CN207755944U - Ink prints exhaust treatment system - Google Patents

Ink prints exhaust treatment system Download PDF

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Publication number
CN207755944U
CN207755944U CN201721914014.XU CN201721914014U CN207755944U CN 207755944 U CN207755944 U CN 207755944U CN 201721914014 U CN201721914014 U CN 201721914014U CN 207755944 U CN207755944 U CN 207755944U
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CN
China
Prior art keywords
gas
layer
water
air inlet
outlet
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Expired - Fee Related
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CN201721914014.XU
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Chinese (zh)
Inventor
蒋伟
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Jiangsu Yongyi Environmental Protection Technology Co Ltd
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Jiangsu Yongyi Environmental Protection Technology Co Ltd
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Priority to CN201721914014.XU priority Critical patent/CN207755944U/en
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Expired - Fee Related legal-status Critical Current
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Abstract

The utility model discloses a kind of ink to print exhaust treatment system, including water scrubber, except fog chamber, activated carbon adsorption desorption case, condenser and main air blower, except fog chamber is located at the downstream of the water scrubber, activated carbon adsorption is desorbed case and is located at the downstream for removing fog chamber, condenser is located at the downstream except fog chamber, and main air blower is located at the downstream of activated carbon adsorption desorption case.When using the utility model, exhaust gas first passes through water scrubber, big particle and portion is dissolved in water, later by removing the moisture that exhaust gas is brought into because flowing through water scrubber except fog chamber, activated carbon adsorption desorption case is entered back into, then qualified discharge, using this exhaust treatment system, to the high treating effect of organic exhaust gas, the treatment effeciency of organic exhaust gas is more than 95%, can ensure organic exhaust gas qualified discharge;And the waste liquid centralized recovery processing generated during this, it is environmentally protective.

Description

Ink prints exhaust treatment system
Technical field
The utility model belongs to environmental technology field, and exhaust treatment system is used more particularly to a kind of.
Background technology
Industrial waste gas usually contains the pollutants such as exhaust gas, dust, these pollutants usually to health and environment have compared with Big harm.For example, these pollutants enter human body by breathing, skin contact and alimentary canal, to lead to endocrine function Disorderly and the immune function to human body, angiocarpy and central nervous system etc. have an impact, and therefore, exhaust-gas treatment problem is by pole Big attention.
Current ink printing exhaust treatment efficiency is low, and effect is not apparent enough, and processing procedure is relatively easy, is mostly to use Activated carbon adsorption, then direct emission, cannot meet discharge standard in many cases;Also there is professional person's research later, in work Property charcoal absorption before increase washing, mostly use water scrubber.
Wherein water scrubber is made of, generally reverse-flow spray column, exhaust gas the part such as air inlet, gas outlet, spraying nozzle Air-flow moves upwards, and the liquid that fog-spray nozzle sprays moves downward, to which the dust in air-flow be captured, purified air-flow It is discharged by tower body top, dust then enters tower body bottom precipitation with flow.
A kind of new and effective low consumption water scrubber disclosed in 204522666 U of Chinese patent publication No. CN, including cylindricality washing Tower tower body, the tower body top are equipped with exhaust outlet, and tower body lower part is equipped with leakage fluid dram, and exhaust outlet lower part is equipped with return channel, return channel Lower part is equipped with spray tube, and the spray tube connects circulating water pipe, and spray tube lower part is equipped with adverse current paddle, and adverse current paddle is passed by motor Dynamic, adverse current paddle and motor are set to inside flow spoiler, and flow spoiler lower part is equipped with spoiler, and leakage fluid dram top is equipped with air inlet.Although Washing efficiency can be improved to a certain extent, save the energy, but the devices such as flow spoiler, adverse current paddle and its motor are directly resulted in and set Standby cost is higher, and defogging effect is poor, influences the progress of requirement or the next procedure of exhaust-gas treatment standard.
Utility model content
The utility model is mainly solving the technical problems that provide a kind of ink printing exhaust treatment system, in PLC controls Under the control of system, exhaust gas first passes through water scrubber, and big particle and portion are dissolved in water, later by removing exhaust gas except fog chamber The moisture brought into because flowing through water scrubber enters back into activated carbon adsorption desorption case, then qualified discharge, using this exhaust-gas treatment system System, to the high treating effect of organic exhaust gas, the treatment effeciency of organic exhaust gas is more than 95%, can ensure organic exhaust gas row up to standard It puts;And the waste liquid centralized recovery processing generated during this, it is environmentally protective, while automatic control and intelligence degree are high, reduce Manually keep an eye on.
In order to solve the above technical problems, the technical solution that the utility model uses is:It is useless to provide a kind of ink printing Gas processing system, including water scrubber, except fog chamber, activated carbon adsorption desorption case, condenser and main air blower, it is described except fog chamber is located at institute The downstream of water scrubber is stated, the activated carbon adsorption desorption case is located at the downstream for removing fog chamber, and the condenser is located at described remove The downstream of fog chamber, the main air blower are located at the downstream of activated carbon adsorption desorption case;
The tower body of the water scrubber is equipped with the first air inlet, the first gas outlet, the first water inlet and the first water outlet, described Except the babinet of fog chamber is equipped with the second air inlet, the second gas outlet and the second water outlet, second water outlet is located at the babinet Bottom, the babinet of activated carbon adsorption desorption case is equipped with absorption air inlet, absorption gas outlet, desorption import and is desorbed out Mouthful, the shell of the condenser is equipped with steam inlet, condensation-water drain, gas-liquid import and gas liquid outlet, and the of the water scrubber First gas outlet of the external gas sampling pipeline of one air inlet, the water scrubber passes through pipeline and second air inlet except fog chamber Mouth connection, second gas outlet except fog chamber are connected to the absorption air inlet of the babinet of activated carbon adsorption desorption case, institute State the absorption external first exhaust pipeline in gas outlet;Exhaust gas enters water scrubber by the first air inlet, is passed through later from the first gas outlet Pipeline and the second air inlet, which enter, removes fog chamber, and it is de- then to enter activated carbon adsorption through pipeline and absorption air inlet from the second gas outlet Attached case is most arranged through absorbing outside gas port afterwards;
The water scrubber further includes spray assemblies, water tank and water pump, and the spray assemblies are located at the upper end of tower body, the water The water inlet of case is connect with running water pipe, and the water tank is connect with the water pump, and the water pump is connect with the spray assemblies, institute It states spray assemblies to stretch into tower body by the first water inlet, under the action of water pump, water flows through spray assemblies from water tank, and from One water outlet is discharged;
Activated carbon adsorption desorption case further includes steam pipe road after dry wind air inlet pipe, steam inlet tube and desorption, described dry All with the desorption inlet communication, the desorption connects with steam pipe road after the desorption for dry wind air inlet pipe and the steam inlet tube It is logical, the gas-liquid inlet communication in steam pipe road and the condenser after the desorption, the external delivery pipe of gas liquid outlet of the condenser Road;
Further include PLC control system, the PLC control system includes PLC controller, touch screen, the water set on water scrubber Pump, set on water tank liquid level sensor, set on except fog chamber the first wind pressure sensor, set on activated carbon adsorption be desorbed case second Wind pressure sensor, is set to institute at the temperature sensor that case is desorbed set on the third wind pressure sensor of main air blower, set on activated carbon adsorption The first cylinder valve of activated carbon adsorption desorption case is stated, the second cylinder valve of case is desorbed set on the activated carbon adsorption, is set to The third cylinder valve of condenser and the first solenoid valve set on pipeline, second solenoid valve and third solenoid valve, the water pump, The touch screen, the liquid level sensor, first wind pressure sensor, second wind pressure sensor, third wind pressure sensing Device, the temperature sensor, first solenoid valve, the second solenoid valve, the third solenoid valve, first cylinder valve Door, second cylinder valve, the third cylinder valve and the main air blower are electrically connected with the PLC controller respectively;
The liquid level sensor is located in the water tank, and first wind pressure sensor and second wind pressure sensor are all Including the first probe and the second probe, the first probe of first wind pressure sensor is located at second air inlet for removing fog chamber Place, and the second probe of first wind pressure sensor is located at second gas outlet except fog chamber, second wind pressure passes First probe of sensor is located at the absorption air inlet of activated carbon adsorption desorption case, and the of second wind pressure sensor Two probes are located at the absorption gas outlet of activated carbon adsorption desorption case;First cylinder valve is located at activated carbon suction At the absorption air inlet of attached desorption case, second cylinder valve is located at the absorption gas outlet of activated carbon adsorption desorption case Place, the third cylinder valve are located at the gas liquid outlet of the condenser, and first solenoid valve is located at the dry air hose Road, the second solenoid valve are located at jet chimney, and the third solenoid valve is located at steam pipe road after the desorption.
