CN105888716A - Biological liquid film dedusting system - Google Patents
Biological liquid film dedusting system Download PDFInfo
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- CN105888716A CN105888716A CN201610373047.1A CN201610373047A CN105888716A CN 105888716 A CN105888716 A CN 105888716A CN 201610373047 A CN201610373047 A CN 201610373047A CN 105888716 A CN105888716 A CN 105888716A
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- foam
- water
- tank body
- liquid film
- joint
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- E—FIXED CONSTRUCTIONS
- E21—EARTH DRILLING; MINING
- E21F—SAFETY DEVICES, TRANSPORT, FILLING-UP, RESCUE, VENTILATION, OR DRAINING IN OR OF MINES OR TUNNELS
- E21F5/00—Means or methods for preventing, binding, depositing, or removing dust; Preventing explosions or fires
- E21F5/02—Means or methods for preventing, binding, depositing, or removing dust; Preventing explosions or fires by wetting or spraying
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/04—Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour through foam
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/06—Spray cleaning
Abstract
The invention discloses a biological liquid film dedusting system which comprises an aerodynamic force device, a generating body device, a foam conveying device and a controlling and adjusting device. The generating body device is divided into a water-medicine mixing device and a foam generating device. The biological liquid film dedusting system is characterized in that the aerodynamic force device and the water-medicine mixing device are connected with two inlets of the foam generating device respectively, a foam spraying device is connected with an outlet of the foam generating device, the aerodynamic force device and the foam generating device are arranged independently, and the aerodynamic force device provides compressed air participating in reaction to the foam generating device and provides power to the system through the foam generating device. A power system and a generating system which are independent are arranged, so that diverse combining can be realized by increasing or decreasing single mainframe bodies according to different working environments and different working state needs.
Description
Technical field
The invention belongs to environmental technology field, relate to a kind of biological liquid film dust pelletizing system.
Background technology
The dust Control of the mine shattering process of China is administered at present is to process dust by the subsequent treatment of the chief minister's seal after dust produces, such as cloth bag dust suction, electrostatic precipitation and water spray dedusting etc..Process at pass-through mode after dust produces owing to belonging to sporadic at dust, the process needing to select multiple different equipment jointly to complete dust under different duties can be caused.
Liquid film dedusting is that the source of the dust to dust is controlled, thus reaches effective improvement of dust.Principle: the liquid film produced by biological liquid film dust removal machine is sprayed at the surface of ore uniformly, forms parcel to the surface of ore, also forms parcel rapidly thus reach the portion of dust and distribute during the continuous attrition crushing of ore.Also dust has been wrapped up while parcel ore, because liquid film is to pass through ionization process, its surface is with certain ionization, also dust is allowed to create electrostatic while liquid film parcel dust, allow mutually absorption between dust that little granule dust is aggregated into big dust particle, thus increase deadweight, automatic sedimentation.
Such as denomination of invention " liquid membrane dust suppression device " CN200910053553.2, disclose a kind of liquid membrane dust suppression device, the dust suppression being applied in the processing of solid material or migration process, including: dust suppression liquid film generator, there is housing, this housing is provided with dust suppression solution input, compressed air input and dust suppression liquid film output, dust suppression solution and compressed air and forms the dust suppression liquid film of thin-walled intensive rill shape through described dust suppression liquid film generator；And liquid film sprays portion, it is connected to liquid film output.This dust-arrest device also includes automatic control component, telecommunication parts and on-the-spot meteorological and dust monitoring parts, to be automatically adjusted the dust suppression liquid film amount of spraying according to field condition, and can realize remotely operating.In accordance with the invention it is possible to make the Dust Capacity at scene decline 80-95%, effect is fairly obvious, makes the dust pollution at scene be effectively controlled before not occurring at source, has both protected environment, be of value to again the healthy of site operation personnel.
Existing liquid film dust removal device or system mainly there is also technical deficiency in the following aspects:
1, existing main dust removal machine is integral type form, and dynamical system and generation system footprint are in a main body.Under different work installation environments, equipment cannot be reasonably installed, causing using scene, the parameter that can only set in producing device procedures according to it and size, to adapt to work on the spot state, can not make the adjustment of oneself because work on the spot state changes.As used the disintegrating apparatus at scene to carry out because equipment is old to upgrade or replacing etc., just cannot change the equipment of oneself, the most fixed working environment can only be adapted to.
