CN203807216U - Raw water pretreatment system for power plant - Google Patents
Raw water pretreatment system for power plant Download PDFInfo
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- CN203807216U CN203807216U CN201320770058.5U CN201320770058U CN203807216U CN 203807216 U CN203807216 U CN 203807216U CN 201320770058 U CN201320770058 U CN 201320770058U CN 203807216 U CN203807216 U CN 203807216U
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- water
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Abstract
The utility model discloses a pretreatment system and a treating method for power plant raw water. The system is mainly composed of an efficient sedimentation tank, a V-shaped filter pool, a matched sludge buffer tank, and relevant sludge lifting equipment, wherein the efficient sedimentation tank is composed of a flocculation zone, a plug flow zone, a sedimentation zone, a concentration zone, and a sludge backflow system, as well as a residual sludge discharge system; a propeller mixer capable of accelerating a flocculation reaction is arranged in the flocculation zone; the flocculation zone is connected with the sedimentation zone through the plug flow zone; the sedimentation zone is connected with a water collecting trough used for collecting clear water through an oblique pipe; the concentration zone used for concentrating the settled sludge is arranged at the bottom of the sedimentation zone. The method comprises the following steps: a, the raw water mixed with coagulant is added into the flocculation pool, and is mixed with part sludge in the concentration zone of the sedimentation tank, the flocculating agent is added into the flocculation zone, and the reaction is finished through the propeller mixer; b, the water after the reaction enters the sedimentation zone via the plug flow zone; c, the sludge settles in the sedimentation zone, and the clarified water is separated through the oblique pipe, is collected by the water collecting trough, and is discharged; d, settled sludge is concentrated at the bottom of the sedimentation tank; the upper layer of the concentrated sludge flows back through a screw pump, and is mixed with the raw water, and the excess sludge at the bottom is discharged to a sludge dewatering system through the sludge lifting equipment.
Description
Technical field
The utility model relates to the former water pretreatment system in a kind of power station, comprise the former water pretreatment system of power plant of fire coal, fuel oil, combustion gas, nuclear power etc., belong to the former water-treatment technology field in power station.
Background technology
Deposits in Eastern Coastal China Economic development is at present rapid, and power demand is large, the requirement improving in order to meet this area Economic development and people's standard of living, and country often needs every year to drop into huge fund and is used for building large-size thermal power plant.The increase of fuel-burning power plant scale, also the corresponding water treatment amount of whole power plant of having brought is increasing, and the water consumption index to per kilowatt and the water quality requirement of former water pretreatment are higher, also should consider to save the factor such as soil and environmental protection simultaneously.
Current numerous large-size thermal power plant water is mainly the water coolant of condenser cooling water, various utility appliance, chemical moisturizing, process water, life water for fire-fighting purpose, ash disposal water, desulfurization water and other waters.Wherein condenser cooling water is when adopting direct current circulation time, generally do not need to carry out former water pretreatment, but in the time adopting secondary circulation, this part water changes the moisturizing of circulating water supply system into, content requirement working control to suspended substance in water is not more than 5～10mg/L, need to carry out former water pretreatment; The water coolant of utility appliance and service water require fundamental sum condenser cooling water require identical; The water quality requirement of chemical feed water is that the content of suspended substance is not more than 2～5mg/L, and the current power plant of the waters such as desulfurization, ash discharge all adopts the principle of step water, adopts reuse water; Domestic water and water for fire-fighting purpose require to meet existing related specifications requirement.Power plant's moisturizing is at present mostly the network of waterways, the reservoir water of near power station, the coastal power plant of secondary circulation, near the seawater also can adopting, in this class water all there is seasonal variation in suspended substance, cannot meet the water quality requirement of power plant water, therefore general power plant is equipped with purifying station, former water be carried out to pre-treatment.
The former water pretreatment technique of power plant is selected conventionally at present: dosing mixes, chlorination, and former water, coagulating sedimentation or clarification, filter, clarification water.
According to above treatment process, power plant is in the time of coagulating sedimentation or clarifying treatment, mostly select the treatment facilities such as conventional rectangular sedimentation tank, accelerator, circulatior clarifier, and supporting corresponding sludge thickener and sludge dehydration device, process for the spoil disposal water to treating pond.
We are just illustrated according to the former water pretreatment design of Zhejiang Sweet natural gas cogeneration engineering.
