CN109966925A - It is a kind of to dodge the clear membrane process of quick-fried method recoil and its device - Google Patents
It is a kind of to dodge the clear membrane process of quick-fried method recoil and its device Download PDFInfo
- Publication number
- CN109966925A CN109966925A CN201910173793.XA CN201910173793A CN109966925A CN 109966925 A CN109966925 A CN 109966925A CN 201910173793 A CN201910173793 A CN 201910173793A CN 109966925 A CN109966925 A CN 109966925A
- Authority
- CN
- China
- Prior art keywords
- gas
- dirt
- membrane
- recoil
- filter
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000012528 membrane Substances 0.000 title claims abstract description 74
- 238000000034 method Methods 0.000 title claims abstract description 63
- 238000001914 filtration Methods 0.000 claims abstract description 61
- 239000007789 gas Substances 0.000 claims description 58
- 239000002699 waste material Substances 0.000 claims description 45
- 230000004308 accommodation Effects 0.000 claims description 41
- 239000010865 sewage Substances 0.000 claims description 19
- 239000012530 fluid Substances 0.000 claims description 17
- 238000003860 storage Methods 0.000 claims description 13
- 238000003466 welding Methods 0.000 claims description 12
- 230000008676 import Effects 0.000 claims description 5
- 230000001681 protective effect Effects 0.000 claims description 5
- 238000011010 flushing procedure Methods 0.000 claims description 4
- 238000009434 installation Methods 0.000 claims description 4
- 230000002265 prevention Effects 0.000 claims description 4
- 230000000694 effects Effects 0.000 claims description 3
- 239000011261 inert gas Substances 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 3
- 238000003825 pressing Methods 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 3
- 238000009628 steelmaking Methods 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 230000000903 blocking effect Effects 0.000 claims description 2
- 230000005484 gravity Effects 0.000 claims description 2
- 230000002093 peripheral effect Effects 0.000 claims description 2
- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
- 239000010935 stainless steel Substances 0.000 claims description 2
- 241000233855 Orchidaceae Species 0.000 claims 2
- 239000003570 air Substances 0.000 claims 1
- 239000002737 fuel gas Substances 0.000 claims 1
- 239000003921 oil Substances 0.000 claims 1
- 238000004140 cleaning Methods 0.000 abstract description 8
- 239000000428 dust Substances 0.000 abstract description 7
- 238000011109 contamination Methods 0.000 abstract description 2
- 210000003205 muscle Anatomy 0.000 description 4
- 239000000567 combustion gas Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000001186 cumulative effect Effects 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/42—Auxiliary equipment or operation thereof
- B01D46/44—Auxiliary equipment or operation thereof controlling filtration
- B01D46/446—Auxiliary equipment or operation thereof controlling filtration by pressure measuring
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/54—Particle separators, e.g. dust precipitators, using ultra-fine filter sheets or diaphragms
- B01D46/543—Particle separators, e.g. dust precipitators, using ultra-fine filter sheets or diaphragms using membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/66—Regeneration of the filtering material or filter elements inside the filter
- B01D46/70—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter
- B01D46/71—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter with pressurised gas, e.g. pulsed air
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/02—Membrane cleaning or sterilisation ; Membrane regeneration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/04—Backflushing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/18—Use of gases
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/03—Pressure
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The clear membrane process of quick-fried method recoil and its device are dodged the invention discloses a kind of, it recoils clear membrane process and to realize device set by this method including dodging quick-fried method, compressed gas can be passed through by dodging the clear membrane process of quick-fried method recoil and its device, quick-fried remove contamination instantaneously is dodged to the dust and dirt that are attached to membrane surface, reach the thorough cleaning to membrane, membrane is made to restore original state.It is recoiled the dirt that clear film ejected to receive by filtration fraction, the anti-dirt containing section that cleans is divided into Open architecture and closed structure.
Description
Technical field
The present invention relates to fluid purification technical fields, especially a kind of to dodge the clear membrane process of quick-fried method recoil and its device.
Background technique
In cleaner, bag filter is a kind of equipment being widely adopted.Since the frame mode of filter bag determines
This bag-type dust equipment can only and its low pressure under run, and running resistance rapidly increases.Running resistance determines
Dust pelletizing system energy consumption, filter efficiency and cleaning cycle.Once running resistance is excessively high, it will cause equipment work efficiency drops
It is low, cause dust collection capacity insufficient, also will affect the load of whole system.It is clear when carrying out very brief injection to filter bag using compressed air
When grey, deashing effect is weaker, and which define the sound development of this kind of equipment.Especially removed in the gentle box pulse of pulse
In dirt device, dust is attached to the outer surface of cloth bag.When dusty gas passes through deduster, dust is trapped in the appearance of filter bag
At this moment face carries out deashing, form gas tank and contend with the pressure inside filter bag, and recoil deashing is forced to cannot achieve.
Based on this, the present invention provides a kind of recoil clear membrane process and its devices of quick-fried method that dodge to be asked with solving above-mentioned technology
Topic.
Summary of the invention
The object of the invention is to solve problems of the prior art, provide it is a kind of dodge quick-fried method recoil clear membrane process and
Its device, the quick-fried method of the sudden strain of a muscle recoil clear membrane process and its device can by compressed gas, to the dust for being attached to membrane surface and
Dirt instantaneously dodged it is quick-fried remove contamination, reach the thorough cleaning to membrane, make membrane restore original state.
To achieve the above object, the clear membrane process of quick-fried method recoil and its device are dodged the invention proposes a kind of, membrane is carried out
Instantaneously dodge quick-fried cleaning.It due to dodging the quick-fried method clear membrane process that recoils is realized by device, dodges quick-fried method and recoil clear film device
Including filtration fraction and anti-cleaning dirt containing section composition.
The present invention adopts the following technical scheme that realization: device filtration fraction is the filtering appearance that can bear certain pressure
Device filters device filter membrane part in container, and filter membrane part is fixed in the device aperture of orifice plate, and orifice plate is placed in filtering vessel flange
Top is pressed with upper cover, and import is arranged an entirety is synthesized, in the side of filtering lower vessel portion in blending bolt,
Top is provided with outlet, and sewage draining exit is arranged in bottom.It is recoiled the dirt that clear film ejected to receive by filtration fraction, anti-cleaning is dirty
Object containing section uses dirt receiving container equally to receive and store dirt.Device dirt containing section is divided into Open architecture
And closed structure, Open architecture is the upper unit filtering membrane in waste rexeptacle, in the side of waste rexeptacle lower part
Import is set, sewage draining exit is set in waste rexeptacle bottom, is then communicated with atmosphere at the top of waste rexeptacle;Dirt containing section it is closed
Formula structure is cylinder body, piston structure, i.e., dress sets the piston that can be floated up and down in outer housing.When the surface of filtering portions membrane
It is covered by dirt, can make to increase by the Fluid pressure of membrane, when reaching set pressure, stored by gas tank
Gas can be inflated filtering container, and the gas filtered in container exists in a manner of pressure, when reaching set pressure
When, the sewage draining exit for filtering container bottom is instantaneously opened, and the gas moment that filtering container contents are stayed goes out sewage draining exit, is filtered in container
Instantaneous loss of pressure, the gas that space is stored in membrane while decompression are gone out inside-out by the filter membrane of membrane, make membrane
The dirt that outer surface is detained is carried out several times, by gas clean-up until membrane restores as before repeatedly.
When the filtering or the clear film medium that recoils are fluids, when fluid media (medium) is gaseous state, included fluid media (medium) is can
Combustion gas body, inert gas, air, steam or other gases;When fluid media (medium) is liquid, included fluid media (medium) is water, oil
Or sewage.
The filtering case or the shell of open waste accommodation device and closed waste accommodation device be not using
Become rusty steel making.
The shell for filtering case or open waste accommodation device and closed waste accommodation device, using stainless steel
Manufacture.