It further says, the inside of the tower body of the water scrubber is equipped with the first padding support frame, gas-liquid successively from top to bottom The side wall of mixed layer, the second padding support frame, the first demisting layer and tower top web plate, the tower body is equipped with the first observation window, second Observation window and third observation window, first water outlet are located at the lower section of first air inlet and first observation window, institute It states the first air inlet and first observation window is located at the lower section of first padding support frame, second observation window is located at institute It states between spray assemblies and the gas-liquid mixed layer, the third observation window is located at the tower top web plate and the first demisting layer Between, the tower top web plate is located at below first gas outlet;
If support chip and position that first padding support frame and second padding support frame are all mutually parallel by dry plate The fixed ring is fixed at fixed ring composition in the periphery of the support chip, the both ends of the support chip, the support chip with The angle of horizontal direction is 30-45 °;
The gas-liquid mixed layer be Raschig ring layer, Bauer circular layer, rectangular saddle ring layer or arc saddle ring layer, the gas-liquid mixed layer Thickness is 180-220mm, and the volume of the gas-liquid mixed layer is 6.5-7m3
The first demisting layer is the first polyhedron empty ball layer, and the thickness of the first demisting layer is 180-220mm, described The volume of first demisting layer is 7.5-8m3
It further says, the spray assemblies include that a spray manifold and several sprays are in charge of, the spray supervisor It is in charge of setting perpendicular to the spray, the spray manifold is connect with the water outlet of the water pump, and several sprays are in charge of Be mutually parallel and the adjacent spray the distance between be in charge of it is equal, it is described spray the length be in charge of from the center of the tower body to Both sides are gradually shortened, and the every lower section being in charge of that sprays is evenly distributed with several spray heads.
It further says, the box house except fog chamber has two layers of second demisting layers, and one end of the babinet is equipped with The other end of second air inlet, the babinet is equipped with the second gas outlet, and two layers of second demisting layer is along the babinet Length direction setting and be gas flow between the bottom surface of the babinet, two layers of second demisting layer, described the Two demisting layers include inside air inlet face between being located at two layers second demisting layer and opposite with the inside air inlet face outer Side outlet face, second air inlet and the inside air inlet face communicate, the inside air inlet face and outside outlet face phase Logical, outside outlet face and second gas outlet communicate;
The second demisting layer includes the second polyhedron empty ball layer, stainless steel cloth and wire netting, two layers of wire netting Between be equipped with two layers of stainless steel cloth, two layers of polyhedron empty ball layer is equipped between two layers of stainless steel cloth;
The top surface of the babinet and the bottom surface of the babinet are all equipped with opening, and the opening of the top surface of the babinet is positioned at described The top of polyhedron empty ball layer, the opening of the bottom surface of the babinet is positioned at the lower section of the polyhedron empty ball layer, the opening Equipped with matched cover board, the cover board is fixed on the babinet by screw, and the cover board of the bottom surface of the babinet is equipped with Second water outlet;
Further include air flap and outlet baffle, two layers of second demisting layer is set close to one end of second air inlet There is the air flap, the side of the air flap to be connect with one end of the second demisting layer, the air flap it is another Side is connect with the babinet, and two layers of second demisting layer is kept off close to one end of second gas outlet equipped with the outlet The both sides of plate, the outlet baffle are connect with one end of two layers of second demisting layer respectively.
It further says, the cross-sectional area of the second polyhedron empty ball layer is 250-270dm2, the second multi-panel sky The thickness of bulbus cordis layer is 290-310mm, and the spacing between two layers of second demisting layer is 650-750mm.
It further says, the spacing d2 between the spray assemblies and the gas-liquid mixed layer is 750mm, the adjacent spray Spacing d3 between leaching is in charge of is 400mm, and each spacing d4 sprayed between the adjacent spray head being in charge of is 300mm.
Further say, the water tank is internally provided with screen pack 118 and level sensor 119, the water tank into The water outlet of the mouth of a river and the water tank is located at the both sides of the screen pack, screen pack flow in water tank Dynamic direction setting, the level sensor are located at the lower section of the water inlet of the water tank.
It further says, the second polyhedron empty ball layer is polypropylene polyhedron empty ball layer, and the polypropylene multi-panel is empty A diameter of 25mm of the polyhedron empty ball of bulbus cordis layer.
It further says, the condenser includes trumpet cooler module and spiral plate condensation module, the tubular type condensation Device module and spiral plate condensation module series connection, and the trumpet cooler module is located at the upper of the spiral plate condensation module Trip.
It further says, the discharge tube includes second exhaust pipeline and Drainage pipe, the second exhaust pipeline It is connected by threeway with the Drainage pipe, the Drainage pipe connects waste liquor recycling bin, the second exhaust pipeline and chimney Connection.
Further say, the water tank is internally provided with screen pack and level sensor, the water inlet of the water tank and The water outlet of the water tank is located at the both sides of the screen pack, the side of screen pack water flowing in water tank To setting, the level sensor is located at the lower section of the water inlet of the water tank.
It further says, the height of the tower body is 4800-5000mm, a diameter of 2400-2600mm of the tower body.
It further says, the internal diameter of the internal diameter of the air inlet and the gas outlet is all 800-900mm, the sewage draining exit Internal diameter be 30-35mm.
It further says, second air inlet and the babinet junction are air inlet inclined-plane, and the air inlet inclined-plane inclines Tilted direction is gradually tilted to far from the direction except the center of fog chamber along the direction of the internal gas flow except fog chamber, described Second gas outlet and the junction of the babinet are outlet inclined-plane, and the inclined direction on the outlet inclined-plane is along described except fog chamber Gradually the centroclinal of fog chamber is removed to described in the direction of internal gas flow.
It further says, the polyhedron empty ball layer is polypropylene polyhedron empty ball layer, the polypropylene polyhedron empty ball A diameter of 25mm of the polyhedron empty ball of layer.
It further says, the lower section of the babinet is equipped with several equally distributed support bases, the upper end of the support base It is connect with the babinet, ground is fixed in the lower end of the support base.
It further says, the air flap and the outlet baffle are all steel plate, and the outer surface of the steel plate is equipped with zinc The thickness of layer, the zinc layers is 0.5-1mm.
It further says, the cross-sectional area of second air inlet is 50-60dm2, the cross section of second gas outlet Product is 50-60dm2
It further says, the mesh number of the stainless steel cloth is 70-90 mesh.
The internal diameter of the second water outlet mouth is 25mm.
The utility model has the beneficial effects that:
In the utility model, under the control of PLC control system, and under the attraction of main air blower, exhaust gas passes through first Air inlet enters water scrubber, and big particle and portion are dissolved in water, later from the first gas outlet through pipeline and the second air inlet Into except fog chamber, remove the moisture that exhaust gas is brought into because flowing through water scrubber, then from the second gas outlet through pipeline and absorption air inlet Mouth enters activated carbon adsorption and case is desorbed, and is most arranged outside gas port through absorbing afterwards, using this exhaust treatment system, to the place of organic exhaust gas Reason effect is good, and the treatment effeciency of organic exhaust gas is more than 95%, can ensure organic exhaust gas qualified discharge, while the operation of this system The operation to equipment or ON/OFF control are completed according to the operating mode of offgas treatment station and production requirement by PLC control system completely, Without manual intervention, automatic control and intelligence degree are high;
This exhaust treatment system realizes Data Detection, data by PLC control system collection site Various types of data and signal Storage, dynamic menu such as shows at the function of realizations monitoring, for interruption of service can in advance automatic decision, accurately reflect and be out of order State, fault time and relevant information are simultaneously and alarm, failure code are shown in the form of text;Whole system can be normal, steady Fixed, safe efficient, low consumption operation;Each control loop is all provided with the protections systems such as having air switch, fusing insurance, electrothermal relay, really Insurance system safe operation, main air blower motor have short circuit and overload protection arrangement, it is ensured that and extend motor service life;
One, the tower body of the water scrubber of the utility model is internally provided with gas-liquid mixed layer, gas-liquid mixed layer be Raschig ring layer, Bauer circular layer, rectangular saddle ring layer or arc saddle ring layer, using exhaust gas uplink, the thickness of the principle of underwater row, gas-liquid mixed layer is 200mm makes exhaust gas and water be come into full contact between gas-liquid mixed layer, and exhaust gas is small in the resistance of gas-liquid mixed layer, in the unit interval Exhaust-gas treatment amount be 4000m3/ h, to improve washing efficiency;
Two, the water scrubber of the utility model is additionally provided with demisting layer, when gas flows through demisting layer with certain flow velocity, due to The inertial impaction of gas acts on, and gas is made to form larger liquid between the inside of polyhedron empty ball and adjacent polyhedron empty ball Drop, can effectively filter the moisture in gas, and to reach exhaust-gas treatment standard, polyhedron empty ball layer also can remove having in exhaust gas Evil gas and impurity;
If three, the first padding support frame of the water scrubber of the utility model and the second padding support frame are all mutually flat by dry plate The angle of capable support chip and the fixed ring composition positioned at the periphery of support chip, support chip and horizontal direction is 30-45 °, is being protected It demonstrate,proves in the case that the filler on the first filler support and the second filler support do not reveal, substantially increases contact of the gas with filler Area;
Four, the side wall of the water scrubber of the utility model be equipped with the first observation window, the second observation window and third observation window, first Whether observation window is uniform for observing the sewage that gas-liquid mixed layer is fallen, and understands whether gas-liquid mixed layer blocks, observation tower body bottom The sewage level in portion, whether the water that the second observation window is used to observe spray assemblies ejection is uniform, and third observation window is for the row of observation The case where going out the gas of tower body, to understand defogging effect;
Five, the utility model except fog chamber two layers of demisting layer along babinet length direction setting and perpendicular to babinet Bottom surface increases the contact area of demisting layer and exhaust gas, can effectively filter fog therein, promotes demisting efficiency;
Six, the utility model except the demisting layer of fog chamber includes polyhedron empty ball layer, stainless steel cloth and wire netting, two layers It is equipped with two layers of stainless steel cloth between wire netting, is equipped with two layers of polyhedron empty ball layer between two layers of stainless steel cloth, multi-panel is hollow Layers of balls is polypropylene polyhedron empty ball layer, and the mesh number of stainless steel cloth is 80 mesh, and the multi-panel of polyhedron empty ball layer can be prevented hollow Ball leaks out, and influences filter efficiency, and wire netting plays the role of support to polyhedron empty ball layer, improves demisting layer and bears to come from babinet The ability of interior air pressure, when fog flows through polyhedron empty ball layer with certain flow velocity, since the inertial impaction of fog is made With making fog form larger drop between the inside of polyhedron empty ball and adjacent polyhedron empty ball, polypropylene multi-panel is hollow Layers of balls also can remove pernicious gas and impurity in exhaust gas;
Seven, the utility model except fog chamber babinet top surface and babinet bottom surface all be equipped with opening, the top surface of babinet Opening is positioned at the top of polyhedron empty ball layer, and positioned at the lower section of polyhedron empty ball layer, opening is equipped with the opening of the bottom surface of babinet Matched cover board, cover board are fixed on babinet by screw, and polyhedron empty ball is added from the opening of the top surface of babinet, uses After a period of time, discarded polyhedron empty ball is discharged from the opening of the bottom surface of babinet, is regularly replaced convenient for polyhedron empty ball layer, section Human-saving;
Eight, the utility model except fog chamber babinet bottom surface cover board be equipped with the second water outlet, the second water outlet it is interior Diameter is 25mm, in the case where ensureing that polyhedron empty ball layer is not leaked out from discharge outlet, will be pressed from both sides in the moisture and moisture in demisting layer Miscellaneous harmful substance is discharged from discharge outlet;
Nine, the utility model except the second air inlet of fog chamber and babinet junction be air inlet inclined-plane, gas outlet and babinet Junction be outlet air inclined-plane, meet the flow direction except gas in fog chamber, reduce air drag, increased efficiency;
Ten, the utility model except fog chamber into windshield plate and air outlet guard board is all steel plate, the outer surface of steel plate is equipped with zinc Layer, can prevent steel plate corrosion, increase its service life.
The above description is merely an outline of the technical solution of the present invention, in order to better understand the skill of the utility model Art means, and can be implemented in accordance with the contents of the specification, below on the preferred embodiment of the present invention and the accompanying drawings in detail It describes in detail bright as after.
Description of the drawings
Fig. 1 .1 are the technical process schematic diagrames (for setting there are one activated carbon adsorption desorption case) of the utility model;
Fig. 1 .2 are the control principle drawings of the utility model;
Fig. 2 is the elevation of the utility model;
Fig. 3 is the plan view of the utility model;
Fig. 4 is the structural schematic diagram of the water scrubber of the utility model;
Fig. 5 is the structural schematic diagram of the spray assemblies of the water scrubber of the utility model;
Fig. 6 is the structural schematic diagram of the water tank of the water scrubber of the utility model;
Fig. 7 is the structural schematic diagram of the first padding support frame of the water scrubber of the utility model;
Fig. 8 be the utility model except fog chamber structural schematic diagram (main view);
Fig. 9 be the utility model except fog chamber structural schematic diagram (vertical view);
Figure 10 be the utility model except fog chamber internal structure schematic diagram (vertical view);
Figure 11 be the utility model except fog chamber the second demisting layer structural schematic diagram;
Each section label is as follows in attached drawing:
Water scrubber 1, the first air inlet 11, the first gas outlet 12, the first water inlet 13, the first water outlet 14, the first filler Supporting rack 15, gas-liquid mixed layer 16, the second padding support frame 17, the first demisting layer 18, tower top web plate 19, the first observation window 110, Second observation window 111, third observation window 112, support chip 113, fixed ring 114, spray manifold 115, spray are in charge of 116, spray First 117, screen pack 118, level sensor 119, water tank 120, water pump 121, except fog chamber 2, the second air inlet 21, the second outlet The 22, second water outlet 23 of mouth, the second demisting layer 24, support base 25, the second polyhedron empty ball layer 26, stainless steel cloth 27, iron wire Net 28, opening 29, cover board 210, screw 211, air flap 213, outlet baffle 214, activated carbon adsorption desorption case 3, adsorb into Gas port 31, absorption gas outlet 32, desorption import 33, desorption 34, condenser 4, steam inlet 41, condensation-water drain 42, gas Liquid import 43, gas liquid outlet 44, second exhaust pipeline 45, Drainage pipe 46, recycling bin 47, main air blower 5, gas sampling pipeline 6, First exhaust pipeline 7, PLC controller 100, touch screen 200, the first wind pressure sensor 300, the second wind pressure sensor 400, temperature Sensor 500, the first cylinder valve 600, the second cylinder valve 700, third cylinder valve 800, the first solenoid valve 900, second Steam pipe road 1400, third after solenoid valve 1000, third solenoid valve 1100, dry wind air inlet pipe 1200, steam inlet tube 1300, desorption Spacing d1, the spray assemblies between wind pressure sensor 1500, two layers of second demisting layer and the gas-liquid mixed layer it Between spacing d2, the adjacent spray be in charge of between spacing d3, it is each it is described spray between the adjacent spray head be in charge of between Away from the spacing between d4, the height h1 of the tower body, the diameter d5 of the tower body, the tower top web plate and the first demisting layer D6, the diameter d7 of the tower top web plate, the height h2 except the length L1 of fog chamber, the width W1 of the babinet, the babinet.
Specific implementation mode
Illustrate that specific embodiment of the present utility model, those skilled in the art can below by way of particular specific embodiment The advantages of the utility model is understood by content disclosed in the present specification easily and effect.The utility model can also it is other not Same mode is practiced, that is, under the scope of revealed without departing substantially from the utility model, can give different modification and change.
Embodiment:A kind of ink prints exhaust treatment system, as shown in Fig. 1 .1 to Figure 11, including water scrubber 1, removes fog chamber 2, activated carbon adsorption desorption case 3, condenser 4 and main air blower 5, the downstream that the water scrubber is located at except fog chamber, the activity Charcoal adsorption/desorption case is located at the downstream for removing fog chamber, and the condenser is located at the downstream for removing fog chamber, the main air blower position The downstream of case is desorbed in the activated carbon adsorption;
The tower body of the water scrubber is equipped with the first air inlet 11, the first gas outlet 12, the water outlet of the first water inlet 13 and first Mouth 14, the babinet except fog chamber are equipped with the second air inlet 21, the second gas outlet 22 and the second water outlet 23, second water outlet Mouthful be located at the bottom of the babinet, the babinet of activated carbon adsorption desorption case be equipped with absorption air inlet 31, absorption gas outlet 32, Import 33 and desorption 34 is desorbed, the shell of the condenser is equipped with steam inlet 41, condensation-water drain 42, gas-liquid import 43 It is logical with the first gas outlet of gas liquid outlet 44, the external gas sampling pipeline 6 of the first air inlet of the water scrubber, the water scrubber Piping is connected to second air inlet except fog chamber, and second gas outlet except fog chamber is desorbed with the activated carbon adsorption The absorption air inlet of the babinet of case is connected to, the external first exhaust pipeline in the absorption gas outlet 7;Exhaust gas by the first air inlet into Enter water scrubber, enters from the first gas outlet through pipeline and the second air inlet remove fog chamber later, then from the second gas outlet through pipeline Enter activated carbon adsorption with absorption air inlet and case is desorbed, is most arranged outside gas port through absorbing afterwards;
The water scrubber further includes spray assemblies, water tank 120 and water pump 121, and the spray assemblies are located at the upper end of tower body, The water inlet of the water tank is connect with running water pipe, and the water tank is connect with the water pump, the water pump and the spray assemblies Connection, the spray assemblies are stretched by the first water inlet in tower body, and under the action of water pump, water flows through spray group from water tank Part, and be discharged from the first water outlet;
Steam pipe road after the activated carbon adsorption desorption case further includes dry wind air inlet pipe 1200, steam inlet tube 1300 and is desorbed 1400, the dry wind air inlet pipe and the steam inlet tube all with the desorption inlet communication, the desorption with it is described de- Attached steam pipe road is connected to, and the gas-liquid inlet communication in steam pipe road and the condenser, the gas-liquid of the condenser go out after the desorption The external discharge tube of mouth;
Further include PLC control system, the PLC control system includes PLC controller 100, touch screen 200, is set to washing The water pump 121 of tower, set on water tank liquid level sensor 119, set on except fog chamber the first wind pressure sensor 300, be set to activated carbon Second wind pressure sensor 400 of adsorption/desorption case takes off set on the third wind pressure sensor 1500 of main air blower, set on activated carbon adsorption The temperature sensor 500 of attached case, is set to the activated carbon at the first cylinder valve 600 that case is desorbed set on the activated carbon adsorption The second cylinder valve 700, the third cylinder valve 800 set on condenser and the first electromagnetism set on pipeline of adsorption/desorption case Valve 900, second solenoid valve 1000 and third solenoid valve 1100, it is the water pump, the touch screen, the liquid level sensor, described First wind pressure sensor, second wind pressure sensor, third wind pressure sensor, the temperature sensor, first electromagnetism Valve, the second solenoid valve, the third solenoid valve, first cylinder valve, second cylinder valve, the third gas Cylinder valve door and the main air blower are electrically connected with the PLC controller respectively;
The liquid level sensor is located in the water tank, and first wind pressure sensor and second wind pressure sensor are all Including the first probe and the second probe, the first probe of first wind pressure sensor is located at second air inlet for removing fog chamber Place, and the second probe of first wind pressure sensor is located at second gas outlet except fog chamber, second wind pressure passes First probe of sensor is located at the absorption air inlet of activated carbon adsorption desorption case, and the of second wind pressure sensor Two probes are located at the absorption gas outlet of activated carbon adsorption desorption case;First cylinder valve is located at activated carbon suction At the absorption air inlet of attached desorption case, second cylinder valve is located at the absorption gas outlet of activated carbon adsorption desorption case Place, the third cylinder valve are located at the gas liquid outlet of the condenser, and first solenoid valve is located at the dry air hose Road, the second solenoid valve are located at jet chimney, and the third solenoid valve is located at steam pipe road after the desorption.
In the present embodiment, the main air blower is the frequency conversion fan with frequency converter.
The first cylinder valve and the second gas is respectively adopted in the absorption air inlet of activated carbon adsorption desorption case and absorption gas outlet Cylinder valve door, good airproof performance are opened flexible and sturdy and durable.
Preferably, the activated carbon adsorption desorption case has 2, but as the modification and replacement of the utility model, not Case is desorbed in the activated carbon adsorption for limiting other quantity, and main installation warrants are the treating capacity of exhaust gas.
Preferably, desorption and absorption are chain each other, and desorption is made to be acted respectively with absorption, compared to there are one traditional only tools The controlling device of activated carbon adsorption case, needing absorption, stop line carries out desorption purification again after the completion, and efficient, effect is good, Er Qieke The quantity of absorption casing is set according to the treating capacity of exhaust gas
The inside of the tower body of the water scrubber from top to bottom successively be equipped with the first padding support frame 15, gas-liquid mixed layer 16, Second padding support frame 17, the first demisting layer 18 and tower top web plate 19, the side wall of the tower body are equipped with the first observation window 110, the Two observation windows 111 and third observation window 112, first water outlet are located at first air inlet and first observation window Lower section, first air inlet and first observation window are located at the lower section of first padding support frame, second observation For window between the spray assemblies and the gas-liquid mixed layer, the third observation window is located at the tower top web plate and described Between one demisting layer, the tower top web plate is located at below first gas outlet;
If support chip 113 that first padding support frame and second padding support frame are all mutually parallel by dry plate and Fixed ring 114 positioned at the periphery of the support chip forms, and the fixed ring, the support are fixed in the both ends of the support chip Piece and the angle of horizontal direction are 30-45 °;
The gas-liquid mixed layer be Raschig ring layer, Bauer circular layer, rectangular saddle ring layer or arc saddle ring layer, the gas-liquid mixed layer Thickness is 180-220mm, and the volume of the gas-liquid mixed layer is 6.5-7m3
The first demisting layer is the first polyhedron empty ball layer, and the thickness of the first demisting layer is 180-220mm, described The volume of first demisting layer is 7.5-8m3
In the present embodiment, it is preferred that the thickness of the gas-liquid mixed layer is 200mm, and the volume of the gas-liquid mixed layer is 6.8m3;The thickness of the first demisting layer is 200mm, and the volume of the first demisting layer is 7.8m3
In the present embodiment, it is preferred that the water pump is acid and alkali-proof pump.
The spray assemblies include that a spray manifold 115 and several sprays are in charge of 116, the spray be responsible for perpendicular to The spray is in charge of setting, and the spray manifold is connect with the water outlet of the water pump, and several sprays are in charge of mutually flat The capable and adjacent spray the distance between be in charge of it is equal, it is described spray the length be in charge of from the center of the tower body to both sides by Tapered short, the every lower section being in charge of that sprays is evenly distributed with several spray heads 117.
The box house except fog chamber has two layers of second demisting layers 24, one end of the babinet be equipped with described second into Gas port, the other end of the babinet are equipped with the second gas outlet, two layers of second demisting layer along the babinet length direction It is arranged and is gas flow, the second demisting layer packet between the bottom surface of the babinet, two layers of second demisting layer Include the inside air inlet face between two layers of second demisting layer and the outside outlet face opposite with the inside air inlet face, institute It states the second air inlet and the inside air inlet face communicates, the inside air inlet face and outside outlet face communicate, the outside Outlet face and second gas outlet communicate;
The second demisting layer includes the second polyhedron empty ball layer 26, stainless steel cloth 27 and wire netting 28, described in two layers It is equipped with two layers of stainless steel cloth between wire netting, two layers of polyhedron empty ball is equipped between two layers of stainless steel cloth Layer;
The top surface of the babinet and the bottom surface of the babinet are all equipped with opening 29, and the opening of the top surface of the babinet is located at institute The top of polyhedron empty ball layer is stated, the opening of the bottom surface of the babinet is positioned at the lower section of the polyhedron empty ball layer, the opening Place is equipped with matched cover board 210, and the cover board is fixed on the babinet by screw 211, the bottom surface of the babinet Cover board is equipped with second water outlet;
Further include air flap 213 and outlet baffle 214, two layers of second demisting layer is close to second air inlet One end is equipped with the air flap, and the side of the air flap is connect with one end of the second demisting layer, the air inlet gear The other side of plate is connect with the babinet, and two layers of second demisting layer goes out close to one end of second gas outlet equipped with described in The both sides of gas baffle, the outlet baffle are connect with one end of two layers of second demisting layer respectively.
The cross-sectional area of the second polyhedron empty ball layer is 250-270dm2, the thickness of the second polyhedron empty ball layer For 290-310mm, the spacing d1 between two layers of second demisting layer is 650-750mm.
Preferably, the cross-sectional area of the second polyhedron empty ball layer is 260dm2, the second polyhedron empty ball layer Thickness is 300mm, and the spacing between two layers of second demisting layer is 700mm.