The maximum amount of water that the Zhejiang full factory of Sweet natural gas cogeneration engineering planning to build need clarify is about 4189m
3/ h, wherein further needs the chemical water 690m filtering
3/ h.The water supply object of considering this preprocessing station is 6 390MW Sweet natural gas units and 2 coal-fired units of 125MW, the unlatching number of units difference of power plant's Various Seasonal and unit, and water consumption changes greatly, and according to calculating, 5 groups of 1000m need be selected in former water pretreatment station
3/ h mechanical accelerating purifying pool, 2 groups of 450m
3the V-type filter tank of/h, supporting 2 groups of 1500m
3/ h sludge thickener and relevant sludge lifting equipment.Former water is by 5 groups of 1000m
3/ h mechanical accelerating purifying pool clarifying treatment, makes suspended substance be less than 10mg/L, wherein 690m
3the primary water of/h is further by 2 groups of 450m
3the V-type filter of/h makes suspended substance be less than 3mg/L after processing, and enters chemical principle pond, and all the other primary waters directly enter industrial former pond.5 groups of 1000m
3the solid content of the discharge mud of/h mechanical accelerating purifying pool can reach 1.5%～2%, cannot directly enter device for dehydrating sladge waste Direct Dehydration, be concentrated into solid content and can reach more than 3% therefore need enter sludge thickener, then dewatered by sludge lifting equipment lifting to sludge dewatering equipment.According to layout, former water pretreatment system takes up an area 5982m
2.
Due to these traditional coagulating sedimentation or clarifying treatment facility floor space very large, with power plant save the area aim require contradict, this finds better former water pretreatment technique and facility just in the urgent need in the situation that economic influence is little.
Summary of the invention
The purpose of this utility model is to overcome the excessive deficiency that waits of pre existing treatment station area, and provide a kind of power plant former water pretreatment system, it makes, under the prerequisite of the former water pretreatment water quality requirement of guarantee, greatly to save the area by selecting current existing advanced efficient sedimentation tank.
The purpose of this utility model completes by following technical solution, the former water pretreatment system of a kind of power plant described in the utility model, it is mainly by efficient sedimentation tank, V-type filter tank, supporting mud surge tank and relevant sludge lifting equipment form, described efficient sedimentation tank is made up of flocculation zone, plug-flow district, settling region, enrichment region and sludge backflow system and residue body refuse blowdown system, is provided with and makes the propeller stirrer that can accelerate flocculation reaction after added flocculation agent in described flocculation zone; Between described flocculation zone and settling region, be connected by plug-flow district; Described settling region is connected with the water leg of collecting primary water by an inclined tube; Described bottom, settling region is provided with and the body refuse of sedimentation can be carried out to concentrated enrichment region.
Water leg behind described settling region is connected in the described V-type filter tank to the further filtration treatment of primary water, and the chemical principle pond that is connected thereafter; Described water leg is also connected with the former pond of industry that part primary water directly can be introduced; The bottom concentration zone of described settling region is provided with mud surge tank, and described mud surge tank is by sludge lifting equipment connection and sludge dewatering system.
The preferred technical scheme of the utility model is: described former water pretreatment system is selected 5 groups of 1000m
3/ h efficient sedimentation tank, 2 groups of 450m
3the V-type filter tank of/h, supporting 1 30m
3mud surge tank and relevant sludge lifting equipment; Former water is by 5 groups of 1000m
3/ h efficient sedimentation tank clarifying treatment, makes suspended substance be less than 10mg/L, wherein 690m
3the primary water of/h is further by 2 groups of 450m
3the V-type filter of/h makes suspended substance be less than 3mg/L after processing, and enters chemical principle pond, and all the other primary waters directly enter industrial former pond.
A method of utilizing the former water pretreatment system of power plant as above to carry out former water treatment, described method comprises the steps:
The former water of filling coagulating agent after short mix, is entered flocculation basin by a, and mix with the partly precipitated body refuse of settling tank enrichment region, adds flocculation agent and adopt propeller stirrer to complete reaction in flocculation zone;
B enters settling region in the mode of plug-flow by pushing district through the water of stirring reaction;
C body refuse in settling region sinks, and primary water is further collected water outlet by water leg after inclined tube separates;
The body refuse of d sedimentation is concentrated in settling tank bottom, reflux and mix with former water with spiral pump in the upper strata of concentrated body refuse, to maintain best solids concn, the unnecessary body refuse in bottom uses the sludge lifting equipment being made up of spiral pump to drain into sludge dewatering system, and adopts sludge dewatering equipment Direct Dehydration.
Efficient sedimentation tank described in the utility model is on the basis of traditional horizontal sedimentation tank, utilize dynamic coagulation, accelerated flocculating principles and shallow pool theory, coagulation, enhanced flocculation, three processes of sloping plate deposition are optimized, flocculation, precipitation, mud are concentrated and is incorporated in a pond, external recycle of sludge makes floss more evenly closely knit, there is the incomparable performance of routine techniques, reach higher load.
Compared with prior art, the utility model has the advantages that: in former water pretreatment station, by flocculation sedimentation tank and the organic combination of sludge thickener, and adopt the technology of settling tank sludge reflux and add polymeric flocculant, the even floccule that flocculation is formed is intensive, thereby there is higher settling velocity, reduce flocculation water required sedimentation time in reaction precipitation, effectively reduce the volume of settling tank, and in settling tank bottom, enrichment region is set, make the solid content that discharges mud can reach 3%～5%, reduced preprocessing station from water, when to next stage sludge dewatering, save sludge thickener.Like this, just greatly save power plant's land used.
Brief description of the drawings
Fig. 1 is the structural arrangement schematic diagram of former water pretreatment system described in the utility model.
Fig. 2 is the structure sectional view in efficient sedimentation tank described in the utility model and V-type filter tank.
Embodiment
Below in conjunction with accompanying drawing, the utility model is shown in detailed introduction: Fig. 1,2, the former water pretreatment system of a kind of power plant described in the utility model, it is mainly by efficient sedimentation tank 1, V-type filter tank 2, supporting mud surge tank 3 and relevant sludge lifting equipment 4 form, described efficient sedimentation tank 1 is made up of flocculation zone 1-1, plug-flow district 1-2, settling region 1-3, enrichment region 1-4 and sludge backflow system 1-5 and residue body refuse blowdown system 1-6, is provided with the propeller stirrer that can accelerate flocculation reaction after making added flocculation agent in described flocculation zone 1-1; Between described flocculation zone 1-1 and settling region 1-3, be connected by plug-flow district 1-2; Described settling region 1-3 is connected with the water leg 1-8 that collects primary water by an inclined tube 1-7; Described settling region 1-3 bottom is provided with can carry out the body refuse of sedimentation concentrated enrichment region 1-4.
Water leg 1-8 after described settling region 1-3 is connected in the described V-type filter tank 2 to the further filtration treatment of primary water, and the chemical principle pond that is connected thereafter; Described water leg 1-8 is also connected with the former pond of industry that part primary water directly can be introduced; The bottom concentration zone 1-4 of described settling region 1-3 is provided with excess sludge discharge system 1-6 and drains into mud surge tank 3, and in described mud surge tank, mud connects and sludge dewatering system by sludge lifting equipment 4.
The utility model preferred embodiment is: described former water pretreatment system is selected 5 groups of 1000m
3/ h efficient sedimentation tank, 2 groups of 450m
3the V-type filter tank of/h, supporting 1 30m
3mud surge tank and relevant sludge lifting equipment; Former water is by 5 groups of 1000m
3/ h efficient sedimentation tank clarifying treatment, makes suspended substance be less than 10mg/L, wherein 690m
3the primary water of/h is further by 2 groups of 450m
3the V-type filter of/h makes suspended substance be less than 3mg/L after processing, and enters chemical principle pond, and all the other primary waters directly enter industrial former pond.
A method of utilizing the former water pretreatment system of described power plant to carry out former water treatment, described method comprises the steps:
The former water of filling coagulating agent after short mix, is entered flocculation basin by a, and mix with the partly precipitated body refuse of settling tank enrichment region, adds flocculation agent and adopt propeller stirrer to complete reaction in flocculation zone;
B enters settling region in the mode of plug-flow by pushing district through the water of stirring reaction;
C body refuse in settling region sinks, and primary water is further collected water outlet by water leg after inclined tube separates;
The body refuse of d sedimentation is concentrated in settling tank bottom, reflux and mix with former water with spiral pump in the upper strata of concentrated body refuse, to maintain best solids concn, the unnecessary body refuse in bottom uses the sludge lifting equipment being made up of spiral pump to drain into sludge dewatering system, and adopts sludge dewatering equipment Direct Dehydration.
Embodiment:
The maximum amount of water that full factory of certain power plant need clarify is about 4189m
3/ h, wherein further needs the chemical water 690m filtering
3/ h.The water supply object that can consider this preprocessing station is 6 390MW Sweet natural gas units and 2 coal-fired units of 125MW, the unlatching number of units difference of power plant's Various Seasonal and unit, and water consumption changes greatly.
The utility model is selected 5 groups of 1000m
3/ h efficient sedimentation tank, 2 groups of 450m
3the V-type filter tank of/h, supporting 1 30m
3mud surge tank and relevant sludge lifting equipment.Former water is by 5 groups of 1000m
3/ h efficient sedimentation tank clarifying treatment, makes suspended substance be less than 10mg/L, wherein 690m
3the primary water of/h is further by 2 groups of 450m
3the V-type filter of/h makes suspended substance be less than 3mg/L after processing, and enters chemical principle pond, and all the other primary waters directly enter industrial former pond.Due to 5 groups of 1000m
3the solid content of the discharge mud of/h efficient sedimentation tank can reach 3%～5%, can directly be dewatered to sludge dewatering equipment by sludge lifting equipment lifting, this engineering installation 30m
3mud surge tank, configuration sludge pump is promoted to sludge dewatering equipment.According to layout, former water pretreatment system takes up an area 1515m
2, be only 1/4 of conventional pretreatment technology occupation of land.
The utility model is incorporated into the theory of efficient sedimentation tank in water treatment of power plant technology, utilize efficient sedimentation tank sludge reflux and the technology that adds polymeric flocculant, the even floccule that flocculation is formed is intensive, thereby there is higher settling velocity, reduce sedimentation time, effectively reduce the required area of settling tank, improved the adaptability to water intake of power plant water source; Utilize efficient sedimentation tank bottom that the feature of enrichment region is directly set, solved the not high enough problem of conventional settling pond spoil disposal solid content, reduced the setting of sludge thickener; The improvement of above two aspects, larger saving the floor space of power plant's preprocessing station.
Above example is only an aspect in the utility model application process; protection domain of the present utility model is not limited to above embodiment; can also be widely used in the construction project of other field, as the former water pretreatment field of the engineering construction such as petroleum and petrochemical industry, paper industry.All distortion that those of ordinary skill in the art can directly quote or associate from the disclosed content of the utility model, all should think protection domain of the present utility model.
Claims (4)
1. the former water pretreatment system of power plant, it is mainly by efficient sedimentation tank, V-type filter tank, supporting mud surge tank and relevant sludge lifting equipment form, it is characterized in that described efficient sedimentation tank is made up of flocculation zone, plug-flow district, settling region, enrichment region and sludge backflow system and residue body refuse blowdown system, in described flocculation zone, be provided with and make the propeller stirrer that can accelerate flocculation reaction after added flocculation agent; Between described flocculation zone and settling region, be connected by plug-flow district; Described settling region is connected with the water leg of collecting primary water by an inclined tube; Described bottom, settling region is provided with and the body refuse of sedimentation can be carried out to concentrated enrichment region.
2. the former water pretreatment system of power plant according to claim 1, is characterized in that the water leg behind described settling region is connected in the described V-type filter tank to the further filtration treatment of primary water, and the chemical principle pond that is connected thereafter; Described water leg is also connected with the former pond of industry that part primary water directly can be introduced.
3. the former water pretreatment system of power plant according to claim 1 and 2, is characterized in that the bottom concentration zone of described settling region is provided with mud surge tank, and described mud surge tank is by sludge lifting equipment connection and sludge dewatering system.
4. the former water pretreatment system of power plant according to claim 1, the former water pretreatment system described in it is characterized in that is selected 5 groups of 1000m
3/ h efficient sedimentation tank, 2 groups of 450m
3the V-type filter tank of/h, supporting 1 30m
3mud surge tank and relevant sludge lifting equipment; Former water is by 5 groups of 1000m
3/ h efficient sedimentation tank clarifying treatment, makes suspended substance be less than 10mg/L, wherein 690m
3the primary water of/h is further by 2 groups of 450m
3the V-type filter of/h makes suspended substance be less than 3mg/L after processing, and enters chemical principle pond, and all the other primary waters directly enter industrial former pond.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320770058.5U CN203807216U (en) | 2013-11-30 | 2013-11-30 | Raw water pretreatment system for power plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320770058.5U CN203807216U (en) | 2013-11-30 | 2013-11-30 | Raw water pretreatment system for power plant |
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| Publication Number | Publication Date |
|---|---|
| CN203807216U true CN203807216U (en) | 2014-09-03 |
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| CN201320770058.5U Withdrawn - After Issue CN203807216U (en) | 2013-11-30 | 2013-11-30 | Raw water pretreatment system for power plant |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103708643A (en) * | 2013-11-30 | 2014-04-09 | 浙江省电力设计院 | System and method for pretreatment on raw water of power plant |
-
2013
- 2013-11-30 CN CN201320770058.5U patent/CN203807216U/en not_active Withdrawn - After Issue
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103708643A (en) * | 2013-11-30 | 2014-04-09 | 浙江省电力设计院 | System and method for pretreatment on raw water of power plant |
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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: 20140903 Effective date of abandoning: 20151230 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |