CN201250153Y - Boiler feed water full-film treatment testing device - Google Patents
Boiler feed water full-film treatment testing device Download PDFInfo
- Publication number
- CN201250153Y CN201250153Y CN 200820025607 CN200820025607U CN201250153Y CN 201250153 Y CN201250153 Y CN 201250153Y CN 200820025607 CN200820025607 CN 200820025607 CN 200820025607 U CN200820025607 U CN 200820025607U CN 201250153 Y CN201250153 Y CN 201250153Y
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- Prior art keywords
- reverse osmosis
- water tank
- filtration
- water
- clarification
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- Expired - Lifetime
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 66
- 238000012360 testing method Methods 0.000 title claims abstract description 24
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 44
- 238000001914 filtration Methods 0.000 claims abstract description 16
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 14
- 239000000126 substance Substances 0.000 claims abstract description 13
- 238000001728 nano-filtration Methods 0.000 claims abstract description 7
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 20
- 230000000630 rising effect Effects 0.000 claims description 20
- 229910052708 sodium Inorganic materials 0.000 claims description 20
- 239000011734 sodium Substances 0.000 claims description 20
- 238000005352 clarification Methods 0.000 claims description 19
- 238000001471 micro-filtration Methods 0.000 claims description 17
- 239000003814 drug Substances 0.000 claims description 10
- 238000013019 agitation Methods 0.000 claims description 6
- 230000015271 coagulation Effects 0.000 claims description 6
- 238000005345 coagulation Methods 0.000 claims description 6
- 229940079593 drug Drugs 0.000 claims description 6
- 238000010992 reflux Methods 0.000 claims description 4
- 239000004576 sand Substances 0.000 claims description 4
- 235000014347 soups Nutrition 0.000 claims description 3
- 238000004088 simulation Methods 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 5
- 238000004458 analytical method Methods 0.000 description 4
- 239000012528 membrane Substances 0.000 description 3
- 230000000295 complement effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses an industrial flow simulation control testing device, in particular to a boiler feed water full-film treatment testing device, which comprises a chemical pre-treating device, a multi-medium filtering and treating device, a micro-filtering device, an ultra-filtration device, a reverse osmosis device, a second-level reverse osmosis device and a nano-filtration device; wherein, all the devices can be optionally combined so as to facilitate the simulation of the treating devices and the combination of the devices. The utility model provides a boiler feed water full-film treatment testing device capable of effectively assessing the use value and the benefits of the combination of various boiler feed water film treating equipment.
Description
(1) technical field
The utility model relates to a kind of industrial flow simulation control test device, specifically relates to the full film Processing Test of a kind of oiler feed device.
(2) background technology
In recent years, along with more and more stricter to the restriction of process water, especially in the water shortage in north china area, the water price increases day by day, brings heavy economical load for a large amount of water enterprise, and therefore its enterprise competitiveness also descends.Along with rising steadily of water price, further strengthen water conservation and seem and become more and more important.With utilizing again after the processing of recirculated cooling water sewer,, be a major technique direction of water unit's water conservation as boiler feedwater.Because membrane technology has compact construction, floor space is little, strong to raw water quality adaptability, and characteristics such as stable effluent quality, environmental protection are applied to obtain common recognition in the boiler feedwater preparation.But recirculated water sewer treatment technology still is in the starting stage at present technically, and recirculated water sewer water quality complexity, can adopt full membrane technology well export obtains, perhaps to what extent obtain required qualified water, if simple dependency analysis reasoning, then actual application value is little.If have defective in the technical process of engineering design, behind the last practical project equipment, technology and the economic quality in combination can't realize contrast to different process flow process and various membrane technique, and then runing risk can increase undoubtedly greatly.The more important thing is that because the oiler feed equipment scale is bigger, the cost that equipment is transformed or changed is huge, and influences ordinary production.
(3) summary of the invention
The utility model is at present at water treatment field, especially do not assess the present situation of the testing apparatus of the use value of various oiler feed film treatment facilities combination and benefit in the oiler feed industry, provide a kind of and can effectively assess the use value of various oiler feed film treatment facilities combinations and the full film Processing Test of the oiler feed device of benefit.
The technical solution adopted in the utility model is:
The full film Processing Test of the utility model oiler feed device, comprise Chemical Pretreatment device, multi-medium filtering treatment unit, micro-filtration, ultra-filtration equipment, reverse osmosis unit, two-pass reverse osmosis device and sodium filter device, wherein: the Chemical Pretreatment device comprises inlet channel, be arranged on the drug feeding pipeline on this pipeline and be arranged at the compressed air line on its coagulation agitation vat top, and outlet conduit is connected to the clarification water tank, and this clarification radiator drain then joins with described multi-medium filtering treatment unit water-in; Multi-medium filtering treatment unit water outlet is connected to the clarification water tank, micro-filtration and ultra-filtration equipment that this clarification water tank subordinate then is and connects, and both subordinates are connected to micro-filtration product water tank, ultrafiltered product water tank respectively, and two radiator drains also connect the back and join with sodium filter device or reverse osmosis unit described and that connect; Nanofiltration device one rising pipe is provided with and has sodium filter product rising pipe sodium filter product water tank; Reverse osmosis unit links to each other with described two-pass reverse osmosis device through intermediate water tank; Two-pass reverse osmosis device rising pipe is connected to the reverse osmosis product water tank that has reverse osmosis product rising pipe; Described micro-filtration and ultra-filtration equipment water-in and water-out pipeline are provided with control valve, and nanofiltration device and reverse osmosis unit water inlet pipe are provided with control valve.
The full film Processing Test of above-mentioned oiler feed device, described Chemical Pretreatment device comprise that clarification first reactor and the subordinate thereof of coagulation agitation vat subordinate clarify second reactor.The activated filter film device that described multi-medium filtering treatment unit is provided with and connects, extra large sand filter and more medium filter, three inlet tube and outlet tubes are provided with control valve.
The full film Processing Test of above-mentioned oiler feed device, described sodium filter device, reverse osmosis unit and two-pass reverse osmosis device are equipped with the soup reflux line.
The full film Processing Test of the utility model oiler feed device is incorporated into Chemical Pretreatment device, multi-medium filtering treatment unit, micro-filtration, ultra-filtration equipment, sodium filter device, reverse osmosis unit on the test platform by pipeline, wherein micro-filtration and ultra-filtration equipment and connect, and its water inlet pipe and water outlet pipe is provided with control valve, both can choose one wantonly in test, in like manner sodium filter device and reverse osmosis unit also can be chosen one wantonly, if selection reverse osmosis unit, its subordinate also is connected to the two-pass reverse osmosis device, can certainly only use reverse osmosis unit as required.As testing apparatus, itself scale is smaller, with respect to the mode of former reliable theoretical analysis or physical varification, save cost and shortened proving period, and in principle, each device all is to rely on principle of work in kind to make in the system, system is the object simulating operating mode effectively, and respectively installs each device of main phase, can arbitrary combination, can can finish the checking and the analysis of mass data in a short time, efficiency-cost ratio is than higher.Each testing apparatus subordinate all comprises a water tank simultaneously, naturally this product comprises the component of this grade equipment institute treating water, testing crew can take out and test, so the utility model can effectively carry out check analysis to each device of system and various various combination mode thereof.
(3) description of drawings
Fig. 1 is the utility model embodiment structural representation.