2, the heat radiation of existing containment housing is the heat radiation realizing in casing by additional exhaust equipment, is outwards extracted hot blast in certain side of casing by machine power and realizes cooling.Cooling is realized owing to machine power can only be selected outwards to extract hot blast.The blocking that can cause air outlet long-term on probation of equipment, heat radiation easily causes equipment not in time because of high temperature, the service life of reduction equipment.
3, the water yield owing to requiring in the magnetization degree difference of different operating environment requirements water is different, if the tank body of magnetizing assembly is all to use fixed form, then magnetization treatment is also relatively fixed, and magnetized changeability is the strongest.
4, it is different due to different ore properties to foam and the absorption of water and adsorption capacity, under different geographical environments and different weathers, ore is the most different to foam and the absorption of water and adsorption capacity, simultaneously, different uses on-the-spot number of devices and the ratio difference to on-the-spot dust suppression, different bores and quantity number, the concrete condition being based on scene can be challenged flexibly.Therefore in the different foam of different operating environment requirements and the quantity of different foam, and existing foam-making apparatus is all set one or several fixing bore outside tank body straight-through, in hermetically sealed can, forms high pressure by gas and make foaming agent produce foam to pass through the straight-through outlet of one or several fixing bore.Cause selecting the multiple foaming generator set under different duties.The long-term on probation of equipment can result in blockage, and because fixed outlet body cannot be disassembled thus decreases the service life of tank body.
5, due to the fountain height different at different operating environment requirements and spray area, required place to be processed is different with position, is accomplished by bigger jet length and large-area sprinkling at depletion region.In narrow and small factory floor, it is accomplished by orientation or FX is sprayed.And if use single Gu Ding, sprayed to discharge end by pipeline chaining after pressurization, fountain height and limited area.
Meanwhile, because the equipment of dust point has multiple pattern and Multiple Type, the mode of its dust also has suction type and distributes the multiple different forms such as formula, therefore, what is desired is that different use spray patterns under different forms.
Summary of the invention
For above-mentioned the deficiencies in the prior art, present invention aim at providing a kind of biological liquid film dust removal machine, be made up of dynamical system and two independent systems of generation system.Dynamical system is to provide the liquid film of whole biological liquid film dust removal machine and occurs and the power of conveying.Generation system is to carry out output tables by several groups of generators to wear the liquid film of ionization.
The technical solution used in the present invention is:
A kind of biological liquid film dust pelletizing system, it includes jet power unit, there is agent set, foam delivery device and control and regulation device, agent set is occurred to be divided into water medicine mixing arrangement and foam-making apparatus, jet power unit is connected with two inlet part of foam-making apparatus respectively with water medicine mixing arrangement, foam unit is connected with the exit portion of foam-making apparatus, jet power unit is independently arranged with foam-making apparatus, on the one hand jet power unit provides the compressed air participating in reaction for foam-making apparatus, on the other hand power is provided further through foam-making apparatus for system.
Further, described jet power unit includes that dynamic host casing, screw air compressor and bedroom air accumulator, screw air compressor and bedroom air accumulator are arranged in dynamic host casing side by side, and dynamic host casing upper end is provided with the eaves formula ceiling that wafts；
Further preferably, described jet power unit also includes sensor, electrical ball valve and pressure regulator valve；Pipeline between screw air compressor and bedroom air accumulator is provided with sensor, and the outlet conduit of bedroom air accumulator is provided with sensor and pressure regulator valve, and the compressed gas in the air accumulator of bedroom enters foam-making apparatus through pressure regulator valve pressure regulation.
Further, described water medicine mixing arrangement is divided into passway for water arranged side by side and medicine road device；
Further preferably, described passway for water includes the first ionizing magnetizing device and inner water-tank, water pipe is connected by the import of electrical ball valve and the first ionizing magnetizing device, the outlet conduit of the first ionizing magnetizing device is provided with flowmeter, the outlet conduit end of the first ionizing magnetizing device accesses in inner water-tank casing, and inner water-tank is provided with liquid level gauge；
Further preferably, described medicine road device includes the second ionizing magnetizing device and built-in medicine-chest, water pipe is connected by the import of electrical ball valve and the second ionizing magnetizing device, the outlet conduit of the second ionizing magnetizing device is provided with flowmeter, the outlet conduit end of the second ionizing magnetizing device accesses in built-in medicine-chest casing, and built-in medicine-chest is provided with liquid level gauge.
Further, ionizing magnetizing device includes main tank body and permanent magnetic strong magnetic rod；Main tank body one end is connected with reducing inlet union, and the upside end of main tank body is connected with reducing outlet connection, and permanent magnetic strong magnetic rod is arranged on the periphery of main tank body；
Further preferably, main tank body is provided with a pair bar magnet snap joint, and permanent magnetic strong magnetic rod is arranged on the periphery of main tank body by a pair bar magnet snap joint, and excellent and main tank body the axis of permanent magnetic strong magnetic is parallel；
Further preferred, bar magnet snap joint is snap ring-type chuck, and bar magnet snap joint is enclosed within main tank body, is provided with bar magnet erection joint inside the snap ring of bar magnet snap joint.
Further, the outlet conduit of passway for water is provided with centrifugal pump, and water enters proportioning pump by centrifugal pump pressurization；The outlet conduit of medicine road device is connected with proportioning pump；The outlet conduit of passway for water is connected in parallel by proportioning pump with the outlet conduit of medicine road device, after water and medicament carry out dosages distribution by proportioning pump, externally exports.
Further, the pipeline between water medicine mixing arrangement and foam-making apparatus is provided with flowmeter, electrical ball valve and sensor.
Further, the generation tank body of foam-making apparatus includes that upper tank body and lower tank, upper tank body top are provided with foam outlet device；
Further preferably, generation tank body is connected by external screw thread lower tank and the upper tank body of internal thread connection form；
Further preferably, foam outlet device is made up of at least two elbow, and elbow is each provided with foam outlet, and foam outlet is set up in parallel；
Further preferably, foam-making apparatus includes that aqueous vapor enters device altogether, enters device with aqueous vapor altogether and be connected bottom lower tank.
Further, aqueous vapor is entered device altogether and is included triple valve, excessively leather pipe joint and hydraulic conversion joint, is connected with the straight-through port of triple valve by straight through flow adjustable valve bottom lower tank, and triple valve one end is connected with water leather pipe joint by quick slip-knot, leather pipe joint excessively；The triple valve other end is connected with gas-tpe fitting by hydraulic conversion joint.
Further, foam delivery device includes that dry fog flusher and/or foam unit, one end of dry fog flusher and/or foam unit are connected with foam-making apparatus.
Further preferably, dry fog flusher includes hydraulic conversion joint, stainless steel mobile jib and stainless steel connecting rod, hydraulic conversion joint is connected with stainless steel mobile jib, stainless steel mobile jib is divided into two sections, connect between two sections and have 360 degree of chicksans, stainless steel mobile jib top is connected with stainless steel connecting rod by threeway, and the two ends of stainless steel connecting rod are provided with gimbaled nozzle joint；
Further preferably, foam unit includes that component is curved through pipe and component main body tube, component is curved through managing as semicircular ring tubular structure, component is curved is provided with leather pipe joint in the middle part of pipe ring tube, the curved two ends through pipe of component connect with component main body tube, component main body tube is uniformly provided with several foams and sprays the mouth of pipe.
Further preferably, the two ends of component main body tube be provided with semicircle capping seal.
Beneficial effect of the present invention is obvious:
Total beneficial effect: split-type design, dynamical system is separately easy to can separate under different duties from generation system reasonably adjust.Waft eaves formula ceiling, it is not necessary to the most quickly dissipates by external force.Bedroom air accumulator increases the reserves of caching gas in limited space, reduces frequently loading and unloading of air compressor machine.Dismountable type generator and the loose joint of setting and adjustable straight-through adjusting valve, the consumption that in the case of not changing whole dynamic host structure, can strengthen biological liquid film guarantees stablizing of onsite application.Therefore, split-type design of the present invention, dismountable type parts, can effectively guarantee that different duties is on-the-spot, either change because of ore properties or the renewal etc. of the equipment of production reasonably can adjust the dust removing effects that parts reach constant in the case of not changing complete machine.
1, it is made up of two independent systems (dynamical system and generation system).Dynamical system is to provide the liquid film of whole biological liquid film dust removal machine and occurs and the power of conveying.Generation system is to carry out output tables by several groups of generators to wear the liquid film of ionization.Duty that can be according to different working environments and different needs, and can carry out multiple combinations by the size increasing or reducing individual host main body.
2, waft the design at eaves formula ceiling top, natural heat dissipation, it is not necessary to by other mechanical energy.
3, duty that can be according to different working environments and different needs, and import in agent set can be occurred directly to be actually needed through reaching by increasing or reducing.
4, it is easy to, according to actual duty, change and clean foam-making apparatus tank interior the most efficiently, extends the life-span on probation.After solution equipment uses for a long time, in tank body can generation dirt more or less or other sediments, the most do not clean the using effect that is easy for resulting in blockage or reducing, arrive and the most just cannot use, can only the problem of integral replacing.
5, when after formation of foam, can be according to different working environments, and different duties needs, can be stimulated the menstrual flow by the export volume or outlet that foam delivery device is increased or decreased and reach to be actually needed, the most also pipe interior can be maintained and clears up by disassembling of stimulating the menstrual flow, solution equipment uses the generation dirt or other sediments understood in tank body more or less for a long time, long-time cleaning is easy for resulting in blockage or reducing using effect, arrive and the most just cannot use, can only the problem of integral replacing.
6,360 degree rotate can be according to different working environments and different duty need, can select to be rotated up to be actually needed.
Accompanying drawing explanation
Fig. 1 is the general system set-up schematic diagram of the embodiment of the present invention 1.
Fig. 2 is the structural representation of the embodiment of the present invention 1 power subject.
Fig. 3 is the structural representation that the embodiment of the present invention 1 occurs main body.
Fig. 4 is the partial structurtes schematic diagram that the embodiment of the present invention 1 occurs main body.
Fig. 5 is the angle quick change fixed platform mounting structure schematic diagram that the embodiment of the present invention 1 occurs main body.
Fig. 6 is the magnetization ionization device structural representation of the embodiment of the present invention 1.
Fig. 7 is the embodiment of the present invention 1 foam-making apparatus structural representation.
Fig. 8 is the embodiment of the present invention 1 foam outlet device main TV structure schematic diagram.
Fig. 9 is the embodiment of the present invention 1 foam outlet device side-looking structural representation.
Figure 10 is that the aqueous vapor of the embodiment of the present invention 1 enters apparatus structure schematic diagram altogether.
Figure 11 is the embodiment of the present invention 1 dry fog flusher structural representation.
Figure 12 is the embodiment of the present invention 1 foam unit structural representation.
Detailed description of the invention
The present invention is described further with specific embodiment below in conjunction with the accompanying drawings, but, the scope of the present invention is not limited to following embodiment.
Embodiment 1:
With reference to Fig. 2, the integral power device of equipment is mainly by dynamic host casing (eaves formula structure of wafing), screw air compressor 1 and bedroom air accumulator 2 form, the buffer storage of the integral power that screw air compressor 1 is the generating means of the integral power of equipment and bedroom air accumulator 2 is equipment, and above-mentioned two device is to be arranged on side by side in dynamic host casing, it is to meet the effective natural heat dissipation of high temperature energy because producing when screw air compressor 1 produces that dynamic host casing upper end is provided with the eaves formula ceiling 11 that wafts, performance is arranged to obtain according to air heat air lift is outer, there is the cooling system of setting upper end plus air compressor machine 1, it it is upwards air draft principle.
The gas that screw air compressor 1 operationally produces is transported in bedroom air accumulator 2 caching, then is provided the aerodynamic force of constant voltage 8 kilograms to required equipment by bedroom air accumulator 2.The heat that screw air compressor produces is got rid of by the eaves formula ceiling 11 that wafts.
With reference to Fig. 3, generation main body is the generation part of whole equipment.Main body is occurred to include main body cabinet, water tank 3, chemical tank 4, generator tank body 6, ionizing magnetizing device 307, proportioning pump 507 and centrifugal multistage pump multiple centrifugal pump 306；Water pipe is connected with water tank 3 by flowmeter 304, flowmeter 304 is arranged on generation main body cabinet, water tank 3 provides the constant pressure of 6 kilograms to enter generator tank body 6 after drawing the medicament in chemical tank 4 by proportioning pump 507 by centrifugal multistage pump multiple centrifugal pump 306, the gas provided by dynamical system forms fission in generation tank body and connects with the external efferent duct of form of foam, ionizing magnetizing device 307 at least two compositions carry out ionizing magnetizing to the water of the medicament and water tank that are input into medicine-chest respectively, water medicine mixture is connected with generator tank body 6 by water inlet leather pipe joint 69, one stomidium pipe of generator tank body 6 is connected with bedroom air accumulator 2 by gas-tpe fitting 60.
Water is transported to inner water-tank 3 through ionizing magnetizing device 307 by flowmeter 304 from outer, and the water in water tank 3 is pressurizeed by centrifugal multistage pump multiple centrifugal pump, and the water after pressurization is drawn the external efferent duct of the medicament in chemical tank 4 by proportioning pump 507 and connected；Water medicine mixture enters generator tank body 6 by water inlet leather pipe joint 69 again, simultaneously, in gas in bedroom air accumulator 2 is transported to tank body 6 by gas-tpe fitting 60, in there is tank body 6, fast-neutron fission generation is carried out with water medicine mixture, and make the water medicine mixture after fission generate foam, occur the pressure in tank body 6 by regulation, control between 3.5 kilograms to 4.5 kilograms.
Occur main body partial structurtes with reference to Fig. 4,5, Fig. 5 angle quick change fixed platform mounting structure, be fixed platform itself be cave in occur main frame main body case in, arranging 129 ° of angles installed and being because fixed platform itself is to cave in the main body case that main frame occurs, in view of the size of hydraulic quick coupler and the size of other outlet devices of fixed platform, when using 129 ° of setting angles, ensure that snap joint does not highlights in whole casing, additionally also comply with replacing snap joint, enough spaces can be left, operate easier.Water medicine mixture, after occurring tank body 6 to occur, is transported to the position of required dust suppression through snap joint adapter.
Main tank body 72 and permanent magnetic strong magnetic rod 76 is included with reference to Fig. 6 ionizing magnetizing device；Main tank body 72 one end is connected with reducing inlet union 74, the upside end of main tank body 72 is connected with reducing outlet connection 71, main tank body 72 is provided with a pair bar magnet snap joint 73, permanent magnetic strong magnetic rod 76 is arranged on the tank wall of main tank body 72 by a pair bar magnet snap joint 73, permanent magnetic strong magnetic rod 76 is parallel with the axis of main tank body 72, bar magnet snap joint 73 is snap ring-type chuck, and bar magnet snap joint 73 is enclosed within main tank body 72, and the inside of bar magnet snap joint 73 is provided with bar magnet erection joint.Main tank body 72 is arranged on casing floor by main tank support 75.
Water inlet enters main tank body 72 by reducing inlet union 74 and water carries out under the strong magnetic action of permanent magnetic strong magnetic rod 76 electron ion strengthening, then is transported in required inner water-tank 3 by reducing outlet connection 71.
Medicament enters main tank body 72 by reducing inlet union 74 and medicament carries out under the strong magnetic action of permanent magnetic strong magnetic rod 76 electron ion strengthening, then is transported in required built-in medicine-chest 4 by reducing outlet connection 71.
Wherein under quickly the changing the outfit of bar magnet snap joint 73, quantity and the diameter of permanent magnetic strong magnetic rod can be quickly increased or decreased, strengthen or reduces magnetic, thus the ionization situation of water or medicament is produced change.
With reference to Fig. 7, foam-making apparatus includes upper tank body 62, lower tank 63 and triple valve 66；Lower tank 63 and the upper tank body 62 of internal thread connection that generation tank body is connected by external screw thread form, and upper tank body 62 top is provided with 90 degree of elbows 65 and foam outlet 61；Being connected with the straight-through port of triple valve 66 by straight through flow adjustable valve 64 bottom lower tank 63, triple valve 66 one end is connected with water leather pipe joint 69 by quick slip-knot 67, leather pipe joint 681 excessively；Triple valve 66 other end is connected with gas-tpe fitting 60 by hydraulic conversion joint 682.
Water medicine mixture enters triple valve 66 by water leather pipe joint 69, excessively leather pipe joint 681, quick slip-knot 67, enter in the generation tank body that the upper tank body 62 that the lower tank 63 connected by external screw thread and internal thread connect forms from straight through flow adjustable valve 64, pressed gas is entered in the generation tank body that the upper tank body 62 that triple valve 66, water medicine mixture and pressed gas enter the lower tank 63 connected by external screw thread simultaneously from straight through flow adjustable valve 64 and internal thread connects forms by gas-tpe fitting 60, hydraulic conversion joint 682 simultaneously.
Pressed gas and water medicine mixture are transported to required place to foam outlet 61, such as dry fog flusher and foam unit with form of foam by 90 degree of elbows 65 after fissioning in generation tank body.
The upper tank body 62 that the lower tank 63 connected by external screw thread with reference to the generation tank body of Fig. 8,9 foam-making apparatuses and internal thread connect forms, and upper tank body 62 top is provided with 90 degree of elbows 65 and foam outlet 61；By straight through flow adjustable valve 64 bottom lower tank 63；Foam outlet device is made up of 90 degree of elbows 65 of at least two, and elbow 65 is each provided with foam outlet 61, and foam outlet 61 is set up in parallel.The quantity of foam outlet 61 can be able to be increased or decreased according to on-the-spot needs among these.
The aqueous vapor of reference Figure 10 foam-making apparatus enters device altogether
Triple valve 66 one end is connected with water leather pipe joint 69 by quick slip-knot 67, leather pipe joint 681 excessively；Triple valve 66 other end is connected with gas-tpe fitting 60 by hydraulic conversion joint 682, and the straight-through port of triple valve 66 is connected bottom lower tank 63 by straight through flow adjustable valve 64.
Hydraulic conversion joint 85, stainless steel mobile jib 83 and stainless steel connecting rod 82 is included with reference to Figure 11 dry fog flusher；
Water with high pressure is connected with stainless steel mobile jib 83 by hydraulic conversion joint 85, stainless steel mobile jib 83 is divided into two sections, connect between two sections and have 360 degree of chicksans 84, stainless steel mobile jib 83 top is connected with stainless steel connecting rod 82 by threeway, and the two ends of stainless steel connecting rod 82 are provided with gimbaled nozzle joint 81.
Water through high pressure is entered high pressure internal thread stainless steel mobile jib 83 by hydraulic conversion joint 85, among these by 360 degree of chicksans 84, received by a threeway and set female high pressure stainless steel connecting rod 82, then assign on the gimbaled nozzle joint 81 at two ends.
Dry fog flusher one end is connected with foam-making apparatus, and the other end is sprayed directly in dust.
Include that component is curved through pipe 54 with component main body tube 51 with reference to Figure 12 foam unit, component curved through pipe 54 be semicircular ring tubular structure, component is curved is provided with leather pipe joint 55 in the middle part of pipe 54 ring tube, the curved two ends through pipe 54 of component connect with component main body tube 51, component main body tube 51 is uniformly provided with several foams and sprays the mouth of pipe 52.
Foam after generation passes through leather pipe joint 55, is being passed through to component main body tube 51 through pipe 54 by component is curvedManyIndividual foam sprays the mouth of pipe 52 and sprays the component of foam.Component main body tube 51 two ends are to be sealed by semicircle capping 53 among these.
General system set-up:
With reference to Fig. 1, biological liquid film dust pelletizing system includes jet power unit, agent set, foam unit and control and regulation device occurs, agent set is occurred to be divided into water medicine mixing arrangement and foam-making apparatus, it is divided into two tunnels from the point of view of pipeline is distributed, being gas circuit and water medicine mixing road respectively, water medicine mixing road is divided into again water route arranged side by side and medicine road.
Gas circuit, gas circuit is provided with sensor 101, electrical ball valve 102 and pressure regulator valve 103 etc. and controls device.
The pressed gas produced by screw air compressor 1 enters bedroom air accumulator 2 by sensor 101, Reasonable Regulation And Control by sensor 101 with electrical ball valve 102, it is transported to pressure regulator valve 103 and carries out constant pressure regulation, in pressed gas after regulation is delivered to tank body 6, in there is tank body 6, water medicine mixture after pressed gas and water medicine mixture occur fission and make fission generates foam, then is sprayed onto required position by foam unit 5.
Water medicine mixing road, connects with water medicine mixing road after being divided into water route arranged side by side and medicine road, water route and medicine road side by side in water medicine mixing road.
Water route, water route is provided with electrical ball valve 302, ionizing magnetizing device 307, flowmeter 304 and liquid level gauge 305 etc. and controls device.
The water ionizing magnetizing by ionizing magnetizing device 307, at electrical ball valve 302 with under the reasonable adjusting of flowmeter 304 and liquid level gauge 305, being transported in inner water-tank 3, the exit of inner water-tank 3 is provided with centrifugal pump 306, by the pressurization of centrifugal pump 306, enter proportioning pump 507.
Medicine road, medicine road is provided with electrical ball valve 402, flowmeter 404 and liquid level gauge 405 etc. and controls device.
The medicament (water medicament) ionizing magnetizing by ionizing magnetizing device 407, at electrical ball valve 402 and flowmeter 404 and the reasonable adjusting of liquid level gauge 405, it is transported in built-in medicine-chest 4, the outlet conduit of built-in medicine-chest 4 is connected with proportioning pump 507, after reasonably carrying out dosages distribution by proportioning pump 507, externally output is to water medicine mixing road.
Water medicine mixing road, water medicine mixing road is provided with electrical ball valve 602, flowmeter 604 and sensor 601 etc. and controls device.
Centrifugal pump 306 externally export into proportioning pump 507 draw after medicament after externally output merges, centrifugal pump 306 and proportioning pump 507 are under the common reasonable adjusting of flowmeter 604, electrical ball valve 602 and sensor 601, carry out the water medicine mixture after rational proportion and jointly enter in generation tank body 6, in there is tank body 6, water medicine mixture after pressed gas and water medicine mixture occur fission and make fission generates foam, then is sprayed onto required position by foam unit 5 and/or dry fog flusher.
When foam unit 5 and dry fog flusher are applied in combination, the gimbaled nozzle joint of the both ends or one end of stainless steel connecting rod 82 is connected with foam unit 5 by leather pipe joint.
Foam is entered high pressure internal thread stainless steel mobile jib through high pressure by hydraulic conversion joint, among these by 360 degree of chicksans, received by a threeway and set female high pressure stainless steel connecting rod, assign on the gimbaled nozzle joint at two ends again, entered component by leather pipe joint curved through pipe, spray the mouth of pipe from foam and be sprayed directly on dust.When gimbaled nozzle joint is connected with leather pipe joint, leather pipe joint is also to carry out 360 degree of rotations.Accordingly, it is capable to carry out 360 degree of rotations in the two directions, spraying range is wider, and adaptability is higher.
The constant air pressure of air compressor machine 8 kilograms, the air pressure constant of arrival generator is at 4 kilograms, and the constant water pressure of centrifugal multistage pump multiple centrifugal pump is at 6 kilograms.High water tank meter is set setting high, normal, basic three gears according to water tank size, and all systems of low water level are automatically switched off, and middle water level opens moisturizing, and high water level stops moisturizing.Medicine-chest liquid level gauge arranges two gears of height, low level Automatic Dosing, high-order stopping dosing.
Claims (9)
1. a biological liquid film dust pelletizing system, it includes jet power unit, there is agent set, foam delivery device and control and regulation device, agent set is occurred to be divided into water medicine mixing arrangement and foam-making apparatus, it is characterized in that, jet power unit is connected with two inlet part of foam-making apparatus respectively with water medicine mixing arrangement, foam unit is connected with the exit portion of foam-making apparatus, jet power unit is independently arranged with foam-making apparatus, on the one hand jet power unit provides the compressed air participating in reaction for foam-making apparatus, on the other hand power is provided further through foam-making apparatus for system.
A kind of biological liquid film dust pelletizing system the most according to claim 1, it is characterized in that, described jet power unit includes dynamic host casing, screw air compressor and bedroom air accumulator, screw air compressor and bedroom air accumulator are arranged in dynamic host casing side by side, and dynamic host casing upper end is provided with the eaves formula ceiling that wafts；
Further preferably, described jet power unit also includes sensor, electrical ball valve and pressure regulator valve；Pipeline between screw air compressor and bedroom air accumulator is provided with sensor, and the outlet conduit of bedroom air accumulator is provided with sensor and pressure regulator valve, and the compressed gas in the air accumulator of bedroom enters foam-making apparatus through pressure regulator valve pressure regulation.
A kind of biological liquid film dust pelletizing system the most according to claim 1, it is characterised in that described water medicine mixing arrangement is divided into passway for water arranged side by side and medicine road device；
Further preferably, described passway for water includes the first ionizing magnetizing device and inner water-tank, water pipe is connected by the import of electrical ball valve and the first ionizing magnetizing device, the outlet conduit of the first ionizing magnetizing device is provided with flowmeter, the outlet conduit end of the first ionizing magnetizing device accesses in inner water-tank casing, and inner water-tank is provided with liquid level gauge；
Further preferably, described medicine road device includes the second ionizing magnetizing device and built-in medicine-chest, water pipe is connected by the import of electrical ball valve and the second ionizing magnetizing device, the outlet conduit of the second ionizing magnetizing device is provided with flowmeter, the outlet conduit end of the second ionizing magnetizing device accesses in built-in medicine-chest casing, and built-in medicine-chest is provided with liquid level gauge.
A kind of biological liquid film dust pelletizing system the most according to claim 3, it is characterised in that ionizing magnetizing device includes main tank body and permanent magnetic strong magnetic rod；Main tank body one end is connected with reducing inlet union, and the upside end of main tank body is connected with reducing outlet connection, and permanent magnetic strong magnetic rod is arranged on the periphery of main tank body；
Further preferably, main tank body is provided with a pair bar magnet snap joint, and permanent magnetic strong magnetic rod is arranged on the periphery of main tank body by a pair bar magnet snap joint, and excellent and main tank body the axis of permanent magnetic strong magnetic is parallel；
Further preferred, bar magnet snap joint is snap ring-type chuck, and bar magnet snap joint is enclosed within main tank body, is provided with bar magnet erection joint inside the snap ring of bar magnet snap joint.
A kind of biological liquid film dust pelletizing system the most according to claim 3, it is characterised in that the outlet conduit of passway for water is provided with centrifugal pump, and water enters proportioning pump by centrifugal pump pressurization；The outlet conduit of medicine road device is connected with proportioning pump；The outlet conduit of passway for water is connected in parallel by proportioning pump with the outlet conduit of medicine road device, after water and medicament carry out dosages distribution by proportioning pump, externally exports.
A kind of biological liquid film dust pelletizing system the most according to claim 1, it is characterised in that the pipeline between water medicine mixing arrangement and foam-making apparatus is provided with flowmeter, electrical ball valve and sensor.
A kind of biological liquid film dust pelletizing system the most according to claim 1, it is characterised in that the generation tank body of foam-making apparatus includes that upper tank body and lower tank, upper tank body top are provided with foam outlet device；
Further preferably, generation tank body is connected by external screw thread lower tank and the upper tank body of internal thread connection form；
Further preferably, foam outlet device is made up of at least two elbow, and elbow is each provided with foam outlet, and foam outlet is set up in parallel；
Further preferably, foam-making apparatus includes that aqueous vapor enters device altogether, enters device with aqueous vapor altogether and be connected bottom lower tank.
A kind of biological liquid film dust pelletizing system the most according to claim 7, it is characterized in that, aqueous vapor is entered device altogether and is included triple valve, crosses leather pipe joint and hydraulic conversion joint, being connected with the straight-through port of triple valve by straight through flow adjustable valve bottom lower tank, triple valve one end is connected with water leather pipe joint by quick slip-knot, leather pipe joint excessively；The triple valve other end is connected with gas-tpe fitting by hydraulic conversion joint.
A kind of biological liquid film dust pelletizing system the most according to claim 1, it is characterised in that foam delivery device includes that dry fog flusher and/or foam unit, one end of dry fog flusher and/or foam unit are connected with foam-making apparatus；
Further preferably, dry fog flusher includes hydraulic conversion joint, stainless steel mobile jib and stainless steel connecting rod, hydraulic conversion joint is connected with stainless steel mobile jib, stainless steel mobile jib is divided into two sections, connect between two sections and have 360 degree of chicksans, stainless steel mobile jib top is connected with stainless steel connecting rod by threeway, and the two ends of stainless steel connecting rod are provided with gimbaled nozzle joint；
Further preferably, foam unit includes that component is curved through pipe and component main body tube, component is curved through managing as semicircular ring tubular structure, component is curved is provided with leather pipe joint in the middle part of pipe ring tube, the curved two ends through pipe of component connect with component main body tube, component main body tube is uniformly provided with several foams and sprays the mouth of pipe；
Further preferably, the two ends of component main body tube be provided with semicircle capping seal.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201610373047.1A CN105888716A (en) | 2016-05-31 | 2016-05-31 | Biological liquid film dedusting system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201610373047.1A CN105888716A (en) | 2016-05-31 | 2016-05-31 | Biological liquid film dedusting system |
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| CN105888716A true CN105888716A (en) | 2016-08-24 |
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| CN201610373047.1A Pending CN105888716A (en) | 2016-05-31 | 2016-05-31 | Biological liquid film dedusting system |
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Application publication date: 20160824 |