CN102107101A - High-temperature condensed water recycling and purifying system with ceramic membrane filter - Google Patents
High-temperature condensed water recycling and purifying system with ceramic membrane filter Download PDFInfo
- Publication number
- CN102107101A CN102107101A CN 200910260224 CN200910260224A CN102107101A CN 102107101 A CN102107101 A CN 102107101A CN 200910260224 CN200910260224 CN 200910260224 CN 200910260224 A CN200910260224 A CN 200910260224A CN 102107101 A CN102107101 A CN 102107101A
- Authority
- CN
- China
- Prior art keywords
- water
- membrane filter
- ceramic membrane
- filter device
- water inlet
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 163
- 239000012528 membrane Substances 0.000 title claims abstract description 73
- 239000000919 ceramic Substances 0.000 title claims abstract description 72
- 238000004064 recycling Methods 0.000 title abstract description 6
- 238000004140 cleaning Methods 0.000 claims abstract description 24
- 238000001914 filtration Methods 0.000 claims abstract description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 29
- 238000010926 purge Methods 0.000 claims description 26
- 238000000746 purification Methods 0.000 claims description 25
- 229910052742 iron Inorganic materials 0.000 claims description 16
- 239000010865 sewage Substances 0.000 claims description 16
- 239000012530 fluid Substances 0.000 claims description 6
- 125000004122 cyclic group Chemical group 0.000 claims description 3
- 230000001737 promoting effect Effects 0.000 claims description 3
- 230000001105 regulatory effect Effects 0.000 claims description 3
- 238000012545 processing Methods 0.000 abstract description 7
- 238000010276 construction Methods 0.000 abstract description 2
- 230000010354 integration Effects 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- 239000007788 liquid Substances 0.000 description 9
- 230000004907 flux Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- -1 iron ion Chemical class 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- RZVAJINKPMORJF-UHFFFAOYSA-N Acetaminophen Chemical compound CC(=O)NC1=CC=C(O)C=C1 RZVAJINKPMORJF-UHFFFAOYSA-N 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000008358 core component Substances 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910001410 inorganic ion Inorganic materials 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000012163 sequencing technique Methods 0.000 description 1
- 230000005619 thermoelectricity Effects 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Images
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention provides a high-temperature condensed water recycling and purifying with a ceramic membrane filter. The high-temperature condensed water recycling and purifying with the ceramic membrane filter comprises a concentrating tank, a dual-pump structure, the ceramic membrane filter, a cleaning tank and a water purifying tank; the water outlet of the concentrating tank is connected with the water inlet of the dual-pump structure through a pipeline; the water outlet of the dual-pump structure is connected with the circulating water inlet of the ceramic membrane filter; the circulating water outlet of the ceramic membrane filter is connected with a communicating pipe of the dual-pump structure through a pipeline; the water purifying port of the ceramic membrane filter is connected to the water purifying tank through a pipeline; the water inlet of the cleaning tank is connected with the water purifying port of the ceramic membrane filter through a three-way pipeline; the cleaning solution outlet of the cleaning tank is connected with the water inlet of the dual-pump structure through a three-way pipe; and the cleaning water returning port of the cleaning tank is connected with the circulating water inlet of the ceramic membrane filter. The high-temperature condensed water recycling and purifying with the ceramic membrane filter is divided into two processing units so that separation and filtration can be separated; and by continuous concentration of water, a processing device for separating according to the physical characteristics of a medium is provided. The device occupies a small area, has high integration degree and a short construction period, and is easy to install.
Description
Technical field
The present invention relates to a kind of sewage-treatment plant, particularly a kind of ceramic membrane filter device reclaiming clean condensed water in high temperature system.
Background technology
At present, industries such as chemical industry, thermoelectricity extensively adopt superheated steam to use as heat power and thermal source, become condensate water after superheated steam process power consumption and the heat exchange, and its temperature is between 20 ℃-99 ℃, if not comtaminated, steam condensate is bordering on pure distilled water.But the steam condensate of most of enterprises is because reasons such as corrosive pipeline, material leakage, mismanagements, exist pollutants such as certain oily substance, iron, so can not directly advance the boiler recycling, causing now, the condensed water in high temperature great majority of most of enterprises discharge on the spot, not only wasted great amount of water resources and heat energy, also caused water pollution to a certain degree to environment.Therefore, impurity such as removing that the condensed water in high temperature reuse at first will solve deoiled, iron make water quality reach requirement.
Given this plant the result, the patent No. is that 02236450.1 utility model discloses a kind of condensed water in high temperature deironing apparatus, employing can be removed iron ion in the condensed water in high temperature with iron ion rapid-action filler, but this device is primarily aimed at the removal of the iron ion in the condensed water in high temperature and designs, and very poor to the removal effect of oil, colloid, solubility small organic molecule and inorganic ions, also exist oil simultaneously and coat the drawback that filler can not effectively be removed iron ion.The patent No. is 200820078553.9, name is called " a kind of composite membrane condensate water oil removing deironing apparatus " and discloses a kind of composite membrane processing condensate water oil removing deironing apparatus that utilizes, this device in use needs continuous overlay film, cycle is short, the very complicated of process exception consumes lot of manpower and material resources.The patent No. is 200820078652.7, name is called " condensate water combined type high temperature oil removing deironing apparatus " utility model and adopts high-temperature resin class extraction+accurate filter complex technique, though this kind technology can reclaim the condensate water of high temperature, but resin extraction oily substance is short service life when high temperature, needs frequent more conversion materials; Use accurate filter when deironing, this moment need be at filter element surface pre-coating film, and whole oil removing deironing apparatus control point and maintenance point in running increase, and processing cost increases, the program very complicated.
Summary of the invention
In view of above reason; main purpose of the present invention is to provide a kind of ceramic membrane filter device reclaiming clean condensed water in high temperature system; utilize this system can realize direct oil removing, the deironing of condensed water in high temperature; export the high temperature water purification simultaneously; can directly use or advanced treating once more for medium-pressure boiler; thereby guaranteeing under the prerequisite of environmental protection, reducing the recycling cost of condensate water.Whole system automaticity height, easy to operate and safe.
For achieving the above object, technical scheme of the present invention is:
A kind of ceramic membrane filter device reclaiming clean condensed water in high temperature system, it comprises concentration tank 1, double pump structure 2, ceramic membrane filter device 3, purge tank 4 and water purification jar 5, the delivery port 17 of concentration tank 1 is connected with the water inlet 21 of double pump structure 2 by pipeline 6; The delivery port 22 of described double pump structure 2 is connected with the circulation water inlet 31 of ceramic membrane filter device 3, the circulating outlet 32 of described ceramic membrane filter device 3 joins communicating pipe by pipeline 6 and double pump structure 2, the water purification mouth 33 of described ceramic membrane filter device 3 is connected to water purification jar 5 by pipeline 6, the water inlet 41 of described purge tank 4 and the water purification mouth of ceramic membrane filter device 3 33 link to each other by three-way pipeline, the cleaning fluid delivery port 42 of described purge tank 4 and the water inlet of double pump structure 2 21 link to each other by three-way pipe, and the cleaning water return outlet 43 of described purge tank 4 links to each other with the circulation water inlet 31 of ceramic membrane filter device 3.
Further, concentration tank 1 internal upper part is provided with except that oil system 11, bottom and is provided with deironing system 12, be respectively arranged with overfall 13, water inlet 14, concentration tank sewage draining exit 15, water return outlet 16 and delivery port 17 on described concentration tank 1 sidewall, described deironing system 12 is that iron plate is received in an inclination that is arranged on concentration tank 1 bottom, and described concentration tank sewage draining exit 15 is arranged on receives place, iron plate bottom.
Further, double pump structure 2 is that two water pumps are formed, be respectively feed pump 23 and circulating pump 24, the water inlet 21 of described feed pump 23 is connected with the delivery port 17 of concentration tank 1 and is used for promoting condensed water in high temperature, its feed pump 23 delivery ports link to each other with communicating pipe with the water inlet of circulating pump 24, and described feed pump 23 is used for the cyclic high-temperature condensate water with being connected with the circulating outlet 32 of ceramic membrane filter device 3 communicating pipe of circulating pump 24.
Further, purge tank 4 tops are provided with water inlet 41 and clean water return outlet 43, and described purge tank 4 bottoms are provided with cleaning fluid delivery port 42 and clean sewage draining exit 44.
Further, ceramic membrane filter device 3 is that the film pipe 36 of 5-800nm is formed by housing 35 and aperture, described film pipe 36 complex roots vertically are filled in the housing 35, be respectively equipped with loop exit 32 and circulation water inlet 31 at described housing 35 upper/lower terminals, at upper and lower pure water inlet 33 and the filtration sewage draining exit 34 of being respectively equipped with of housing 35 sidewalls.
Further, the water return outlet 16 of the circulation water inlet 31 of ceramic membrane filter device 3 and concentration tank 1 is connected by pipeline.
Further, be provided with recoil pump 7 between ceramic membrane filter device 3 and the water purification jar 5, described recoil pump 7 water inlets link to each other with ceramic membrane filter device 3 by pipeline, and delivery port links to each other with water purification jar 5 by pipeline.
Further, the pipeline 6 that connects between concentration tank 1, double pump structure 2, ceramic membrane filter device 3, purge tank 4 and the water purification jar 5 is respectively arranged with magnetic valve, and described magnetic valve is regulated and control by robot control system(RCS).
The present invention adopts the ceramic membrane filter device that condensed water in high temperature is handled recovery, and native system has the following advantages:
1. native system adopts ceramic ultra-filtration filters element as processing condensate water oil removing deironing core component, and adopts the working method of emission type cross-flow as ceramic filter element.Have the good temperature resistance energy, and the antipollution impact capacity is remarkable, is applicable to the processing of companion's thermal coagulation water that impact may be bigger.The cross-flow mode has delayed to pollute the formation cycle of filter cake, makes that producing water flux is kept.
2. this mounting ceramics filter element physical property is good, and service life, renewal cost was low greater than 4 years.
3. this device uses when water inlet and receives oil receipts iron concentration tank, not only can guarantee that subsequent treatment unit ceramic membrane filter device treatment effect is stable, obvious, and having prolonged the concentration time of circulating backwater, the tank body blowing period increases, and has more effectively saved the high-temperature water resource.
4. this device stored program controlled adopts compressed air-driven, and the variation affected by environment of the viscosity of medium is very little, and the physical property of drive medium is constant substantially throughout the year, can guarantee sequencing valve unanimity actuation time throughout the year; System is simple, operates steadily; Move safe and reliable, non-environmental-pollution.
5. this device uses the medicament that is specifically designed to the ceramic membrane filter device to clean, and makes the online non-stop run of the real realization of daily cleaning, does not influence product water, and keeps the long-term stability of filter element flux reliably, the regeneration period of more effectively reducing filter element.
6. this device is a same chassis skid mounted equipment.Little, the integrated degree height of plant area, simple installation, short construction period.
Relevant detailed description of the present invention and technology contents, conjunction with figs. is described as follows.
Description of drawings
Accompanying drawing 1 is a structural representation of the present invention;
Accompanying drawing 2 is the structural representation of concentration tank of the present invention;
Accompanying drawing 3 is the structural representation of ceramic membrane filter device of the present invention;
Accompanying drawing 4 is the structural representation of purge tank of the present invention;
Accompanying drawing 5 has recoil cleaning device structural representation for the present invention;
Accompanying drawing 6 is the structural representation of this recoil cleaning device.
The specific embodiment
The invention will be further described below in conjunction with specific embodiment, but the present invention is not limited to following examples.
As shown in Figure 1, a kind of ceramic membrane filter device reclaiming clean condensed water in high temperature system, it comprises concentration tank 1, double pump structure 2, ceramic membrane filter device 3, purge tank 4 and water purification jar 5, and the delivery port 17 of concentration tank 1 is connected with the water inlet 21 of double pump structure 2 by pipeline 6; The delivery port 22 of described double pump structure 2 is connected with the circulation water inlet 31 of ceramic membrane filter device 3, the circulating outlet 32 of described ceramic membrane filter device 3 joins communicating pipe by pipeline 6 and double pump structure 2, the water purification mouth 33 of described ceramic membrane filter device 3 is connected to water purification jar 5 by pipeline 6, water purification jar 5 mainly is the good water after when being used for collecting normal product water, so that being used as subsequent treatment uses, the water inlet 41 of described purge tank 4 and the water purification mouth of ceramic membrane filter device 3 33 link to each other by three-way pipeline, the cleaning fluid delivery port 42 of described purge tank 4 and the water inlet of double pump structure 2 21 link to each other by three-way pipe, and the cleaning water return outlet 43 of described purge tank 4 links to each other with the circulation water inlet 31 of ceramic membrane filter device 3.
As shown in Figure 2, concentration tank 1 internal upper part is provided with except that oil system 11, bottom and is provided with deironing system 12, be respectively arranged with overfall 13, water inlet 14, concentration tank sewage draining exit 15, water return outlet 16 and delivery port 17 on described concentration tank 1 sidewall, described deironing system 12 is that iron plate is received in an inclination that is arranged on concentration tank 1 bottom, and described concentration tank sewage draining exit 15 is arranged on receives place, iron plate bottom.
Condensate water enters in the jar by water inlet 14, condensate water in jar is collected oil of the part in the condensate water and iron respectively by oil extraction device 11 and the effect of receiving iron plate 12, water enters ceramic membrane filter device 3 by the lifting of double pump 2 from delivery port 17, water after ceramic membrane filter device 3 circulation enters oil removing deironing concentration tank 1 by water return outlet 16 and concentrates, when cycles of concentration acquires a certain degree, carry out the blowdown of iron by the lower end sewage draining exit, the upper end oil collector is collected blowdown.
Double pump structure 2 is that two water pumps are formed, be respectively feed pump 23 and circulating pump 24, the water inlet 21 of described feed pump 23 is connected with the delivery port 17 of concentration tank 1 and is used for promoting condensed water in high temperature, its feed pump 23 delivery ports link to each other with communicating pipe with the water inlet of circulating pump 24, and the delivery port 22 of described circulating pump 24 is connected with the circulating outlet 32 of ceramic membrane filter device 3 and is used for the cyclic high-temperature condensate water.
As shown in Figure 3, purge tank 4 tops are provided with water inlet 41 and clean water return outlet 43, and described purge tank 4 bottoms are provided with cleaning fluid delivery port 42 and clean sewage draining exit 44.
The use of purge tank 4 is seriously polluted at film pipe 36, when membrane flux descends rapidly, uses purge tank 4 to clean.At first consider to use and produce the cleaning of water high temperature,, then need to carry out soda acid and wash if flux can not return to normal value.Certain density acid solution (or alkali lye) is put into purge tank 4, it is squeezed in the back with water inlet line, the same with normal product water it is carried out interior circulation, behind the circulation certain hour blowdown end valve door of ceramic membrane filter device 3 and purge tank 4 opened and carry out blowdown with pump.
As shown in Figure 4, ceramic membrane filter device 3 is that the film pipe 36 of 5-800nm is formed by housing 35 and aperture, described film pipe 36 complex roots vertically are filled in the housing 35, be respectively equipped with loop exit 32 and circulation water inlet 31 at described housing 35 upper/lower terminals, at upper and lower pure water inlet 33 and the filtration sewage draining exit 34 of being respectively equipped with of housing 35 sidewalls.
Ceramic membrane filter device 3 is main processing units of condensed water in high temperature, adopt the cross-flow method of operation, condensed water in high temperature is admitted to the feed side of ceramic membrane filter device 3 under the effect of pump, be parallel to face continuous-flow, certain crossflow velocity is set, wherein the part clear liquid sees through the side that sees through that fenestra enters film, not seeing through liquid discharges and turns back to the back with water inlet line from the outlet of film feed side at last, feed liquid constantly circulates, constantly leach simultaneously clear liquid, the contained pollutant of feed liquid thickens gradually, after membrane flux is reduced to a certain degree, cleans with concentrated sewage discharge and to film.
The circulation water inlet 31 of ceramic membrane filter device 3 and the water return outlet of concentration tank 1 16 are connected by pipeline.
As shown in Figure 5, for having the ceramic membrane filter device reclaiming clean condensed water in high temperature system of recoil cleaning function, be provided with recoil pump 7 between ceramic membrane filter device 3 and the water purification jar 5, described recoil pump 7 water inlets link to each other with ceramic membrane filter device 3 by pipeline, delivery port links to each other with water purification jar 5 by pipeline, when stopping state appears in film pipe 36, can extract by recoil pump 7 and filter the water purification cleaning that recoils.
