CN205275386U - Open -air relief of disaster, fire control water purification system - Google Patents

Open -air relief of disaster, fire control water purification system Download PDF

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Publication number
CN205275386U
CN205275386U CN201521030799.5U CN201521030799U CN205275386U CN 205275386 U CN205275386 U CN 205275386U CN 201521030799 U CN201521030799 U CN 201521030799U CN 205275386 U CN205275386 U CN 205275386U
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water
feed
unit
gas
liquid mixed
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沈睿
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Wuxi Keliya Water Technology Co Ltd
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Wuxi Keliya Water Technology Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

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Abstract

The utility model discloses an open -air relief of disaster, fire control water purification system, system include self priming pump, compressed air machine, the ware that removes sand, pocket type filter unit, multimedium filter unit, active carbon filter unit, ultrafiltration unit, life water tank, dual sterilizing equipment and pure water case, and the play water end (W. E. ) of self priming pump is connected through the gas -liquid mixture tee bend and the end of intaking of the ware that removes sand, and the compressed air machine is connected through the gas -liquid mixture tee bend and the end of intaking of the ware that removes sand, water end (W. E. ) and the pocket type filter unit's of ware the end of intaking of removing sand is connected, pocket type filter unit's play water end (W. E. ) is connected with multimedium filter unit's the end of intaking, the play water end (W. E. ) of many filter medium filtration unit is connected with active carbon filter unit's the end of intaking, active carbon filter unit's play water end (W. E. ) is connected with the end of intaking of ultrafiltration unit, the play water end (W. E. ) of ultrafiltration unit is connected with the end of intaking of life water tank, the play water end (W. E. ) and the dual sterilizing equipment of life water tank are intake to hold and are connected, dual sterilizing equipment goes out the water end (W. E. ) and is connected with the pure water case. The utility model discloses possess good water purification, it is longe -lived.

Description

The field disaster relief, fire-fighting water cleaning systems
Technical field
The utility model relates to water purification field.
Background technology
Pollute in various degree owing to drinking water source is caused by the reason such as mankind's activity, natural disaster, usually make the drinking-water quality of the personnel of field work, exploring travel, earthquake relief work be more difficult to get guarantee. Field and disaster region situation are complicated, and water quality is various, and in water, dissolved matter composition difficulty is differentiated, concentration difficulty is differentiated, operation in the wild is earthquake relief work and so on action particularly, and in order to ensure that troop personnel's is healthy, the tap water that existing water cleaning systems purifies is also unreliable.
Summary of the invention
Goal of the invention: in order to overcome the deficiencies in the prior art, the utility model provides a kind of the field disaster relief, fire-fighting water cleaning systems, possesses good purifying water effect, it may also be useful to the life-span is long.
Technical scheme: for achieving the above object, the technical solution of the utility model is as follows:
The field disaster relief, fire-fighting water cleaning systems, comprise vacuum primingpump, pressurized air machine, sand cleaning machine, bag type filtering unit, multi-medium filtering unit, activated carbon filtration unit, ultra filtration unit, water supply tank, double sterilization device and pure water tank, the water side of described vacuum primingpump is connected with the feed-water end of sand cleaning machine by gas-liquid mixed threeway, and described pressurized air machine is connected with the feed-water end of sand cleaning machine by gas-liquid mixed threeway; The water side of described sand cleaning machine is connected with the feed-water end of bag type filtering unit, the water side of described bag type filtering unit is connected with the feed-water end of multi-medium filtering unit, the water side of described multi-medium filtering unit is connected with the feed-water end of activated carbon filtration unit, the described water side of activated carbon filtration unit is connected with the feed-water end of ultra filtration unit, the water side of described ultra filtration unit is connected with the feed-water end of water supply tank, the water side of described water supply tank is connected with double sterilization device feed-water end, and described double sterilization device water side is connected with pure water tank. Structure is simple, and purifying water effect is excellent.