Among the figure: 1, compressed air line, 2, the Chemical Pretreatment device, 3, clarify second reactor, 4, outlet conduit, 5, the clarification water tank, 6, micro-filtration, 7, rising pipe, 8, micro-filtration product water tank, 9, middle Send out pump, 10, control valve, 11, the ultrafiltered product water tank, 12, ultra-filtration equipment, 13, rising pipe, 14, sodium filter product water tank, 15, sodium filter product rising pipe, 16, medicine is washed water return pipeline, and 17, intermediate water tank, 18, medicine is washed water return pipeline, 19, rising pipe, 20, reverse osmosis product water tank, 21, reverse osmosis product rising pipe, 22, medicine is washed reflux line, 23, the two-pass reverse osmosis device, 24, reverse osmosis unit, 25, the sodium filter device, 26, the activated filter film device, 27, the sea sand filter, 28, more medium filter, 29, the multimedium treatment unit, 30, inlet channel, 31, drug feeding pipeline, 32, outlet conduit, 33, the clarification water tank, 34, drug feeding pipeline, 35, inlet channel.
(4) embodiment
Specify structural principle of the present utility model below in conjunction with Figure of description:
With reference to explanation accompanying drawing 1, the full film Processing Test of this embodiment oiler feed device, comprise Chemical Pretreatment device 2, multi-medium filtering treatment unit 29, micro-filtration 6, ultra-filtration equipment 12, sodium filter device 25, reverse osmosis unit 24 and two-pass reverse osmosis device 23, wherein the Chemical Pretreatment device comprises inlet channel 30, be arranged on drug feeding pipeline 31 and the compressed air line 1 that is arranged at its coagulation agitation vat top on this pipeline, and outlet conduit 4 is connected to clarification water tank 5, also be provided with control valve between the two, this clarification radiator drain then joins with described multi-medium filtering treatment unit water-in.
Multi-medium filtering treatment unit water outlet is connected to clarification water tank 33, micro-filtration and ultra-filtration equipment that this clarification water tank subordinate then is and connects, and both subordinates are connected to micro-filtration product water tank 8, ultrafiltered product water tank 11 respectively, transferpump in the middle of both rising pipes are provided with, a pair of system carries out supercharging, two water tanks, 11 rising pipes and connect the back with and the described sodium filter device and the reverse osmosis unit that connect join, and the clarification water tank of both its water outlets is provided with one at least.
Nanofiltration device one rising pipe 13 is provided with and has sodium filter product rising pipe 15 sodium filter product water tank 14; Reverse osmosis unit links to each other with described two-pass reverse osmosis device through intermediate water tank.
Two-pass reverse osmosis device rising pipe 19 is connected to the reverse osmosis product water tank 20 that has reverse osmosis product rising pipe 21.
Described micro-filtration and ultra-filtration equipment water-in and water-out pipeline, nanofiltration device and reverse osmosis unit water inlet pipe, be provided with control valve, so that system's control and each device are selected as required.
But in order to obtain reasonable result, so that be complementary with physical device, described Chemical Pretreatment device 2 comprises that clarification first reactor of coagulation agitation vat subordinate and subordinate thereof clarify second reactor 3.
In like manner in order better to verify the performance perameter of each equipment in the multi-medium filtering treatment unit, the activated filter film device 26 that described multi-medium filtering treatment unit 29 is provided with and connects, extra large sand filter 27 and 28, three inlet tube and outlet tubes of more medium filter are provided with control valve.
For system because of the processing mode difference, needed medicine is also different, clarification water tank 33 is provided with drug feeding pipeline 34 to the pipeline of micro-filtration and ultra-filtration equipment, other install also the same with the physical device chemicals dosing plant that is provided with, simultaneously, described sodium filter device 25, reverse osmosis unit 24 and two-pass reverse osmosis device 23 are equipped with the soup reflux line.
Claims (4)
1. the full film Processing Test of oiler feed device, it is characterized in that: comprise Chemical Pretreatment device (2), multi-medium filtering treatment unit (29), micro-filtration (6), ultra-filtration equipment (12), sodium filter device (25), reverse osmosis unit (24) and two-pass reverse osmosis device (23), wherein:
The Chemical Pretreatment device comprises middle water inlet channel (30), be arranged on the drug feeding pipeline (31) on this pipeline and be arranged at the high-pressure air pipeline (1) on its coagulation agitation vat top, and outlet conduit (4) is connected to clarification water tank (5), and this clarification radiator drain then joins with described multi-medium filtering treatment unit water-in;
Multi-medium filtering treatment unit water outlet is connected to clarification water tank (33), micro-filtration and ultra-filtration equipment that this clarification water tank subordinate then is and connects, and both subordinates are connected to micro-filtration product water tank (8), ultrafiltered product water tank (11) respectively, and two radiator drains also connect the back and join with sodium filter device and reverse osmosis unit described and that connect;
Nanofiltration device one rising pipe (13) is provided with and has sodium filter product rising pipe (15) sodium filter product water tank (14); Reverse osmosis unit links to each other with described two-pass reverse osmosis device through intermediate water tank;
Two-pass reverse osmosis device rising pipe (19) is connected to the reverse osmosis product water tank (20) that has reverse osmosis product rising pipe (21);
Described micro-filtration and ultra-filtration equipment water-in and water-out pipeline are provided with control valve, and nanofiltration device and reverse osmosis unit water inlet pipe are provided with control valve.
2. the full film Processing Test of oiler feed according to claim 1 device is characterized in that: described Chemical Pretreatment device (2) comprises that clarification first reactor of coagulation agitation vat subordinate and subordinate thereof clarify second reactor (3).
3. the full film Processing Test of oiler feed according to claim 1 device, it is characterized in that: the activated filter film device (26) that described multi-medium filtering treatment unit (29) is provided with and connects, extra large sand filter (27) and more medium filter (28), three inlet tube and outlet tubes are provided with control valve.
4. according to the full film Processing Test of the described oiler feed of one of claim 1 to 3 device, it is characterized in that: described sodium filter device (25), reverse osmosis unit (24) and two-pass reverse osmosis device (23) are equipped with the soup reflux line.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200820025607 CN201250153Y (en) | 2008-07-11 | 2008-07-11 | Boiler feed water full-film treatment testing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200820025607 CN201250153Y (en) | 2008-07-11 | 2008-07-11 | Boiler feed water full-film treatment testing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201250153Y true CN201250153Y (en) | 2009-06-03 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200820025607 Expired - Lifetime CN201250153Y (en) | 2008-07-11 | 2008-07-11 | Boiler feed water full-film treatment testing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201250153Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102320706A (en) * | 2011-07-08 | 2012-01-18 | 上海希沃环境科技有限公司 | System for deep recovery and treatment of coking wastewater biochemical effluent |
| CN107638809A (en) * | 2017-11-06 | 2018-01-30 | 哈尔滨工业大学水资源国家工程研究中心有限公司 | The multipurpose drinking water film piece-rate system of Driven by Solar Energy and the method using system processing polluted surface water and underground water |
-
2008
- 2008-07-11 CN CN 200820025607 patent/CN201250153Y/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102320706A (en) * | 2011-07-08 | 2012-01-18 | 上海希沃环境科技有限公司 | System for deep recovery and treatment of coking wastewater biochemical effluent |
| CN107638809A (en) * | 2017-11-06 | 2018-01-30 | 哈尔滨工业大学水资源国家工程研究中心有限公司 | The multipurpose drinking water film piece-rate system of Driven by Solar Energy and the method using system processing polluted surface water and underground water |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: STATE ELECTRIC NET CROP. Free format text: FORMER OWNER: SHANDONG RESEARCH INST. OF ELECTRIC POWER Effective date: 20130508 Owner name: SHANDONG RESEARCH INST. OF ELECTRIC POWER Effective date: 20130508 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 250002 JINAN, SHANDONG PROVINCE TO: 100000 XICHENG, BEIJING |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20130508 Address after: 100000 Xicheng District West Chang'an Avenue, No. 86, Beijing Patentee after: State Grid Corporation of China Patentee after: Shandong Research Inst. of Electric Power Address before: 250002 Ji'nan City Central District, Shandong, No. 2 South Road, No. 500 Patentee before: Shandong Research Inst. of Electric Power |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20090603 |