The clear membrane process of the quick-fried method recoil of above-mentioned sudden strain of a muscle and its apparatus structure are simple, and use cost is low, takes up little area, and low energy consumption, behaviour
Facilitate.
The present invention is described in further detail with reference to the accompanying drawings and detailed description.
Detailed description of the invention
In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below
There is attached drawing needed in technical description to be briefly described.
Fig. 1 is that the present invention dodges the clear membrane process process schematic of quick-fried method recoil.
Fig. 2 is that the present invention dodges the quick-fried method clear film device of recoil and open dirt containing section structural schematic diagram.
Fig. 3 is that the present invention dodges the quick-fried method clear film device of recoil and closed dirt containing section structural schematic diagram.
Main appended drawing reference meaning is as follows in figure:
1- filter vessel housings, 2- filter membrane, porose disc among 3-, and 4- filters container upper flange, seals on 5- filtering container
Head flange, 6- filter medium inlet, the clear film gas feed of 7- recoil, the outlet of 8- filter medium, 9- sewage draining exit, 10K1Normally opened control
Valve, 10K2Normally opened control valve, 11- waste accommodation device shell, 12- refilter membrane, 13- waste accommodation device porose disc, 14-
Waste accommodation device upper flange, the open top cover of 15-, 16- recoil dirt store entrance, the open gas outlet 17-, 18- cleaning
Gas discharge outlet, 19- dirt sewage draining exit, 20B1Normally closed control valve, 20B2Normally closed control valve, 20B3Normally closed control valve, 21- are close
Enclosed waste accommodation device cylinder body, 22- piston, 23- top cover pressure ring, 24- cylinder body flange, 25- only rush ring, 26- recoil dirt
Import, 27- air entrapment dissipate mouth, the secondary outlet of 28- gas, the regular discharge outlet of 29- dirt, and 30- solenoid valve seals on 31-
Head, 32- lower head, 33- filter container lower flange, 34- lower head flange, 35- porose disc device aperture, 36- support rod, 37- blowout prevention
Protective cover, the closed waste accommodation device of 38-, 39- sealing ring.
Specific embodiment
As shown in Figure 1, the quick-fried method of sudden strain of a muscle of the invention recoils, clear membrane process process is that the dirt on 2 surface of membrane is filtered in filtering
Can be cumulative, cause filter pressure to increase, when reaching set constant-pressure, device is normally opened 1 side of filter vessel housings
Control valve 10K1With the normally opened control valve 10 on topK2It simultaneously closes off, and the solenoid valve 30 installed in the clear film gas feed 7 that recoils is beaten
It opens, compressed gas enters in filter vessel housings 1, and the pressure of gas entered in filtering container gradually rises, when reaching
When the clear membrane process pressure of set recoil (pressure is usually 0.25MPa), in filtering container bottom sewage draining exit 9 and with
Normally closed control valve 20 between its recoil dirt storage import 16 being connectedB1It opens, the defaulted band in filtering container is calmed the anger
Instantaneously towards discharging in the cavity in waste accommodation device shell 11, the compressed gas in filtering membrane 2 is perforated through body at once
Filter membrane part filter membrane, and the dirt for filtering membrane surface is carried, if method is repeated a number of times, to filter in membrane 2
Dirt is cleaned, and since compressed gas is when going out filtering membrane 2, is had and is dodged quick-fried effect, therefore it is clear referred to as to dodge quick-fried method recoil
Membrane process;The back flushing gas ejected in from filter is not directly discharged to atmosphere, by waste accommodation device filter membrane
Part 12 is discharged into atmosphere after filtering.
The quick-fried method of the sudden strain of a muscle of present invention described above recoils possessed by clear membrane process the utility model has the advantages that [one] cleans the dirt in membrane
Object;[two] noise generated when dodging quick-fried is eliminated;[three] pollutant being discharged is received, in favor of centralized processing.