The utility model further improves scheme, the feed-water end of described vacuum primingpump is connected with water source by water source water inlet pipe, described water source water inlet pipe is serially connected with electric heater, it is possible to melt ice cube in time, effectively melts the inner ice cube entered with frozen water of pipeline or device to the impact of system.
The utility model further improves scheme, and described gas-liquid mixed threeway comprises three ports, is respectively gas-liquid mixed feed-water end, gas-liquid mixed air inlet end and gas-liquid and blends water end, and the relative aperture of three ports is 3:1:2; And the axis angle between described gas-liquid mixed feed-water end and gas-liquid mixed air inlet end is 30-40 ��; On the sidewall of the connecting pipeline between described gas-liquid mixed water side and sand cleaning machine, flood dragon is spiral is connected some gas-liquids acceleration arm, the current direction angle that described gas-liquid is accelerated in arm and connecting water pipe is 5-10 ��, and the air inlet end that described gas-liquid accelerates arm is connected with pressurized air machine outlet side. By lead in pressurized air into high pressure, high-speed gas can strengthen the working efficiency of sand cleaning machine, in addition, when system is without the need to water purification, first close vacuum primingpump and sand separator, then the continuation of pressurized air is kept to import, the water of emptying whole internal system water pipe, when the water in each pressure transmitter indicating system inner main component is emptying, closes compression air engine again, the expand tube booster phenomenon that the internal system water freezing preventing cold weather from causing causes.
The utility model further improves scheme, comprise auxiliary feed-water end, for the muddy water that rareization gas-liquid mixed feed-water end enters, the angle between described auxiliary feed-water end and gas-liquid mixed feed-water end is 30-40 ��, and the angle between described auxiliary feed-water end and gas-liquid mixed air inlet end is 30-40 ��. When the water source that vacuum primingpump extracts is enough muddy, it is possible to coordinate and open auxiliary feed-water end, auxiliary water inlet pipe imports clean water, dilution muddy water, thus alleviates the operating pressure of sand separator.
The utility model further improves scheme, described bag type filtering unit comprises the first bag type filtering device and the 2nd bag type filtering device, described multi-medium filtering unit comprises the first multi-medium filtering device and the 2nd multi-medium filtering device, and described activated carbon filtration unit comprises the first multi-medium filtering device and the 2nd multi-medium filtering device; Described bag type filtering unit feed-water end is connected with the first pressure transmitter, and described first pressure transmitter is connected with the first bag type filtering device and the 2nd bag type filtering device respectively; Described multi-medium filtering unit feed-water end is connected with the 2nd pressure transmitter, and described 2nd pressure transmitter is connected with the first multi-medium filtering device and the 2nd multi-medium filtering device respectively; Described activated carbon filtration unit feed-water end is connected with the 3rd pressure transmitter, and described 3rd pressure transmitter is connected with the first active carbon filtering device and the 2nd active carbon filtering device respectively. By the first water pressure sensor, the 2nd water pressure sensor and the 3rd water pressure sensor can the Water warfare using state of the inner each integral part of monitor in real time water pretreatment unit, if desired can according to the numerical value a preparation and a use of pressure transmitter or directly modularization change.
The utility model further improves scheme, the water side of described ultra filtration unit is divided into ultrafiltration primary effluent end and ultrafiltration secondary effluent end, described ultrafiltration primary effluent end and ultrafiltration secondary effluent end are connected with water supply tank respectively, and in the one-level water torage tank being stored in respectively in water supply tank and two grades of water torage tankes; Also comprising backwashing pump, the feed-water end of described backwashing pump is connected with the water side of two grades of water torage tankes, and the water side of described backwashing pump is connected with the feed-water end backflow of ultra filtration unit. The water of water supply tank store, when reaching available levels water, such as washes clothes, has a bath, when washing dish, can use two grades of water, can use one-level water as drunk; On this basis, two grades of water can be connected with ultra filtration unit backflow by anti-pump of inhaling, filter further, obtain more one-level water.
The utility model further improves scheme, the water side of described one-level water torage tank is connected with the feed-water end of reverse osmosis unit by high-pressure pump, the water side of described reverse osmosis unit is divided into reverse osmosis first water side and reverse osmosis the 2nd water side, described reverse osmosis first water side is connected with double sterilization device feed-water end, and described reverse osmosis the 2nd water side is connected with the backflow of one-level water torage tank. From reverse osmosis unit first water side, water out is under the cooperation of double sterilization device, available obtain pure rank water, from reverse osmosis unit the 2nd water side water out can with being back to one-level water torage tank, with this obtain more pure rank with water, it is to increase water purification quality and efficiency.
The utility model further improves scheme, described sand cleaning machine comprises inverted cone formula elastic helix pipe and spiral tube altitude mixture control support, fix with sand cleaning machine housing bottom bottom described inverted cone formula elastic helix pipe, the often circle spiral tube of described inverted cone formula elastic helix pipe at least with two tie-in module level connection joints, each tie-in module is connected with spiral tube altitude mixture control support respectively, is changed relative height and the relative radius of inverted cone formula elastic helix pipe by adjusting screw pipe altitude mixture control support; Described inverted cone formula elastic helix pipe is uniformly distributed along spiral tube tube wall and arranges some micron openings, the upper inlet of described inverted cone formula elastic helix pipe is connected with gas-liquid mixed threeway outlet, the outlet at bottom of described inverted cone formula elastic helix pipe is connected with sediment ejection opening, and the water flowed out in the micron openings of described inverted cone formula elastic helix pipe is connected with bag type filtering unit through confluxing. The cooperation of inverted cone formula elastic helix pipe and spiral tube altitude mixture control support, realize removing sand efficiency and the selection of removing sand between effect by the relative height of spiral tube altitude mixture control bracket adjustment inverted cone formula elastic helix pipe and relative radius.
The utility model further improves scheme, storage water heating container it is provided with between the water side of described sand cleaning machine and bag type filtering unit, temperature measurement unit, the auxiliary unit of electrically heated and sun power heat exchange unit it is provided with in described storage water heating container, described temperature measurement unit unit control auxiliary with electrically heated is connected, and described electricity boosting unit and sun power heat exchange unit are connected in series with solar energy hot water tank inlet tube and outlet tube. The water temperature entered in pretreatment unit and downstream unit thereof can be ensured, in order to avoid too low water temperature or unstable water temperature cause the damage of equipment and the reduction of decontamination effect improving. Long-time too low water temperature can cause the damage for the treatment of plant, and unstable water temperature can cause equipment pipeline and filter expanding with heat and contract with cold of kapillary, causes the blocking of the kapillary of equipment and the instability of water quality.
The utility model further improves scheme, and sun power heat exchange unit comprises the first interchanger being connected in series successively, many wheel water flow buffer devices and the 2nd interchanger; Described first interchanger/the 2nd interchanger is inner hollow cylinder body structure, and its inside distributes the penetrating tubule in some two ends along axis and radial direction, and the junction in described tubule outer wall and the wall face of the first interchanger/the 2nd interchanger is connected for sealing No leakage; Described many wheel water flow buffer devices are arranged between the first interchanger and the 2nd interchanger, it is provided with in described many wheel air-flow buffer devices and multiple takes turns sheet, connection is penetrated along the diameter direction taking turns sheet by three little axles, the two ends of the little axle of every root are contained on many wheel water flow buffer device inwalls respectively, the current of solar water container are through out-of-date, and wheel sheet independently rotates. The design of the first interchanger, many wheel water flow buffer devices and the 2nd interchanger, homogeneity and the thoroughness of whole heat exchange can be realized, the design of wheel sheet, first can slow down current, water is obtained slow down fully, realize the heat exchange of sufficient time, simultaneously, the water of pipe interior produces local temperature difference in the water temperature after the first round heat exchange of the first interchanger, and water flow to wheel sheet, when driving wheel sheet overturns so that water is obtaining on the basis slowed down, the effect stirring current can also be played, dissolve the drawback of the local temperature difference in current.
Useful effect: the utility model provides a kind of the field disaster relief, fire-fighting water cleaning systems, it is possible to adapts to severe field environment, completes high quality, independent water purification function, possess good purifying water effect, and long service life
Accompanying drawing explanation
Accompanying drawing 1 is structural representation of the present utility model.
Accompanying drawing 2 is the utility model storage water heating container structural representation;
Accompanying drawing 3 is the utility model sun power heat exchange unit structural representation;
Accompanying drawing 4 is the structural representation of the utility model sand cleaning machine;
Accompanying drawing 5 is the utility model gas-liquid mixed three-port structure schematic diagram.
Embodiment
Below in conjunction with accompanying drawing, the utility model is further described.
Such as accompanying drawing 1, the field disaster relief, fire-fighting water cleaning systems, comprise vacuum primingpump 1, pressurized air machine 2, sand cleaning machine 3, bag type filtering unit 4, multi-medium filtering unit 5, activated carbon filtration unit 6, ultra filtration unit 7, water supply tank 8, double sterilization device 11 and pure water tank 12, the water side of described vacuum primingpump 1 is connected with the feed-water end of sand cleaning machine 3 by gas-liquid mixed threeway 11, and described pressurized air machine 2 is connected with the feed-water end of sand cleaning machine 3 by gas-liquid mixed threeway, the water side of described sand cleaning machine 3 is connected with the feed-water end of bag type filtering unit 4, the water side of described bag type filtering unit 4 is connected with the feed-water end of multi-medium filtering unit 5, the water side of described multi-medium filtering unit 5 is connected with the feed-water end of activated carbon filtration unit 6, the water side of described activated carbon filtration unit 6 is connected with the feed-water end of ultra filtration unit 7, the water side of described ultra filtration unit 7 is connected with the feed-water end of water supply tank 8, the water side of described water supply tank 8 is connected with double sterilization device 11 feed-water end, described double sterilization device 11 water side is connected with pure water tank 12, described double sterilization device 11 comprises ultraviolet and ozone double sterilization.
The feed-water end of described vacuum primingpump 1 is connected with water source by water source water inlet pipe, and described water source water inlet pipe is serially connected with electric heater, it is possible to melt ice cube in time, effectively melts ice cube that pipeline or device inside enters with frozen water to the impact of system.
Such as Fig. 5, described gas-liquid mixed threeway 11 comprises three ports, and being respectively the relative aperture that gas-liquid mixed feed-water end 111, gas-liquid mixed air inlet end 112 and gas-liquid blend water end 113, three ports is 3:1:2; And the axis angle between described gas-liquid mixed feed-water end 111 and gas-liquid mixed air inlet end 112 is 30-40 ��; On the sidewall of the connecting pipeline between described gas-liquid mixed water side 113 and sand cleaning machine 3, flood dragon is spiral is connected some gas-liquids acceleration arm 114, described gas-liquid is accelerated arm 114 and is 5-10 �� with the current direction angle in connecting water pipe, and the air inlet end that described gas-liquid accelerates arm 114 is connected with pressurized air machine 2 outlet side. By lead in pressurized air into high pressure, high-speed gas can strengthen the working efficiency of sand cleaning machine, in addition, when system is without the need to water purification, first close vacuum primingpump and sand separator, then the continuation of pressurized air is kept to import, the water of emptying whole internal system water pipe, when the water in each pressure transmitter indicating system inner main component is emptying, closes compression air engine again, the expand tube booster phenomenon that the internal system water freezing preventing cold weather from causing causes.
Comprising auxiliary feed-water end, for the muddy water that rareization gas-liquid mixed feed-water end 111 enters, the angle between described auxiliary feed-water end and gas-liquid mixed feed-water end is 30-40 ��, and the angle between described auxiliary feed-water end and gas-liquid mixed air inlet end 112 is 30-40 ��. When the water source that vacuum primingpump extracts is enough muddy, it is possible to coordinate and open auxiliary feed-water end, auxiliary water inlet pipe imports clean water, dilution muddy water, thus alleviates the operating pressure of sand separator.
Described bag type filtering unit 4 comprises the first bag type filtering device and the 2nd bag type filtering device, described multi-medium filtering unit 5 comprises the first multi-medium filtering device and the 2nd multi-medium filtering device, and described activated carbon filtration unit 6 comprises the first multi-medium filtering device and the 2nd multi-medium filtering device; Described bag type filtering unit 4 feed-water end is connected with the first pressure transmitter, and described first pressure transmitter is connected with the first bag type filtering device and the 2nd bag type filtering device respectively; Described multi-medium filtering unit 5 feed-water end is connected with the 2nd pressure transmitter, and described 2nd pressure transmitter is connected with the first multi-medium filtering device and the 2nd multi-medium filtering device respectively; Described activated carbon filtration unit 6 feed-water end is connected with the 3rd pressure transmitter, and described 3rd pressure transmitter is connected with the first active carbon filtering device and the 2nd active carbon filtering device respectively. By the first water pressure sensor, the 2nd water pressure sensor and the 3rd water pressure sensor can the Water warfare using state of the inner each integral part of monitor in real time water pretreatment unit, if desired can according to the numerical value a preparation and a use of pressure transmitter or directly modularization change.
The water side of described ultra filtration unit 7 is divided into ultrafiltration primary effluent end and ultrafiltration secondary effluent end, described ultrafiltration primary effluent end and ultrafiltration secondary effluent end are connected with water supply tank 8 respectively, and in the one-level water torage tank being stored in respectively in water supply tank 8 and two grades of water torage tankes; Also comprising backwashing pump 16, the feed-water end of described backwashing pump 16 is connected with the water side of two grades of water torage tankes, and the water side of described backwashing pump 16 is connected with the feed-water end backflow of ultra filtration unit 7. The water of water supply tank store, when reaching available levels water, such as washes clothes, has a bath, when washing dish, can use two grades of water, can use one-level water as drunk; On this basis, two grades of water can be connected with ultra filtration unit backflow by anti-pump of inhaling, filter further, obtain more one-level water.
The water side of described one-level water torage tank is connected with the feed-water end of reverse osmosis unit 10 by high-pressure pump 9, the water side of described reverse osmosis unit 10 is divided into reverse osmosis first water side and reverse osmosis the 2nd water side, described reverse osmosis first water side is connected with double sterilization device 11 feed-water end, and described reverse osmosis the 2nd water side is connected with the backflow of one-level water torage tank. From reverse osmosis unit first water side, water out is under the cooperation of double sterilization device, available obtain pure rank water, from reverse osmosis unit the 2nd water side water out can with being back to one-level water torage tank, with this obtain more pure rank with water, it is to increase water purification quality and efficiency.
Such as Fig. 4, described sand cleaning machine 3 comprises inverted cone formula elastic helix pipe 31 and spiral tube altitude mixture control support 32, fix bottom described inverted cone formula elastic helix pipe 31 with bottom sand cleaning machine housing 33, the often circle spiral tube of described inverted cone formula elastic helix pipe 31 at least with two tie-in module level connection joints, each tie-in module is connected with spiral tube altitude mixture control support respectively, is changed relative height and the relative radius of inverted cone formula elastic helix pipe 31 by adjusting screw pipe altitude mixture control support; Specifically, by upper and lower to mobile cross bar, change the relative height of inverted cone formula elastic helix pipe 31, move montant by direction, left and right, change the relative radius of inverted cone formula elastic helix pipe 31. Described inverted cone formula elastic helix pipe 31 is uniformly distributed along spiral tube tube wall and arranges some micron openings, the upper inlet of described inverted cone formula elastic helix pipe 31 is connected with gas-liquid mixed threeway outlet, the outlet at bottom of described inverted cone formula elastic helix pipe 31 is connected with sediment ejection opening, and the water flowed out in the micron openings of described inverted cone formula elastic helix pipe 31 is connected with bag type filtering unit 4 through confluxing. The cooperation of inverted cone formula elastic helix pipe 31 and spiral tube altitude mixture control support 32, realize removing sand efficiency and the selection of removing sand between effect by the relative height of spiral tube altitude mixture control bracket adjustment inverted cone formula elastic helix pipe 31 and relative radius.
Such as Fig. 2, storage water heating container 17 it is provided with between the water side of described sand cleaning machine 3 and bag type filtering unit 4, temperature measurement unit 171, the auxiliary unit 172 of electrically heated and sun power heat exchange unit 173 it is provided with in described storage water heating container 17, described temperature measurement unit 171 unit 172 control linkage auxiliary with electrically heated, described electricity boosting unit 172 and sun power heat exchange unit 173 are connected in series with solar energy hot water tank inlet tube and outlet tube. The water temperature entered in pretreatment unit and downstream unit thereof can be ensured, in order to avoid too low water temperature or unstable water temperature cause the damage of equipment and the reduction of decontamination effect improving. Long-time too low water temperature can cause the damage for the treatment of plant, and unstable water temperature can cause equipment pipeline and filter expanding with heat and contract with cold of kapillary, causes the blocking of the kapillary of equipment and the instability of water quality.
Such as Fig. 3, sun power heat exchange unit 173 comprises the first interchanger 174 being connected in series successively, many wheel water flow buffer devices 175 and the 2nd interchanger 176, described first interchanger 174/ the 2nd interchanger 176 is inner hollow cylinder body structure, its inside distributes the penetrating tubule in some two ends along axis and radial direction, and the junction in described tubule outer wall and the wall face of the first interchanger 174/ the 2nd interchanger 176 is connected for sealing No leakage, described many wheel water flow buffer devices 175 are arranged between the first interchanger 174 and the 2nd interchanger 176, it is provided with in described many wheel air-flow buffer devices 175 and multiple takes turns sheet 177, connection is penetrated along the diameter direction taking turns sheet 177 by three little axles, the two ends of the little axle of every root are contained on many wheel water flow buffer device 175 inwalls respectively, the current of solar water container are through out-of-date, and wheel sheet 177 independently rotates. first interchanger 174, the design of many wheel water flow buffer devices 175 and the 2nd interchanger 176, homogeneity and the thoroughness of whole heat exchange can be realized, the design of wheel sheet, first can slow down current, water is obtained slow down fully, realize the heat exchange of sufficient time, simultaneously, the water of pipe interior produces local temperature difference in the water temperature after the first round heat exchange of the first interchanger, and water flow to wheel sheet, when driving wheel sheet overturns, water is made to obtain on the basis slowed down, the effect stirring current can also be played, dissolve the local temperature difference in current, brought the drawback that purification brings.
The above is only preferred implementation of the present utility model; it is noted that, for those skilled in the art; under the prerequisite not departing from the utility model principle; can also making some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.

Claims (10)

1. the field disaster relief, fire-fighting water cleaning systems, it is characterized in that: comprise vacuum primingpump (1), pressurized air machine (2), sand cleaning machine (3), bag type filtering unit (4), multi-medium filtering unit (5), activated carbon filtration unit (6), ultra filtration unit (7), water supply tank (8), double sterilization device (11) and pure water tank (12), the water side of described vacuum primingpump (1) is connected with the feed-water end of sand cleaning machine (3) by gas-liquid mixed threeway (11), described pressurized air machine (2) is connected by the feed-water end of gas-liquid mixed threeway with sand cleaning machine (3), the water side of described sand cleaning machine (3) is connected with the feed-water end of bag type filtering unit (4), the water side of described bag type filtering unit (4) is connected with the feed-water end of multi-medium filtering unit (5), the water side of described multi-medium filtering unit (5) is connected with the feed-water end of activated carbon filtration unit (6), the water side of described activated carbon filtration unit (6) is connected with the feed-water end of ultra filtration unit (7), the water side of described ultra filtration unit (7) is connected with the feed-water end of water supply tank (8), the water side of described water supply tank (8) is connected with double sterilization device (11) feed-water end, described double sterilization device (11) water side is connected with pure water tank (12).
2. the field according to claim 1 disaster relief, fire-fighting water cleaning systems, it is characterised in that: the feed-water end of described vacuum primingpump (1) is connected with water source by water source water inlet pipe, and described water source water inlet pipe is serially connected with electric heater.
3. the field according to claim 1 disaster relief, fire-fighting water cleaning systems, it is characterized in that: described gas-liquid mixed threeway (11) comprises three ports, being respectively gas-liquid mixed feed-water end (111), gas-liquid mixed air inlet end (112) and gas-liquid and blend water end (113), the relative aperture of three ports is 3:1:2; And the axis angle between described gas-liquid mixed feed-water end (111) and gas-liquid mixed air inlet end (112) is 30-40 ��; On the sidewall of the connecting pipeline between described gas-liquid mixed water side (113) and sand cleaning machine (3), flood dragon is spiral is connected some gas-liquids acceleration arm (114), described gas-liquid is accelerated arm (114) and is 5-10 �� with the current direction angle in connecting water pipe, and the air inlet end that described gas-liquid accelerates arm (114) is connected with pressurized air machine (2) outlet side.
4. the field according to claim 3 disaster relief, fire-fighting water cleaning systems, it is characterized in that: comprise auxiliary feed-water end, for the muddy water that rareization gas-liquid mixed feed-water end (111) enters, angle between described auxiliary feed-water end and gas-liquid mixed feed-water end is 30-40 ��, and the angle between described auxiliary feed-water end and gas-liquid mixed air inlet end (112) is 30-40 ��.
5. the field according to claim 1 disaster relief, fire-fighting water cleaning systems, it is characterized in that: described bag type filtering unit (4) comprises the first bag type filtering device and the 2nd bag type filtering device, described multi-medium filtering unit (5) comprises the first multi-medium filtering device and the 2nd multi-medium filtering device, and described activated carbon filtration unit (6) comprises the first active carbon filtering device and the 2nd active carbon filtering device; Described bag type filtering unit (4) feed-water end is connected with the first pressure transmitter, and described first pressure transmitter is connected with the first bag type filtering device and the 2nd bag type filtering device respectively; Described multi-medium filtering unit (5) feed-water end is connected with the 2nd pressure transmitter, and described 2nd pressure transmitter is connected with the first multi-medium filtering device and the 2nd multi-medium filtering device respectively; Described activated carbon filtration unit (6) feed-water end is connected with the 3rd pressure transmitter, and described 3rd pressure transmitter is connected with the first active carbon filtering device and the 2nd active carbon filtering device respectively.
6. the field according to claim 1 disaster relief, fire-fighting water cleaning systems, it is characterized in that: the water side of described ultra filtration unit (7) is divided into ultrafiltration primary effluent end and ultrafiltration secondary effluent end, described ultrafiltration primary effluent end and ultrafiltration secondary effluent end are connected with water supply tank (8) respectively, and in the one-level water torage tank being stored in respectively in water supply tank (8) and two grades of water torage tankes; Also comprising backwashing pump (16), the feed-water end of described backwashing pump (16) is connected with the water side of two grades of water torage tankes, and the water side of described backwashing pump (16) is connected with the feed-water end backflow of ultra filtration unit (7).
7. the field according to claim 6 disaster relief, fire-fighting water cleaning systems, it is characterized in that: the water side of described one-level water torage tank is connected with the feed-water end of reverse osmosis unit (10) by high-pressure pump (9), the water side of described reverse osmosis unit (10) is divided into reverse osmosis first water side and reverse osmosis the 2nd water side, described reverse osmosis first water side is connected with double sterilization device (11) feed-water end, and described reverse osmosis the 2nd water side is connected with the backflow of one-level water torage tank.
8. the field according to claim 1 disaster relief, fire-fighting water cleaning systems, it is characterized in that: described sand cleaning machine (3) comprises inverted cone formula elastic helix pipe (31) and spiral tube altitude mixture control support (32), described inverted cone formula elastic helix pipe (31) bottom is fixing with sand cleaning machine housing (33) bottom, the often circle spiral tube of described inverted cone formula elastic helix pipe (31) at least with two tie-in module level connection joints, each tie-in module is connected with spiral tube altitude mixture control support respectively, relative height and the relative radius of inverted cone formula elastic helix pipe (31) is changed by adjusting screw pipe altitude mixture control support, described inverted cone formula elastic helix pipe (31) is uniformly distributed along spiral tube tube wall and arranges some micron openings, the upper inlet of described inverted cone formula elastic helix pipe (31) is connected with gas-liquid mixed threeway outlet, the outlet at bottom of described inverted cone formula elastic helix pipe (31) is connected with sediment ejection opening, and the water flowed out in the micron openings of described inverted cone formula elastic helix pipe (31) is connected with bag type filtering unit (4) through confluxing.
9. the field according to claim 1 disaster relief, fire-fighting water cleaning systems, it is characterized in that: between the water side of described sand cleaning machine (3) and bag type filtering unit (4), be provided with storage water heating container (17), it is provided with temperature measurement unit (171) in described storage water heating container (17), unit (172) and sun power heat exchange unit (173) are assisted in electrically heated, described temperature measurement unit (171) unit (172) control linkage auxiliary with electrically heated, described electrically heated assists unit (172) (172) and sun power heat exchange unit (173) to enter with solar energy hot water tank, rising pipe is connected in series.
10. the field according to claim 9 disaster relief, fire-fighting water cleaning systems, it is characterised in that: sun power heat exchange unit (173) comprises the first interchanger (174) being connected in series successively, many wheels water flow buffer device (175) and the 2nd interchanger (176); Described first interchanger (174)/the 2nd interchanger (176) is inner hollow cylinder body structure, its inside distributes the penetrating tubule in some two ends along axis and radial direction, and the junction in described tubule outer wall and the wall face of the first interchanger (174)/the 2nd interchanger (176) is connected for sealing No leakage; Described many wheels water flow buffer device (175) are arranged between the first interchanger (174) and the 2nd interchanger (176), it is provided with in described many wheels air-flow buffer device (175) and multiple takes turns sheet (177), connection is penetrated along the diameter direction taking turns sheet (177) by three little axles, the two ends of the little axle of every root are contained on many wheel water flow buffer device (175) inwalls respectively, the current of solar water container are through out-of-date, and wheel sheet (177) independently rotates.
CN201521030799.5U 2015-12-11 2015-12-11 Open -air relief of disaster, fire control water purification system Active CN205275386U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105366858A (en) * 2015-12-11 2016-03-02 无锡科立雅纯水科技有限公司 Water purification system for field disaster rescue and fire protection
CN106673249A (en) * 2017-03-19 2017-05-17 无锡远及科技有限公司 Water purifying system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105366858A (en) * 2015-12-11 2016-03-02 无锡科立雅纯水科技有限公司 Water purification system for field disaster rescue and fire protection
CN105366858B (en) * 2015-12-11 2017-11-21 无锡科立雅纯水科技有限公司 The field disaster relief, fire-fighting water cleaning systems
CN106673249A (en) * 2017-03-19 2017-05-17 无锡远及科技有限公司 Water purifying system
CN106673249B (en) * 2017-03-19 2018-05-22 佛山市禅城区供水有限公司 A kind of water cleaning systems

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