CN201144171Y - Solid medicating device - Google Patents
Solid medicating device Download PDFInfo
- Publication number
- CN201144171Y CN201144171Y CNU2007201995366U CN200720199536U CN201144171Y CN 201144171 Y CN201144171 Y CN 201144171Y CN U2007201995366 U CNU2007201995366 U CN U2007201995366U CN 200720199536 U CN200720199536 U CN 200720199536U CN 201144171 Y CN201144171 Y CN 201144171Y
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- storage tank
- dry powder
- controller
- chemicals dosing
- dosing plant
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- Expired - Lifetime
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Abstract
The utility model discloses a solid drug-adding device; the drug-adding device includes a suction storage component, a cutting-in controller and a mixing conveying component; the suction storage component includes a blower and a dry power storage tank; one end of the blower is communicated with the upper end of the dry power storage tank by a pipeline; the cutting-in controller is arranged at the bottom part of the dry power storage tank; the mixing conveying component includes a drug receiver, a jet apparatus and a solvent storage tank that are communicated; one side of the drug receiver is provided with a high pressure water input pipeline which is respectively communicated with the drug receiver and the jet apparatus; one end of the solvent storage tank is provided with an output pipeline; the drug-adding device adopts the mode of directly adding solid and sucks the dry power drugs into the dry power storage tank by the blower, carries out adding and concentration control by the cutting-in controller and then carries out fully and effective mixing by the drug receiver, the jet apparatus and the solvent storage tank, thus not only ensuring the continuity of manufacture, avoiding the medicament from volatilization and losing effect, but also preventing environment pollution and hurting the health of a human body; the medicament concentration is also effectively controlled and the using effect of the medicament is improved.
Description
Technical field
The utility model relates to the medicine machine that is used for wastewater treatment, more particularly, relates to a kind of solid chemicals dosing plant, and this chemicals dosing plant can carry out solid and directly add, and the volatilization after avoiding dissolving was for a long time lost efficacy.
Background technology
At present, in field of waste water treatment, dosing method commonly used carries out for timing is concentrated, need earlier to adopt a dead lift that dry powder pharmaceutical is poured in the storage tank, by artificial estimation or distribution plate metering, dry powder pharmaceutical is added in the medicament dissolving tank, and mixes then by stirrer, carry out the drug concentration proportioning, thereby realize that liquid adds.But there is following shortcoming in this class I liquid I dosing method: because some dry powder pharmaceutical dissolves for a long time and deposits, volatilize easily and lost efficacy, thereby influenced water treatment effect; When a dead lift fell with throwing, dry powder pharmaceutical Chang Jiyi flew upward with floating, and very easily contaminate environment, and dry powder pharmaceutical very easily absorbs water, and corrodibility is very strong, and easily the physical and mental health to the workman can work the mischief; Artificial estimation is more rough, poor accuracy, adding consistency can't effectively be controlled, cause existing in the water excess enthalpy residual easily, and there is an interim decolorizing effect, and adopt distribution plate to be used for adding by the self gravitation of dry powder pharmaceutical, easily the caking because of dry powder pharmaceutical causes material stifled, and can't satisfy the quantity-produced needs; In addition, the density of the dry powder pharmaceutical that has is less, because the tension effect meeting of water swims on the water surface this dry powder pharmaceutical, makes stirring and mixing effect relatively poor, causes certain waste.
Therefore, need a kind of solid chemicals dosing plant that adopt the mode that solid directly adds, be used for overcoming the liquid dosing dry powder pharmaceutical of prior art volatile and lost efficacy, easy contaminate environment and cause human injury, adding consistency can't effectively be controlled and the dosing degree of mixing is relatively poor shortcoming.
The utility model content
At the above-mentioned shortcoming that exists in the prior art, the purpose of this utility model provides a kind of solid chemicals dosing plant, and this chemicals dosing plant not only can avoid the volatilization after the long-time dissolving to lose efficacy, and can also accurately control adding consistency and degree of mixing.
For achieving the above object, the utility model adopts following technical scheme:
This solid chemicals dosing plant comprises suction storage assembly, incision controller and mixes conveying assembly, sucks storage assembly and comprises blower fan and dry powder storage tank, and blower fan one end is communicated with dry powder storage tank upper end by pipeline; The incision controller is located at dry powder storage tank bottom, and is communicated with dry powder storage tank bottom; Mix conveying assembly and comprise and be subjected to medicine device, injector and solvent storage tank, be subjected to medicine device upper end to be positioned at the below of incision controller one end, be communicated with injector by medicine device lower end, be provided with respectively and the high pressure water input channel that be connected by medicine device and injector by medicine device one side; Injector one end is communicated with the solvent storage tank by pipeline, and solvent storage tank one end is provided with output channel.
Described incision controller one end is provided with electric motor, is provided with spiral conveyor rod in the incision controller, and spiral conveyor rod one end is connected with the transmission shaft of electric motor, and the other end is provided with scraper.
Also be connected with blade on the described spiral conveyor rod.
The other end of described incision controller is provided with medicine outlet, and the medicine outlet place also is provided with nichrome wire.
Described medicine outlet one end also is provided with the gland suitable with medicine outlet.
The bottom of described dry powder storage tank is awl bucket type structure, and the upper end of dry powder storage tank is provided with considers bag, and the inside of dry powder storage tank is provided with stirrer.
Also be provided with Powder level meter in the described dry powder storage tank.
It is described that to be subjected to the bottom of medicine device be the pyramid type structure.
Also be provided with the liquid level controller in the described solvent storage tank.
In technique scheme, solid chemicals dosing plant of the present utility model comprises suction storage assembly, incision controller and mixes conveying assembly, sucks storage assembly and comprises blower fan and dry powder storage tank, and blower fan one end is communicated with dry powder storage tank upper end by pipeline; The incision controller is located at dry powder storage tank bottom; Mix conveying assembly comprise be connected be subjected to medicine device, injector and solvent storage tank, be provided with respectively and the high pressure water input channel that be connected by medicine device and injector by medicine device one side; Solvent storage tank one end is provided with output channel.This chemicals dosing plant adopts the direct addition manner of solid, by blower fan dry powder pharmaceutical is directly sucked the dry powder storage tank, and add and concentration control by the incision controller, again by being subjected to the medicine device, injector and solvent storage tank carry out fully effectively mixing, just can be delivered to the on-the-spot use of wastewater treatment, guaranteed the continuity of producing, avoided long dissolving and deposit the medicament volatilization of existence and lost efficacy, prevent contaminate environment and injury HUMAN HEALTH, drug concentration also is controlled effectively, improve the result of use of medicament, saved cost, increased economic benefit.
Description of drawings
Fig. 1 is the structural representation of solid chemicals dosing plant of the present utility model;
Fig. 2 is the structural representation of the incision controller of chemicals dosing plant of the present utility model.
Embodiment
Further specify the technical solution of the utility model below in conjunction with drawings and Examples.
See also shown in Figure 1, chemicals dosing plant 10 of the present utility model comprises suction storage assembly 11, incision controller 12 and mixes conveying assembly 13, suck storage assembly 11 and comprise blower fan 111 and dry powder storage tank 112, blower fan 111 can adopt common roots blower, and these blower fan 111 1 ends are communicated with dry powder storage tank 112 upper ends by pipeline 14a; Dry powder storage tank 112 upper ends also are provided with the pipeline 14a place of communicating considers bag 113, be used for the dry powder pharmaceutical that sucks is filtered, dry powder storage tank 112 inside are provided with stirrer 114, by motor drive the dry powder pharmaceutical in the dry powder storage tank 112 is carried out elementary stirring, also be provided with Powder level meter 115 in the dry powder storage tank 112, the Powder level meter 115 that is provided with among Fig. 1 is two, is respectively applied for to measure the high spacing and low spacing of control dry powder storage tank 112 interior dry powder pharmaceuticals, and the bottom design of dry powder storage tank 112 is the pyramid type structure.Incision controller 12 is located at dry powder storage tank 112 bottoms, and is communicated with dry powder storage tank 112 bottoms; Please in conjunction with shown in Figure 2, incision controller 12 1 ends are provided with electric motor 121, incision controller 12 inside are provided with spiral conveyor rod 122, spiral conveyor rod 122 1 ends are connected with the transmission shaft of electric motor 121, drive by electric motor 121, spiral conveyor rod 122 rotations are advanced, and spiral conveyor rod 122 rotation advance distances are directly proportional with the rotating speed of electric motor 121, add dose thereby just can regulate, promptly effectively controlled the concentration of medicament by control electric motor 121 rotating speeds.Also be connected with blade on the spiral conveyor rod 122, it is built on stilts effectively to prevent to lump after dry powder pharmaceutical from making moist, and guarantees medicament whereabouts uniformity; The other end of spiral conveyor rod 122 is provided with scraper 123, is used to prevent that medicament from piling up because of making moist, and guarantees that the precision of medicament adds.The other end of incision controller 12 is provided with medicine outlet 124 because when dosing, medicine outlet 124 belows had on certain water vapour by the medicine device to emit, heat, prevent the dry powder pharmaceutical deliquescence by nichrome wire 125 being set at medicine outlet 124 places.Nichrome wire 125 1 ends also are provided with baffle plate 126, and medicine outlet 124 1 ends also are provided with the gland 127 suitable with medicine outlet 124, when carrying out dosing, gland 127 must be opened, when stopping dosing, then gland 127 is covered on the medicine outlet 124, play the seal isolation effect.Mixing conveying assembly 13 comprises and is subjected to medicine device 131, injector 132 and solvent storage tank 133, be subjected to medicine device 131 upper ends to be positioned at medicine outlet 124 belows of incision controller 12 1 ends, receive the medicament of incision controller 12 outputs, be subjected to the bottom of medicine device 131 also to be designed to the pyramid type structure, and be communicated with injector 132, injector 132 can adopt common Wen's injector, and these injector 132 1 ends are communicated with solvent storage tank 133 by pipeline 14b.Be provided with respectively and the high pressure water input channel 14c that be connected by medicine device 131 and injector 132 by medicine device 131 1 sides, be respectively equipped with magnetic valve 141 on the high pressure water input channel 14c, the switch of control high pressure water input.Solvent storage tank 133 has agitating function, can prevent precipitation, and solvent storage tank 133 1 ends are provided with output channel 14d, and output channel 14d is provided with turbo-pump 134, for the output of liquid medicine provides power.Also be provided with liquid level controller 135 in the solvent storage tank 133, the liquid level in the solvent storage tank 133 is detected and controls.
During use, this chemicals dosing plant 10 can also can be controlled operation by PLC automatically directly by the manual operation operation.At this automatic control operation is illustrated: measure and output signal to PLC by the dry powder pharmaceutical in 115 pairs of dry powder storage tanks 112 of Powder level meter earlier, when the medicament position reaches low spacing height, PLC not only can control and carry out light and audible alarm, also may command starts blower fan 111, aspirate dry powder pharmaceutical by the negative-pressure siphon effect, and be delivered in the dry powder storage tank 112; When the medicament input position in the dry powder storage tank 112 reached the upper limit height of setting, PLC sends control signal made blower fan 111 stop suction, thereby can avoid wasting time and energy of artificial remote carrying, contaminate environment and cause personal injury; The stirrer 114 that starts then in the dry powder storage tank 112 carries out the dry powder stirring, dry powder input incision controller 12 in the dry powder storage tank 112, open the gland 127 of medicine outlet 124 and start spiral conveyor rod 122 this moment, the dry powder input is subjected in the medicine device 131, and can control electric motor 121 rotating speeds of spiral conveyor rod by PLC, thereby regulate the work output of dry powder, play the effect of accurate control dry powder pharmaceutical concentration; Simultaneously, magnetic valve 141 on the high pressure water input channel 14c is opened automatically, high pressure water is along injected by the tangential direction of medicine device 131, and form vortex and carry out mixed dissolution with dry powder pharmaceutical, and pass through injector 132 under the effect of high pressure water, with the dissolving of dry powder pharmaceutical uniform and complete be absorbed in the water, be delivered to then in the solvent storage tank 133, effectively solve the easy buoyant dry powder of some dry powder and be difficult to the blended problem, improved degree of mixing and service efficiency, saved cost; By turbo-pump 134 liquid medicine in the solvent storage tank 133 is delivered to the production scene that needs dosing at last, and carry out Level Detection and control by liquid level controller 135, when liquid level is lower than setting height, closes turbo-pump 134 automatically, and continue the input liquid medicine.More than all controls all can by with upper computer networking, realize Long-distance Control.
After having adopted this chemicals dosing plant 10, regulate dry powder pharmaceutical concentration according to water yield size, and control stabilization makes that at 60~80mg/L wastewater treatment 100% is up to standard, effect is fairly obvious.
Those of ordinary skill in the art will be appreciated that, above embodiment is used for illustrating the utility model, and be not to be used as qualification of the present utility model, as long as in connotation scope of the present utility model, all will drop in claims scope of the present utility model variation, the modification of the above embodiment.
Claims (9)
1. solid chemicals dosing plant is characterized in that:
This chemicals dosing plant comprises suction storage assembly, incision controller and mixing conveying assembly,
Suck storage assembly and comprise blower fan and dry powder storage tank, blower fan one end is communicated with dry powder storage tank upper end by pipeline;
The incision controller is located at dry powder storage tank bottom, and is communicated with dry powder storage tank bottom;
Mix conveying assembly and comprise and be subjected to medicine device, injector and solvent storage tank, be subjected to medicine device upper end to be positioned at the below of incision controller one end, be communicated with injector by medicine device lower end, be provided with respectively and the high pressure water input channel that be connected by medicine device and injector by medicine device one side; Injector one end is communicated with the solvent storage tank by pipeline, and solvent storage tank one end is provided with output channel.
2. solid chemicals dosing plant as claimed in claim 1 is characterized in that:
Described incision controller one end is provided with electric motor, is provided with spiral conveyor rod in the incision controller, and spiral conveyor rod one end is connected with the transmission shaft of electric motor, and the other end is provided with scraper.
3. solid chemicals dosing plant as claimed in claim 2 is characterized in that:
Also be connected with blade on the described spiral conveyor rod.
4. solid chemicals dosing plant as claimed in claim 2 is characterized in that:
The other end of described incision controller is provided with medicine outlet, and the medicine outlet place also is provided with nichrome wire.
5. solid chemicals dosing plant as claimed in claim 4 is characterized in that:
Described medicine outlet one end also is provided with the gland suitable with medicine outlet.
6. solid chemicals dosing plant as claimed in claim 1 is characterized in that:
The bottom of described dry powder storage tank is awl bucket type structure, and the upper end of dry powder storage tank is provided with considers bag, and the inside of dry powder storage tank is provided with stirrer.
7. solid chemicals dosing plant as claimed in claim 6 is characterized in that:
Also be provided with Powder level meter in the described dry powder storage tank.
8. solid chemicals dosing plant as claimed in claim 1 is characterized in that:
It is described that to be subjected to the bottom of medicine device be the pyramid type structure.
9. solid chemicals dosing plant as claimed in claim 1 is characterized in that:
Also be provided with the liquid level controller in the described solvent storage tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNU2007201995366U CN201144171Y (en) | 2007-12-20 | 2007-12-20 | Solid medicating device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CNU2007201995366U CN201144171Y (en) | 2007-12-20 | 2007-12-20 | Solid medicating device |
Publications (1)
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CN201144171Y true CN201144171Y (en) | 2008-11-05 |
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Family Applications (1)
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CNU2007201995366U Expired - Lifetime CN201144171Y (en) | 2007-12-20 | 2007-12-20 | Solid medicating device |
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Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102531074A (en) * | 2010-12-21 | 2012-07-04 | 苏州市甘泉自动化环保设备厂 | Vibration rotation push type powder adding device |
CN104624071A (en) * | 2013-11-14 | 2015-05-20 | 宁夏中远天晟科技有限公司 | Automatic reagent feeding device of combined type automatic reagent feeding sledge for pretreating raw water of power plant |
CN105386080A (en) * | 2015-12-21 | 2016-03-09 | 云南驰宏锌锗股份有限公司 | Purifying additive pretreatment device with washing function for zinc hydrometallurgy |
CN108339423A (en) * | 2017-01-22 | 2018-07-31 | 温康 | A kind of continuous compounding process method of pulvis fracturing fluid |
CN108751422A (en) * | 2018-04-09 | 2018-11-06 | 沈阳双壹市政工程有限公司 | A kind of medicament delivery device |
CN109292929A (en) * | 2018-10-19 | 2019-02-01 | 南京瑞迪建设科技有限公司 | Water treatment agent dosing apparatus |
CN110156227A (en) * | 2019-05-31 | 2019-08-23 | 濮阳可利威化工有限公司 | A kind of sewage disposal system and method |
CN110180430A (en) * | 2019-05-17 | 2019-08-30 | 天津国投津能发电有限公司 | A kind of universal automatic preparing device of mushy stage medicament |
CN111825187A (en) * | 2020-08-13 | 2020-10-27 | 李佳海 | Energy-concerving and environment-protective sewage treatment plant that medicine can self-loopa |
CN113023797A (en) * | 2019-12-25 | 2021-06-25 | 江苏恒玮环保设备有限公司 | Add medicine mixed treatment device |
-
2007
- 2007-12-20 CN CNU2007201995366U patent/CN201144171Y/en not_active Expired - Lifetime
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102531074A (en) * | 2010-12-21 | 2012-07-04 | 苏州市甘泉自动化环保设备厂 | Vibration rotation push type powder adding device |
CN104624071A (en) * | 2013-11-14 | 2015-05-20 | 宁夏中远天晟科技有限公司 | Automatic reagent feeding device of combined type automatic reagent feeding sledge for pretreating raw water of power plant |
CN105386080A (en) * | 2015-12-21 | 2016-03-09 | 云南驰宏锌锗股份有限公司 | Purifying additive pretreatment device with washing function for zinc hydrometallurgy |
CN108339423A (en) * | 2017-01-22 | 2018-07-31 | 温康 | A kind of continuous compounding process method of pulvis fracturing fluid |
CN108751422A (en) * | 2018-04-09 | 2018-11-06 | 沈阳双壹市政工程有限公司 | A kind of medicament delivery device |
CN108751422B (en) * | 2018-04-09 | 2021-08-03 | 沈阳双壹市政工程有限公司 | Medicament delivery device |
CN109292929A (en) * | 2018-10-19 | 2019-02-01 | 南京瑞迪建设科技有限公司 | Water treatment agent dosing apparatus |
CN110180430A (en) * | 2019-05-17 | 2019-08-30 | 天津国投津能发电有限公司 | A kind of universal automatic preparing device of mushy stage medicament |
CN110156227A (en) * | 2019-05-31 | 2019-08-23 | 濮阳可利威化工有限公司 | A kind of sewage disposal system and method |
CN113023797A (en) * | 2019-12-25 | 2021-06-25 | 江苏恒玮环保设备有限公司 | Add medicine mixed treatment device |
CN111825187A (en) * | 2020-08-13 | 2020-10-27 | 李佳海 | Energy-concerving and environment-protective sewage treatment plant that medicine can self-loopa |
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GR01 | Patent grant | ||
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CX01 | Expiry of patent term |
Granted publication date: 20081105 |