Spacing d2 between the spray assemblies and the gas-liquid mixed layer is 750mm, between the adjacent spray is in charge of Spacing d3 be 400mm, each spacing d4 sprayed between the adjacent spray head be in charge of is 300mm.
The water tank is internally provided with screen pack 118 and level sensor 119, the water inlet of the water tank and the water The water outlet of case is located at the both sides of the screen pack, and the screen pack is set in the direction of water flowing in water tank It sets, the level sensor is located at the lower section of the water inlet of the water tank.
In the present embodiment, the condenser includes trumpet cooler module and spiral plate condensation module, the tubular type condensation Device module and spiral plate condensation module series connection, and the trumpet cooler module is located at the upper of the spiral plate condensation module Trip.
The discharge tube includes second exhaust pipeline 45 and Drainage pipe 46, the second exhaust pipeline and the row Liquid pipe road is connected by threeway, and the Drainage pipe connects waste liquor recycling bin 47, and the second exhaust pipeline is connect with chimney.
In the present embodiment, the first exhaust pipeline and second exhaust pipeline are all connect with chimney.
The water tank is internally provided with screen pack 118 and level sensor 119, the water inlet of the water tank and the water The water outlet of case is located at the both sides of the screen pack, and the screen pack is set in the direction of water flowing in water tank It sets, the level sensor is located at the lower section of the water inlet of the water tank, the water inlet of the level sensor and the water tank Solenoid valve be electrically connected with the controller respectively.
When it is implemented, the volume of the water tank is 0.5-1m3, the internal diameter of the water inlet of the water tank is 45-55mm.
The height h1 of the tower body is 4800-5000mm, and the diameter d5 of the tower body is 2400-2600mm.
Preferably, the height of the tower body is 4900mm, and the basal diameter of the tower body is 2500mm.
The internal diameter of the air inlet and the internal diameter of the gas outlet are all 800-900mm, and the internal diameter of the sewage draining exit is 30- 35mm。
Preferably, the internal diameter of the air inlet and the internal diameter of the gas outlet are all 850mm, and the internal diameter of the sewage draining exit is 32mm。
First observation window, second observation window and the third observation window are all acrylic observation window, The diameter of the diameter of first observation window, the diameter of the second observation window and the third observation window is all 450-550mm.
Preferably, the diameter of the diameter of first observation window, the diameter of the second observation window and the third observation window is all For 500mm.
The tower body is stainless steel tower body, and the thickness of the top surface of the thickness of the side wall of the tower body and the tower body is 3mm, The thickness of the bottom surface of the tower body is 4mm.
The water tank is stainless steel water tank, and the wall thickness of the water tank is 2mm.
Spacing d6 between the tower top web plate and the first demisting layer is 400mm, the diameter d7 of the tower top web plate For 1180mm.
Second air inlet and the babinet junction are air inlet inclined-plane, the inclined direction on the air inlet inclined-plane along except The direction of the internal gas flow of fog chamber is gradually tilted to far from the direction except the center of fog chamber, second gas outlet and The junction of the babinet is outlet inclined-plane, and the inclined direction on the outlet inclined-plane is along the internal gas flow except fog chamber Direction it is gradually centroclinal except fog chamber to described.
The second polyhedron empty ball layer is polypropylene polyhedron empty ball layer, the multi-panel of the polypropylene polyhedron empty ball layer A diameter of 25mm of hollow ball.
The lower section of the babinet is equipped with several equally distributed support bases 25, the upper end of the support base and the babinet Connection, ground is fixed in the lower end of the support base.
The air flap and the outlet baffle are all steel plate, and the outer surface of the steel plate is equipped with zinc layers, the zinc layers Thickness be 0.5-1mm.
Preferably, the thickness of the zinc layers is 1mm.
The width W1 of the length L1 2400-2600mm except fog chamber, the babinet are 1900-2100mm, the babinet Height h2 be 1900-2100mm.
The preferred length 2500mm for removing fog chamber, the width of the babinet is 2000mm, and the height of the babinet is 2000mm。
When it is implemented, the wall thickness except fog chamber is 3mm, the material except fog chamber is steel.
The cross-sectional area of second air inlet is 50-60dm2, the cross-sectional area of second gas outlet is 50-60dm2
Preferably, the cross-sectional area of second air inlet is 55dm2, the cross-sectional area of second gas outlet is 55dm2
The mesh number of the stainless steel cloth is 70-90 mesh.
Preferably, the mesh number of the stainless steel cloth is 80 mesh.
The internal diameter of the second water outlet mouth is 25mm.
In the present embodiment, the activated carbon that the activated carbon adsorption desorption is inwardly filled is cylindrical pellet, and height is 4mm, a diameter of 3mm, iodine sorption value 900mg/g, benzene adsorption rate>45%, positive resistance to compression>0.7mpa, side resistance to compression>0.3mpa, production Product tolerance+0.1mm, activated carbon density:680kg/m3
Due to cylindrical activated carbon large specific surface area, adsorption capacity is strong, and column carbon loading is small to decide that exhaust-gas treatment is set The height of standby purification efficiency, so will be on the basis of ensureing qualified discharge, the loading of reasonable disposition activated carbon.
Pipeline in the present embodiment uses galvanized pipe, wall thickness 2mm.
The gas sampling pipeline includes printing the first gas sampling pipeline of exhaust gas and for receiving for collecting ink Collect the second gas sampling pipeline of oven exhaust gas, the velocity in pipes control of the first gas sampling pipeline is described in 8-10m/s The velocity in pipes of second gas sampling pipeline is controlled in 1m/s.
In the present embodiment, the specified processing air quantity of the water scrubber is 3000m3/ h, resistance 500Pa, the water scrubber Interior wind speed is 8/mm.
The specified processing air quantity of each activated carbon adsorption desorption case is 3000m3/ h, resistance 1300-1500Pa are living Property charcoal loading 5m3
The operation principle and the course of work of the utility model are as follows:
Under the monitoring of PLC control system:
Under the action of main air blower, exhaust gas enters water scrubber by the first air inlet, and big particle and portion are dissolved in Water enters through pipeline and the second air inlet from the first gas outlet remove fog chamber later, removes what exhaust gas was brought into because flowing through water scrubber Then moisture enters activated carbon adsorption through pipeline and absorption air inlet from the second gas outlet and case is desorbed, most afterwards through absorbing gas port Outer row, using this exhaust treatment system, to the high treating effect of organic exhaust gas, the treatment effeciency of organic exhaust gas is more than 95%, energy Enough ensure organic exhaust gas qualified discharge;
Since main air blower is frequency conversion fan, i.e., main air blower is by frequency converter start and stop, and the entrance of main air blower installs third wind Pressure sensor, third wind pressure sensor output signals to PLC control system and to frequency converters, and frequency converter is in PLC control system Frequency conversion interval range carry out frequency control main air blower motor speed, when main air blower entrance wind pressure becomes larger, frequency converter is automatic Change frequency and control the faster rotational speed of main air blower motor, when wind pressure reduces at fan inlet, frequency converter changes frequency automatically Rate simultaneously controls the reduction of main air blower motor speed, and the traffic coverage of frequency converter frequency is arranged to ensure wind turbine simultaneously in PLC control system Ordinary life;
During this, when exhaust gas enters water scrubber, tap water is under the action of water pump through spray assemblies and the first water inlet It is sprayed downwards from the upper end of water scrubber, from below to up by gas-liquid mixed layer, impurity and portion gas in exhaust gas are dissolved in exhaust gas Water, treated, and exhaust gas is discharged into from the first gas outlet except fog chamber;Water under spraying simultaneously goes out from the first of the lower end of water scrubber The mouth of a river is discharged;
From water scrubber come out exhaust gas from the second air inlet enter remove fog chamber, then from the inside between two layers of demisting layer into Gas face, by polyhedron empty ball layer demisting filter, by the harmful substance being mingled in the moisture and moisture in polyhedron empty ball layer from Second water outlet is discharged, and using outside outlet face, is discharged by the second gas outlet, and case is desorbed into activated carbon adsorption, passes through Aforesaid way increases the contact area of demisting layer and exhaust gas, can effectively filter fog therein, promotes demisting efficiency;
Enter activated carbon adsorption from absorption air inlet from the exhaust gas come out except fog chamber and case is desorbed, through in activated carbon adsorption exhaust gas Harmful substance after from absorption gas outlet through first exhaust pipeline discharge, carry out at this time is activated carbon adsorption desorption case absorption Process in adsorption process, is desorbed import and desorption all closes, in use for some time, be desorbed, the process In, import and desorption is desorbed and all opens, absorption intake interface and absorption gas outlet are closed, high-temperature steam from desorption import into In cartonning body, desorption process is carried out, the gas-liquid after desorption enters condenser, after condensation separation, gas part qualified discharge, liquid Body portion is due to being waste liquid, centralized recovery processing;Separately after steam is desorbed, due to what can be brought into containing steam in activated carbon Steam, therefore activated carbon is dried with dry wind, extend the service life of activated carbon;
During this system is run, except fog chamber is equipped with the first wind pressure sensor, for detecting the wind pressure except fog chamber, and will Real-time data transmission reminds staff to check in time to PLC controller when pressure difference is more than setting value, replaces except fog chamber Demisting layer etc.;
Activated carbon adsorption is desorbed case and is equipped with the second wind pressure sensor, for detecting the wind pressure except fog chamber, and data are real-time It is transferred to PLC controller, when pressure difference is more than setting value, staff is reminded to check in time, replaces activated carbon etc., timely processing Failure ensures the normal work of equipment;And also there is temperature sensor, also can by temperature parameter real-time Transmission to PLC controller, It is further ensured that the normal operation of equipment.
The above description is only the embodiments of the present invention, and it does not limit the scope of the patent of the present invention, every Equivalent structure made based on the specification and figures of the utility model is applied directly or indirectly in other relevant technologies Field is equally included in the patent within the scope of the utility model.

Claims (10)

1. a kind of ink prints exhaust treatment system, it is characterised in that:Including water scrubber (1), except fog chamber (2), activated carbon adsorption Case (3), condenser (4) and main air blower (5), the downstream that the water scrubber is located at except fog chamber, the activated carbon adsorption is desorbed Case is desorbed and is located at the downstream for removing fog chamber, the condenser is located at the downstream for removing fog chamber, and the main air blower is located at described The downstream of case is desorbed in activated carbon adsorption;
The tower body of the water scrubber goes out equipped with the first air inlet (11), the first gas outlet (12), the first water inlet (13) and first The mouth of a river (14), the babinet except fog chamber are equipped with the second air inlet (21), the second gas outlet (22) and the second water outlet (23), institute State the bottom that the second water outlet is located at the babinet, the babinet of the activated carbon adsorption desorption case be equipped with absorption air inlet (31), Adsorb gas outlet (32), desorption import (33) and desorption (34), the shell of the condenser is equipped with steam inlet (41), cold Condensate exports (42), gas-liquid import (43) and gas liquid outlet (44), the external gas sampling pipe of the first air inlet of the water scrubber First gas outlet in road (6), the water scrubber is connected to by pipeline with second air inlet except fog chamber, described except fog chamber Second gas outlet is connected to the absorption air inlet for the babinet that case is desorbed in the activated carbon adsorption, the absorption gas outlet external first Discharge duct (7);Exhaust gas enters water scrubber by the first air inlet, later from the first gas outlet through pipeline and the second air inlet into Enter to remove fog chamber, then entering activated carbon adsorption through pipeline and absorption air inlet from the second gas outlet is desorbed case, most afterwards through absorbing It is arranged outside gas port;
The water scrubber further includes spray assemblies, water tank (120) and water pump (121), and the spray assemblies are located at the upper end of tower body, The water inlet of the water tank is connect with running water pipe, and the water tank is connect with the water pump, the water pump and the spray assemblies Connection, the spray assemblies are stretched by the first water inlet in tower body, and under the action of water pump, water flows through spray group from water tank Part, and be discharged from the first water outlet;
Steam pipe road after the activated carbon adsorption desorption case further includes dry wind air inlet pipe (1200), steam inlet tube (1300) and is desorbed (1400), the dry wind air inlet pipe and the steam inlet tube all with the desorption inlet communication, the desorption with it is described Steam pipe road is connected to after desorption, the gas-liquid inlet communication in steam pipe road and the condenser, the gas-liquid of the condenser after the desorption Export external discharge tube;
Further include PLC control system, the PLC control system includes PLC controller (100), touch screen (200), is set to washing The water pump (121) of tower, set on water tank liquid level sensor (119), set on except fog chamber the first wind pressure sensor (300), be set to Activated carbon adsorption be desorbed case the second wind pressure sensor (400), set on main air blower third wind pressure sensor (1500), be set to live Property charcoal adsorption/desorption case temperature sensor (500), set on the activated carbon adsorption be desorbed case the first cylinder valve (600), Set on the activated carbon adsorption be desorbed case the second cylinder valve (700), set on condenser third cylinder valve (800) and Set on the first solenoid valve (900) of pipeline, second solenoid valve (1000) and third solenoid valve (1100), the water pump, it is described touch Touch the screen, liquid level sensor, first wind pressure sensor, second wind pressure sensor, third wind pressure sensor, described It is temperature sensor, first solenoid valve, the second solenoid valve, the third solenoid valve, first cylinder valve, described Second cylinder valve, the third cylinder valve and the main air blower are electrically connected with the PLC controller respectively;
The liquid level sensor is located in the water tank, and first wind pressure sensor and second wind pressure sensor all include First probe of the first probe and the second probe, first wind pressure sensor is located at second air inlet except fog chamber, And the second probe of first wind pressure sensor is located at second gas outlet except fog chamber, second wind pressure sensor First probe be located at the activated carbon adsorption desorption case absorption air inlet at, and second wind pressure sensor second visit Head is located at the absorption gas outlet of activated carbon adsorption desorption case;It is de- that first cylinder valve is located at the activated carbon adsorption At the absorption air inlet of attached case, second cylinder valve is located at the absorption gas outlet of activated carbon adsorption desorption case, institute It states third cylinder valve to be located at the gas liquid outlet of the condenser, first solenoid valve is located at the dry wind pipeline, institute It states second solenoid valve and is located at jet chimney, the third solenoid valve is located at steam pipe road after the desorption.
