CN201896103U - Process condensed water processing system - Google Patents
Process condensed water processing system Download PDFInfo
- Publication number
- CN201896103U CN201896103U CN2010206404063U CN201020640406U CN201896103U CN 201896103 U CN201896103 U CN 201896103U CN 2010206404063 U CN2010206404063 U CN 2010206404063U CN 201020640406 U CN201020640406 U CN 201020640406U CN 201896103 U CN201896103 U CN 201896103U
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- water
- filter
- pipe
- activated charcoal
- wash
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Abstract
The utility model relates to a condensed water processing system, belonging to the technical field of implementation of water processing. The condensed water processing system comprises a surface condensate liquid filter, an activated carbon filter, a precision filter and a flushing water manifold, wherein the flushing water manifold is used for introducing flushing water for flushing the surface condensate liquid filter, the activated carbon filter and the precision filter, the water inlet at the lower part of the surface condensate liquid filter is connected with a process condensed water introducing pipe, the water outlet at the upper part of the surface condensate liquid filter is connected with the water inlet pipe of the activated carbon filter, the water outlet at the lower part of the activated carbon filter is connected with the water inlet pipe of the precision filter, the water outlet at the upper part of the precision filter is connected with the process condensed water introducing pipe, the flushing water manifold is provided with a first front-flushing branch pipe, a second front-flushing branch pipe and a third front-flushing branch pipe, the first front-flushing branch pipe is connected with the water outlet pipe of the condensate liquid filter, the second front-flushing branch pipe is connected with the water inlet pipe of the activated carbon filter, the third front-flushing branch pipe is connected with a process condensed water outlet pipe, and the activated carbon filter is arranged between the surface condensate liquid filter and the precision filter. The condensed water processing system has the advantages that not only are water resources saved, but also energy sources are saved.
Description
Technical field
The utility model belongs to water treatment technical application field, be specifically related to a kind of technology condensate polishing system, be applied to such as petrochemical complex, medication chemistry or oil refining industry, be back in the production after various hydrocarbons contained in the technology condensed water, high volence metal ion, organism, suspended substance and/or wet goods are removed.
Background technology
As the industry's knowledge of the reason, in the past, because it is just have aforesaid oil (oil slick and floating carburetion), hydrocarbons, high volence metal ion, organism and/or suspended substance etc. in the technology condensed water that enterprises such as petrochemical complex and medication chemistry are produced in the process of producing product, thereby usually that this technology condensed water is discarded.Yet, in recent years, along with people's significantly improving to energy conservation consciousness and water resources protection consciousness; the recycling of technology condensed water more and more comes into one's own; correspondingly, the technology condensate polishing system is favored by industry, and can be seen in disclosed patent documentation.
The condensed water precision processing system that Chinese invention patent application publication number CN101530684A recommends is regulated the shop film thickness that is located at the filter element top in the strainer by adjustable baffle plate is set, and improves the treatment effect of strainer with the quality that ensures the shop film.But, because being single-stage, this scheme filters, therefore be difficult to make the treatment effect of the technology condensed water of aforementioned circumstances to show gratifying degree.The technical scheme that CN2404870Y provides (a kind of process unit of condensed water oil removing) only is suitable for removing the oil in the technology condensed water, has the fastidious property on the purposes.
Summary of the invention
Task of the present utility model be to provide a kind of help with hydrocarbons, high volence metal ion, organism, suspended substance and/or wet goods once effectively overall treatment and nationality to satisfy the technology condensate polishing system of reuse requirement.
Task of the present utility model is finished like this, a kind of technology condensate polishing system, comprise the surface condensation liquid filter, activated charcoal filter, accurate filter and being used for to described surface condensation liquid filter, activated charcoal filter and accurate filter are implemented flushing and the wash-down water house steward of introducing wash-down water, the lower water inlet of described surface condensation liquid filter is connected with technology condensed water inlet tube by the phlegma filter inleting pipe, and the top water outlet of surface condensation liquid filter is connected with the activated charcoal filter water inlet pipe of the top water-in of described activated charcoal filter by the phlegma filter outlet pipe, and the bottom water outlet of activated charcoal filter is connected with the accurate filter water inlet pipe of the lower water inlet of described accurate filter by the activated charcoal filter rising pipe, the top water outlet of the accurate filter technology condensed water inlet tube that continues, described wash-down water house steward has first, second arm and the 3rd arm of just washing by water of just washing by water, first arm of just washing by water is connected with described phlegma filter outlet pipe, second arm of just washing by water is connected with described activated charcoal filter water inlet pipe, and the 3rd arm of just washing by water is connected with described technology condensed water fairlead, and described activated charcoal filter is between surface condensation liquid filter and accurate filter.
In a specific embodiment of the present utility model, also be connected with first on the described wash-down water house steward, the second recoil water arm and the 3rd recoil water arm, the first recoil water arm is connected with described phlegma filter inleting pipe, the second recoil water arm is connected with described activated charcoal filter rising pipe, and described the 3rd recoil water arm is connected with described accurate filter water inlet pipe, and on described phlegma filter outlet pipe, be connected with one first wash-down water fairlead, on described activated charcoal filter water inlet pipe, be connected with one second wash-down water fairlead, on described technology condensed water fairlead, be connected with one the 3rd wash-down water fairlead.
In another specific embodiment of the present utility model, also be connected with one first pressurized air inlet tube on the described phlegma filter outlet pipe, this first pressurized air inlet tube is connected with pneumatic manifold, also be connected with one second pressurized air inlet tube on the described activated charcoal filter water inlet pipe, this second pressurized air inlet tube is connected with pneumatic manifold, also be connected with one the 3rd pressurized air inlet tube on the described technology condensed water fairlead, the 3rd pressurized air inlet tube is connected with pneumatic manifold.
The technical scheme that the utility model provides is owing to adopted the combination of surface condensation liquid filter, activated charcoal filter and accurate filter, thereby by oil slick and the oil in water emulsion in the surface condensation liquid filter removal technology condensed water, and remove high volence metal ion and suspended substance etc., by the organism in the activated charcoal filter removal technology condensed water, and then by the smart filter of accurate filter, make the technology condensed water reach the water quality requirement that enters the boiler reuse, both embodied the conserve water resource, embody save energy again.
Description of drawings
Fig. 1 is example structure of the present utility model and application examples synoptic diagram.
Embodiment
For the auditor that the makes Patent Office especially public can be expressly understood technical spirit of the present utility model and beneficial effect more, the applicant is described in more detail in the mode of embodiment below, but embodiment is not the restriction to the technical solution of the utility model.
Ask for an interview Fig. 1, provided the surface condensation strainer 1, activated charcoal filter 2 and the accurate filter 3 that are arranged in order and connect each other, wherein, activated charcoal filter 2 is between surface condensation liquid filter 1 and accurate filter 3.
The lower water inlet of surface condensation liquid filter 1 is connected with technology condensed water inlet tube 5 from the technology condensed water that is produced in the production process by phlegma filter inleting pipe 11, and the phlegma filter outlet pipe 12 of surface condensation liquid filter 1 is connected with the activated charcoal filter water inlet pipe 21 of the top water-in of activated charcoal filter 2, and on the pipeline of this activated charcoal filter water inlet pipe 21, be equipped with first valve 213 and second valve 214, the bottom water outlet of this activated charcoal filter 2 is connected with the accurate filter water inlet pipe 31 of the lower water inlet of accurate filter 3 by activated charcoal filter rising pipe 22, and the pipeline at this activated charcoal filter rising pipe 22 is equipped with the 3rd valve 221 and the 4th valve 222, the top water outlet of accurate filter 3 connects technology condensed water rising pipe 32, and is equipped with the 5th valve 323 on this technology condensed water rising pipe 32.
It is the disclosed middle water-freeing arrangement structure of utility model patent ZL200820236958.0 that filter core in the aforesaid surface condensation liquid filter 1 preferably uses by Chinese invention patent application publication number CN101480546A, the disclosed filtration device structure of aforesaid accurate filter 3 preferred employing Chinese patent ZL200710019210.5, and the filter core for precision filter that used filter core excessively preferentially uses ZL200920255310.2 to disclose in this accurate filter 3.
Be used for surperficial phlegma strainer 1, activated charcoal filter 2 and accurate filter 3 provide on the wash-down water house steward 4 of wash-down water (just washing and back flushing) and are connected with first, the second positive wash-down water arm 41, the 42 and the 3rd positive wash-down water arm 43, the first positive wash-down water arm 41 is connected with aforesaid phlegma filter outlet pipe 12, and the first positive wash-down water arm 41 is provided with the 6th valve 411, the second positive wash-down water arm 42 is connected with aforesaid activated charcoal filter water inlet pipe 21, and on the pipeline of this second positive wash-down water arm 42, be equipped with the 7th valve 421, the 3rd positive wash-down water arm 43 is connected with aforesaid technology condensed water rising pipe 32, and is provided with the 8th valve 431 on the pipeline of the 3rd positive wash-down water arm 43.In addition, on phlegma filter outlet pipe 12, be connected with one first wash-down water inlet tube 121, on the pipeline of this first wash-down water fairlead 121, be equipped with the 9th valve 1211, and be connected with one first pressurized air inlet tube 122 on the first wash-down water fairlead 121, the first pressurized air inlet tube 122 is connected with pneumatic manifold 6, and is equipped with 1 the tenth valve 1221 on pipeline.On activated charcoal filter water inlet pipe 21, be connected with one second wash-down water fairlead 211, on the pipeline of the second wash-down water fairlead 211, be provided with the 11 valve 2111, and on the second wash-down water fairlead 211, be connected with one second pressurized air inlet tube 212, this second pressurized air inlet tube 212 is connected with pneumatic manifold 6, and is furnished with the 12 valve 2121 on the pipeline of the second pressurized air inlet tube 212.On technology condensed water fairlead 32, be connected with one the 3rd wash-down water fairlead 321, the pipeline of the 3rd wash-down water fairlead 321 is provided with the 13 valve 3211, and on the 3rd wash-down water fairlead 321, be connected with one the 3rd pressurized air inlet tube 322, the 3rd pressurized air inlet tube 322 is connected with pneumatic manifold 6, and is furnished with 1 the 14 valve 3221.
On aforesaid wash-down water house steward 4, be connected with first a recoil water arm 44 of being furnished with the 15 valve 441, this first recoil water arm 44 is connected with aforesaid phlegma filter inleting pipe 11, also be connected with the second recoil water arm 45 of 1 the 16,17 valve 451,452 on wash-down water house steward 4, this second recoil water arm 45 is connected with aforesaid activated charcoal filter water inlet pipe 21; On wash-down water house steward 4 and then be connected with the 3rd recoil water arm 46, the three recoil water arms 46 of being furnished with the 18 valve 461 and the 19 valve 462 and be connected with aforesaid accurate filter water inlet pipe 31.On the pipeline of aforesaid technology condensed water inlet tube 5, be furnished with the 20 valve 51 and the 21 valve 52.
Apply for below narrating principle of work of the present utility model in conjunction with Fig. 1, in the time will handling to the technology condensed water, open the 20, first, second, the 3rd, the 4th valve 51,213,214,221, the 222 and the 5th valve 323, all the other valves are all closed, the technology condensed water enters 1 filtration of surface condensation liquid filter from technology condensed water inlet tube 5 through the 20 valve 51 and phlegma filter inleting pipe 11, filter after phlegma filter outlet pipe 12, first, second valve 213,214 and activated charcoal filter water inlet pipe 21 enter activated charcoal filter 2 and filter, filter after activated charcoal filter rising pipe 22, the 3rd valve 221, the 4th valve 222 and accurate filter water inlet pipe 31 enter accurate filter 3 and filter, filter after technology condensed water rising pipe 32 and the 5th valve 323 are drawn reuse, for example introduce the boiler reuse.Filter owing to passed through three roads, the water quality of the therefore filtering technology condensed water that remains reuse can reach the reuse requirement fully.
In the time will implementing flushing to aforesaid surface condensation liquid filter 1, activated charcoal filter 2 and accurate filter 3, enable wash-down water house steward 5 so, by schematic structure as can be known, flushing has comprised just washes and back flushing, before just washing, carry out back flushing earlier, enter square impact after back flushing finishes and wash.
The process of back flushing is: with regard to the strainer 1 of surface condensation, open the 15 valve 441 on the first wash-down water arm 44 that is connected with wash-down water house steward 5, backwashing water self-condensation liquid filter water inlet pipe 11 enters surface condensation liquid filter 1, and then draw through the phlegma filter outlet pipe 12 and the first wash-down water fairlead 121, the 9th valve 1211 on the pipeline of the first wash-down water fairlead 121 is opened, the first pressurized air inlet tube 122 through being connected with pneumatic manifold 6 in back flushing is introduced pressurized air (also can claim compress wind or compressed gas), and the tenth valve 1221 of this moment is opened; With regard to activated charcoal filter 2, open the 16 valve 451 on the second backwashing water arm 45 that is connected with wash-down water house steward 5, backwashing water enters activated charcoal filter 2 from activated charcoal filter rising pipe 22, and then draw through the activated charcoal filter water inlet pipe 21 and the second wash-down water fairlead 211, the 11 valve 2111 on the pipeline of the second wash-down water fairlead 211 is opened, in back flushing, introduce pressurized air by the second pressurized air inlet tube 212 under the 12 valve 2121 opened conditions; With regard to accurate filter 3, open the 18 valve 461, by the 3rd recoil water arm 46 that is connected with wash-down water house steward 4 backwashing water is entered accurate filter 3 through accurate filter water inlet pipe 31, and then the 3rd backwashing water fairlead 321 that warp is connected with industrial condensed water rising pipe 32 is drawn, the 13 valve 3211 on the pipeline of the 3rd backwashing water fairlead 321 is opened, in back flushing, introduce pressurized air by the 3rd pressurized air inlet tube 322 that the 14 valve 3221 is under the opened condition.In above-mentioned backwash process, all NM valves all are in closing condition, after back flushing finishes, just enter and wash.
The process of just washing is: with regard to surface condensation liquid filter 1 and for, open the 6th valve 411, wash-down water enters surface condensation liquid filter 1 through first just washing by water arm 41 and the phlegma filter outlet pipe 12, draws through phlegma filter inleting pipe 11 again, opens the 21 valve 52 this moment; With regard to activated charcoal filter 2, open the 7th valve 421, wash-down water enters in the activated charcoal filter 2 through second just washing by water arm 42 and the activated charcoal filter water inlet pipe 21, draws through activated charcoal filter rising pipe 22 again, at this moment, opens the 17 valve 452; With regard to accurate filter 3, open the 8th valve 431, wash-down water enters in the accurate filter 3 through the 3rd just washing by water arm 43 and technology condensed water rising pipe 32, draws through accurate filter water inlet pipe 31 again, opens the 19 valve 462 this moment.In above-mentioned positive flushing process, all NM valves all are in closing condition.
Claims (3)
1. technology condensate polishing system, it is characterized in that comprising surface condensation liquid filter (1), activated charcoal filter (2), accurate filter (3) and being used for to described surface condensation liquid filter (1), activated charcoal filter (2) and accurate filter (3) are implemented flushing and the wash-down water house steward (4) of introducing wash-down water, the lower water inlet of described surface condensation liquid filter (1) is connected with technology condensed water inlet tube (5) by phlegma filter inleting pipe (11), and the top water outlet of surface condensation liquid filter (1) is connected with the activated charcoal filter water inlet pipe (21) of the top water-in of described activated charcoal filter (2) by phlegma filter outlet pipe (12), and the bottom water outlet of activated charcoal filter (2) is connected with the accurate filter water inlet pipe (31) of the lower water inlet of described accurate filter (3) by activated charcoal filter rising pipe (22), the top water outlet of accurate filter (3) the technology condensed water inlet tube (32) that continues, described wash-down water house steward (4) has first, second arm (41 of just washing by water, 42) and the 3rd arm (43) of just washing by water, first arm (41) of just washing by water is connected with described phlegma filter outlet pipe (12), second arm (42) of just washing by water is connected with described activated charcoal filter water inlet pipe (21), and the 3rd arm (43) of just washing by water is connected with described technology condensed water fairlead (32), and described activated charcoal filter (2) is positioned between surface condensation liquid filter (1) and the accurate filter (3).
2. technology condensate polishing system according to claim 1, it is characterized in that also being connected with first on the described wash-down water house steward (4), the second recoil water arm (44,45) and the 3rd the recoil water arm (46), the first recoil water arm (44) is connected with described phlegma filter inleting pipe (11), the second recoil water arm (45) is connected with described activated charcoal filter rising pipe (22), and described the 3rd recoil water arm (46) is connected with described accurate filter water inlet pipe (31), and on described phlegma filter outlet pipe (12), be connected with one first wash-down water fairlead (121), on described activated charcoal filter water inlet pipe (21), be connected with one second wash-down water fairlead (211), on described technology condensed water fairlead (32), be connected with one the 3rd wash-down water fairlead (321).
3. technology condensate polishing system according to claim 1, it is characterized in that also being connected with on the described phlegma filter outlet pipe (12) one first pressurized air inlet tube (122), this first pressurized air inlet tube (13) is connected with pneumatic manifold (6), also be connected with one second pressurized air inlet tube (212) on the described activated charcoal filter water inlet pipe (21), this second pressurized air inlet tube (212) is connected with pneumatic manifold (6), also be connected with one the 3rd pressurized air inlet tube (322) on the described technology condensed water fairlead (32), the 3rd pressurized air inlet tube (322) is connected with pneumatic manifold (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206404063U CN201896103U (en) | 2010-12-03 | 2010-12-03 | Process condensed water processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206404063U CN201896103U (en) | 2010-12-03 | 2010-12-03 | Process condensed water processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201896103U true CN201896103U (en) | 2011-07-13 |
Family
ID=44254017
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010206404063U Expired - Lifetime CN201896103U (en) | 2010-12-03 | 2010-12-03 | Process condensed water processing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201896103U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102091480A (en) * | 2010-12-03 | 2011-06-15 | 常熟市华能水处理设备有限责任公司 | System for treating process condensed water |
| CN103482779A (en) * | 2013-09-27 | 2014-01-01 | 常熟市华能水处理设备有限责任公司 | Process condensation water treatment system |
-
2010
- 2010-12-03 CN CN2010206404063U patent/CN201896103U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102091480A (en) * | 2010-12-03 | 2011-06-15 | 常熟市华能水处理设备有限责任公司 | System for treating process condensed water |
| CN103482779A (en) * | 2013-09-27 | 2014-01-01 | 常熟市华能水处理设备有限责任公司 | Process condensation water treatment system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20110713 Effective date of abandoning: 20130306 |
|
| RGAV | Abandon patent right to avoid regrant |