The pipeline 2 that connects between concentration tank 1, double pump structure 2, ceramic membrane filter device 3, purge tank 4 and the water purification jar 5 is respectively arranged with magnetic valve, and described magnetic valve is regulated and control by robot control system(RCS).
Condensed water in high temperature enters oil removing deironing concentration tank 1, is connected with water pump through piping, is promoted in the ceramic membrane filter device 3 by double pump 2, and water outlet end adopts pipeline to be connected to water purification jar 5.Not seeing through liquid discharges and turns back in the oil removing deironing concentration tank 1 by the outlet of ceramic membrane filter device 3, feed liquid is constantly circulation between ceramic membrane filter device 3 and oil removing deironing concentration tank 1, constantly leach simultaneously clear liquid, the contained pollutant of feed liquid thickens gradually, after the flux of ceramic membrane filter device 3 is reduced to a certain degree, clean with concentrated sewage discharge and to the ceramic membrane filter device.At first produce water high temperature during cleaning and clean, adopt alkali cleaning, pickling to clean as seriously polluted.The water that 3 outlets are collected through the ceramic membrane filter device is through detecting the national boiler water quality standard that reaches.
The above is the preferred embodiments of the present invention only, is not limited to the present invention, and obviously, those skilled in the art can carry out various changes and modification and not break away from the spirit and scope of the present invention the present invention.Like this, if of the present invention these are revised and modification belongs within the scope of claim of the present invention and equivalent technologies thereof, then the present invention also is intended to comprise these changes and modification interior.
Claims (8)
1. ceramic membrane filter device reclaiming clean condensed water in high temperature system, it comprises concentration tank (1), double pump structure (2), ceramic membrane filter device (3), purge tank (4) and water purification jar (5), it is characterized in that: the delivery port (17) of described concentration tank (1) is connected with the water inlet (21) of double pump structure (2) by pipeline (6); Described concentration tank water return outlet (16) links to each other by threeway with the circulation water inlet (31) of ceramic membrane filter device (3); The delivery port (22) of described double pump structure (2) is connected with the circulation water inlet (31) of ceramic membrane filter device (3), the circulating outlet (32) of described ceramic membrane filter device (3) joins communicating pipe by pipeline (6) and double pump structure (2), the water purification mouth (33) of described ceramic membrane filter device (3) is connected to water purification jar (5) by pipeline (6), the water inlet (41) of described purge tank (4) links to each other by three-way pipeline with the water purification mouth (33) of ceramic membrane filter device (3), the cleaning fluid delivery port (42) of described purge tank (4) links to each other by three-way pipe with the water inlet (21) of double pump structure (2), and the cleaning water return outlet (43) of described purge tank (4) links to each other with the circulation water inlet (31) of ceramic membrane filter device (3).
2. condensed water in high temperature according to claim 1 system, it is characterized in that: described concentration tank (1) internal upper part is provided with except that oil system (11), bottom and is provided with deironing system (12), be respectively arranged with overfall (13), water inlet (14), concentration tank sewage draining exit (15), water return outlet (16) and delivery port (17) on described concentration tank (1) sidewall, described deironing system (12) is that iron plate is received in an inclination that is arranged on concentration tank (1) bottom, and described concentration tank sewage draining exit (15) is arranged on receives place, iron plate bottom.
3. condensed water in high temperature according to claim 1 system, it is characterized in that: described double pump structure (2) is that two water pumps are formed, be respectively feed pump (23) and circulating pump (24), the water inlet (21) of described feed pump (23) is connected with the delivery port (17) of concentration tank (1) and is used for promoting condensed water in high temperature, its feed pump (23) delivery port links to each other with communicating pipe with the water inlet of circulating pump (24), and described feed pump (23) is used for the cyclic high-temperature condensate water with being connected with the circulating outlet (32) of ceramic membrane filter device (3) communicating pipe of circulating pump (24).
4. condensed water in high temperature according to claim 1 system is characterized in that: described purge tank (4) top is provided with water inlet (41) and cleans water return outlet (43), and described purge tank (4) bottom is provided with cleaning fluid delivery port (42) and cleaning sewage draining exit (44).
