CN109603363A - Aqueous vapor seperating vale, environment-friendly type air dust pelletizing system - Google Patents
Aqueous vapor seperating vale, environment-friendly type air dust pelletizing system Download PDFInfo
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- CN109603363A CN109603363A CN201910071984.5A CN201910071984A CN109603363A CN 109603363 A CN109603363 A CN 109603363A CN 201910071984 A CN201910071984 A CN 201910071984A CN 109603363 A CN109603363 A CN 109603363A
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- flf
- zxq
- seperating vale
- lnq
- aqueous vapor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/05—Separating dispersed particles from gases, air or vapours by liquid as separating agent by condensation of the separating agent
Abstract
Aqueous vapor seperating vale (FLF), it is characterised in that: include outlet pipe (FLF-CSG), conical cavity (FLF-ZXQ), heavy ball (FLF-ZQ), floating ball (FLF-FQ).Environment-friendly type air dust pelletizing system has the aqueous vapor seperating vale (FLF).The configuration of the present invention is simple, energy consumption are less, high-efficient, effect is good, have started new technical thought.
Description
Technical field
The present invention relates to gas cleanings, and in particular to aqueous vapor seperating vale, environment-friendly type air dust pelletizing system.
Background technique
Dedusting dedusting；Dust a } mement abbreviation dedusting.Removing is suspended in the process that dust is offered in gas:
In the industry such as chemistry, fuel, metallurgy, can often it generate containing a large amount of powder r, the gas of is washed one's hair, it is necessary to remove dust, be produced after making
Process is successfully continued.Such as in contact method manufacture sulfuric acid, if the arsenic that left floating in unstripped gas, selenium etc. are micro-
Grain not removes, and will make catalyst poisoning.In addition to factory meets industrial requirement, dedusting is also for recycling, labor
The exhaust gas that two for example certain industrial enterprises such as the protection of dynamic protection, urban and rural health and crops are given off should carry out certain journey
The dedusting of degree directly puts National People's Congress's gas without stining.
Environmental protection generally refers to the mankind to solve reality or potential environmental problem, coordinates the relationship of the mankind and environment,
Protect the general name of the living environment of the mankind, the various action for ensureing the sustainable development of economic society and taking.Environmental protection is related to
Cannot private adopt (mine) denudation (tree), cannot disorderly arrange (sewage) and leave about (dirty gas), cannot overgraze, cannot excessively open up wasteland, no
It can excessively develop natural resources, ecological balance of nature etc. cannot be destroyed.Environmental protection needs the flue gas generated to production process
Etc. being dusted, the equipment that dust is separated from flue gas is deduster.There are many existing deduster type, also have very much
Defect is as low (such as in do not adapted to high-temperature flue gas (such as bag filter), maintenance cost height (such as electrostatic precipitator), efficiency of dust collection
Cyclone dust collectors).
Prior art dedusting have gravitational settling, centrifuge separation, filtering (T- method), liquid scrubbing (wet process), electrostatic, sound wave and
The methods such as ultrasonic wave, these methods are each advantageous also respectively to have deficiency.
Summary of the invention
In view of drawbacks described above in the prior art or deficiency, the invention proposes aqueous vapor seperating vales, environment-friendly type air dedusting
System has started new approaches.
1, aqueous vapor seperating vale (FLF), it is characterised in that: include outlet pipe (FLF-CSG), conical cavity (FLF-ZXQ), heavy ball
(FLF-ZQ), floating ball (FLF-FQ)；
In aqueous vapor seperating vale (FLF): conical cavity (FLF-ZXQ's) is placed in a manner of axis vertical, conical cavity (FLF-
ZXQ big end) is upper, and the small end of conical cavity (FLF-ZXQ) is under；
In aqueous vapor seperating vale (FLF): the density of heavy ball (FLF-ZQ) is greater than the water in application environment；
In aqueous vapor seperating vale (FLF): the density of floating ball (FLF-FQ) is less than the water in application environment；
In aqueous vapor seperating vale (FLF): the lower end of conical cavity (FLF-ZXQ) is connected with the highest point of outlet pipe (FLF-CSG)；
In aqueous vapor seperating vale (FLF): the diameter of heavy ball (FLF-ZQ) is less than the big end of conical cavity (FLF-ZXQ), heavy ball
(FLF-ZQ) diameter is greater than the small end of conical cavity (FLF-ZXQ)；
In aqueous vapor seperating vale (FLF): heavy ball (FLF-ZQ) device is in conical cavity (FLF-ZXQ)；
In aqueous vapor seperating vale (FLF): floating ball (FLF-FQ) is connected by flexible cord with heavy ball (FLF-ZQ), when aqueous vapor seperating vale
(FLF) heavy ball (FLF-ZQ) is by floating ball (FLF-FQ) pull-up, conical cavity when the water of cavity floats floating ball (FLF-FQ) where
(FLF-ZXQ) lower end is decontroled, water pass sequentially through the upper end of conical cavity (FLF-ZXQ), conical cavity (FLF-ZXQ) lower end, go out
Water pipe (FLF-CSG) discharge, when water surface elevation reduces heavy ball (FLF-ZQ) because gravity is fallen under conical cavity (FLF-ZXQ)
End, the lower end closed of conical cavity (FLF-ZXQ) are not then exhausted from water, since floating ball (FLF-FQ) passes through flexible cord and heavy ball (FLF-
ZQ) be connected thus when the water surface drop to heavy ball height ledger line it is long when conical cavity (FLF-ZXQ) lower end closed, so gas can not
It is discharged.
2, the aqueous vapor seperating vale (FLF) as described in technology contents 1, it is characterised in that: the lumen of outlet pipe (FLF-CSG) is
It is round.
3, the aqueous vapor seperating vale (FLF) as described in technology contents 1, it is characterised in that: the position floating ball (FLF-FQ) solid foam
Ball.
4, the aqueous vapor seperating vale (FLF) as described in technology contents 1, it is characterised in that: floating ball (FLF-FQ) is hollow plastics
Ball.
5, the aqueous vapor seperating vale (FLF) as described in technology contents 1, it is characterised in that: the material of heavy ball (FLF-ZQ) is rubber
Glue.
6, the aqueous vapor seperating vale (FLF) as described in technology contents 1, it is characterised in that: the material of heavy ball (FLF-ZQ) is cream
Glue.
7, the aqueous vapor seperating vale (FLF) as described in technology contents 1, it is characterised in that: by connection floating ball (FLF-FQ) and again
The flexible cord of ball (FLF-ZQ) is substituted for chain made of hard material.
8, environment-friendly type air dust pelletizing system, it is characterised in that: there is aqueous vapor seperating vale (FLF) described in technology contents 1.
Technical principle and its advantages.
The configuration of the present invention is simple, energy consumption are less, high-efficient, effect is good, have started new technical thought.
Detailed description of the invention
Fig. 1 is the frame diagram of embodiment 1, and which show the design sides of the gas purge system of application environment of the invention
Method.
Fig. 2 is the structure chart of embodiment 2.
Fig. 3 is the structure chart of the gas condenser of embodiment 2.
Fig. 4 is the structure chart of the heat-exchange tube (LNQ-HG) of the gas condenser of embodiment 2.
Fig. 5 is the structure chart of the aqueous vapor seperating vale (FLF) of the gas condenser of embodiment 2.
The structure chart of the position Fig. 6 embodiment 3.
Fig. 7 is the structure chart of the rotor (1) of the machinery rotating type air bubble generator of embodiment 3.
Fig. 8 is the structure chart of the container (2) of the machinery rotating type air bubble generator of embodiment 3.
Fig. 9 is the structure chart of the lid (3) of the machinery rotating type air bubble generator of embodiment 3.
Figure 10 is the structure chart of the bearing (4) of the machinery rotating type air bubble generator of embodiment 3.
Figure 11 is the schematic diagram of the motor (5) of the machinery rotating type air bubble generator of embodiment 3.
Figure 12 is the schematic diagram of the assembly of the machinery rotating type air bubble generator of embodiment 3.Wherein 6 be connection bearing (4)
With the rivet of rotor (1).
Figure 13 is the whole schematic diagram of the machinery rotating type air bubble generator of embodiment 3.
Specific embodiment
Embodiment 1, a kind of system of dedusting, it is characterised in that: including gas cooling container, steam generator, gas
Body mixing vessel, gas condenser；
Gas cooling container is for reducing gas temperature；
Steam generator is for generating vapor；
It needs processing gas after gas cooling container is cooling, becomes cooled gas, it is mixed that cooled gas enters gas
Clutch and vapor are mixed into mixed gas, and after water vapour molecule collides the dust in cooled gas, cooling is attached to
On dust, rain core is formed；
Mixed gas enters gas condenser, and after supercooling, vapor is further attached to form droplet, shape on rain core
At rainfall or condensation, rainfall or condensation take away dust granules.
Embodiment 2, as shown in Figure 2-5, dedusting system, it is characterised in that: by Refrigerating container (R1), heating container
(R2), mixing vessel (R3), gas condenser, admission line (JQG), refrigerating and heating device (ZLQ-3), collectively form；
Refrigerating container (R1) has isolation board (R1-GLB), and Refrigerating container (R1) is divided into the first appearance by isolation board (R1-GLB)
Chamber, second cavity two parts, isolation board (R1-GLB) lower section have connecting hole (R1-LJK), and connecting hole (R1-LJK) makes the first appearance
Chamber and the second cavity communicate；
Part is full of cold water in Refrigerating container (R1), and the height of the cold water water surface of Refrigerating container (R1) is lower than isolation board (R1-
GLB top)；
Refrigerating container (R1) also has sewage pipe (R1-PWG), blowdown valve (R1-PWF), sewage pipe (R1-PWG) and first
The bottom of cavity communicates, and blowdown valve (R1-PWF) is located on sewage pipe (R1-PWG) for controlling Refrigerating container (R1) bottom deposit
The discharge of object；
The wall that admission line (JQG) penetrates Refrigerating container (R1) enters in the cold water of the first cavity, admission line (JQG)
Opening is higher than connecting hole (R1-LJK), and the opening of admission line (JQG) is higher than sewage pipe (R1-PWG)；
It heats container (R2) inner part and is full of hot water；
There is blender (JBQ) inside mixing vessel (R3), blender (JBQ) drives by motor；
There is the first seperating vale (FLF1) in mixing vessel (R3)；
The first seperating vale (FLF1) of mixing vessel (R3) is located at the bottom of mixing vessel (R3), for discharging mixing vessel
(R3) water of bottom；
The first seperating vale (FLF1) of mixing vessel (R3) is that a kind of aqueous vapor seperating vale (FLF) only discharges water and do not discharge gas
Body；
Aqueous vapor seperating vale (FLF) includes outlet pipe (FLF-CSG), conical cavity (FLF-ZXQ), heavy ball (FLF-ZQ), floating ball
(FLF-FQ)；
In aqueous vapor seperating vale (FLF): conical cavity (FLF-ZXQ's) is placed in a manner of axis vertical, conical cavity (FLF-
ZXQ big end) is upper, and the small end of conical cavity (FLF-ZXQ) is under；
In aqueous vapor seperating vale (FLF): the density of heavy ball (FLF-ZQ) is greater than the water in application environment；
In aqueous vapor seperating vale (FLF): the density of floating ball (FLF-FQ) is less than the water in application environment；
In aqueous vapor seperating vale (FLF): the lower end of conical cavity (FLF-ZXQ) is connected with the highest point of outlet pipe (FLF-CSG)；
In aqueous vapor seperating vale (FLF): the diameter of heavy ball (FLF-ZQ) is less than the big end of conical cavity (FLF-ZXQ), heavy ball
(FLF-ZQ) diameter is greater than the small end of conical cavity (FLF-ZXQ)；
In aqueous vapor seperating vale (FLF): heavy ball (FLF-ZQ) device is in conical cavity (FLF-ZXQ)；
In aqueous vapor seperating vale (FLF): floating ball (FLF-FQ) is connected by flexible cord with heavy ball (FLF-ZQ), when aqueous vapor seperating vale
(FLF) heavy ball (FLF-ZQ) is by floating ball (FLF-FQ) pull-up, conical cavity when the water of cavity floats floating ball (FLF-FQ) where
(FLF-ZXQ) lower end is decontroled, water pass sequentially through the upper end of conical cavity (FLF-ZXQ), conical cavity (FLF-ZXQ) lower end, go out
Water pipe (FLF-CSG) discharge, when water surface elevation reduces heavy ball (FLF-ZQ) because gravity is fallen under conical cavity (FLF-ZXQ)
End, the lower end closed of conical cavity (FLF-ZXQ) are not then exhausted from water, since floating ball (FLF-FQ) passes through flexible cord and heavy ball (FLF-
ZQ) be connected thus when the water surface drop to heavy ball height ledger line it is long when conical cavity (FLF-ZXQ) lower end closed, so gas can not
It is discharged；
The upper end of the conical cavity (FLF-ZXQ) of the first seperating vale (FLF1) of mixing vessel (R3) and cavity of resorption (LNQ-XQ) phase
Logical, the lower end of the conical cavity (FLF-ZXQ) of the first seperating vale (FLF1) is higher than the bottom of cavity of resorption (LNQ-XQ), the first seperating vale
(FLF1) minimum point of the outlet of outlet pipe (FLF-CSG) is higher than the bottom of cavity of resorption (LNQ-XQ)；
Refrigerating and heating device (ZLQ-3) has heating end and refrigeration end, the refrigeration end and refrigeration of refrigerating and heating device (ZLQ-3)
Container (R1) is connected for cooling down the cold water in Refrigerating container (R1), the heating end and heating container of refrigerating and heating device (ZLQ-3)
(R1) it is connected for the hot water in heating container (R2)；
The top of Refrigerating container (R1) by communicating at the top of the first instlated tubular (GRG1) and mixing vessel (R3), first every
There is the first check valve (DXF1) on the pipeline of heat pipe (GRG1), the gas of mixing vessel (R3) can not be countercurrently to Refrigerating container
(R1)；
The side wall for heating the left side water surface of container (R2) or more and the wall on the right side of mixing vessel (R3) are heat-insulated by second
Pipe (GRG2) communicates；
The outlet pipe for heating first seperating vale (FLF1) of container (R2) passes through third instlated tubular (GRG3) and heating container
(R2) it is communicated below the water surface；
Gas condenser, including epicoele (LNQ-SQ), cavity of resorption (LNQ-XQ), air inlet pipe (LNQ-JG), exhaust pipe (LNQ-
PQG), heat exchanger, balance tracheae (LNQ-QG2), the second seperating vale (FLF2), drainpipe (LNQ-PSG), exhaust pump (B2)；
In gas condenser: epicoele (LNQ-SQ) is full of cooling water for cooling down；
In gas condenser: the cavity of cavity of resorption (LNQ-XQ) is not filled with water, and there are the gas compartment, the gas compartment passes through flat
Weighing apparatus tracheae (LNQ-QG2) is communicated with atmosphere, and the height of the aperture position of balance tracheae (LNQ-QG2) in an atmosphere is higher than epicoele
(LNQ-SQ) highest point of institute's water flowing；
The second seperating vale (FLF2) of gas condenser as the first seperating vale (FLF1) of mixing vessel (R3), and
A kind of aqueous vapor seperating vale (FLF) only discharges water and does not discharge gas；
The upper end of the conical cavity (FLF-ZXQ) of the second seperating vale (FLF2) of gas condenser and cavity of resorption (LNQ-XQ) phase
Logical, the lower end of the conical cavity (FLF-ZXQ) of the second seperating vale (FLF2) is higher than the bottom of cavity of resorption (LNQ-XQ), the second seperating vale
(FLF2) minimum point of the outlet of outlet pipe (FLF-CSG) is higher than the bottom of cavity of resorption (LNQ-XQ)；
The heat exchanger of gas condenser is made of multiple heat-exchange tubes (LNQ-HG)；
The heat-exchange tube (LNQ-HG) of gas condenser includes the first pipe (LNQ-HG-1), the second pipe (LNQ-HG-2), the
Three pipes (LNQ-HG-3), the 4th pipe (LNQ-HG-4), the 5th pipe (LNQ-HG-5), the 6th pipe (LNQ-HG-6), the 7th pipe (LNQ-
HG-7)；
In the heat-exchange tube (LNQ-HG) of gas condenser: the first pipe (LNQ-HG-1) is put in a manner of axis horizontal；
In the heat-exchange tube (LNQ-HG) of gas condenser: the second pipe (LNQ-HG-1) is put in a manner of axis vertical；
In the heat-exchange tube (LNQ-HG) of gas condenser: third pipe (LNQ-HG-3) is put in a manner of axis vertical；
In the heat-exchange tube (LNQ-HG) of gas condenser: the 4th pipe (LNQ-HG-4) is put in a manner of axis horizontal；
In the heat-exchange tube (LNQ-HG) of gas condenser: the 5th pipe (LNQ-HG-5) is put in a manner of axis vertical；
In the heat-exchange tube (LNQ-HG) of gas condenser: the 6th pipe (LNQ-HG-6) is put in a manner of axis vertical；
In the heat-exchange tube (LNQ-HG) of gas condenser: the 7th pipe (LNQ-HG-7) is put in a manner of axis horizontal；
In the heat-exchange tube (LNQ-HG) of gas condenser: the lower end of the second pipe (LNQ-HG-1) has opening to outside；
In the heat-exchange tube (LNQ-HG) of gas condenser: the lower end of the 6th pipe (LNQ-HG-6) has opening to outside；
In the heat-exchange tube (LNQ-HG) of gas condenser: the left end of the first pipe (LNQ-HG-1), third pipe (LNQ-HG-
3) upper end of lower end, the second pipe (LNQ-HG-2), three connect and communicate；
In the heat-exchange tube (LNQ-HG) of gas condenser: the right end of the 7th pipe (LNQ-HG-7), the 5th pipe (LNQ-HG-
5) upper end of lower end, the 6th pipe (LNQ-HG-6), three connect and communicate；
In the heat-exchange tube (LNQ-HG) of gas condenser: the upper end of third pipe (LNQ-HG-3) and the 4th pipe (LNQ-HG-
4) right end connects and communicates；
In the heat-exchange tube (LNQ-HG) of gas condenser: the upper end of the 5th pipe (LNQ-HG-5) and the 4th pipe (LNQ-HG-
4) left end connects and communicates；
The combined method that the heat-exchange tube (LNQ-HG) of gas condenser constitutes heat exchanger is to hand over two adjacent heat
It changes pipe (LNQ-HG) and is named as left heat-exchange tube, right heat-exchange tube, then have the first pipe (LNQ-HG-1) and the right side of left heat-exchange tube
7th pipe (LNQ-HG-7) of heat-exchange tube connects and communicates；
In gas condenser: the lower end of the second pipe (LNQ-HG-1) of all heat-exchange tubes (LNQ-HG) of heat exchanger
The horizontal position of the opening of the lower end of opening and the 6th pipe (LNQ-HG-6) is lower than the conical cavity (FLF- of the second seperating vale (FLF2)
ZXQ) upper end；
In gas condenser: the lower end of the second pipe (LNQ-HG-1) of all heat-exchange tubes (LNQ-HG) of heat exchanger
The lower end of opening and the 6th pipe (LNQ-HG-6) is in cavity of resorption (LNQ-XQ)；
In gas condenser: the lower end of the second pipe (LNQ-HG-1) of all heat-exchange tubes (LNQ-HG) of heat exchanger
Opening and the 6th pipe (LNQ-HG-6)
In gas condenser: the air intake of exhaust pump (B2) and the 7th pipe of leftmost heat-exchange tube (LNQ-HG)
(LNQ-HG-7) it communicates, the gas outlet of exhaust pump (B2) is communicated with the air intake of drainpipe (LNQ-PSG), air inlet pipe (LNQ-JG)
It is communicated with the first pipe (LNQ-HG-1) of the heat-exchange tube (LNQ-HG) of rightmost, gas passes through cooling, gas after heat exchanger
Included in water droplet be condensed into droplet, droplet is fallen into cavity of resorption (LNQ-XQ), and cavity of resorption (LNQ-XQ) interior water reaches certain water
Behind position, a part is discharged by the second seperating vale (FLF2) and retains a part, reaches and removes water constituent contained in gas；
Mixing vessel (R3) is identical as air inlet pipe (LNQ-JG) of gas condenser；
The epicoele (LNQ-SQ) of gas condenser passes through the first condensation exchange water pipe (SG1), the second condensation exchange water pipe
(SG2) it is communicated with the second cavity of Refrigerating container (R1), in the second condensation exchange water pipe (SG2) there is circulating pump (SG2) to make gas
Cooling water and Refrigerating container (R1) inner cold water in the epicoele (LNQ-SQ) of condenser body recycle；
The exhaust pump (B2) of gas condenser starts, and holds since the gas of air inlet pipe (JQG) after suction function enters refrigeration
Device (R1) generates bubble, bubble and Cold Water Exposure cooling, and the portion gas dust in gas falls in the cold water of Refrigerating container (R1)
In, after bubble eruption, pass through the first instlated tubular (GRG1) through overcooled gas, into mixing vessel (R3)；Since negative pressure is made
Enter mixing vessel (R3) with the hot steam of heating container (R2)；Due to the stirring of blender (JBQ), cooled gas and heat
Steam is sufficiently mixed, the lower composition raindrop core of the temperature of the solid dust contained in cooled gas, and hot steam contacts raindrop
Temperature decreasing concentration is attached on raindrop core when core, and due to the effect of gas condenser so that hot steam cohesion, forms bigger rain
Drop, the cavity of resorption that raindrop fall into gas condenser in the heat-exchange tube (LNQ-HG) of gas condenser carry solid dust and return to system
In heat container (R2).
Embodiment 3, such as Fig. 6-13, dedusting system, it is characterised in that: by machinery rotating type air bubble generator (R1),
Container (R2), mixing vessel (R3), gas condenser, admission line (JQG), refrigerating and heating device (3) are heated, is collectively formed；
Machinery rotating type air bubble generator (R1) include rotor (1), container (2), lid (3), bearing (4), motor (5),
Rivet (6)；
Rotor (1) includes interconnecting piece (1-1), back-off container (1-2), waist mouth (1-3), venthole (1-4), air inlet openings
(1-8), driving blade group (1-5)；
In rotor (1): interconnecting piece (1-1) is cylinder, has connecting hole (1-7) on interconnecting piece (1-1), interconnecting piece (1-
1) axis of axis and connecting hole (1-7) intersects vertically, and the interconnecting piece upper end (1-1) has motor connecting structure；
In rotor (1): back-off container (1-2) is cylinder, has cylindrical cavity (1-6) in back-off container (1-2), circle
Cylindrical cavity (1-6) is coaxial with back-off container (1-2), is buckled to the upper end closed of container (1-2)；
In rotor (1): waist mouth (1-3) be it is pyramidal, waist mouth (1-3) have pyramidal cavity, waist mouth (1-3) it is pyramidal
The axis of cavity is overlapped with the axis of Yao Kou (1-3), the big end of the opening of the pyramidal cavity of waist mouth (1-3) and back-off container
The lower end (1-2) communicates；
In rotor (1): air inlet openings (1-8) be it is cylindric, air inlet openings (1-8) have cylindrical cavity, air inlet openings
The axis of (1-8) is coaxial with the cylindrical cavity of air inlet openings (1-8), the cylindrical cavity and Yao Kou (1- of air inlet openings (1-8)
3) end that the opening of pyramidal cavity is small communicates；
In rotor (1): driving blade group (1-5) is made of blade (1-5-3-1) and lower blade (1-5-3-2), upper leaf
Piece and lower blade are arc；Blade (1-5-3-1) is parallel with lower blade (1-5-3-2), the inside of blade (1-5-3-1)
It is connected with the outer wall of back-off container (1-2), the inside of lower blade (1-5-3-2) is connected with the outer wall of back-off container (1-2), upper leaf
Be between the outside of piece (1-5-3-1) and the outside of lower blade (1-5-3-2) it is open, the head end of blade (1-5-3-1) arrives
Be buckled to container (1-2) upper end distance greater than blade (1-5-3-1) tail end to be buckled to container (1-2) upper end away from
From；The head end of lower blade (1-5-3-2) is greater than the tail end of lower blade (1-5-3-2) to the distance of the upper end of back-off container (1-2)
To the distance of the upper end of back-off container (1-2)；The outer rim camber line of lower blade (1-5-3-2) and the outer rim of blade (1-5-3-1)
Camber line is coplanar；The length of the outer rim camber line of blade (1-5-3-1) is 1/6th of circle where foreign aid's camber line；Driving blade group
The quantity of (1-5) is 3 (1-5-1,1-5-2,1-5-3), and 3 driving blade groups (1-5-1,1-5-2,1-5-3) are to be buckled to container
The axis of (1-2) is center line circumferentially array distribution；
In rotor (1): venthole (1-4) penetrates the wall of back-off container (1-2), and the inner end of venthole (1-4) and back-off are held
The cylindrical cavity (1-6) of device (1-2) communicates；The outer end spatial position of venthole (1-4) is located at the upper of driving blade group (1-5)
The centre of the tail end of the lower blade (1-5-3-2) of the tail end and driving blade group (1-5) of blade (1-5-3-1), venthole (1-4)
Quantity be 3, the corresponding venthole (1-4) of each driving blade group (1-5), 3 ventholes (1-4) are to be buckled to container (1-
2) axis is center line circumferentially array distribution；
Container (2) include cavity, make unrestrained cylinder (2-1), air inlet pipe (2-2), water-permeable passage (2-3), support portion (2-4),
Container foot (2-5)；
In container (2): cavity is pyramidal cavity, and upward, lower end is downward for big end；
In container (2): making unrestrained cylinder (2-1) and be located in cavity, make unrestrained cylinder (2-1) as cylindrical shape, make unrestrained cylinder (2-1)
Inner wall on have 3 recess cambered surfaces (2-1-1), 3 recess cambered surfaces (2-1-1) are centered on the axis for making unrestrained cylinder (2-1)
Line circumferentially array distribution, the surface of recess cambered surface (2-1-1), which is arrived, makes the distance of unrestrained cylinder (2-1) axis greater than making unrestrained cylinder
Do not have the place of recess cambered surface (2-1-1) on the inner wall of (2-1) to the distance for making unrestrained cylinder (2-1) axis；Be recessed cambered surface (2-
First end and second end 1-1) is to make the inner section circle of unrestrained cylinder (2-1) in the span for the inner section circle for making unrestrained cylinder (2-1)
1/6th；Unrestrained cylinder (2-1) outer wall is made in the first end connection of support portion (2-4), and the second end of support portion (2-4), which connects, to be held
Chamber side plays support and makes unrestrained cylinder (2-1)；It makes that unrestrained cylinder (2-1) is coaxial with cavity, makes the upper end unrestrained cylinder (2-1)
Level height of the level height lower than the big end of cavity；
In container (2): water-permeable passage (2-3), which is located at, to be made between the lower end and cavity bottom of unrestrained cylinder (2-1), in cavity
Water energy, which is enough entered by water-permeable passage (2-3), makes unrestrained cylinder (2-1)；
In container (2): air inlet pipe (2-2) is coaxial with unrestrained cylinder (2-1) is made, and air inlet pipe (2-2) passes through cavity bottom by outside
Portion interface, which enters, makes in unrestrained cylinder (2-1)；
In container (2): container foot (2-5) is located at lower vessel portion, plays a supportive role, and facilitates placement；
Lid (3) includes ontology, motor support portion (3-1), motor axis hole (3-2), escape pipe (3-3), motor shaft waterproof
Column (3-4)；
In lid (3): ontology be it is discoid, motor support portion (3-1) be cylindrical shape, be used to support motor；
In lid (3): motor support portion (3-1) is located above ontology, and motor support portion (3-1) is coaxial with ontology, motor
The overall diameter of support portion (3-1) is less than the overall diameter of ontology；
In lid (3): the anti-water column of motor shaft (3-4) is located at below ontology, and the anti-water column of motor shaft (3-4) is coaxial with ontology；
In lid (3): the interior diameter of motor axis hole (3-2) is less than the overall diameter of motor support portion (3-1)；Motor axis hole
(3-2) is coaxial with motor shaft anti-water column (3-4), and motor axis hole (3-2) first end is communicated with motor support portion (3-1), motor shaft
Hole (3-2) second end is located on the lower surface the anti-water column of motor shaft (3-4)；
In lid (3): escape pipe (3-3) is located above ontology, and the lumen of escape pipe (3-3) penetrates ontology；Escape pipe (3-
3) lumen open is located at the lower surface of ontology；
Bearing (4) is used to connect the interconnecting piece (1-1) and lid of rotor (1)；Motor (5) is mounted on the motor of lid (3)
On support portion (3-1), the interconnecting piece of rotor (1) passes through lid (3) and is connected with motor axis hole (3-2), and lid (3) is mounted on container
(2) upper end；The air inlet pipe (2-2) of container (2) protrudes into the cylindrical cavity (1-6) of the back-off container (1-2) of rotor (1)；
Rotor (1) and back-off container (1-2) to make unrestrained cylinder (2-1) coaxial；
The driving blade group (1-5) of rotor (1) makes unrestrained cylinder (2-1) inside, rotor (1) positioned at back-off container (1-2)
Driving blade group (1-5) lower blade (1-5-3-2) outer rim camber line and container (2) make unrestrained cylinder (2-1) do not have it is recessed
The distance for falling into the place of cambered surface (2-1-1) is less than the thickness of lower blade (1-5-3-2)；Motor (5) is for driving rotor (1) at the uniform velocity
Rotation.
Part is full of cold water, the cold water of machinery rotating type air bubble generator (R1) in machinery rotating type air bubble generator (R1)
The height of the water surface is higher than the top for making unrestrained cylinder (2-1)；
It heats container (R2) inner part and is full of hot water；
There is blender (JBQ) inside mixing vessel (R3), blender (JBQ) drives by motor；
There is the first seperating vale (FLF1) in mixing vessel (R3)；
The first seperating vale (FLF1) of mixing vessel (R3) is located at the bottom of mixing vessel (R3), for discharging mixing vessel
(R3) water of bottom；
The second seperating vale (FLF2) of mixing vessel (R3) is that a kind of aqueous vapor seperating vale (FLF) only discharges water and do not discharge gas
Body；
Aqueous vapor seperating vale (FLF) includes outlet pipe (FLF-CSG), conical cavity (FLF-ZXQ), heavy ball (FLF-ZQ), floating ball
(FLF-FQ)；
In the second seperating vale (FLF2) of mixing vessel (R3): conical cavity (FLF-ZXQ's) is pacified in a manner of axis vertical
It puts, the big end of conical cavity (FLF-ZXQ) is upper, and the small end of conical cavity (FLF-ZXQ) is under；
In the second seperating vale (FLF2) of mixing vessel (R3): the density of heavy ball (FLF-ZQ) is greater than in application environment
Water；
In the second seperating vale (FLF2) of mixing vessel (R3): the density of floating ball (FLF-FQ) is less than in application environment
Water；
In the second seperating vale (FLF2) of mixing vessel (R3): the lower end of conical cavity (FLF-ZXQ) and outlet pipe (FLF-
CSG highest point) is connected；
In the second seperating vale (FLF2) of mixing vessel (R3): the diameter of heavy ball (FLF-ZQ) is less than conical cavity (FLF-
ZXQ big end), the diameter of heavy ball (FLF-ZQ) are greater than the small end of conical cavity (FLF-ZXQ)；
In the second seperating vale (FLF2) of mixing vessel (R3): heavy ball (FLF-ZQ) device is in conical cavity (FLF-ZXQ)；
In the second seperating vale (FLF2) of mixing vessel (R3): floating ball (FLF-FQ) is connected by flexible cord with heavy ball (FLF-ZQ), and water is worked as
Heavy ball (FLF-ZQ) is by floating ball (FLF-FQ) pull-up when the water of cavity where gas seperating vale (FLF) floats floating ball (FLF-FQ),
The lower end of conical cavity (FLF-ZXQ) is decontroled, and water passes sequentially through under the upper end of conical cavity (FLF-ZXQ), conical cavity (FLF-ZXQ)
End, outlet pipe (FLF-CSG) discharge, when water surface elevation reduces heavy ball (FLF-ZQ) because gravity falls in conical cavity (FLF-ZXQ)
Lower end, the lower end closed of conical cavity (FLF-ZXQ) is not then exhausted from water, since floating ball (FLF-FQ) passes through flexible cord and heavy ball
(FLF-ZQ) be connected thus when the water surface drop to heavy ball height ledger line it is long when conical cavity (FLF-ZXQ) lower end closed, so gas
Body can not be discharged；
The upper end of the conical cavity (FLF-ZXQ) of the second seperating vale (FLF2) of mixing vessel (R3) and cavity of resorption (LNQ-XQ) phase
Logical, the lower end of the conical cavity (FLF-ZXQ) of the second seperating vale (FLF2) is higher than the bottom of cavity of resorption (LNQ-XQ), the second seperating vale
(FLF2) minimum point of the outlet of outlet pipe (FLF-CSG) is higher than the bottom of cavity of resorption (LNQ-XQ)；
Refrigerating and heating device (3) has heating end and refrigeration end, the refrigeration end and machinery rotating type gas of refrigerating and heating device (3)
Bubble generator (R1) is connected for cooling down the cold water in machinery rotating type air bubble generator (R1), the heating of refrigerating and heating device (3)
End is connected with heating container (R2) for the hot water in heating container (R2)；
The top of machinery rotating type air bubble generator (R1) passes through the top of the first instlated tubular (GRG1) and mixing vessel (R3)
Portion communicates, and has the first check valve (DXF1) on the pipeline of the first instlated tubular (GRG1), the gas of mixing vessel (R3) can not be inverse
It flow to machinery rotating type air bubble generator (R1)；
The side wall for heating the left side water surface of container (R2) or more and the wall on the right side of mixing vessel (R3) are heat-insulated by second
Pipe (GRG2) communicates；
The outlet pipe for heating first seperating vale (FLF1) of container (R2) passes through third instlated tubular (GRG3) and heating container
(R2) it is communicated below the water surface；
Gas condenser, including epicoele (LNQ-SQ), cavity of resorption (LNQ-XQ), air inlet pipe (LNQ-JG), exhaust pipe (LNQ-
PQG), heat exchanger, balance tracheae (LNQ-QG2), the second seperating vale (FLF2), drainpipe (LNQ-PSG), exhaust pump (B2)；
In gas condenser: epicoele (LNQ-SQ) is full of cooling water for cooling down；
In gas condenser: the cavity of cavity of resorption (LNQ-XQ) is not filled with water, and there are the gas compartment, the gas compartment passes through flat
Weighing apparatus tracheae (LNQ-QG2) is communicated with atmosphere, and the height of the aperture position of balance tracheae (LNQ-QG2) in an atmosphere is higher than epicoele
(LNQ-SQ) highest point of institute's water flowing；
The second seperating vale (FLF2) of gas condenser is that a kind of aqueous vapor seperating vale (FLF) only discharges water and do not discharge gas；
Aqueous vapor seperating vale (FLF) includes outlet pipe (FLF-CSG), conical cavity (FLF-ZXQ), heavy ball (FLF-ZQ), floating ball
(FLF-FQ)；
In the second seperating vale (FLF2) of gas condenser: conical cavity (FLF-ZXQ's) is placed in a manner of axis vertical,
The big end of conical cavity (FLF-ZXQ) is upper, and the small end of conical cavity (FLF-ZXQ) is under；
In the second seperating vale (FLF2) of gas condenser: the density of heavy ball (FLF-ZQ) is greater than the water in application environment；
In the second seperating vale (FLF2) of gas condenser: the density of floating ball (FLF-FQ) is less than the water in application environment；
In the second seperating vale (FLF2) of gas condenser: the lower end of conical cavity (FLF-ZXQ) and outlet pipe (FLF-CSG)
Highest point be connected；
In the second seperating vale (FLF2) of gas condenser: the diameter of heavy ball (FLF-ZQ) is less than conical cavity (FLF-ZXQ)
Big end, the diameter of heavy ball (FLF-ZQ) is greater than the small end of conical cavity (FLF-ZXQ)；
In the second seperating vale (FLF2) of gas condenser: heavy ball (FLF-ZQ) device is in conical cavity (FLF-ZXQ)；
In the second seperating vale (FLF2) of gas condenser: floating ball (FLF-FQ) passes through flexible cord and heavy ball (FLF-ZQ) phase
Even, heavy ball (FLF-ZQ) is by floating ball (FLF- when the water of cavity floats floating ball (FLF-FQ) where aqueous vapor seperating vale (FLF)
FQ the lower end of) pull-up, conical cavity (FLF-ZXQ) is decontroled, and water passes sequentially through the upper end of conical cavity (FLF-ZXQ), conical cavity (FLF-
ZXQ lower end), outlet pipe (FLF-CSG) discharge, when water surface elevation reduces heavy ball (FLF-ZQ) because gravity falls in conical cavity
(FLF-ZXQ) lower end, the lower end closed of conical cavity (FLF-ZXQ), is not then exhausted from water, since floating ball (FLF-FQ) passes through flexible cord
Be connected with heavy ball (FLF-ZQ) thus when the water surface drop to heavy ball height ledger line it is long when conical cavity (FLF-ZXQ) lower end closed,
So gas can not be discharged；
The upper end of the conical cavity (FLF-ZXQ) of the second seperating vale (FLF2) of gas condenser and cavity of resorption (LNQ-XQ) phase
Logical, the lower end of the conical cavity (FLF-ZXQ) of the second seperating vale (FLF2) is higher than the bottom of cavity of resorption (LNQ-XQ), the second seperating vale
(FLF2) minimum point of the outlet of outlet pipe (FLF-CSG) is higher than the bottom of cavity of resorption (LNQ-XQ)；
The heat exchanger of gas condenser is made of multiple heat-exchange tubes (LNQ-HG)；
The heat-exchange tube (LNQ-HG) of gas condenser includes the first pipe (LNQ-HG-1), the second pipe (LNQ-HG-2), the
Three pipes (LNQ-HG-3), the 4th pipe (LNQ-HG-4), the 5th pipe (LNQ-HG-5), the 6th pipe (LNQ-HG-6), the 7th pipe (LNQ-
HG-7)；
In the heat-exchange tube (LNQ-HG) of gas condenser: the first pipe (LNQ-HG-1) is put in a manner of axis horizontal；
In the heat-exchange tube (LNQ-HG) of gas condenser: the second pipe (LNQ-HG-1) is put in a manner of axis vertical；
In the heat-exchange tube (LNQ-HG) of gas condenser: third pipe (LNQ-HG-3) is put in a manner of axis vertical；
In the heat-exchange tube (LNQ-HG) of gas condenser: the 4th pipe (LNQ-HG-4) is put in a manner of axis horizontal；
In the heat-exchange tube (LNQ-HG) of gas condenser: the 5th pipe (LNQ-HG-5) is put in a manner of axis vertical；
In the heat-exchange tube (LNQ-HG) of gas condenser: the 6th pipe (LNQ-HG-6) is put in a manner of axis vertical；
In the heat-exchange tube (LNQ-HG) of gas condenser: the 7th pipe (LNQ-HG-7) is put in a manner of axis horizontal；
In the heat-exchange tube (LNQ-HG) of gas condenser: the lower end of the second pipe (LNQ-HG-1) has opening to outside；
In the heat-exchange tube (LNQ-HG) of gas condenser: the lower end of the 6th pipe (LNQ-HG-6) has opening to outside；
In the heat-exchange tube (LNQ-HG) of gas condenser: the left end of the first pipe (LNQ-HG-1), third pipe (LNQ-HG-
3) upper end of lower end, the second pipe (LNQ-HG-2), three connect and communicate；
In the heat-exchange tube (LNQ-HG) of gas condenser: the right end of the 7th pipe (LNQ-HG-7), the 5th pipe (LNQ-HG-
5) upper end of lower end, the 6th pipe (LNQ-HG-6), three connect and communicate；
In the heat-exchange tube (LNQ-HG) of gas condenser: the upper end of third pipe (LNQ-HG-3) and the 4th pipe (LNQ-HG-
4) right end connects and communicates；
In the heat-exchange tube (LNQ-HG) of gas condenser: the upper end of the 5th pipe (LNQ-HG-5) and the 4th pipe (LNQ-HG-
4) left end connects and communicates；
The combined method of the heat-exchange tube (LNQ-HG) of gas condenser is, by two adjacent heat-exchange tubes (LNQ-HG)
Be named as left heat-exchange tube, right heat-exchange tube, then have left heat-exchange tube the first pipe (LNQ-HG-1) and right heat-exchange tube the
Seven pipes (LNQ-HG-7) connect and communicate；
In gas condenser: the lower end of the second pipe (LNQ-HG-1) of all heat-exchange tubes (LNQ-HG) of heat exchanger
The horizontal position of the opening of the lower end of opening and the 6th pipe (LNQ-HG-6) is lower than the conical cavity (FLF- of the second seperating vale (FLF2)
ZXQ) upper end；
In gas condenser: the lower end of the second pipe (LNQ-HG-1) of all heat-exchange tubes (LNQ-HG) of heat exchanger
The lower end of opening and the 6th pipe (LNQ-HG-6) is in cavity of resorption (LNQ-XQ)；
In gas condenser: the lower end of the second pipe (LNQ-HG-1) of all heat-exchange tubes (LNQ-HG) of heat exchanger
Opening and the 6th pipe (LNQ-HG-6)
In gas condenser: the air intake of exhaust pump (B2) and the 7th pipe of leftmost heat-exchange tube (LNQ-HG)
(LNQ-HG-7) it communicates, the gas outlet of exhaust pump (B2) is communicated with the air intake of drainpipe (LNQ-PSG), air inlet pipe (LNQ-JG)
It is communicated with the first pipe (LNQ-HG-1) of the heat-exchange tube (LNQ-HG) of rightmost, gas passes through cooling, gas after heat exchanger
Included in water droplet be condensed into droplet, droplet is fallen into cavity of resorption (LNQ-XQ), and cavity of resorption (LNQ-XQ) interior water reaches certain water
Behind position, a part is discharged by the second seperating vale (FLF2) and retains a part, reaches and removes water constituent contained in gas；
Mixing vessel (R3) is communicated with the air inlet pipe (LNQ-JG) of gas condenser；
The epicoele (LNQ-SQ) of gas condenser passes through the first condensation exchange water pipe (SG1), the second condensation exchange water pipe
(SG2) it is communicated with machinery rotating type air bubble generator (R1), there is circulating pump (SG2) in the second condensation exchange water pipe (SG2)
Recycle cooling water and machinery rotating type air bubble generator (R1) inner cold water in the epicoele (LNQ-SQ) of gas condenser；
The exhaust pump (B2) of gas condenser starts, since the gas of air inlet pipe (JQG) after suction function enters mechanical rotation
Rotatable air bubble generator (R1) generates bubble, bubble and Cold Water Exposure cooling, and the portion gas dust in gas falls in mechanical rotation
In the cold water of rotatable air bubble generator (R1), after bubble eruption, passes through the first instlated tubular (GRG1) through overcooled gas, enter
Mixing vessel (R3)；Since the hot steam of suction function heating container (R2) enters mixing vessel (R3)；Due to blender (JBQ)
Stirring, cooled gas is sufficiently mixed with hot steam, the lower structure of the temperature of the solid dust contained in cooled gas
At raindrop core, hot steam contact raindrop core when temperature decreasing concentration be attached on raindrop core, and due to the effect of gas condenser so that
Hot steam cohesion, forms bigger raindrop, and raindrop fall into gas condenser in the heat-exchange tube (LNQ-HG) of gas condenser
Cavity of resorption carry solid dust return to heating container (R2) in；First condensation exchange water pipe (SG1) is produced in machinery rotating type bubble
The horizontal position of the opening of raw device (R1) is lower than the top for making unrestrained cylinder (2-1) of machinery rotating type air bubble generator (R1), the
One condensation exchange water pipe (SG1) is higher than machinery rotating type gas in the horizontal position of the opening of machinery rotating type air bubble generator (R1)
Steep the bottom end for making unrestrained cylinder (2-1) of generator (R1)；Second condensation exchange water pipe (SG2) is in machinery rotating type air bubble generator
(R1) horizontal position of opening is lower than the top for making unrestrained cylinder (2-1) of machinery rotating type air bubble generator (R1), and second is cold
Solidifying exchange water pipe (SG2) produces in the horizontal position of the opening of machinery rotating type air bubble generator (R1) higher than machinery rotating type bubble
The bottom end for making unrestrained cylinder (2-1) of raw device (R1).
The improvement of embodiment 4, scheme based on embodiment 2 or 3: further: the bottom of heating container (R2) has row
Dirty valve is used for blowdown.
The improvement of embodiment 5, scheme based on embodiment 2 or 3: further: Refrigerating container (R1) is canister.
The improvement of embodiment 6, scheme based on embodiment 2 or 3: further: heating container (R2) is canister.
The improvement of embodiment 7, scheme based on embodiment 2 or 3: further: mixing vessel (R3) is canister.
The improvement of embodiment 8, scheme based on embodiment 2 or 3: further: the main member of refrigerating and heating device (ZLQ-3)
Part is that semiconductor chilling plate is also Peltier.
The improvement of embodiment 9, scheme based on embodiment 2 or 3: further: the main member of refrigerating and heating device (ZLQ-3)
Part is vortex cooler, is also vortex tube or cool-air device or vortex cooler.
When the rotor rotation of the rotary air bubble generator of tool (R1), driving blade group (1-5) rotates blade (1-5-3-1)
Water flow is formed between lower blade (1-5-3-2), the venthole (1-4) of rotor out (1) is caused to impact, due to container (2)
Making the unrestrained cylinder surface (2-1) has recess cambered surface (2-1-1), leads to the pressure in the liquid driven channel of driving blade group (1-5)
Cyclically-varying, and then cyclic fluctuation is presented in the water flow for causing driving blade group (1-5) to drive, stomata nearby is not allowed to be also easy to produce
Air band, conducive to improving efficiency；Due to not needing rotor speed change, so the bulk life time of device can be improved in electrical machinery life；By
Impact is generated to bubble in no solid structure, advantageously reduces local temperature；Due to there is no solid structure to generate punching to bubble
It hits, bubble eruption impingment corrosion solid structure is not present, so the service life of the rotary air bubble generator of tool (R1) is higher.Tool rotation
Service life of formula air bubble generator (R1) is high, advantageously reduces that local temperature, low energy consumption, structure is simple.
The rotary air bubble generator of tool (R1) creates new approaches.
Claims (8)
1. aqueous vapor seperating vale (FLF), it is characterised in that: include outlet pipe (FLF-CSG), conical cavity (FLF-ZXQ), heavy ball
(FLF-ZQ), floating ball (FLF-FQ)；
In aqueous vapor seperating vale (FLF): conical cavity (FLF-ZXQ's) is placed in a manner of axis vertical, conical cavity (FLF-ZXQ)
Big end is upper, and the small end of conical cavity (FLF-ZXQ) is under；
In aqueous vapor seperating vale (FLF): the density of heavy ball (FLF-ZQ) is greater than the water in application environment；
In aqueous vapor seperating vale (FLF): the density of floating ball (FLF-FQ) is less than the water in application environment；
In aqueous vapor seperating vale (FLF): the lower end of conical cavity (FLF-ZXQ) is connected with the highest point of outlet pipe (FLF-CSG)；
In aqueous vapor seperating vale (FLF): the diameter of heavy ball (FLF-ZQ) is less than the big end of conical cavity (FLF-ZXQ), heavy ball (FLF-
ZQ diameter) is greater than the small end of conical cavity (FLF-ZXQ)；
In aqueous vapor seperating vale (FLF): heavy ball (FLF-ZQ) device is in conical cavity (FLF-ZXQ)；
In aqueous vapor seperating vale (FLF): floating ball (FLF-FQ) is connected by flexible cord with heavy ball (FLF-ZQ), when aqueous vapor seperating vale
(FLF) heavy ball (FLF-ZQ) is by floating ball (FLF-FQ) pull-up, conical cavity when the water of cavity floats floating ball (FLF-FQ) where
(FLF-ZXQ) lower end is decontroled, water pass sequentially through the upper end of conical cavity (FLF-ZXQ), conical cavity (FLF-ZXQ) lower end, go out
Water pipe (FLF-CSG) discharge, when water surface elevation reduces heavy ball (FLF-ZQ) because gravity is fallen under conical cavity (FLF-ZXQ)
End, the lower end closed of conical cavity (FLF-ZXQ) are not then exhausted from water, since floating ball (FLF-FQ) passes through flexible cord and heavy ball (FLF-
ZQ) be connected thus when the water surface drop to heavy ball height ledger line it is long when conical cavity (FLF-ZXQ) lower end closed, so gas can not
It is discharged.
2. aqueous vapor seperating vale (FLF) as described in claim 1, it is characterised in that: the lumen of outlet pipe (FLF-CSG) is circle
Shape.
3. aqueous vapor seperating vale (FLF) as described in claim 1, it is characterised in that: the position floating ball (FLF-FQ) solid foam ball.
4. aqueous vapor seperating vale (FLF) as described in claim 1, it is characterised in that: floating ball (FLF-FQ) is hollow plastic ball.
5. aqueous vapor seperating vale (FLF) as described in claim 1, it is characterised in that: the material of heavy ball (FLF-ZQ) is rubber.
6. aqueous vapor seperating vale (FLF) as described in claim 1, it is characterised in that: the material of heavy ball (FLF-ZQ) is latex.
7. aqueous vapor seperating vale (FLF) as described in claim 1, it is characterised in that: by connection floating ball (FLF-FQ) and heavy ball
(FLF-ZQ) flexible cord is substituted for chain made of hard material.
8. environment-friendly type air dust pelletizing system, it is characterised in that: have aqueous vapor seperating vale (FLF) described in claim 1.
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|---|---|---|---|
| CN201910071984.5A CN109603363B (en) | 2019-01-25 | 2019-01-25 | Environment-friendly air dust removal system |
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| CN112870901A (en) * | 2021-01-28 | 2021-06-01 | 福建德尔科技有限公司 | Novel aqueous vapor autosegregation device |
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| Publication number | Publication date |
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| CN109603363B (en) | 2021-06-15 |
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