CN105080296B - Zero-gas consumption blowing-type suction drying machine - Google Patents

Zero-gas consumption blowing-type suction drying machine Download PDF

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CN105080296B
CN105080296B CN201510005852.4A CN201510005852A CN105080296B CN 105080296 B CN105080296 B CN 105080296B CN 201510005852 A CN201510005852 A CN 201510005852A CN 105080296 B CN105080296 B CN 105080296B
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adsorption tower
gas outlet
charge
parallel
gas
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CN105080296A (en
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林锦志
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Hangzhou Fan Tai Machinery Co Ltd
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Hangzhou Fan Tai Machinery Co Ltd
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Abstract

The invention discloses a zero-gas consumption blowing-type suction drying machine. The zero-gas consumption blowing-type suction drying machine comprises an air inlet pipe, a gas outlet pipe, three adsorption towers, a blower, a compressor, a condenser and an evaporator. The air inlet pipe is respectively connected to gas inlets of the three adsorption towers in parallel by pipes with electrically operated valves. The gas outlet pipe is respectively connected to gas outlets of the three adsorption towers in parallel by pipes with check valves, a gas outlet of the blower is connected to a heating main pipe and a cooling main pipe by pipes, wherein the heating main pipe and the cooling main pipe are connected in parallel, the heating main pipe is connected to the condenser and the corresponding electrically operated valve and then is orderly connected to gas outlets of the first, second and third adsorption towers in parallel, and the cooling main pipe is connected to the evaporator and the corresponding electrically operated valve and then is orderly connected to gas outlets of the first, second and third adsorption towers in parallel. The zero-gas consumption blowing-type suction drying machine keeps zero gas consumption, does not increase compressed air resistance, really realizes zero gas consumption and effectively reduces regeneration energy consumption by heat transfer between the condenser and the evaporator.

Description

A kind of zero QI consumed blowing-type dryer
Technical field
The present invention relates to a kind of gas drier, is used for drying compressed air and pressure is not lost more particularly, to a kind of The dryer of stream of compressed air amount.
Background technology
Compressed air using front needing first to carry out dried, to remove compressed air in steam.Dryer is to use In the common equipment of drying compressed air, it generally includes to arrange the granule with adsorption function in two adsorption towers, adsorption tower The adsorbent of shape, when compressed air passes through adsorption tower, the steam in the adsorbable compressed air of adsorbent is dry so as to export Compressed air.When the steam that the adsorbent in adsorption tower is adsorbed reaches saturation, then hot-air can be input into into adsorption tower, be made The water evaporation that adsorbent is adsorbed to realize thermal regeneration, then again into adsorption tower be input into cold air to adsorbent cold blowing again Raw, so as to recover adsorption function, two adsorption towers can be toggled adsorbing and regenerating between two states, so as to realize compression Air it is continuous drying.When an adsorption tower is operated in adsorbed state, the compressed air of part is right after heater heating Another adsorption tower carries out thermal regeneration, then again by the compressed air of part by cooler cooling after to thermal regeneration after Adsorption tower carries out cold blowing regeneration.Because the regeneration source of the gas of adsorption tower is from compressed air, therefore dryer operationally can be consumed A certain amount of compressed air, so as to reduce the work efficiency of dryer.For this purpose, people have invented the dryer of zero QI consumed, example Such as, disclosed a kind of " compression waste heat zero regeneration gas loss absorption drier " in Chinese patent literature, notification number is CN203803342U, by dryer entrance, A adsorption towers, B adsorption towers, dryer outlet, the first after cooler, gas-liquid point From device, the second after cooler, bubbler composition.Dryer entrance is arranged on the side of B adsorption towers, dryer outlet difference Connected with A absorption training and B adsorption towers by flanged pipe, bubbler is separately positioned on the top and the bottom of A adsorption towers and B adsorption towers, Second after cooler is arranged between A adsorption towers and B adsorption towers, and with flanged pipe connection, the first after cooler passes through method Blue pipe connects gas-liquid separator.During work, compressed air passes sequentially through two adsorption towers of A, B, makes two adsorption towers work respectively In absorption and reproduced state, so as to avoid consumption of compressed air amount, the flow for making compressed air keeps constant.But it is still There are the following problems:Firstly, since the compressed air of whole simultaneously participates in the regeneration of adsorption tower, that is to say, that compressed air must Must just be sent after two adsorption towers, therefore the resistance suffered by compressed air is greatly increased, so that the compressor of upstream Load is dramatically increased, and then is increased the power of compressor and caused to waste;Secondly, the heater and cooler for regeneration is both needed to Consume substantial amounts of electric energy, thus high energy consumption of dryer when running.
The content of the invention
It is an object of the invention to solve compressed air resistance existing for existing zero QI consumed dryer it is big, so as to need Correspondingly improve the high problem of the power and regeneration energy consumption of compressor, there is provided a kind of zero QI consumed blowing-type dryer, it is being protected The resistance of compressed air will not be increased on the premise of holding zero QI consumed, so as to really realize zero QI consumed of dryer, and can be notable Ground reduces regeneration energy consumption.
To achieve these goals, the present invention is employed the following technical solutions:
A kind of zero QI consumed blowing-type dryer, including air inlet pipe, the dried compressed air of output of input compressed air Escape pipe and the first adsorption tower for drying compressed air successively, the second adsorption tower and the 3rd adsorption tower, the air inlet Pipe is in parallel respectively by pipeline with the air inlet of first, second, third adsorption tower, and is respectively provided with three parallel pipelines The electrodynamic valve of break-make can be automatically controlled;The escape pipe passes through respectively the gas outlet phase of pipeline and first, second, third adsorption tower Parallel connection, and the gas outlet from first, second, third adsorption tower is respectively provided with three parallel pipelines to escape pipe one-way conduction Check-valves;Additionally, the condenser being also connected with compressor including aerator, compressor and vaporizer, the air-out of aerator Mouthful by pipeline and heating main parallel with one another and cool down house steward and be connected, the heating main connect after condenser with it is mutual The first heating in parallel is in charge of, the second heating is in charge of, the 3rd heating is in charge of and is connected, after the cooling house steward connection vaporizer with First cooling parallel with one another is in charge of, the second cooling is in charge of, the 3rd cooling is in charge of and is connected, and the first heating is in charge of by an electricity It is in charge of with the gas outlet of first, second adsorption tower and the first cooling after dynamic valve and is in parallel, and inhales in two connections first, second The non-return of the gas outlet one-way conduction from aerator to first, second adsorption tower is respectively provided with the parallel pipeline of attached tower gas outlet Valve, the first cooling is in charge of, and is provided with electrodynamic valve;Second heating is in charge of after an electrodynamic valve and second, third adsorption tower Gas outlet and the second cooling are in charge of and are in parallel, and on two parallel pipelines for connecting second, third adsorption tower gas outlet point The check-valves of the gas outlet one-way conduction from aerator to second, third adsorption tower are not set, and the second cooling is in charge of, is provided with Electrodynamic valve;The gas outlet with the first, the 3rd adsorption tower is in charge of after an electrodynamic valve in 3rd heating and the 3rd cooling is in charge of Be in parallel, and be respectively provided with two articles of parallel pipelines for connecting the first, the 3rd adsorption tower gas outlet from aerator to first, the The check-valves of the gas outlet one-way conduction of three adsorption towers, the 3rd cooling is in charge of, and is provided with electrodynamic valve;The air inlet of aerator leads to Cross pipeline to be in parallel with the air inlet of first, second, third adsorption tower, and be respectively provided with three parallel pipelines and can control automatically The electrodynamic valve of break-make processed.
There is the dryer of the present invention absorption, thermal regeneration and cold blowing to regenerate three gas circuits, and three adsorption towers work respectively Switch in adsorbed state, thermal regeneration state and cold blowing reproduced state and successively, therefore, compressed air only needs Jing in dryer Directly export from escape pipe by crossing an adsorption tower adsorption dry, and required for the thermal regeneration of adsorption tower and cold blowing regenerate Air-flow is produced by the aerator in regeneration gas circuit, so, zero QI consumed of dryer both can have really been realized, while making to blot Machine is reduced to minimum level to the resistance of compressed air, so as to advantageously reduce the power and energy consumption of upstream compressor.When first When adsorption tower is operated in adsorbed state, we only need to control to be arranged on the air inlet of air inlet pipe and first, second, third adsorption tower The opening and closing of three electrodynamic valves on the pipeline being in parallel, you can control compressed gas complete to inhale into the air inlet of the first adsorption tower Attached drying.Due to first, second, third adsorption tower gas outlet and escape pipe between be provided with the check-valves of one-way conduction, therefore, Mutually isolated effect is formed between the gas outlet of first, second, third adsorption tower, completing the compressed air of adsorption dry can pass through The check-valves being connected between the gas outlet of the first adsorption tower and escape pipe are all exported from escape pipe, so as to form an absorption Gas circuit, the compressed gas flowed out from the gas outlet of the first adsorption tower can't reversely be entered from the gas outlet of second, third adsorption tower Enter in second, third adsorption tower.Additionally, we are by the opening and closing air inlet of aerator and entering for first, second, third adsorption tower The electrodynamic valve on parallel pipeline between QI KOU, you can make the air inlet of second, third adsorption tower and the air inlet phase of aerator Connection, so, aerator can drive the gas in pipeline respectively through condenser heating and vaporizer cooling, so as in heating The hot-air needed for thermal regeneration is formed in house steward, while forming the cold air needed for cold blowing regeneration in cooling house steward.Due to The present invention is to realize thermal regeneration and cold blowing regeneration by condenser and vaporizer, therefore heats and cool down without the need for individually consuming Electric energy, compressor operating forms high temperature liquid refrigerant, the cold-producing medium that is in a liquid state then is cooled down within the condenser, while making heating again The regeneration gas heating on angry road;At the same time, liquid refrigerant evaporation endothermic in vaporizer, makes cold blowing regeneration gas circuit again Raw gas cooling, that is to say, that by the work of compressor, the heat " carrying " cold blowing regenerated in gas circuit arrives heating regeneration gas Lu Zhong, so as to realize the transfer of energy, thus can greatly reduce regeneration energy consumption.Hot-air in heating main adds by first Heat is in charge of the electrodynamic valve of unlatching and the check-valves that are connected with the gas outlet of the second adsorption tower are entered in the second adsorption tower, with A thermal regeneration gas circuit is formed, so as to carry out thermal regeneration to the second adsorption tower.Due to the gas outlet of now the first adsorption tower Gas pressure will be far above thermal regeneration gas circuit gas pressure, therefore, the hot-air being thermally formed through condenser will not In the absorption gas circuit of the gas outlet side for entering into the first adsorption tower, so as to be capable of achieving between absorption gas circuit and thermal regeneration gas circuit It is completely isolated.Cooling house steward in cold air by the 3rd cooling be in charge of unlatching electrodynamic valve and with the 3rd adsorption tower The connected check-valves in gas outlet are entered in the 3rd adsorption tower, to form a cold blowing regeneration gas circuit, so as to the 3rd adsorption tower Carry out cold blowing regeneration.Because the gas pressure of the now gas outlet of the first adsorption tower will be far above the gas pressure that cold blowing regenerates gas circuit Power, therefore, the cold air being cooled into through vaporizer will not enter into the absorption gas circuit of the gas outlet side of the first adsorption tower In, it is completely isolated between absorption gas circuit and cold blowing regeneration gas circuit so as to be capable of achieving.By optionally controlling the electronic of correlation The opening and closing of valve, we can easily switch the working condition of first, second, third adsorption tower, so as to realize the continuous of dryer It is dried operation.
Preferably, between the gas outlet of first, second adsorption tower, between the gas outlet of second, third adsorption tower with And the first, the 3rd adsorption tower gas outlet between be connected by pipeline respectively, and concatenate handss respectively on three connecting lines It is dynamic to adjust flow valve and the electrodynamic valve of break-make be automatically controlled.
When being operated in adsorbed state due to adsorption tower, the gas pressure in its tower is higher, and adsorption tower is operated in regeneration shape During state, the gas pressure in its tower is relatively low, therefore, when three adsorption tower switch operating states, we can first open the electricity of correlation Dynamic valve, makes the gases at high pressure in absorption gas circuit quickly enter in cold blowing regeneration gas circuit, so, original suction in adsorbed state Gas pressure in attached tower is lowered into rapidly thermal regeneration state, and adjusts flow valve manually and then can control the connecting line Gas flow, so as to control the switch speed of adsorption tower working condition.
Preferably, the air inlet in aerator is also connected with electrodynamic valve and suction filter in turn by pipeline.
So, when one of adsorption tower is switched to reproduced state from adsorbed state, the gas in its regeneration gas circuit can From outside atmosphere suction, and clean regeneration gas is formed after suction filter is filtered, so as to form open regeneration gas Road.When closing is connected to the electrodynamic valve after suction filter, suction filter quits work, and regeneration gas circuit formation now is closed Gas circuit is closed, the gas circulating flow in gas circuit is regenerated, thermal regeneration is carried out to one of adsorption tower another adsorption tower is entered Row cold blowing regenerates.
Preferably, the adsorbent in first, second, third adsorption tower adopts alumina particle.
Aluminium oxide has good adsorption, be conducive to improve dryer drying efficiency, simultaneous oxidation aluminum have compared with High hardness, is hardly damaged, and is conducive to increasing the service life.
Therefore, the present invention has the advantages that:The resistance of compressed air can not be increased on the premise of zero QI consumed is kept Power, so as to really realize zero QI consumed of dryer, and is effectively reduced regeneration energy consumption.
Description of the drawings
Fig. 1 is a kind of pipeline connection diagram of the present invention.
In figure:1st, the first adsorption tower 2, the second adsorption tower 3, air inlet pipe 4, escape pipe 501, the first electrodynamic valve 502, Second electrodynamic valve 503, the 3rd electrodynamic valve 504, the 4th electrodynamic valve 505, the 5th electrodynamic valve 506, the 6th electrodynamic valve 507, Seven electrodynamic valves 508, the 8th electrodynamic valve 509, the 9th electrodynamic valve 510, the tenth electrodynamic valve 511, the 11st electrodynamic valve 512, 12 electrodynamic valves 513, the 13rd electrodynamic valve 514, the 14th electrodynamic valve 515, the 15th electrodynamic valve the 516, the 16th are electronic Valve 517, the 17th electrodynamic valve 518, the 18th electrodynamic valve 61, first check-valve 62, second check-valve 63, the 3rd non-return Valve 64, the 4th check-valves 65, the 5th check-valves 66, the 6th check-valves 67, the 7th check-valves 68, the 8th check-valves 69, 9th check-valves 7, aerator 8, vaporizer 9, manually condenser 10, regulation flow valve 11, suction filter 12, noise reduction Device 13, the 3rd adsorption tower 14, compressor.
Specific embodiment
Below in conjunction with the accompanying drawings the present invention will be further described with specific embodiment.
As shown in figure 1, after a kind of zero QI consumed blowing-type dryer, including air inlet pipe 3, the output drying of input compressed air Compressed air escape pipe 4 and the first adsorption tower 1 for drying compressed air successively, the second adsorption tower 2 and the 3rd inhale Attached tower 13, the adsorbent in first, second, third adsorption tower adopts the alumina particle with good adsorption efficiency, with favourable In the drying efficiency for improving dryer, while increasing the service life.In the first adsorption tower, second, third adsorption tower, when one When adsorption tower is operated in adsorbed state, another two adsorption tower is then operated in respectively thermal regeneration state and cold blowing reproduced state.Enter Trachea is formed with the air inlet of first, second, third adsorption tower by pipeline be connected in parallel respectively, and on three parallel pipelines Being respectively provided with can automatically control the electrodynamic valve of break-make, wherein being connected to electronic between the air inlet of air inlet pipe and the first adsorption tower Valve is the 3rd electrodynamic valve 503, and the electrodynamic valve being connected between the air inlet of air inlet pipe and the second adsorption tower is the 4th electrodynamic valve 504, the electrodynamic valve being connected between the air inlet of air inlet pipe and the 3rd adsorption tower is the 15th electrodynamic valve 515, by control three The opening and closing of individual electrodynamic valve, you can optionally the compressed air of air inlet pipe is sent in first, second or third adsorption tower, three are made Individual adsorption tower realizes the continuous work of dryer by mutual switch operating state.Additionally, the escape pipe of output squeezing air point Do not formed by the gas outlet of pipeline and first, second, third adsorption tower and be connected in parallel, and set respectively on three parallel pipelines Put can one-way conduction check-valves, wherein the check-valves being connected between the gas outlet of escape pipe and the first adsorption tower stop for first Valve 61 is returned, the check-valves being connected between the gas outlet of escape pipe and the second adsorption tower are second check-valve 62, are connected to outlet Check-valves between the gas outlet of the adsorption towers of Guan Yu tri- are the 5th check-valves 65, and the conducting direction of three check-valves is respectively from the First, the gas outlet side of second, third adsorption tower is towards escape pipe side, that is to say, that from first, second, third adsorption tower The compressed air of gas outlet output can enter escape pipe by check-valves, and the compressed air in escape pipe then cannot be flowed back to First, second, third adsorption tower.
In order to realize zero QI consumed of dryer and reduce regeneration energy consumption, present invention additionally comprises aerator 7, compressor 14 and The connected condenser 9 of compressor and vaporizer 8, the air outlet of aerator is by pipeline and heating main parallel with one another and cold But house steward is connected, and condenser is first connected on heating main, is then in charge of with first heating parallel with one another, the second heating point Pipe, the 3rd heating are in charge of and are connected.Cooling house steward then first connects vaporizer, is then in charge of with first cooling parallel with one another, the Two coolings are in charge of, the 3rd cooling is in charge of and is connected.The present invention is, by condenser, vaporizer heating, cooling regeneration gas, to inhale When dry machine works, high temperature liquid refrigerant is formed by compressor, the high temperature liquid refrigerant sent by compressor is in condenser In in heated house steward the cooling of regeneration gas be accordingly changed into liquid refrigerant, while making the regeneration gas by heating main Heating is for thermal regeneration;At the same time, liquid refrigerant evaporation endothermic in vaporizer, makes the regeneration by cooling down house steward Gas turns cold for cold blowing regeneration.That is, the gas in heating main can be had respectively entered after condenser heating In first, second, third heating is in charge of, similarly, the gas cooled down in house steward can be had respectively entered after vaporizer cooling In first, second, third cooling is in charge of.
First heating is in charge of by the gas outlet after the 9th electrodynamic valve 509 with first, second adsorption tower and the first cooling It is in charge of and is in parallel, and stopping for one-way conduction is respectively provided with two parallel pipelines for connecting first, second adsorption tower gas outlet Valve is returned, the check-valves being provided with the parallel pipeline for connecting the first adsorption tower gas outlet are the 3rd check-valves 63, are arranged on It is the 4th check-valves 64 to connect the check-valves on the parallel pipeline of the second adsorption tower gas outlet, and the first cooling is in charge of, and arranges 12nd electrodynamic valve 512, the conducting direction of the 3rd, the 4th check-valves is respectively from the air outlet side of aerator towards first, The gas outlet side of two adsorption towers, that is to say, that when the 9th electrodynamic valve is opened, exports and through cold from the air outlet of aerator The thermal regeneration gas of condenser heating can be by the 3rd check-valves into the first absorption after being in charge of by heating main, the first heating Tower enters the second adsorption tower by the 4th check-valves;When the 12nd electrodynamic valve is opened, export simultaneously from the air outlet of aerator The can be entered through the cold blowing regeneration gas of vaporizer cooling by the 3rd check-valves after being in charge of by cooling house steward, the first cooling One adsorption tower enters the second adsorption tower by the 4th check-valves.
Second heating is in charge of by the gas outlet after the tenth electrodynamic valve 510 with second, third adsorption tower and the second cooling It is in charge of and is in parallel, and stopping for one-way conduction is respectively provided with two parallel pipelines for connecting second, third adsorption tower gas outlet Valve is returned, the check-valves being provided with the parallel pipeline for connecting the second adsorption tower gas outlet are the 6th check-valves 66, are arranged on It is the 7th check-valves 67 to connect the check-valves on the parallel pipeline of the 3rd adsorption tower gas outlet, and the second cooling is in charge of, and arranges 13rd electrodynamic valve 513, the conducting direction of the 5th, the 6th check-valves is respectively from the air outlet side of aerator towards second, The gas outlet side of three adsorption towers, that is to say, that when the tenth electrodynamic valve is opened, exports and through cold from the air outlet of aerator The thermal regeneration gas of condenser heating can be by the 6th check-valves into the second absorption after being in charge of by heating main, the second heating Tower enters the 3rd adsorption tower by the 7th check-valves;When the 13rd electrodynamic valve is opened, export simultaneously from the air outlet of aerator The can be entered through the cold blowing regeneration gas of vaporizer cooling by the 6th check-valves after being in charge of by cooling house steward, the second cooling Two adsorption towers enter the 3rd adsorption tower by the 7th check-valves.
3rd heating is in charge of by cold with the gas outlet of the first, the 3rd adsorption tower and the 3rd after the 11st electrodynamic valve 511 But it is in charge of and is in parallel, and one-way conduction is respectively provided with two articles of parallel pipelines for connecting the first, the 3rd adsorption tower gas outlet Check-valves, it is the 8th check-valves 68 to be provided with the check-valves on the parallel pipeline for connecting the first adsorption tower gas outlet, is arranged Check-valves on the parallel pipeline for connecting the 3rd adsorption tower gas outlet are the 9th check-valves 69, and the 3rd cooling is in charge of, and sets Put the 14th electrodynamic valve 514, the conducting direction of the eight, the 9th check-valves respectively from the air outlet side of aerator towards first, The gas outlet side of the 3rd adsorption tower, that is to say, that when the 11st electrodynamic valve is opened, the air outlet output and Jing from aerator Crossing the thermal regeneration gas of condenser heating can enter first after being in charge of by heating main, the 3rd heating by the 8th check-valves Adsorption tower enters the 3rd adsorption tower by the 9th check-valves;When the 14th electrodynamic valve is opened, the air outlet from aerator is defeated Go out and can be entered by the 8th check-valves after being in charge of by cooling house steward, the 3rd cooling through the cold blowing regeneration gas of vaporizer cooling Enter the first adsorption tower or enter the 3rd adsorption tower by the 9th check-valves.
The air inlet of aerator is then formed with the air inlet of first, second, third adsorption tower by pipeline and is connected in parallel, and Being respectively provided with three parallel pipelines can automatically control the electrodynamic valve of break-make, wherein being connected to the air inlet and first of aerator Electrodynamic valve between the air inlet of adsorption tower is first electrodynamic valve 501, is connected to the air inlet and the second adsorption tower of aerator Electrodynamic valve between air inlet be the second electrodynamic valve 502, be connected to aerator air inlet and the 3rd adsorption tower air inlet it Between electrodynamic valve be the 16th electrodynamic valve 516.
Operationally, three adsorption towers are operated in respectively adsorbed state, thermal regeneration state, cold blowing to the dryer of the present invention Reproduced state simultaneously switches successively, and by three switch operating states a circulation can be completed, and switches first three with regard to three times below The operation principle of adsorption tower is made one and is specifically described:
Switch the working condition of first three adsorption tower for the first time:First adsorption tower is operated in adsorbed state, the second adsorption tower Thermal regeneration state is operated in, and the 3rd adsorption tower is then operated in cold blowing reproduced state.Now the 3rd electrodynamic valve is opened, air inlet pipe Compressed air entered in the first adsorption tower from the air inlet of the first adsorption tower by the 3rd electrodynamic valve, the moisture of compressed air Absorbed by the adsorbent in the first adsorption tower, then, dry compressed air flows out from the gas outlet of the first adsorption tower, and passes through First check-valve is exported from escape pipe, so as to form an independent absorption gas circuit;At the same time, aerator by gas from air-out Mouth is sent, and compressor now is in running status is opened, and the gas that aerator is sent is partly into heating main, cold in Jing Thermal regeneration gas is formed after condenser heating;Another part then enters cooling house steward, and cold blowing is being formed again Jing after vaporizer cooling Angry body.Thermal regeneration gas in heating main is in charge of by the 9th electrodynamic valve opened into the first heating, and by the Four check-valves are entered in the second adsorption tower from the gas outlet of the second adsorption tower, so as to carry out to the adsorbent in the second adsorption tower Thermal regeneration.Then, the thermal regeneration gas that temperature is reduced flows out from the air inlet of the second adsorption tower, and by the second of unlatching Electrodynamic valve flow back into the air inlet of aerator, so as to form the thermal regeneration gas circuit of a closure;In addition, cold in cooling house steward Blow regeneration gas to be in charge of into the 3rd cooling by the 14th electrodynamic valve opened, and by the 9th check-valves from the 3rd adsorption tower Gas outlet enter in the 3rd adsorption tower, so as to carry out cold blowing regeneration to the adsorbent in the 3rd adsorption tower.Then, temperature liter High cold blowing regeneration gas flows out from the air inlet of the 3rd adsorption tower, and flow back into aerator by the 16th electrodynamic valve opened Air inlet, so as to formed one closure cold blowing regeneration gas circuit.
It is understood that now first, the four, the ten, the 11st, the 12nd, the 13rd, the 15th electrodynamic valve should It is closed.Further, since the pressure of the compressed air in absorption gas circuit will be far above thermal regeneration gas circuit and cold blowing again The gas pressure conveyed by aerator in angry road, that is to say, that near the gas outlet side of the first adsorption tower on the 3rd check-valves Absorption gas circuit gas pressure will be far above near first heating be in charge of side thermal regeneration gas circuit gas pressure, because This, interior thermal regeneration gas is in charge of in the first heating will not be passed through in the 3rd check-valves stream to the first adsorption tower, and the first absorption The compressed gas that tower flows out then cannot be entered in the second adsorption tower by the blocking of the 3rd check-valves by the 4th check-valves.With this In the same manner, the gas pressure of the absorption gas circuit on the 8th check-valves near the gas outlet side of the first adsorption tower will be far above close the The gas pressure that the cold blowing of side regenerates gas circuit is in charge of in three coolings, therefore, interior cold blowing regeneration gas is in charge of in the 3rd cooling will not By in the 8th check-valves stream to the first adsorption tower, and the compressed gas that the first adsorption tower flows out then are hindered by the 8th check-valves It is disconnected to be entered in the 3rd adsorption tower by the 9th check-valves.So, you can absorption, thermal regeneration, cold is formed in dryer Blow three separate gas circuits of regeneration.
It should be noted that because the gas pressure of the air inlet side of aerator will be less than the gas pressure of air outlet side Power, that is to say, that in the gas pressure of thermal regeneration and the gas outlet side of second, third adsorption tower of cold blowing reproduced state The gas pressure of air inlet side is higher than, therefore, the thermal regeneration gas flowed out from the air inlet of the second adsorption tower will not be from The air inlet of the 3rd adsorption tower is redirected back into in the 3rd adsorption tower, in the same manner, from the cold blowing that the air inlet of the 3rd adsorption tower flows out Regeneration gas also will not be redirected back into in the second adsorption tower from the air inlet of the second adsorption tower.Thermal regeneration gas and cold blowing are again Angry body is returned to original temperature after merging, and is then again introduced into the air inlet of aerator to form circulation.
When dryer work certain hour after, need to carry out thermal regeneration to the adsorbent in the first adsorption tower, now I Should open the three, the four, the nine, the ten, the 12nd, the 14th, the 16th electrodynamic valve, correspondingly close first, second, the 11, the 13rd, the 15th electrodynamic valve, so as to complete for the first time switching, the work that three adsorption towers are entered before switching for second State.
Switch the working condition of first three adsorption tower for the second time:Now, the 3rd adsorption tower for terminating cold blowing regeneration is switched to Adsorbed state, the first adsorption tower then enters thermal regeneration state, and the second adsorption tower is then switched to cold blowing reproduced state.For this purpose, We open the 15th electrodynamic valve, and the compressed air of air inlet pipe is entered by the 15th electrodynamic valve from the air inlet of the 3rd adsorption tower Enter in the 3rd adsorption tower, the moisture of compressed air is absorbed by the adsorbent of regeneration in the 3rd adsorption tower, then, dry compression Air flows out from the gas outlet of the 3rd adsorption tower, and is exported from escape pipe by the 5th check-valves, independent so as to form one Absorption gas circuit;At the same time, the thermal regeneration gas in heating main is heated by the 11st electrodynamic valve opened into the 3rd It is in charge of, and is entered in the first adsorption tower from the gas outlet of the first adsorption tower by the 8th check-valves, so as to the first adsorption tower Interior adsorbent carries out thermal regeneration.Then, the thermal regeneration gas that temperature is reduced flows out from the air inlet of the first adsorption tower, and The air inlet of aerator is flow back into by the first electrodynamic valve opened, so as to form the thermal regeneration gas circuit of a closure;In addition, Cold blowing regeneration gas in cooling house steward is in charge of by the 13rd electrodynamic valve opened into the second cooling, and by the 6th non-return Valve is entered in the second adsorption tower from the gas outlet of the second adsorption tower, so as to carry out cold blowing again to the adsorbent in the second adsorption tower It is raw.Then, the elevated cold blowing regeneration gas of temperature flows out from the air inlet of the second adsorption tower, and the second electrodynamic valve by opening The air inlet of aerator is flow back into, so as to form the cold blowing regeneration gas circuit of a closure.
Then, dryer needs to carry out thermal regeneration to the adsorbent in the 3rd adsorption tower, now we should open first, Four, the ten, the 12nd, the 16th electrodynamic valve, correspondingly close second, third, the nine, the 11st, the 13rd, the 14th, 15th electrodynamic valve, so as to complete second switching, the working condition that three adsorption towers are entered before third time switches.
Switch the working condition of first three adsorption tower for the second time:Now, the second adsorption tower for terminating cold blowing regeneration is switched to Adsorbed state, the 3rd adsorption tower then enters thermal regeneration state, and the first adsorption tower is then switched to cold blowing reproduced state.For this purpose, We open the 4th electrodynamic valve, and the compressed air of air inlet pipe is entered into by the 4th electrodynamic valve from the air inlet of the second adsorption tower In second adsorption tower, the moisture of compressed air is absorbed by the adsorbent of regeneration in the second adsorption tower, then, dry compressed air Flow out from the gas outlet of the second adsorption tower, and exported from escape pipe by second check-valve, so as to form an independent absorption Gas circuit;At the same time, the thermal regeneration gas in heating main is in charge of by the tenth electrodynamic valve opened into the second heating, and Entered in the 3rd adsorption tower from the gas outlet of the 3rd adsorption tower by the 7th check-valves, so as to the absorption in the 3rd adsorption tower Agent carries out thermal regeneration.Then, the thermal regeneration gas that temperature is reduced flows out from the air inlet of the 3rd adsorption tower, and by opening The 16th electrodynamic valve flow back into the air inlet of aerator, so as to form the thermal regeneration gas circuit of a closure;In addition, cooling is total Cold blowing regeneration gas in pipe is in charge of by the 12nd electrodynamic valve opened into the first cooling, and by the 3rd check-valves from the The gas outlet of one adsorption tower is entered in the first adsorption tower, so as to carry out cold blowing regeneration to the adsorbent in the first adsorption tower.So Afterwards, the elevated cold blowing regeneration gas of temperature flows out from the air inlet of the first adsorption tower, and is flowed back to by the first electrodynamic valve opened To the air inlet of aerator, so as to form the cold blowing regeneration gas circuit of a closure.It is understood that now second, third, Nine, the 11st, the 13rd, the 14th, the 15th electrodynamic valve should be at closed mode.
Then, dryer needs to carry out thermal regeneration to the adsorbent in the second adsorption tower, now we should open second, Three, the nine, the 14th, the 16th electrodynamic valve, correspondingly close first, the four, the ten, the 11st, the 12nd, the 13rd, 15th electrodynamic valve, so as to complete third time switching and a circulation, three adsorption towers are reentered before switching for the first time Working condition.
Additionally, we can also between the gas outlet of first, second adsorption tower, the gas outlet of second, third adsorption tower it Between and the gas outlet of the first, the 3rd adsorption tower between be connected by pipeline respectively, and go here and there respectively on three connecting lines Catcher is dynamic to be adjusted flow valve 10 and can automatically control the electrodynamic valve of break-make.It is provided with the gas outlet of first, second adsorption tower Between connecting tube on electrodynamic valve be the 8th electrodynamic valve 508, the connection being arranged between the gas outlet of the first, the 3rd adsorption tower Electrodynamic valve on pipe be the 18th electrodynamic valve 518, the electricity being arranged in the connecting tube between the gas outlet of second, third adsorption tower Dynamic valve is the 17th electrodynamic valve 517.Eight, the 17th, the 18th electrodynamic valve is closed at ordinary times, so that first, Phase between the gas outlet of two adsorption towers, the gas outlet of second, third adsorption tower and between the gas outlet of the first, the 3rd adsorption tower Mutually separate.When we are when switching for the first time is carried out, the 18th electrodynamic valve can be simultaneously opened, so that the first, the 3rd adsorption tower Gas outlet between be interconnected, so, originally the first adsorption tower in adsorbed state be located in absorption gas circuit be dried it is high Calm the anger to run through by body and adjust manually flow valve and the 18th electrodynamic valve is entered originally in the 3rd of cold blowing reproduced state the In the cold blowing regeneration gas circuit that adsorption tower is located, making the gas pressure of the absorption gas circuit of script reduces rapidly, and then we close again The 18th electrodynamic valve is closed to cut off the contact between absorption gas circuit and cold blowing regeneration gas circuit, so as to complete switching for the first time, you can Restart to carry out compressed air adsorption dry, and originally the gas in the absorption gas circuit of adsorbed state then can be used as cutting The regeneration gas in thermal regeneration gas circuit after changing.When we are when second switching is carried out, then the 17th can be simultaneously opened electric Dynamic valve, so that being interconnected between the gas outlet of second, third adsorption tower, so, originally the 3rd in adsorbed state inhales Being dried gases at high pressure and can run through in absorption gas circuit that attached tower is located adjust manually flow valve and the entrance of the 17th electrodynamic valve Originally in the cold blowing regeneration gas circuit that the second adsorption tower in cold blowing reproduced state is located, the gas pressure of the absorption gas circuit of script is made Power is reduced rapidly, and then we are re-closing off the 17th electrodynamic valve to cut off the connection between absorption gas circuit and cold blowing regeneration gas circuit System, so as to complete second switching.When we are when third time switching is carried out, then the 8th electrodynamic valve can be simultaneously opened, so that It is interconnected between the gas outlet of first, second adsorption tower, so, absorption that the second adsorption tower in adsorbed state is located originally In gas circuit be dried gases at high pressure by run through adjust manually flow valve and the 8th electrodynamic valve enter originally in cold blowing again In the cold blowing regeneration gas circuit that first adsorption tower of raw state is located, making the gas pressure of the absorption gas circuit of script reduces rapidly, so Afterwards we are re-closing off the 8th electrodynamic valve to cut off the contact between absorption gas circuit and cold blowing regeneration gas circuit, so as to complete third time Switching.The manual gas flow for adjusting connecting line when flow valve can control switching therein, so as to control three adsorption tower works Make the switch speed of state.It is understood that adjust flow valve manually only need to be adjusted when dryer runs for the first time, when Fixed manual adjusts flow valve by after adjusting in place so as to which circulation keeps constant.
In addition, we can also be sequentially connected the 5th electrodynamic valve 505 and air-breathing mistake in the air inlet of aerator by pipeline Filter 11.So, when we open five electrodynamic valves, the air inlet of aerator is connected with outside air, and outside air can lead to Cross after suction filter is filtered totally and entered in regeneration gas circuit by the air inlet of aerator, to fill in regeneration gas circuit again Angry body.The 5th electrodynamic valve is then shut off, suction filter quits work, regeneration gas circuit now re-forms closure gas circuit, Gas circulating flow in regeneration gas circuit, thermal regeneration is carried out to one of adsorption tower and cold blowing is carried out to another adsorption tower Regeneration.
Further, we can by connection the first electrodynamic valve and blower inlet pipeline be connected the second electrodynamic valve and The pipeline of blower inlet first merges and is connected on a main pipe rail, and then main pipe rail is connected to the air inlet of aerator On, so, we can arrange the 6th electrodynamic valve 506 on the main pipe rail, so as to can easily control to regenerate the logical of gas circuit It is disconnected.At the same time, we also other on the main pipe rail can connect a noise reduction pipeline, and on the noise reduction pipeline one the 7th is sequentially connected Electrodynamic valve 507 and a deafener 12.So, when dryer is shut down, we can open the 7th and the first, second, the tenth Six electrodynamic valves, to discharge the gas in absorption gas circuit and regeneration gas circuit, and deafener making an uproar when then can effectively eliminate deflation Sound.

Claims (3)

1. a kind of zero QI consumed blowing-type dryer, including input compressed air air inlet pipe, export dried compressed air Escape pipe and the first adsorption tower for drying compressed air successively, the second adsorption tower and the 3rd adsorption tower, is characterized in that, The air inlet pipe is in parallel respectively by pipeline with the air inlet of first, second, third adsorption tower, and on three parallel pipelines Being respectively provided with can automatically control the electrodynamic valve of break-make;The escape pipe is respectively by pipeline and first, second, third adsorption tower Gas outlet is in parallel, and the gas outlet from first, second, third adsorption tower is respectively provided with three parallel pipelines to escape pipe The check-valves of one-way conduction;Additionally, the condenser being also connected with compressor including aerator, compressor and vaporizer, air blast The air outlet of machine is connected by pipeline with heating main parallel with one another and cooling house steward, and the heating main connects condenser It is in charge of with the first heating parallel with one another afterwards, the second heating is in charge of, the 3rd heating is in charge of and is connected, the cooling house steward connection is steamed Send out be in charge of with first cooling parallel with one another after device, the second cooling is in charge of, the 3rd cooling is in charge of and is connected, the first heating is in charge of logical Cross to be in charge of with the gas outlet of first, second adsorption tower and the first cooling after an electrodynamic valve and be in parallel, and in two articles of connections the First, it is respectively provided with the parallel pipeline of the second adsorption tower gas outlet unidirectional to the gas outlet of first, second adsorption tower from aerator The check-valves of conducting, the first cooling is in charge of, and is provided with electrodynamic valve;Second heating is in charge of after an electrodynamic valve with second, the The gas outlet of three adsorption towers and the second cooling are in charge of and are in parallel, and connect at two second, third adsorption tower gas outlet and The check-valves of the gas outlet one-way conduction from aerator to second, third adsorption tower, the second cooling point are respectively provided with union road Electrodynamic valve is then provided with pipe;Gas outlet with the first, the 3rd adsorption tower and the are in charge of after an electrodynamic valve in 3rd heating Three coolings are in charge of and are in parallel, and are respectively provided with by air blast on two articles of parallel pipelines for connecting the first, the 3rd adsorption tower gas outlet Check-valves from machine to the gas outlet one-way conduction of the first, the 3rd adsorption tower, the 3rd cooling be in charge of, be provided with electrodynamic valve;Aerator Air inlet be in parallel with the air inlet of first, second, third adsorption tower by pipeline, and set respectively on three parallel pipelines Putting can automatically control the electrodynamic valve of break-make, between the gas outlet of first, second adsorption tower, the outlet of second, third adsorption tower It is connected by pipeline respectively between mouthful and between the gas outlet of the first, the 3rd adsorption tower, and is divided on three connecting lines Chuan Jie not manually adjust flow valve and the electrodynamic valve of break-make can be automatically controlled.
2. a kind of zero QI consumed blowing-type dryer according to claim 1, is characterized in that, aerator air inlet also Electrodynamic valve and suction filter are connected with turn by pipeline.
3. a kind of zero QI consumed blowing-type dryer according to claim 1 and 2, is characterized in that, described first, second, Adsorbent in three adsorption towers adopts alumina particle.
CN201510005852.4A 2015-01-06 2015-01-06 Zero-gas consumption blowing-type suction drying machine Active CN105080296B (en)

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Denomination of invention: A zero gas consumption blower dryer

Effective date of registration: 20210702

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Pledgee: Zhejiang Tailong Commercial Bank Co.,Ltd. Hangzhou Jiande sub branch

Pledgor: HANGZHOU FANTAI MACHINERY Co.,Ltd.

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