5. condensed water in high temperature according to claim 1 system, it is characterized in that: described ceramic membrane filter device (3) is that the film pipe (36) of 5-800nm is formed by housing (35) and aperture, described film pipe (36) is several vertically to be filled in the housing (35), be respectively equipped with loop exit (32) and circulation water inlet (31) at described housing (35) upper/lower terminal, at upper and lower pure water inlet (33) and the filtration sewage draining exit (34) of being respectively equipped with of housing (35) sidewall.
6. condensed water in high temperature according to claim 1 system, it is characterized in that: the circulation water inlet (31) of described ceramic membrane filter device (3) is connected by pipeline with the water return outlet (16) of concentration tank (1).
7. condensed water in high temperature according to claim 1 system, it is characterized in that: be provided with recoil pump (7) between described ceramic membrane filter device (3) and the water purification jar (5), described recoil pump (7) water inlet links to each other with the pure water inlet (33) of ceramic membrane filter device (3) by pipeline, and delivery port links to each other with water purification jar (5) by pipeline.
8. condensed water in high temperature according to claim 1 system, it is characterized in that: the pipeline (6) that connects between described concentration tank (1), double pump structure (2), ceramic membrane filter device (3), purge tank (4) and the water purification jar (5) is respectively arranged with magnetic valve, and described magnetic valve is regulated and control by robot control system(RCS).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200910260224 CN102107101B (en) | 2009-12-25 | 2009-12-25 | High-temperature condensed water recycling and purifying system with ceramic membrane filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200910260224 CN102107101B (en) | 2009-12-25 | 2009-12-25 | High-temperature condensed water recycling and purifying system with ceramic membrane filter |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102107101A true CN102107101A (en) | 2011-06-29 |
| CN102107101B CN102107101B (en) | 2013-04-10 |
Family
ID=44171451
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200910260224 Expired - Fee Related CN102107101B (en) | 2009-12-25 | 2009-12-25 | High-temperature condensed water recycling and purifying system with ceramic membrane filter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102107101B (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102641615A (en) * | 2012-03-30 | 2012-08-22 | 江苏华杉环保科技有限公司 | Cross-flow ceramic film filter test device |
| CN103349859A (en) * | 2013-04-22 | 2013-10-16 | 天津滨瀚环保科技发展有限公司 | Ceramic filter apparatus for separating calcium carbonate solution, and process thereof |
| CN103933779A (en) * | 2014-04-29 | 2014-07-23 | 江苏省电力设计院 | Protective device of filter element type high-temperature iron removing filter |
| CN107555541A (en) * | 2017-09-04 | 2018-01-09 | 大唐东北电力试验研究所有限公司 | Thermal power plant's low plus hydrophobic iron removaling processing system and method |
| CN107814446A (en) * | 2017-12-02 | 2018-03-20 | 天津海普尔膜科技有限公司 | A kind of electroplating wastewater integrative processing equipment |
| CN107879558A (en) * | 2017-12-02 | 2018-04-06 | 天津海普尔膜科技有限公司 | A kind of river course black and odorous water tubular membrane MBR processing equipments |
| CN109354250A (en) * | 2018-11-20 | 2019-02-19 | 湖北中嘉新材料有限公司 | A kind of high temperature pressure condensed water oil-removing removes iron reuse technology and system |
| CN109665655A (en) * | 2019-01-08 | 2019-04-23 | 华电电力科学研究院有限公司 | A kind of power plant's precision processing system |
-
2009
- 2009-12-25 CN CN 200910260224 patent/CN102107101B/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102641615A (en) * | 2012-03-30 | 2012-08-22 | 江苏华杉环保科技有限公司 | Cross-flow ceramic film filter test device |
| CN103349859A (en) * | 2013-04-22 | 2013-10-16 | 天津滨瀚环保科技发展有限公司 | Ceramic filter apparatus for separating calcium carbonate solution, and process thereof |
| CN103933779A (en) * | 2014-04-29 | 2014-07-23 | 江苏省电力设计院 | Protective device of filter element type high-temperature iron removing filter |
| CN103933779B (en) * | 2014-04-29 | 2016-04-20 | 中国能源建设集团江苏省电力设计院有限公司 | For the protective device of filter element formula high-temperature iron removing filter |
| CN107555541A (en) * | 2017-09-04 | 2018-01-09 | 大唐东北电力试验研究所有限公司 | Thermal power plant's low plus hydrophobic iron removaling processing system and method |
| CN107555541B (en) * | 2017-09-04 | 2024-01-05 | 大唐东北电力试验研究所有限公司 | Low-water-adding, water-draining and iron-removing treatment system and method for thermal power plant |
| CN107814446A (en) * | 2017-12-02 | 2018-03-20 | 天津海普尔膜科技有限公司 | A kind of electroplating wastewater integrative processing equipment |
| CN107879558A (en) * | 2017-12-02 | 2018-04-06 | 天津海普尔膜科技有限公司 | A kind of river course black and odorous water tubular membrane MBR processing equipments |
| CN109354250A (en) * | 2018-11-20 | 2019-02-19 | 湖北中嘉新材料有限公司 | A kind of high temperature pressure condensed water oil-removing removes iron reuse technology and system |
| CN109354250B (en) * | 2018-11-20 | 2022-04-01 | 湖北中嘉新材料有限公司 | High-temperature pressure condensed water oil-removing iron-removing recycling process and system |
| CN109665655A (en) * | 2019-01-08 | 2019-04-23 | 华电电力科学研究院有限公司 | A kind of power plant's precision processing system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102107101B (en) | 2013-04-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102107101B (en) | High-temperature condensed water recycling and purifying system with ceramic membrane filter | |
| CN103525887B (en) | A kind of crystalline dextrose production method of energy-conserving and environment-protective | |
| CN106219895A (en) | A kind of water treatment facilities utilizing fume afterheat and method for treating water | |
| CN108128827A (en) | A kind of vacuum evaporation equipment | |
| CN204824404U (en) | Tar aqueous ammonia separation clean system | |
| CN100400427C (en) | Process of treating and utilizing acid waste water containing heavy metal | |
| CN201971688U (en) | Silicon and oil removing system for oily sewage | |
| CN207046880U (en) | Hydrochloric acid pickling waste liquor recovery and processing system | |
| CN103172191A (en) | Whole coal chemical industry plant condensate water processing system | |
| CN107854857B (en) | Multi-pass concentration and purification device and using method thereof | |
| CN202490504U (en) | Purification recovery device of mercerizing waste alkali liquor | |
| CN206108988U (en) | Utilize water treatment facilities of power plant's waste heat | |
| CN202101561U (en) | Circulatory purification cooling system for electric smelting furnace | |
| CN208791402U (en) | A kind of stainless steel cleaning containing acid wastewater zero discharge waste water unit equipment | |
| CN102416297A (en) | Technical method for recovering waste alkali liquor with composite ceramic membrane in washing of beer bottles | |
| CN108970234A (en) | A kind of photovoltaic laminating machine pumping fluid filtration system | |
| CN220907310U (en) | Emulsion liquid film concentration evaporation disposal system | |
| CN204265570U (en) | Water of condensation deironing filter | |
| CN219317015U (en) | Overflow water recovery system for vacuum pump steam-water separator | |
| CN219023851U (en) | Tail gas steam-water separation recycling device for condensate water tank | |
| CN104843897B (en) | A kind of except aluminum filter | |
| CN114988510B (en) | Total heat recovery static sewage evaporation dryer | |
| CN219058765U (en) | Phenol-containing wastewater treatment system | |
| CN213707798U (en) | Dyeing wastewater reclaimed water recycling device | |
| CN209809917U (en) | Be used for coal-fired steam power plant boiler flue gas demercuration purifier |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20180110 Address after: 100093 North Pao kiln No. 9, Haidian District, Beijing Patentee after: BEIJING ZHAOXIN LVNENG TECHNOLOGY CO.,LTD. Address before: 104218 Beijing Xiangshan 9322 mailbox Patentee before: Yin Weijiang |
|
| CP01 | Change in the name or title of a patent holder |
Address after: 100093 North Pao kiln No. 9, Haidian District, Beijing Patentee after: Beijing Zhongnai Science and Technology Co.,Ltd. Address before: 100093 North Pao kiln No. 9, Haidian District, Beijing Patentee before: BEIJING ZHAOXIN LVNENG TECHNOLOGY CO.,LTD. |
|
| CP01 | Change in the name or title of a patent holder | ||
| DD01 | Delivery of document by public notice |
Addressee: Lou Junjie Document name: Patent termination notice |
|
| DD01 | Delivery of document by public notice | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130410 Termination date: 20211225 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |