CN204298172U - Valve external condensation system wastewater recycling system process equipment - Google Patents
Valve external condensation system wastewater recycling system process equipment Download PDFInfo
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- CN204298172U CN204298172U CN201420679811.4U CN201420679811U CN204298172U CN 204298172 U CN204298172 U CN 204298172U CN 201420679811 U CN201420679811 U CN 201420679811U CN 204298172 U CN204298172 U CN 204298172U
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- 238000009833 condensation Methods 0.000 title claims abstract description 17
- 230000005494 condensation Effects 0.000 title claims abstract description 17
- 230000026676 system process Effects 0.000 title claims abstract description 13
- 239000002351 wastewater Substances 0.000 title claims abstract description 12
- 238000004064 recycling Methods 0.000 title claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 70
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 22
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 21
- 238000001223 reverse osmosis Methods 0.000 claims description 16
- 239000000126 substance Substances 0.000 claims description 14
- 239000008213 purified water Substances 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 4
- 238000001764 infiltration Methods 0.000 abstract description 10
- 238000011001 backwashing Methods 0.000 abstract description 5
- 239000000203 mixture Substances 0.000 abstract description 3
- 241000196324 Embryophyta Species 0.000 description 14
- 239000000835 fiber Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 12
- 230000008569 process Effects 0.000 description 12
- 239000000463 material Substances 0.000 description 7
- 239000003814 drug Substances 0.000 description 6
- 230000009467 reduction Effects 0.000 description 6
- 230000008901 benefit Effects 0.000 description 5
- 238000005260 corrosion Methods 0.000 description 4
- 230000007797 corrosion Effects 0.000 description 4
- 238000012423 maintenance Methods 0.000 description 4
- 241000124033 Salix Species 0.000 description 3
- 238000006073 displacement reaction Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000012528 membrane Substances 0.000 description 3
- 229910000975 Carbon steel Inorganic materials 0.000 description 2
- 229910019142 PO4 Inorganic materials 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000010962 carbon steel Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 238000010612 desalination reaction Methods 0.000 description 2
- 229940079593 drug Drugs 0.000 description 2
- 239000003822 epoxy resin Substances 0.000 description 2
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 2
- 238000002386 leaching Methods 0.000 description 2
- 238000012806 monitoring device Methods 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 2
- 239000010452 phosphate Substances 0.000 description 2
- 229920000647 polyepoxide Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 230000004044 response Effects 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000006004 Quartz sand Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 1
- 239000003830 anthracite Substances 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 239000003899 bactericide agent Substances 0.000 description 1
- 238000009960 carding Methods 0.000 description 1
- POIUWJQBRNEFGX-XAMSXPGMSA-N cathelicidin Chemical compound C([C@@H](C(=O)N[C@@H](CCCNC(N)=N)C(=O)N[C@@H](CCCCN)C(=O)N[C@@H](CO)C(=O)N[C@@H](CCCCN)C(=O)N[C@@H](CCC(O)=O)C(=O)N[C@@H](CCCCN)C(=O)N[C@@H]([C@@H](C)CC)C(=O)NCC(=O)N[C@@H](CCCCN)C(=O)N[C@@H](CCC(O)=O)C(=O)N[C@@H](CC=1C=CC=CC=1)C(=O)N[C@@H](CCCCN)C(=O)N[C@@H](CCCNC(N)=N)C(=O)N[C@@H]([C@@H](C)CC)C(=O)N[C@@H](C(C)C)C(=O)N[C@@H](CCC(N)=O)C(=O)N[C@@H](CCCNC(N)=N)C(=O)N[C@@H]([C@@H](C)CC)C(=O)N[C@@H](CCCCN)C(=O)N[C@@H](CC(O)=O)C(=O)N[C@@H](CC=1C=CC=CC=1)C(=O)N[C@@H](CC(C)C)C(=O)N[C@@H](CCCNC(N)=N)C(=O)N[C@@H](CC(N)=O)C(=O)N[C@@H](CC(C)C)C(=O)N[C@@H](C(C)C)C(=O)N1[C@@H](CCC1)C(=O)N[C@@H](CCCNC(N)=N)C(=O)N[C@@H]([C@@H](C)O)C(=O)N[C@@H](CCC(O)=O)C(=O)N[C@@H](CO)C(O)=O)NC(=O)[C@H](CC=1C=CC=CC=1)NC(=O)[C@H](CC(O)=O)NC(=O)CNC(=O)[C@H](CC(C)C)NC(=O)[C@@H](N)CC(C)C)C1=CC=CC=C1 POIUWJQBRNEFGX-XAMSXPGMSA-N 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000003203 everyday effect Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000007781 pre-processing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- -1 silt Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Valve external condensation system wastewater recycling system process equipment, comprise the outer water-cooled draught engine of valve, the outer water-cooled draught engine of valve connects newly-built inlet well and water receiver, newly-built inlet well and water receiver connect raw water pump, raw water pump connects more medium filter, more medium filter connects active carbon filter, and the utility model is primarily of inlet well and tank, raw water pump, more medium filter, active carbon filter, backwashing pump, composition such as equipment such as pretreatment product water tank, cartridge filter, counter-infiltration system, system pipeline and valve, table meter etc.
Description
Technical field
The utility model relates to a kind of process equipment, specifically a kind of valve external condensation system wastewater recycling system process equipment.
Background technology
The few fibers willow catkins flying in the air that original non-woven material production process equipment produces in production process, the fiber landed and the more broken fiber produced in carding process descend slowly and lightly at Nei Ge position, workshop (comprising the surface of equipment), and non-woven material row yielding is generally no more than 95%.After fiber willow catkins flying in the air, the fiber that lands are cleared up by cleaner, fiber willow catkins flying in the air, the price of fiber of landing are 1/20 of the prices of raw and semifnished materials, and workshop condition is very dirty and messy.
Utility model content
The purpose of this utility model is to provide a kind of valve external condensation system wastewater recycling system process equipment, can solve the problem.
The utility model for achieving the above object, be achieved through the following technical solutions: a kind of valve external condensation system wastewater recycling system process equipment, comprise the outer water-cooled draught engine of valve, the outer water-cooled draught engine of valve connects newly-built inlet well and water receiver, newly-built inlet well and water receiver connect raw water pump, raw water pump connects more medium filter, more medium filter connects active carbon filter, active carbon filter connects cartridge filter, be connected with chemicals dosing plant after active carbon filter is connected with cartridge filter, cartridge filter connects water tank, water tank connects high-pressure pump, high-pressure pump connects reverse osmosis unit, reverse osmosis unit connects purified water storage groove, purified water storage groove connects equalizing reservoir.
In order to realize the purpose of this utility model further, can also by the following technical solutions: described three grades of screen-dividing machines comprise housing, housing is the tubulose shell of lower end end closure, fixed cap is installed on the top of housing, charging aperture is installed on the top of fixed cap, the fixed cap that passes of charging aperture enters enclosure interior, the middle part of fixed cap vertically arranges screw rod, the bottom of screw rod is through fixed cap, the inside bottom of housing installs fixed cover, the lower end of screw rod coordinates with fixed cover, the first filter is installed at the middle part of screw rod, first filter is positioned on the downside of fixed cap, the first through hole is offered at the middle part of the first filter, screw rod is through the first through hole, the first nut is installed at the middle part of screw rod, first nut is positioned on the downside of the first filter, the external diameter of the first nut is greater than the diameter of the first through hole, the second filter is installed at the middle part of screw rod, second filter is positioned on the downside of the first nut, the second through hole is offered in the middle part of second filter, screw rod is through the second through hole, the second nut is installed at the middle part of screw rod, second nut is positioned on the downside of the second filter, the external diameter of the second nut is greater than the diameter of the second through hole, the 3rd filter is installed at the middle part of screw rod, 3rd filter is positioned on the downside of the second nut, third through-hole is offered at the middle part of the 3rd filter, screw rod is through third through-hole, screw rod installs the 3rd nut, 3rd nut is positioned at the downside of the 3rd filter, the external diameter of the 3rd nut is greater than the diameter of third through-hole, the bottom of housing arranges discharging opening.
The left and right sides of the inside of described housing arranges slide rail respectively, and chute is all offered in the left and right sides of the first filter, the second filter and the 3rd filter, and chute coordinates with slide rail.
The upper end mounting knob of described screw rod.
The utility model has the advantage of: the utility model is primarily of inlet well and tank, raw water pump, more medium filter, active carbon filter, backwashing pump, composition such as equipment such as pretreatment product water tank, cartridge filter, counter-infiltration system, system pipeline and valve, table meter etc.Pretreatment is adopted to add reverse osmosis desalination treatment process, pretreatment and counter-infiltration system flow process as follows: is produced from water tank → cartridge filter → high-pressure pump → reverse osmosis membrane assembly → equalizing reservoir in former water (the mainly outer cool equipment draining of valve, need collect in a newly-built pond) → raw water pump → chemicals dosing plant → more medium filter → active carbon filter → pretreatment.When pretreatment system and counter-infiltration system normally run, former water has to pass through pretreatment system process, and after its process, effluent quality is qualified intakes afterwards as reverse osmosis unit.Water after the process of the utility model processing mode advantage does not destroy original water charging system, and directly can fill into equalizing reservoir, later maintenance amount is little.The utility model also has advantage compact, cheap for manufacturing cost and easy to use simple for structure.
Accompanying drawing explanation
Fig. 1 is front view structural representation of the present utility model; Fig. 2 is the structural representation of more medium filter 23.
Mark illustrates: the outer newly-built inlet well of water-cooled draught engine 21 of 1 handle 2 screw rod 3 housing 4 first nut 5 chute 6 slide rail 7 first filter 8 first through hole 10 second filter 11 second through hole 12 the 3rd filter 13 third through-hole 14 fixed cover 15 discharging opening 16 charging aperture 17 fixed cap 18 second nut 19 the 3rd nut 20 valve and water receiver 22 raw water pump 23 more medium filter 24 active carbon filter 25 chemicals dosing plant 26 cartridge filter 27 water tank 28 high-pressure pump 29 reverse osmosis unit 30 pure water 31 equalizing reservoir.
Detailed description of the invention
Valve external condensation system wastewater recycling system process equipment, as depicted in figs. 1 and 2, comprise the outer water-cooled draught engine 20 of valve, the outer water-cooled draught engine 20 of valve connects newly-built inlet well and water receiver 21, newly-built inlet well and water receiver 21 connect raw water pump 22, raw water pump 22 connects more medium filter 23, more medium filter 23 connects active carbon filter 24, active carbon filter 24 connects cartridge filter 26, be connected with chemicals dosing plant 25 after active carbon filter 24 is connected with cartridge filter 26, cartridge filter 26 connects water tank 27, water tank 27 connects high-pressure pump 28, high-pressure pump 28 connects reverse osmosis unit 29, reverse osmosis unit 29 connects purified water storage groove 30, purified water storage groove 30 connects equalizing reservoir 31.
Existing valve external condensation system adopts outer water-cooling pattern, needs to consume a large amount of industry waters, and industry water takes from Jiangzhou Running-water Company and highly dense Running-water Company.The other filter system of valve external condensation system equalizing reservoir has installed conductivity measurement, for detecting equalizing reservoir electrical conductivity of water.When equalizing reservoir electrical conductivity is higher than 1800us/cm, the draining valve of equalizing reservoir can start drain function automatically.When electrical conductivity is lower than 1600us/cm, the draining valve of equalizing reservoir can cut out drain function automatically.When valve external condensation system normally runs, cause the concentration rate of equalizing reservoir higher because outer cold water constantly evaporates, electrical conductivity constantly raises, generally at about 2500uS/cm, therefore draining valve almost all can start draining every day, then dilutes the water of equalizing reservoir by the mode of supplementing new water.Add up through on-the-spot operation maintenance personnel, the displacement of bipolar month is about about 3600 m3.The automatic filtering unit of valve external condensation system, sand filter and softening plant are provided with automatic back-flushing function in addition, and regularly carry out backwash, the displacement of bipolar month is about about 1500m3.COMPREHENSIVE CALCULATING, converting plant, northern Shandong valve external condensation system year displacement reaches 60,000 m3, and loss property more than 25 ten thousand yuan, serious waste water resource, causes property to waste.In order to economize on resources, protection of the environment, active response " State Council is about the suggestion carrying out most stringent water resources management system ", " kind little " produces, extremely urgent to the valve external condensation system water reuse of converting plant, northern Shandong.
The draining of all recoverables is reclaimed by the utility model, can realize about 20W unit Sewage treatment every year, greatly saves to run to rise this, improves economic benefit; Decrease water yield waste every year, further saving water resource, protects water resource environment, protects surrounding enviroment, have effectively achieved the object that company " kind little " produces, active response " State Council is about the suggestion carrying out most stringent water resources management system ".The utility model primarily of between newly-built water treatment facilities, newly-built inlet well and tank, raw water pump, more medium filter, active carbon filter, backwashing pump, pretreatment produce the equipment such as water tank, cartridge filter, counter-infiltration system, system pipeline and valve, table meter composition.Pretreatment is adopted to add reverse osmosis desalination treatment process, pretreatment and counter-infiltration system flow process as follows: is produced from water tank → cartridge filter → high-pressure pump → reverse osmosis membrane assembly → equalizing reservoir in former water (the mainly outer cool equipment draining of valve, need collect in a newly-built pond) → raw water pump → chemicals dosing plant → more medium filter → active carbon filter → pretreatment.When pretreatment system and counter-infiltration system normally run, former water has to pass through pretreatment system process, and after its process, effluent quality is qualified intakes afterwards as reverse osmosis unit.Water after the process of the utility model processing mode advantage does not destroy original water charging system, and directly can fill into equalizing reservoir, later maintenance amount is little.
More medium filter 23 of the present utility model, in order to remove the impurity such as silt, suspension, colloid in former water, reduces SDI value, carries out preliminary purification, automatically run, automatic back-washing to former water.Carbon steel body is through phosphate pretreatment, and ectonexine multilayer loop epoxy resins anticorrosion with coat, has good corrosion resistance.The resistance to pressure energy of filter reaches 1.0MPa.Device efficiency is high, no matter is all reasonably can distribute water at filtration condition or backwash state.
Active carbon filter 24 of the present utility model, in order to remove chlorine residue in water and partial organic substances, inside fills out the media such as anthracite, quartz sand, active fruit shell carbon.Can automatically run, automatic back-washing.Carbon steel body is through phosphate pretreatment, and ectonexine multilayer loop epoxy resins anticorrosion with coat, has good corrosion resistance.Active carbon filter of the present utility model is imported and exported and is provided with pressure reduction monitoring device, controls backwash by time setting and Inlet and outlet water pressure reduction.When pressure reduction is still higher than setting value after backwash for several times, provide alarm signal.Active carbon filter configuration visor, convenient state of observing carbon leaching material.Body should be arranged manhole and charge door, discharge port, facilitate the interpolation of carbon leaching material and the maintenance of filter.The Main Function of cartridge filter 26 of the present utility model retains because leading portion fails the fine particle thing, colloid, suspension etc. removed, better protection RO film.Native system reverse osmosis unit configures 5 μm of cartridge filters that 2 water passing capacities are 15m3/h, enters high-pressure pump and reverse osmosis membrane to prevent bulky grain thing.The shell of cartridge filter adopts stainless steel, in-built precision 5 μm of filter cores.Filter place is provided with pressure reduction monitoring device, should changes when monitoring pressure reduction and being greater than setting pressure reduction (being generally 0.07-0.1MPa).Reverse osmosis unit 29 cleared-out power of the present utility model is 10m3/h.
Chemicals dosing plant 25 of the present utility model is divided into the chemicals dosing plant before pretreatment, the chemicals dosing plant before counter-infiltration system.It is flocculant pole bactericide that chemicals dosing plant before pretreatment adds medicament; Chemicals dosing plant before counter-infiltration system is pH regulating agent and antisludging agent.The volume of all kinds of drug solution case should not be less than the drug dosage of three days.Inside and outside of casing should be considered anticorrosion.The pump inlet of dosing metering diaphragm establishes genuine to join corrosion-resistant filter screen, and outlet should be installed genuine and be joined pressure maintaining valve, safety valve and pulse damper, Pressure gauge is answered tape pulse damper.Corrosion resistant dissolving basket net should be established in the liquor box of dissolved solid.Liquor box all should arrange electric stirring dissolver.The materials such as contact liq equipment component, pipeline will match with the requirement for anticorrosion of medium.The materials such as chemicals dosing plant and medicine injected system valve, pipeline will match with the requirement for anticorrosion of medium.The position of chemical feeding points on system pipeline should guarantee that medicament all fully mixes before entering pre-processing device and counter-infiltration system, and meets the reaction time of medicament.
Described more medium filter 23 comprises housing 3, housing 3 is the tubulose shell of lower end end closure, fixed cap 17 is installed on the top of housing 3, charging aperture 16 is installed on the top of fixed cap 17, the fixed cap 17 that passes of charging aperture 16 enters housing 3 inside, the middle part of fixed cap 17 vertically arranges screw rod 2, the bottom of screw rod 2 is through fixed cap 17, the inside bottom of housing 3 installs fixed cover 14, the lower end of screw rod 2 coordinates with fixed cover 14, the first filter 7 is installed at the middle part of screw rod 2, first filter 7 is positioned on the downside of fixed cap 17, the first through hole 8 is offered at the middle part of the first filter 7, screw rod 2 is through the first through hole 8, the first nut 4 is installed at the middle part of screw rod 2, first nut 4 is positioned on the downside of the first filter 7, the external diameter of the first nut 4 is greater than the diameter of the first through hole 8, the second filter 10 is installed at the middle part of screw rod 2, second filter 10 is positioned on the downside of the first nut 4, the second through hole 11 is offered in the middle part of second filter 10, screw rod 2 is through the second through hole 11, the second nut 18 is installed at the middle part of screw rod 2, second nut 18 is positioned on the downside of the second filter 10, the external diameter of the second nut 18 is greater than the diameter of the second through hole 11, the 3rd filter 12 is installed at the middle part of screw rod 2, 3rd filter 12 is positioned on the downside of the second nut 18, third through-hole 13 is offered at the middle part of the 3rd filter 12, screw rod 2 is through third through-hole 13, screw rod 2 installs the 3rd nut 19, 3rd nut 19 is positioned at the downside of the 3rd filter 12, the external diameter of the 3rd nut 19 is greater than the diameter of third through-hole 13, the bottom of housing 3 arranges discharging opening 15.
First filter 7 of the present utility model, the bottom of the second filter 10 and the 3rd filter 12 arranges the first nut 4 respectively, second nut 18 and the 3rd nut 19, first nut 4, second nut 18 and the 3rd nut 19 are to the first filter 7, the height on screw rod 2 can be regulated arbitrarily by rotating while second filter 10 and the 3rd filter 12 play positioning action, thus regulate the first filter 7, gap between second filter 10 and the 3rd filter 12, make fiber when being filtered to different phase, the suitable holdup time can be had, fiber is filtered fully.Charging aperture 16 of the present utility model can make to enter the fiber in housing 3, has certain pressure, and the filtration time of fiber is accelerated greatly.
Because the first filter 7, second filter 10 and the 3rd filter 12 can swing in filter process, affect filter quality, in order to avoid the problems referred to above, the utility model is in the following ways: the left and right sides of the inside of described housing 3 arranges slide rail 6 respectively, chute 5 is all offered in the left and right sides of the first filter 7, second filter 10 and the 3rd filter 12, and chute 5 coordinates with slide rail 6.First filter 7, second filter 10 of the present utility model and the 3rd filter 12 can be fixed on housing 3 inside by chute 5 with coordinating of slide rail 6, first filter 7, second filter 10 and the 3rd filter 12 can not can be swung in filter process, substantially increase the filter quality of fiber.
Mention screw rod 2 for the convenience of the users, the utility model in the following ways: the upper end mounting knob 1 of described screw rod 2.
The technical solution of the utility model is not restricted in the scope of embodiment described in the utility model.The technology contents of the not detailed description of the utility model is known technology.
Claims (4)
1. valve external condensation system wastewater recycling system process equipment, it is characterized in that: comprise the outer water-cooled draught engine (20) of valve, the outer water-cooled draught engine (20) of valve connects newly-built inlet well and water receiver (21), newly-built inlet well and water receiver (21) connect raw water pump (22), raw water pump (22) connects more medium filter (23), more medium filter (23) connects active carbon filter (24), active carbon filter (24) connects cartridge filter (26), be connected with chemicals dosing plant (25) after active carbon filter (24) is connected with cartridge filter (26), cartridge filter (26) connects water tank (27), water tank (27) connects high-pressure pump (28), high-pressure pump (28) connects reverse osmosis unit (29), reverse osmosis unit (29) connects purified water storage groove (30), purified water storage groove (30) connects equalizing reservoir (31).
2. valve external condensation system wastewater recycling system process equipment according to claim 1, it is characterized in that: described more medium filter (23) comprises housing (3), the tubulose shell that housing (3) is lower end end closure, fixed cap (17) is installed on the top of housing (3), charging aperture (16) is installed on the top of fixed cap (17), the fixed cap (17) that passes of charging aperture (16) enters housing (3) inside, the middle part of fixed cap (17) vertically arranges screw rod (2), the bottom of screw rod (2) is through fixed cap (17), the inside bottom of housing (3) installs fixed cover (14), the lower end of screw rod (2) coordinates with fixed cover (14), the first filter (7) is installed at the middle part of screw rod (2), first filter (7) is positioned at fixed cap (17) downside, the first through hole (8) is offered at the middle part of the first filter (7), screw rod (2) is through the first through hole (8), the first nut (4) is installed at the middle part of screw rod (2), first nut (4) is positioned at the first filter (7) downside, the external diameter of the first nut (4) is greater than the diameter of the first through hole (8), the second filter (10) is installed at the middle part of screw rod (2), second filter (10) is positioned at the first nut (4) downside, the second through hole (11) is offered at second filter (10) middle part, screw rod (2) is through the second through hole (11), the second nut (18) is installed at the middle part of screw rod (2), second nut (18) is positioned at the second filter (10) downside, the external diameter of the second nut (18) is greater than the diameter of the second through hole (11), the 3rd filter (12) is installed at the middle part of screw rod (2), 3rd filter (12) is positioned at the second nut (18) downside, third through-hole (13) is offered at the middle part of the 3rd filter (12), screw rod (2) is through third through-hole (13), screw rod (2) installs the 3rd nut (19), 3rd nut (19) is positioned at the downside of the 3rd filter (12), the external diameter of the 3rd nut (19) is greater than the diameter of third through-hole (13), the bottom of housing (3) arranges discharging opening (15).
3. valve external condensation system wastewater recycling system process equipment according to claim 2, it is characterized in that: the left and right sides of the inside of described housing (3) arranges slide rail (6) respectively, chute (5) is all offered in the left and right sides of the first filter (7), the second filter (10) and the 3rd filter (12), and chute (5) coordinates with slide rail (6).
4. valve external condensation system wastewater recycling system process equipment according to claim 2, is characterized in that: the upper end mounting knob (1) of described screw rod (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420679811.4U CN204298172U (en) | 2014-11-14 | 2014-11-14 | Valve external condensation system wastewater recycling system process equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420679811.4U CN204298172U (en) | 2014-11-14 | 2014-11-14 | Valve external condensation system wastewater recycling system process equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204298172U true CN204298172U (en) | 2015-04-29 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420679811.4U Withdrawn - After Issue CN204298172U (en) | 2014-11-14 | 2014-11-14 | Valve external condensation system wastewater recycling system process equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204298172U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104386856A (en) * | 2014-11-14 | 2015-03-04 | 国家电网公司 | Technological equipment of valve external cooling system wastewater recycling system |
| CN107915350A (en) * | 2017-12-22 | 2018-04-17 | 天津蓝新石油化工有限公司 | A kind of automobile antifreezing liquid preparing system |
-
2014
- 2014-11-14 CN CN201420679811.4U patent/CN204298172U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104386856A (en) * | 2014-11-14 | 2015-03-04 | 国家电网公司 | Technological equipment of valve external cooling system wastewater recycling system |
| CN107915350A (en) * | 2017-12-22 | 2018-04-17 | 天津蓝新石油化工有限公司 | A kind of automobile antifreezing liquid preparing system |
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