CN212864458U - Boiler makeup water deep desalination treatment system - Google Patents
Boiler makeup water deep desalination treatment system Download PDFInfo
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- CN212864458U CN212864458U CN202020853028.0U CN202020853028U CN212864458U CN 212864458 U CN212864458 U CN 212864458U CN 202020853028 U CN202020853028 U CN 202020853028U CN 212864458 U CN212864458 U CN 212864458U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 88
- 238000010612 desalination reaction Methods 0.000 title claims abstract description 26
- 239000011347 resin Substances 0.000 claims abstract description 30
- 229920005989 resin Polymers 0.000 claims abstract description 30
- 239000012528 membrane Substances 0.000 claims abstract description 27
- 238000000926 separation method Methods 0.000 claims abstract description 16
- 238000001223 reverse osmosis Methods 0.000 claims description 13
- 238000001471 micro-filtration Methods 0.000 claims description 5
- 238000000108 ultra-filtration Methods 0.000 claims description 5
- 239000003014 ion exchange membrane Substances 0.000 abstract description 3
- 238000003672 processing method Methods 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 28
- 230000008929 regeneration Effects 0.000 description 21
- 238000011069 regeneration method Methods 0.000 description 21
- 238000005342 ion exchange Methods 0.000 description 15
- 238000000034 method Methods 0.000 description 14
- 150000002500 ions Chemical class 0.000 description 8
- 230000008569 process Effects 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 7
- 230000009471 action Effects 0.000 description 6
- 238000002360 preparation method Methods 0.000 description 6
- 239000003456 ion exchange resin Substances 0.000 description 5
- 229920003303 ion-exchange polymer Polymers 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- 238000011033 desalting Methods 0.000 description 4
- 150000001450 anions Chemical class 0.000 description 3
- 239000002585 base Substances 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- 230000018109 developmental process Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000005684 electric field Effects 0.000 description 3
- 238000009296 electrodeionization Methods 0.000 description 3
- 238000011065 in-situ storage Methods 0.000 description 3
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 150000001768 cations Chemical class 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 235000003332 Ilex aquifolium Nutrition 0.000 description 1
- 241000209027 Ilex aquifolium Species 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000007728 cost analysis Methods 0.000 description 1
- 238000012864 cross contamination Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000002242 deionisation method Methods 0.000 description 1
- 238000000909 electrodialysis Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- -1 pretreatment Substances 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000012492 regenerant Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000012498 ultrapure water Substances 0.000 description 1
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- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The invention discloses a boiler feedwater deep desalination treatment system which comprises a raw water tank, a pretreatment module, a membrane separation module, a NEDI module and a water outlet tank, wherein the raw water tank, the pretreatment module, the membrane separation module, the NEDI module and the water outlet tank are sequentially connected; the NEDI modules comprise a primary NEDI module and a secondary NEDI module; the primary NEDI module and the secondary NEDI module have the same structure and are arranged in parallel; the primary NEDI module includes a pair of positive and negative electrodes, a mixed resin between the electrodes. A processing method of the system is also disclosed. The treatment system does not need an ion exchange membrane, so that the problems of membrane pollution and membrane scaling are avoided, and the treatment system has the advantages of simple device structure, convenience in operation, lower investment cost and the like.
Description
Technical Field
The invention relates to the technical field of water treatment, in particular to a boiler feedwater deep desalination treatment system.
Background
In the early stage, the deep desalination of boiler feedwater systems of power plants at home and abroad mainly adopts a 'yin-yang bed + mixed bed' mode, and in recent years, with the gradual maturity of membrane treatment technology, the 'RO + yin-yang bed + mixed bed' mode, the 'RO + mixed bed' mode and the like are gradually popularized and applied in power plants, the operation load of ion exchange resin is greatly reduced by the application of the membrane treatment technology, and the regeneration period is prolonged. Meanwhile, a deep desalination technology (EDI) which can replace a mixed bed is rapidly developed, and a full membrane process consisting of the EDI and an RO reverse osmosis unit is widely concerned. The conventional ion exchange technology and the electrodeionization technology (EDI) technology were studied and applied as follows.
Ion exchange technology
Both the anion bed and the mixed bed belong to ion exchange technology, which is realized by ion exchange between active groups on an ion exchanger and ions in a solution. In 1935 Adams and Holms synthesized ion exchange resins of the phenolic type, after which in 1945 Alelio developed strong acid resins of the styrene type and weak acid resins of the acrylic type, and by 1949 the development of mixed bed technology enabled the ion exchange process to be applied in the preparation of pure water. Through the development of half a century, the ion exchange technology has made remarkable progress in the aspects of resin type performance and water production process. The ion exchange process has the advantages of high stability, high exchange capacity, high effluent quality, small size, simple operation, low production cost, capacity of regenerating after being failed and capacity of reusing resin for long period. While having so many advantages, there are some problems with this approach. Firstly, the ion exchange resin needs to be regenerated by a large amount of acid and alkali, the utilization rate of the acid and alkali regenerant is low, the regenerated liquid cannot be discharged randomly, and pollution is easily caused. Secondly, the regeneration operation of the ion exchange resin is complex, particularly for the mixed bed resin, the anion and cation resin needs to be separated after layering, and cross contamination can be caused when the layering is difficult to be thorough. Currently, ion exchange technology is still one of the mainstream desalination processes for power plant chemical water preparation.
② electric deionization technology (EDI)
EDI technology is a new deep desalination technology that is receiving increasing attention. The technology organically combines electrodialysis and ion exchange, can realize continuous deep desalination under the non-chemical regeneration condition, and simultaneously obtains high-quality pure water and concentrated water with higher concentration, and is proved to be very effective in the field of high-purity water preparation.
A large number of engineering applications show that compared with the traditional ion exchange technology, the EDI technology has the advantages of good water quality of produced water, high water recovery utilization rate, high automatic control level, small occupied area, low environmental risk and the like, but also has the defects of high requirement on the quality of inlet water, high investment cost, short service life and the like, and the problems are related to the use of the ion exchange membrane.
Disclosure of Invention
In order to solve the problems, the invention discloses a boiler feedwater deep desalination treatment system and a method, and the treatment system avoids the problems of membrane pollution and membrane scaling because an ion exchange membrane is not needed, and has the advantages of simple device structure, convenient operation, lower investment cost and the like.
In order to achieve the above purpose, the invention provides the following technical scheme:
a boiler feedwater deep desalination treatment system comprises a raw water tank, a pretreatment module, a membrane separation module, a NEDI module and a water outlet tank, wherein the raw water tank, the pretreatment module, the membrane separation module, the NEDI module and the water outlet tank are sequentially connected; the NEDI modules comprise a primary NEDI module and a secondary NEDI module; the primary NEDI module and the secondary NEDI module have the same structure and are arranged in parallel; the primary NEDI module includes a pair of positive and negative electrodes, a mixed resin between the electrodes.
According to a further technical scheme, the NEDI modules comprise a plurality of groups, and each group of NEDI modules are arranged in parallel.
According to a further technical scheme, the NEDI module comprises 3 groups.
The further technical scheme of the invention is that the membrane separation module comprises a microfiltration device, an ultrafiltration device and a reverse osmosis device.
Also discloses a boiler feed water deep desalination treatment method, which comprises the following process steps:
firstly, boiler make-up water enters an original water tank and then enters a pretreatment module for pretreatment, wherein large-particle suspended matters, colloidal impurities and the like in the make-up water are mainly removed, and a pretreatment device is a sedimentation tank;
secondly, the pretreated boiler make-up water enters a membrane separation module for micro/ultrafiltration and reverse osmosis (primary or secondary) membrane separation treatment,
thirdly, boiler make-up water after membrane treatment enters an NEDI module, and the operation of the NEDI module is divided into two stages: the water preparation stage and the resin regeneration stage are alternately operated; in the water making stage, the electrodes are not electrified, the water making stage is ended, and the regeneration stage is started;
in the ion regeneration stage, direct current is applied to the failure resin layer, water molecules are quickly ionized under the action of an electric field to generate a large amount of H + and OH-ions, and the ion exchange balance is promoted to greatly move towards the regeneration reaction direction;
meanwhile, under the action of reverse recoil water flow, ions desorbed from the failed resin quickly migrate from the surface of the resin to a water phase and are discharged in a concentrated water form, so that the failed resin can be regenerated in situ;
and fourthly, the boiler make-up water enters the water outlet tank after being treated in the third step.
The invention has the following beneficial effects:
1. the boiler make-up water deep desalination treatment system does not need a regeneration environment-friendly process, and has stronger water quality adaptability.
2. The continuous operation can be realized, and the water production and the regeneration can be realized simultaneously;
3. the equipment is simple to operate, operate and maintain and operates fully automatically;
4. compared with the traditional anion-cation bed and an electric desalting EDI desalting system, the system saves an acid-base regeneration system or a chemical cleaning system, slightly saves the occupied area, can reduce the height of a factory building and saves the civil engineering cost;
5. the process of the system does not need acid-base regeneration and does not discharge acid-base wastewater.
Drawings
FIG. 1 is a schematic diagram of the operation of a water production stage;
FIG. 2 is a schematic diagram of the operation of the resin regeneration stage;
FIG. 3 is a schematic diagram of the operation of the NEDI system;
FIG. 4 is a process technology route of a makeup water treatment system of a power plant boiler;
FIG. 5 is a flow chart of the present invention.
Detailed Description
The present invention will be further illustrated with reference to the accompanying drawings and specific embodiments, which are to be understood as merely illustrative of the invention and not as limiting the scope of the invention.
Example 1
As shown in FIG. 5, the deep desalination treatment system for boiler makeup water comprises a raw water tank, a pretreatment module, a membrane separation module, a NEDI module and a water outlet tank.
The raw water tank, the pretreatment module, the membrane separation module, the NEDI module and the water outlet tank are sequentially connected; wherein the NEDI modules include a primary NEDI module and a secondary NEDI module; the primary NEDI module and the secondary NEDI module have the same structure and are arranged in parallel; the first-level NEDI module comprises a pair of positive and negative electrodes and mixed resin between the electrodes; the secondary NEDI module includes a pair of positive and negative electrodes, mixed resin between the electrodes.
Wherein, first order NEDI module, second grade NEDI module all include 3 groups, and every group NEDI module sets up in parallel.
Wherein, the membrane separation module comprises a microfiltration device, an ultrafiltration device and a reverse osmosis device.
Also discloses a treatment method of the boiler feedwater deep desalination treatment system, which comprises the following process steps:
firstly, boiler make-up water enters an original water tank and then enters a pretreatment module for pretreatment, wherein large-particle suspended matters, colloidal impurities and the like in the make-up water are mainly removed, and a pretreatment device is a sedimentation tank;
secondly, the pretreated boiler make-up water enters a membrane separation module for micro/ultrafiltration and reverse osmosis (primary or secondary) membrane separation treatment,
thirdly, boiler make-up water after membrane treatment enters an NEDI module, and the operation of the NEDI module is divided into two stages: the water preparation stage and the resin regeneration stage are alternately operated; in the water making stage, the electrodes are not electrified, the water making stage is ended, and the regeneration stage is started;
in the ion regeneration stage, direct current is applied to the failure resin layer, water molecules are quickly ionized under the action of an electric field to generate a large amount of H + and OH-ions, and the ion exchange balance is promoted to greatly move towards the regeneration reaction direction;
meanwhile, under the action of reverse recoil water flow, ions desorbed from the failed resin quickly migrate from the surface of the resin to a water phase and are discharged in a concentrated water form, so that the failed resin can be regenerated in situ;
and fourthly, the boiler make-up water enters the water outlet tank after being treated in the third step.
The specific implementation mode is as follows:
a comparison of the performance of the three deep desalination techniques, mixed bed, EDI and NEDI, is shown in Table 1. As can be seen from the table, compared with the traditional mixed bed, the NEDI technology is more environment-friendly and has higher automation degree; compared with EDI technology, NEDI has more advantages in investment cost, maintenance cost, no wastewater discharge, and has better adaptability to the requirement of inlet water quality. EDI intake generally requires second grade RO to produce water, which greatly limits the application and popularization of the technology in power plants, while NEDI can work normally under the condition of first grade RO to produce water, and the investment and operation cost are greatly reduced. In conclusion, the technical route adopted by the project is reasonable.
TABLE 1 comparison of technical Performance of Mixed bed, EDI and NEDI
As shown in fig. 4, the first generation and the second generation are conventional process flows in the prior art, and the third generation is the process flow of the present application. The process technical route of the power plant boiler make-up water treatment system is as follows:
by combining the current situation of the boiler feedwater deep desalination process, the technical route of the boiler feedwater deep desalination treatment system adopted by the invention is as follows: raw water, pretreatment, membrane separation, primary Reverse Osmosis (RO), primary deep electrodeionization (NEDI) and secondary deep electrodeionization (NEDI).
The boiler make-up water deep desalination treatment system has better advantages in the aspects of stability, safety, investment, running cost analysis and the like of a process system in the application of the boiler make-up water deep desalination treatment system in the preparation of chemical water of a large-scale power plant.
As shown in fig. 1 and 2, the working principle of the present invention is as follows: which is equivalent to regenerating the failed resin by current by utilizing an electrochemical desalting technology. The novel desalting module mainly comprises a pair of special positive and negative electrodes and mixed resin between the electrodes. The operation is divided into two stages: the water making stage and the resin stage are alternately operated. In the stage of water production, the electrodes are not electrified, and the novel desalination technology (NEDI) removes anions and cations in water by means of the strong exchange adsorption capacity of ion exchange resin like a common mixed bed. And when the resin is saturated and invalid and the quality of the produced water is reduced to a set value, ending the water production stage and entering an electric regeneration stage.
In the ion regeneration stage, direct current is applied to the failure resin layer, water molecules are quickly ionized under the action of an electric field to generate a large number of H + and OH-ions, and the ion exchange balance is promoted to be greatly moved towards the regeneration reaction direction.
Meanwhile, under the action of reverse recoil water flow, ions desorbed from the failed resin are rapidly transferred to a water phase from the surface of the resin and are discharged in a concentrated water form, and the failed resin can be regenerated in situ.
As shown in fig. 3, the NEDI system operates on the principle: the NEDI system is generally divided into a plurality of groups, each group runs in parallel, each group is formed by connecting a plurality of NEDII modules in parallel, when the NEDI system runs, the modules in each group can be sequentially regenerated in turn, the non-regeneration module can still produce water, the regeneration module stops producing water, concentrated water is discharged, and the concentrated water can be completely recycled to a Reverse Osmosis (RO) water inlet tank, so that the whole NEDI system can realize continuous and stable water production.
Technical route 2
For the chemical water desalination process, the ion exchange technology still dominates, but as the membrane technology becomes mature day by day, the application of the ion exchange technology is also popularized in a large amount, and the full membrane technology is expected to be the future development trend, and the EDI and NEDI technologies have wide market application prospects.
The technical means disclosed in the invention scheme are not limited to the technical means disclosed in the above embodiments, but also include the technical scheme formed by any combination of the above technical features. It should be noted that those skilled in the art can make various improvements and modifications without departing from the principle of the present invention, and such improvements and modifications are also considered to be within the scope of the present invention.
Claims (4)
1. The utility model provides a boiler makeup water advanced desalination processing system which characterized in that: the device comprises a raw water tank, a pretreatment module, a membrane separation module, an NEDI module and a water outlet tank, wherein the raw water tank, the pretreatment module, the membrane separation module, the NEDI module and the water outlet tank are sequentially connected; the NEDI modules comprise a primary NEDI module and a secondary NEDI module; the primary NEDI module and the secondary NEDI module have the same structure and are arranged in parallel; the primary NEDI module includes a pair of positive and negative electrodes, a mixed resin between the electrodes.
2. The system of claim 1, wherein the boiler feedwater deep desalination treatment system comprises: the NEDI modules comprise a plurality of groups, and each group of NEDI modules are arranged in parallel.
3. The system of claim 1, wherein the boiler feedwater deep desalination treatment system comprises: the NEDI modules include 3 sets.
4. The system of claim 1, wherein the boiler feedwater deep desalination treatment system comprises: the membrane separation module comprises a microfiltration device, an ultrafiltration device and a reverse osmosis device.
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| CN111762951A (en) * | 2020-05-20 | 2020-10-13 | 北京朗新明环保科技有限公司南京分公司 | Boiler feedwater deep desalination treatment system and method |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111762951A (en) * | 2020-05-20 | 2020-10-13 | 北京朗新明环保科技有限公司南京分公司 | Boiler feedwater deep desalination treatment system and method |
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Address after: 210000 room 8416, 4th floor, complex building, No. 85 Wentai street, Jiangxinzhou, Jianye District, Nanjing, Jiangsu Province Patentee after: Guoneng (Nanjing) Water and Environmental Protection Technology Co.,Ltd. Country or region after: China Address before: 210000 room 8416, 4th floor, Zhoudao Jiayuan neighborhood center, 86-1 Hongxing street, Jiangxinzhou, Jianye District, Nanjing, Jiangsu Province Patentee before: Guoneng langxinming Nanjing Environmental Protection Technology Co.,Ltd. Country or region before: China |