volume the utility model is set at one liter.LOAD CELLS 15 and weigh and be provided with the draw bail of weighing between the container 16.Be that sensor 15 obtains metrical informations, after the container of weighing advanced or arrange syrup, sensor 15 had to be increased or the phenomenon of minimizing pressure, makes it to produce current signal, and this signal was passed to control box 8 and computing machine 9 converts.The scope of weighing of this LOAD CELLS 15, the utility model are selected five kilograms for use.LOAD CELLS 15 is located on the outside of shell 13, is connected with control box 8 with computing machine 9 by control line 7.LOAD CELLS 15 can be bought on the existing market, is prior art products.Below shell 13, be provided with recirculatory pipe 17, reclaim the syrup of discharging from run-down pipe 12 and the container 16 of weighing, recycling it.Base 10 plays supporting shell 13 and inner structure thereof.Upper and lower solenoid valve 14 and 11 controlled casees 8 and computing machine 9 controls.
The use of this syrup hammer degree on-line automatic detection device is existing explanation in summary of the invention, repeats no more.Need to prove and in above-mentioned, only adopted 5 check points, also establish a plurality of check points in actual applications, satisfy the needs of detection system.

Claims (2)

1, a kind of syrup hammer degree on-line automatic detection device, it controls control box (8) and the computing machine (9) that several syrup evaporator (1) hammer degree detect, and connects with importing/go out pipeline (3) between each evaporator (1), it is characterized in that also comprising:
Feed pipe (5) communicates with described evaporator (1) efferent duct (3), contain bucket type weigh container (16) and run-down pipe (12) and vent pipe (18), and the constant volume weighing apparatus (6) of LOAD CELLS (15), wherein, feed pipe (5) and run-down pipe (12) communicate with it in the upper end of the container of weighing (16), are provided with the control of solenoid valve (14 and 11) controlled casees (8) and computing machine (9) in feed pipe (5) and the vent pipe (18);
The output channel of each evaporator (1) (3,4) is gone up a configuration constant volume weighing apparatus (6).
2, syrup hammer degree on-line automatic detection device according to claim 1 is characterized in that:
Described run-down pipe (12) communicates with it in a side of the container of weighing (16) upper end, and set this overflow mouth of pipe and the following vessel space of weighing of the inboard end surface level of being handed over of the container (16) of weighing, be the known volume of the container of weighing (16), hold required syrup of weighing.
CN 200420065068 2004-06-24 2004-06-24 On-line autocontrol detector for syrup brix Expired - Fee Related CN2713461Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200420065068 CN2713461Y (en) 2004-06-24 2004-06-24 On-line autocontrol detector for syrup brix

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200420065068 CN2713461Y (en) 2004-06-24 2004-06-24 On-line autocontrol detector for syrup brix

Publications (1)

Publication Number Publication Date
CN2713461Y true CN2713461Y (en) 2005-07-27

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CN 200420065068 Expired - Fee Related CN2713461Y (en) 2004-06-24 2004-06-24 On-line autocontrol detector for syrup brix

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CN (1) CN2713461Y (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101968421A (en) * 2010-09-21 2011-02-09 中冶京诚工程技术有限公司 Method and device for monitoring pulp consistency in entire pipeline
CN102431092A (en) * 2010-09-29 2012-05-02 北京中煤矿山工程有限公司 Automatic proportioning device for clay slurry
CN102830670A (en) * 2012-08-17 2012-12-19 钦州市创华工控设备有限公司 Online dilution system and dilution method for sugar boiling material
CN103528919A (en) * 2013-10-22 2014-01-22 广西来宾永鑫小平阳糖业有限公司 Functional syrup brix online detection device with scale prevention character
CN106706469A (en) * 2016-12-16 2017-05-24 青岛海之源智能技术有限公司 In-container liquid information automatic measuring device
CN108414396A (en) * 2018-03-05 2018-08-17 贺明丽 Slurry density measurement device
CN108444865A (en) * 2018-03-05 2018-08-24 贺明丽 Self-cleaning type slurry density measurement device

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101968421A (en) * 2010-09-21 2011-02-09 中冶京诚工程技术有限公司 Method and device for monitoring pulp consistency in entire pipeline
CN102431092A (en) * 2010-09-29 2012-05-02 北京中煤矿山工程有限公司 Automatic proportioning device for clay slurry
CN102431092B (en) * 2010-09-29 2014-06-18 北京中煤矿山工程有限公司 Automatic proportioning device for clay slurry
CN102830670A (en) * 2012-08-17 2012-12-19 钦州市创华工控设备有限公司 Online dilution system and dilution method for sugar boiling material
CN102830670B (en) * 2012-08-17 2014-08-20 钦州市创华工控设备有限公司 Online dilution system and dilution method for sugar boiling material
CN103528919A (en) * 2013-10-22 2014-01-22 广西来宾永鑫小平阳糖业有限公司 Functional syrup brix online detection device with scale prevention character
CN106706469A (en) * 2016-12-16 2017-05-24 青岛海之源智能技术有限公司 In-container liquid information automatic measuring device
CN106706469B (en) * 2016-12-16 2019-08-06 詹夏丹 Fluid information self-operated measuring unit in a kind of container
CN108414396A (en) * 2018-03-05 2018-08-17 贺明丽 Slurry density measurement device
CN108444865A (en) * 2018-03-05 2018-08-24 贺明丽 Self-cleaning type slurry density measurement device

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C19 Lapse of patent right due to non-payment of the annual fee
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