2. ink according to claim 1 prints exhaust treatment system, it is characterised in that:The tower body of the water scrubber it is interior It is removed successively equipped with the first padding support frame (15), gas-liquid mixed layer (16), the second padding support frame (17), first from top to bottom in portion Mist layer (18) and tower top web plate (19), the side wall of the tower body are equipped with the first observation window (110), the second observation window (111) and the Three observation windows (112), first water outlet are located at the lower section of first air inlet and first observation window, and described first Air inlet and first observation window are located at the lower section of first padding support frame, and second observation window is located at the spray Between component and the gas-liquid mixed layer, the third observation window between the tower top web plate and the first demisting layer, The tower top web plate is located at below first gas outlet;
If support chip (113) and position that first padding support frame and second padding support frame are all mutually parallel by dry plate Fixed ring (114) composition in the periphery of the support chip, the fixed ring, the support are fixed in the both ends of the support chip Piece and the angle of horizontal direction are 30-45 °;
The gas-liquid mixed layer is Raschig ring layer, Bauer circular layer, rectangular saddle ring layer or arc saddle ring layer, the thickness of the gas-liquid mixed layer Volume for 180-220mm, the gas-liquid mixed layer is 6.5-7m3
The first demisting layer is the first polyhedron empty ball layer, and the thickness of the first demisting layer is 180-220mm, described first The volume of demisting layer is 7.5-8m3
3. ink according to claim 1 prints exhaust treatment system, it is characterised in that:The spray assemblies include one Spray manifold (115) and several sprays are in charge of (116), and the spray supervisor is in charge of setting, the spray perpendicular to the spray Leaching manifold connect with the water outlet of the water pump, several it is described spray be in charge of be mutually parallel and it is adjacent it is described spray be in charge of between Distance it is equal, the length be in charge of of spraying is gradually shortened from the center of the tower body to both sides, and the every spray is in charge of Lower section be evenly distributed with several spray heads (117).
4. ink according to claim 1 prints exhaust treatment system, it is characterised in that:The box house except fog chamber With two layers of second demisting layers (24), one end of the babinet is equipped with second air inlet, and the other end of the babinet is equipped with Second gas outlet, two layers of second demisting layer are arranged and along the length direction of the babinet perpendicular to the bottom of the babinet Face, is gas flow between two layers of second demisting layer, and the second demisting layer includes being located at two layers of second demisting layer Between inside air inlet face and the outside outlet face opposite with the inside air inlet face, second air inlet and the inside into Gas face communicates, and the inside air inlet face and outside outlet face communicate, outside outlet face and second gas outlet phase It is logical;
The second demisting layer includes the second polyhedron empty ball layer (26), stainless steel cloth (27) and wire netting (28), two layers of institute It states and is equipped with two layers of stainless steel cloth between wire netting, it is hollow to be equipped with two layers of multi-panel between two layers of stainless steel cloth Layers of balls;
The top surface of the babinet and the bottom surface of the babinet are all equipped with opening (29), and the opening of the top surface of the babinet is positioned at described The top of polyhedron empty ball layer, the opening of the bottom surface of the babinet is positioned at the lower section of the polyhedron empty ball layer, the opening Equipped with matched cover board (210), the cover board is fixed on the babinet, the bottom surface of the babinet by screw (211) Cover board be equipped with second water outlet;
Further include air flap (213) and outlet baffle (214), two layers of second demisting layer is close to second air inlet One end is equipped with the air flap, and the side of the air flap is connect with one end of the second demisting layer, the air inlet gear The other side of plate is connect with the babinet, and two layers of second demisting layer goes out close to one end of second gas outlet equipped with described in The both sides of gas baffle, the outlet baffle are connect with one end of two layers of second demisting layer respectively.
5. ink according to claim 4 prints exhaust treatment system, it is characterised in that:The second polyhedron empty ball layer Cross-sectional area be 250-270dm2, the thickness of the second polyhedron empty ball layer is 290-310mm, two layers of second demisting Spacing (d1) between layer is 650-750mm.
6. ink according to claim 3 prints exhaust treatment system, it is characterised in that:The spray assemblies and the gas Spacing (d2) between liquid mixed layer is 750mm, and the spacing (d3) between the adjacent spray is in charge of is 400mm, each described It is 300mm to spray the spacing (d4) between the adjacent spray head being in charge of.
7. ink according to claim 1 prints exhaust treatment system, it is characterised in that:The water tank was internally provided with The water outlet of sieve plate (118) and liquid level sensor (119), the water inlet of the water tank and the water tank is located at the mistake The both sides of sieve plate, the direction setting of screen pack water flowing in water tank, the level sensor is located at described The lower section of the water inlet of water tank.
8. ink according to claim 4 prints exhaust treatment system, it is characterised in that:The second polyhedron empty ball layer For polypropylene polyhedron empty ball layer, a diameter of 25mm of the polyhedron empty ball of the polypropylene polyhedron empty ball layer.
9. ink according to claim 1 prints exhaust treatment system, it is characterised in that:The condenser includes tube type cold Condenser module and spiral plate condensation module, the trumpet cooler module and spiral plate condensation module series connection, and the pipe Formula condenser module is located at the upstream of the spiral plate condensation module.
10. ink according to claim 1 prints exhaust treatment system, it is characterised in that:The discharge tube includes Second exhaust pipeline (45) and Drainage pipe (46), the second exhaust pipeline are connected with the Drainage pipe by threeway, institute Drainage pipe connection waste liquor recycling bin (47) is stated, the second exhaust pipeline is connect with chimney.
CN201721914014.XU 2017-12-31 2017-12-31 Ink prints exhaust treatment system Expired - Fee Related CN207755944U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721914014.XU CN207755944U (en) 2017-12-31 2017-12-31 Ink prints exhaust treatment system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721914014.XU CN207755944U (en) 2017-12-31 2017-12-31 Ink prints exhaust treatment system

Publications (1)

Publication Number Publication Date
CN207755944U true CN207755944U (en) 2018-08-24

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721914014.XU Expired - Fee Related CN207755944U (en) 2017-12-31 2017-12-31 Ink prints exhaust treatment system

Country Status (1)

Country Link
CN (1) CN207755944U (en)

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