First embodiment: referring to Fig. 2, dodging quick-fried method the present invention provides a kind of and recoiling the device of clear membrane process, comprising:
Filtration fraction and the clear film dirt containing section of recoil, the filtration fraction includes the filter membrane of filter vessel housings 1 and interior device
Part 2, for filtering 2 device of membrane among the aperture of intermediate porose disc 3, the intermediate porose disc 3 is placed on filter vessel housings 1
On the upper surface of the filtering container upper flange 4 that is welded, the upper surface of described intermediate porose disc 3 holds with the filtering welded on upper cover 31
Device upper cover flange 5 compresses, then secured closing with bolt, and in 31 middle position of upper cover welding filter medium outlet 8, leans on
The clear film gas feed 7 of side position welding recoil of nearly filter medium outlet 8, the filter medium outlet 8 is the same as normally opened control valve
10K2It is connected, the filter vessel housings 1 are welded with filter medium inlet 6, the upper normally opened control valve of installation close to the position of lower end
10K1, 1 lower end of filter vessel housings is welded with filtering container lower flange 33, connects with 32 or less cover flange 34 of lower head
It connects, when filter vessel housings 1 are especially huge, lower head 32 and filter vessel housings 1 are directly integrally welded, and under
Sewage draining exit 9 is welded with normally closed control valve 10 in 32 bottom middle position of end socketB1Connection, normally closed control valve 10B1The other end is the same as the dirt that recoils
Object is stored entrance 16 and is connected, and the recoil dirt storage entrance 16 is set to 11 lower section of waste accommodation device shell, the dirt
Device refilters membrane 12 in storage device shell 11, and 12 device of membrane that refilters is in the hole of waste accommodation device porose disc 13
In 35 in disk device aperture, described device porose disc 13 is placed on above waste accommodation device upper flange 14, in waste accommodation device hole
The pressing of the upper surface of disk 13 has open top cover 15, by the clean gas that filters again from open gas outlet 17 via cleaning
Gas discharge outlet 18 is discharged into atmosphere, also conduit connectable by gas to high altitude discharge, when waste accommodation device bottom accumulates
Object it is enough when, openable normally closed control valve 10B2The dirt stored can carry out at concentration from 19 outlet of dirt sewage draining exit
Reason.
Second embodiment: referring to Fig. 3, dodging quick-fried method the present invention provides a kind of and recoiling the device of clear membrane process, comprising:
Filtration fraction and the clear film dirt containing section of recoil, the filtration fraction includes the filter membrane of filter vessel housings 1 and interior device
Part 2, for filtering 2 device of membrane among the aperture of intermediate porose disc 3, the intermediate porose disc 3 is placed on filter vessel housings 1
On the upper surface of the filtering container upper flange 4 that is welded, the upper surface of described intermediate porose disc 3 holds with the filtering welded on upper cover 31
Device upper cover flange 5 compresses, then secured closing with bolt, and in 31 middle position of upper cover welding filter medium outlet 8, leans on
The clear film gas feed 7 of side position welding recoil of nearly filter medium outlet 8, the filter medium outlet 8 is the same as normally opened control valve
10K2It is connected, the filter vessel housings 1 are welded with filter medium inlet 6, the upper normally opened control valve of installation close to the position of lower end
10K1, 1 lower end of filter vessel housings is welded with filtering container lower flange 33, connects with 32 or less cover flange 34 of lower head
It connects, when filter vessel housings 1 are especially huge, lower head 32 and filter vessel housings 11 are directly integrally welded, and
Sewage draining exit 9 is welded with normally closed control valve 20 in 32 bottom middle position of lower headB1Connection, normally closed control valve 20B1The other end is the same as recoil
Dirt is stored entrance 26 and is connected, and the recoil dirt storage entrance 26 is set to 21 lower section of waste accommodation device cylinder body, the dirt
The piston 22 that device can float up and down in object storage device cylinder body 21, the piston 22 is when there is back flushing gas to enter, piston 22
Can be headed on by gas and rise upward, make full gas in cylinder body 21, the air being detained outside above piston 22 via
Air entrapment dissipates mouth 27 and dissipates into atmosphere, to prevent piston 22 from going out from closed waste accommodation device 38, closed
38 top of waste accommodation device, which is welded with cylinder body flange 24 and presses on cylinder body flange 24, has top cover pressure ring 23 to prevent piston 22
Go out, fixed below top cover pressure ring 23 one prevent from touching wound only rush 25 device of ring, the peripheral device of the piston 22 has
Sealing ring 39 prevents 22 gas leakage of piston, opposite with recoil dirt storage entrance 26 below the closed waste accommodation device 38
It should be provided with the secondary outlet 28 of gas, inside welding blowout prevention protective cover 37 prevents the secondary outlet 28 of dirt blocking gas, described anti-
Spray protective cover 37 is welded with support rod 36 between the secondary outlet 28 of gas, can be to the entrapped air volume in waste accommodation device 38
It is discharged, when discharge opens normally closed control valve 20B3Entrapped air volume in waste accommodation device 38 is made in the weight gravity of piston
With lower discharge, when the dirt that 38 bottom of waste accommodation device accumulates is enough, openable normally closed control valve 20B2, stored
Dirt can be focused on from 29 outlet of dirt sewage draining exit, and also conduit connectable is by gas to high altitude discharge.
When the filtering or the clear film medium that recoils are fluids, when fluid media (medium) is gaseous state, included fluid media (medium) is can
Combustion gas body, inert gas, air, steam or other gases;When fluid media (medium) is liquid, included fluid media (medium) is water, oil
Or sewage.
The filtering case or the shell of open waste accommodation device and closed waste accommodation device be not using
Become rusty steel making.
Claims (6)
- Dodge quick-fried method 1. a kind of and recoil clear membrane process, which is characterized in that filtered in filtering membrane (2) surface dirt can it is more long-pending more It is more, cause filter pressure to increase, when reaching set constant-pressure, normally opened control valve of the device in filter vessel housings (1) side (10K1) and top normally opened control valve (10K2) solenoid valve (30) that simultaneously closes off, and installed on clear film gas feed (7) of recoiling It opens, compressed gas enters in filter vessel housings (1), and the pressure of the gas entered in filtering container gradually rises, when When the clear membrane process pressure of the recoil for reaching set, sewage draining exit (9) and coupled recoil in filtering container bottom Dirt stores the normally closed control valve (20 between import (16)B1) open, the defaulted compressed gas in filtering container is instantaneously towards dirt Release in cavity in object storage device shell (11), the compressed gas inner in filtering membrane (2) penetrate filter membrane part at once Filter membrane, and the dirt for filtering membrane surface is carried, if method is repeated a number of times, to filter the dirt on membrane (2) It is cleaned, since compressed gas is when going out filtering membrane (2), has and dodge quick-fried effect, therefore be referred to as and dodge the clear film of quick-fried method recoil Technique;The back flushing gas ejected in from filter is not directly discharged to atmosphere, filters membrane by waste accommodation device (12) it is discharged into atmosphere after filtering.
- It dodges quick-fried method 2. a kind of and recoils the device of clear membrane process characterized by comprising filtration fraction and the clear film dirt storage of recoil Part, the filtration fraction include the filtering membrane (2) of filter vessel housings (1) and interior device, filtering membrane (2) device Among the aperture of intermediate porose disc (3), the intermediate porose disc (3) is placed on the filtering welded on filter vessel housings (1) and holds The upper surface of device upper flange (4), filtering container upper cover method of the upper surface of the described intermediate porose disc (3) to be welded on upper cover (31) Orchid (5) compresses, then secured closing with bolt, and in upper cover (31) middle position welding filter medium outlet (8), close to mistake Filter medium exports the clear film gas feed (7) of side position welding recoil of (8), and the filter medium outlet (8) is the same as normally opened control Valve (10K2) be connected, the filter vessel housings (1) are welded with filter medium inlet (6) close to the position of lower end, and upper installation is normal Open control valve (10K1), filter vessel housings (1) lower end be welded with filtering container lower flange (33), same to lower head (32) with Lower head flange (34) connection, when filter vessel housings (1) are especially huge, lower head (32) and filter vessel housings (1) are It is directly integrally welded, and in lower head (32) bottom middle position welding sewage draining exit (9) with normally closed control valve (10B1) even It connects, normally closed control valve (10B1) with recoil dirt storage entrance (16) connection, recoil dirt storage entrance (16) sets the other end It is placed in below waste accommodation device shell (11), the interior device of the waste accommodation device shell (11) refilters membrane (12), institute It states and refilters membrane (12) device in the porose disc device aperture of waste accommodation device porose disc (13) in (35), described device porose disc (13) it is placed on waste accommodation device upper flange (14) above, has in the pressing of the upper surface of waste accommodation device porose disc (13) open Top cover (15) is discharged into from open gas outlet (17) via clean gas discharge outlet (18) by the clean gas filtered again In atmosphere, also conduit connectable by gas to high altitude discharge, it is openable when the object that waste accommodation device bottom accumulates is enough Normally closed control valve (10B2) dirt stored can be focused on from dirt sewage draining exit (19) outlet.
- It dodges quick-fried method 3. a kind of and recoils the device of clear membrane process characterized by comprising filtration fraction and the clear film dirt storage of recoil Part, the filtration fraction include the filtering membrane (2) of filter vessel housings (1) and interior device, filtering membrane (2) device Among the aperture of intermediate porose disc (3), the intermediate porose disc (3) is placed on the filtering welded on filter vessel housings (1) and holds The upper surface of device upper flange (4), filtering container upper cover method of the upper surface of the described intermediate porose disc (3) to be welded on upper cover (31) Orchid (5) compresses, then secured closing with bolt, and in upper cover (31) middle position welding filter medium outlet (8), close to mistake Filter medium exports the clear film gas feed (7) of side position welding recoil of (8), and the filter medium outlet (8) is the same as normally opened control Valve (10K2) be connected, the filter vessel housings (1) are welded with filter medium inlet (6) close to the position of lower end, and upper installation is normal Open control valve (10K1), filter vessel housings (1) lower end be welded with filtering container lower flange (33), same to lower head (32) with Lower head flange (34) connection, when filter vessel housings (1) are especially huge, lower head (32) and filter vessel housings (11) are It is directly integrally welded, and in lower head (32) bottom middle position welding sewage draining exit (9) with normally closed control valve (20B1) even It connects, normally closed control valve (20B1) with recoil dirt storage entrance (26) connection, recoil dirt storage entrance (26) sets the other end It is placed in below waste accommodation device cylinder body (21), the piston that the interior device of the waste accommodation device cylinder body (21) can float up and down (22), when there is back flushing gas to enter, piston (22) can be headed on by gas to rise the piston (22) upward, makes in cylinder body (21) By full gas, the air being detained outside above in piston (22) dissipates mouth (27) via air entrapment and dissipates to atmosphere In, to prevent piston (22) from going out from closed waste accommodation device (38), welded on closed waste accommodation device (38) top Being connected to cylinder body flange (24) and pressing above in cylinder body flange (24) has top cover pressure ring (23) to prevent piston (22) from going out, in top cover pressure Ring (23) fix below one prevent from touching wound only rush ring (25) device, the peripheral device of the piston (22) has sealing ring (39) it prevents piston (22) gas leakage, stores entrance (26) phase with recoil dirt below the closed waste accommodation device (38) It is correspondingly arranged on the secondary outlet (28) of gas, inside welding blowout prevention protective cover (37) prevents dirt from blocking the secondary outlet of gas (28), the blowout prevention protective cover (37) is welded with support rod (36) between the secondary outlet (28) of gas, can store and fill to dirt The entrapped air volume set in (38) is discharged, and when discharge opens normally closed control valve (20B3) delay in waste accommodation device (38) Gas is discharged under the weight gravity of piston, openable when the dirt that 38 bottom of waste accommodation device accumulates is enough Normally closed control valve (20B2), the dirt stored can be focused on, also conduit connectable from dirt sewage draining exit (29) outlet By gas to high altitude discharge.
- It a kind of dodge quick-fried method 4. as described in claim 1 and recoils clear membrane process, which is characterized in that the pressure for the clear film that recoils is usually 0.25MPa。
- It a kind of dodge quick-fried method 5. as described in claim 1 and recoils clear membrane process, which is characterized in that the clear film medium that filters or recoil is When fluid, when fluid media (medium) is gaseous state, included fluid media (medium) is fuel gas, inert gas, air, steam or other gas Body;When fluid media (medium) is liquid, included fluid media (medium) is water, oil or sewage.
- 6. a kind of as claimed in claim 2 or claim 3 dodge quick-fried method and recoil the device of clear membrane process, which is characterized in that the filtering appearance Device device or the shell of open waste accommodation device and closed waste accommodation device use stainless steel making.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910173793.XA CN109966925B (en) | 2019-03-02 | 2019-03-02 | Backflushing film cleaning process and device by flash explosion method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910173793.XA CN109966925B (en) | 2019-03-02 | 2019-03-02 | Backflushing film cleaning process and device by flash explosion method |
Publications (2)
Publication Number | Publication Date |
---|---|
CN109966925A true CN109966925A (en) | 2019-07-05 |
CN109966925B CN109966925B (en) | 2023-11-24 |
Family
ID=67078182
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201910173793.XA Active CN109966925B (en) | 2019-03-02 | 2019-03-02 | Backflushing film cleaning process and device by flash explosion method |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN109966925B (en) |
Citations (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63274405A (en) * | 1987-04-30 | 1988-11-11 | Toshiba Corp | Reverse washing treatment method of hollow fiber membrane filter apparatus |
DE4421639A1 (en) * | 1994-06-21 | 1996-01-04 | Microdyn Modulbau Gmbh & Co Kg | Method for applying gas at two sequential pressures to microporous membrane filter |
EP0900584A1 (en) * | 1997-08-09 | 1999-03-10 | Boll & Kirch Filterbau GmbH | Backwash filter |
JP2000320451A (en) * | 1999-05-11 | 2000-11-21 | Koshin Kogyo Kk | Pump |
CN1321540A (en) * | 2000-04-30 | 2001-11-14 | 中国石油化工集团公司 | Membrane back-washing equipment of cross-flow type membrane filtration system |
US20030042184A1 (en) * | 2001-08-31 | 2003-03-06 | Mcgowan David R. | Pressurized backflush system |
JP2003071254A (en) * | 2001-09-03 | 2003-03-11 | Sumitomo Heavy Ind Ltd | Backward washing method for separation membrane |
CN2843600Y (en) * | 2005-12-09 | 2006-12-06 | 江苏省宜兴非金属化工机械厂 | Membrane filter |
US20100058751A1 (en) * | 2008-09-10 | 2010-03-11 | Julio Chavez | Reciprocating pneumatic piston gravity engine |
CN103084069A (en) * | 2013-02-07 | 2013-05-08 | 深圳市诚德来实业有限公司 | Internal-pressure type ultrafiltration membrane flusher and flushing method |
CN103301743A (en) * | 2013-06-21 | 2013-09-18 | 江苏中金环保科技有限公司 | Flue gas integral dry waste removing system and flue gas waste removing and back washing method |
WO2014095302A1 (en) * | 2012-12-18 | 2014-06-26 | Grundfos Holding A/S | Method of cleaning a liquid fluid filter |
CN109304091A (en) * | 2017-07-29 | 2019-02-05 | 普安县夜郎水饮品开发有限责任公司 | A kind of saving type RO unit |
-
2019
- 2019-03-02 CN CN201910173793.XA patent/CN109966925B/en active Active
Patent Citations (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63274405A (en) * | 1987-04-30 | 1988-11-11 | Toshiba Corp | Reverse washing treatment method of hollow fiber membrane filter apparatus |
DE4421639A1 (en) * | 1994-06-21 | 1996-01-04 | Microdyn Modulbau Gmbh & Co Kg | Method for applying gas at two sequential pressures to microporous membrane filter |
EP0900584A1 (en) * | 1997-08-09 | 1999-03-10 | Boll & Kirch Filterbau GmbH | Backwash filter |
JP2000320451A (en) * | 1999-05-11 | 2000-11-21 | Koshin Kogyo Kk | Pump |
CN1321540A (en) * | 2000-04-30 | 2001-11-14 | 中国石油化工集团公司 | Membrane back-washing equipment of cross-flow type membrane filtration system |
US20030042184A1 (en) * | 2001-08-31 | 2003-03-06 | Mcgowan David R. | Pressurized backflush system |
JP2003071254A (en) * | 2001-09-03 | 2003-03-11 | Sumitomo Heavy Ind Ltd | Backward washing method for separation membrane |
CN2843600Y (en) * | 2005-12-09 | 2006-12-06 | 江苏省宜兴非金属化工机械厂 | Membrane filter |
US20100058751A1 (en) * | 2008-09-10 | 2010-03-11 | Julio Chavez | Reciprocating pneumatic piston gravity engine |
WO2014095302A1 (en) * | 2012-12-18 | 2014-06-26 | Grundfos Holding A/S | Method of cleaning a liquid fluid filter |
CN103084069A (en) * | 2013-02-07 | 2013-05-08 | 深圳市诚德来实业有限公司 | Internal-pressure type ultrafiltration membrane flusher and flushing method |
CN103301743A (en) * | 2013-06-21 | 2013-09-18 | 江苏中金环保科技有限公司 | Flue gas integral dry waste removing system and flue gas waste removing and back washing method |
CN109304091A (en) * | 2017-07-29 | 2019-02-05 | 普安县夜郎水饮品开发有限责任公司 | A kind of saving type RO unit |
Also Published As
Publication number | Publication date |
---|---|
CN109966925B (en) | 2023-11-24 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR100233891B1 (en) | Cyclone dust collector | |
CA2037799A1 (en) | Backwash method and apparatus | |
US4509960A (en) | Dust collector | |
CN102755773A (en) | Filter with squeezing filtering bags | |
JPH11510095A (en) | Hybrid filter system and process fluid filtration method | |
CN109966925A (en) | It is a kind of to dodge the clear membrane process of quick-fried method recoil and its device | |
CN201337842Y (en) | Novel efficient oil filter | |
CN212509574U (en) | Novel slag collecting butterfly valve | |
CN218485467U (en) | High-efficient pulse dust collecting equipment | |
CN2432999Y (en) | Upper installed purging type high flow filter | |
CN213953884U (en) | Filter equipment and contain this filter equipment's pump for pump | |
CN209612473U (en) | A kind of pulsed gas dust removal filter | |
CN112607951A (en) | Energy-saving filtering device | |
CN208396782U (en) | A kind of DPF mounting rack of DPF cleaning plant | |
CN222019046U (en) | Sewage filtering device | |
US3608282A (en) | Filtering systems | |
CN219072174U (en) | Filter material type process condensate recycling device | |
CN215756503U (en) | Filter with filter element convenient to replace | |
CN221905962U (en) | Filtering device | |
CN219481789U (en) | Anti-blocking filter for regeneration of waste lubricating oil | |
CN214066640U (en) | Pipeline on-line sampling valve | |
CN220745363U (en) | Automatic connector for laboratory waste liquid collecting barrel | |
CN206694573U (en) | A kind of chromatographic column Multifunctional pneumatic valve | |
CN214075175U (en) | Movable grid plate with one-way valve function and oil-water separator | |
CN212262606U (en) | Built-in storage partition mechanism for waste water storage tank |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |