CN208104088U - The cooling of thermal power plant bottom ash overflow water process and cyclic utilization system - Google Patents

The cooling of thermal power plant bottom ash overflow water process and cyclic utilization system Download PDF

Info

Publication number
CN208104088U
CN208104088U CN201820304072.9U CN201820304072U CN208104088U CN 208104088 U CN208104088 U CN 208104088U CN 201820304072 U CN201820304072 U CN 201820304072U CN 208104088 U CN208104088 U CN 208104088U
Authority
CN
China
Prior art keywords
water
bottom ash
overflow water
power plant
cooling
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201820304072.9U
Other languages
Chinese (zh)
Inventor
殷世忠
王威
尹导
孙志刚
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Northeast Electric Power Design Institute of China Power Engineering Consulting Group
Original Assignee
Northeast Electric Power Design Institute of China Power Engineering Consulting Group
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Northeast Electric Power Design Institute of China Power Engineering Consulting Group filed Critical Northeast Electric Power Design Institute of China Power Engineering Consulting Group
Priority to CN201820304072.9U priority Critical patent/CN208104088U/en
Application granted granted Critical
Publication of CN208104088U publication Critical patent/CN208104088U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

A kind of thermal power plant bottom ash overflow water process is cooling and cyclic utilization system, including bottom ash overflow water reception tank, filter, cooling tower, it is characterised in that:Connecting pipe chemical-dosing mixer between bottom ash overflow water reception tank and filter, filter connect intermediate pool, and intermediate pool connects cooling tower, and cooling tower connects water purifying tank, connects a grab bucket crane above bottom ash overflow water reception tank.The utility model organic combination and the cooperation for strengthening auxiliary system remove pearl of floaing in waste water, floating ash, the water temperature of overflow water are effectively reduced, make indices in wastewater effluent that can meet bottom ash system water requirement, reduce bottom ash system industrial water rate of water make-up.Therefore, which, which can be subjected to waste water water fluctuation impact, influences, and efficiently removes the polluter in waste water, water temperature is effectively reduced, pH value is adjusted, devices in system configuration and power output can be adjusted flexibly according to each engineering practice, be conducive to the even running maintenance and management of power plant.

Description

The cooling of thermal power plant bottom ash overflow water process and cyclic utilization system
Technical field
The utility model relates to thermal power plant hydraulic slag removal system, more particularly, to a kind of bottom ash overflow water process, cold But and cyclic utilization system.
Background technique
From 1970s, traditional type hydraulic slag removal system begins to thermal power plant extensive use at home and abroad, and The country it is optimized in recent years upgrading, produces self-balancing high inclination-angle formula dragveyer technology.The technology is in thermal power generation The application of factory has faster development, and by the end of the year 2015, the country has put into operation and surpassed in the 300MW ~ 600MW coal unit built 40 are crossed, development is swift and violent.But in actual operation, there are coal quality poor quality, the frequent problem of coal varitation causes the quantity of slag to fluctuate It is larger, so that dragveyer overflow coolant-temperature gage increases, large effect directly is caused to the operation of bottom ash system, is mainly reflected in bottom ash Cooling effect is poor, and the water quality inferiority of bottom ash overflow water, evaporated water is big, and overflow circulating water increases and station service increases etc., shadow The safe and stable operation of unit is rung.
Utility model content
The purpose of this utility model is:External circulation heat exchanging is forced using bottom ash overflow water, water treatment reduces bottom ash overflow Water temperature, increase slag water temperature end is poor, realizes water-saving, water purification, high efficient heat exchanging, it is made to meet the peace of fired power generating unit hydraulic slag removal system Full service requirement.
To achieve the above object, the utility model provides that a kind of thermal power plant bottom ash overflow water process is cooling and circulation benefit With system, including bottom ash overflow water reception tank, filter, cooling tower, it is characterised in that:Bottom ash overflow water reception tank and filter Between connecting pipe chemical-dosing mixer, filter connect intermediate pool, intermediate pool connect cooling tower, cooling tower connect water purification Pond, bottom ash overflow water reception tank top connect a grab bucket crane.
The bottom ash overflow water receives top and connects pH value regulating device, avoids pH value fluctuation pair in wastewater treatment process Equipment, corrosive pipeline.
The utility model organic combination and the cooperation for strengthening auxiliary system remove pearl of floaing in waste water, floating ash, are effectively reduced excessive The water temperature of flowing water makes indices in wastewater effluent that can meet bottom ash system water requirement, reduces bottom ash system industrial water and mends Water.Therefore, which, which can be subjected to waste water water fluctuation impact, influences, and efficiently removes the polluter in waste water, effectively Water temperature is reduced, pH value is adjusted, devices in system configuration and power output can be adjusted flexibly according to each engineering practice, be conducive to The even running maintenance and management of power plant.The system investments are low, and land occupation is extremely compact, have higher requirements to water resource recycling Engineering it is more applicable.
Detailed description of the invention
Fig. 1 is the utility model structure diagram.
In figure:1, bottom ash overflow water reception tank;2, elevator pump;3, pipeline chemical-dosing mixer;4, filter;5, intermediate water Pond;6, middle water pump;7, cooling tower;8, water purifying tank;9, reuse water pump;10, grab bucket crane;11, partition;12, pH value is adjusted Device.
Specific embodiment
Referring to Fig.1, specific embodiment of the present invention includes bottom ash overflow water reception tank 1, elevator pump 2, pipeline dosing Mixer 3, filter 4, intermediate pool 5, middle water pump 6, cooling tower 7, water purifying tank 8, reuse water pump 9, grab bucket crane 10, bottom Connecting pipe chemical-dosing mixer 3 between slag overflow water reception tank 1 and filter 4, added drug are coagulant, flocculation aid, mistake Filter connects intermediate pool 5, and middle water pump 6 is equipped in intermediate pool, and intermediate pool connects cooling tower 7, and cooling tower connects water purification Pond 8, water purifying tank 8 is interior to be equipped with reuse water pump 9.
The utility model technical process:Bottom ash overflow water initially enters bottom ash overflow water reception tank 1, and bottom ash overflow water receives Pond is divided into two lattice by flow direction, and 11 height of partition doubles as overflow plate lower than pond deeply.The bottom ash overflow water reception tank can digest The a large amount of discharge of wastewater of power plant's impact, while slag, the ash content in bottom ash overflow water can be precipitated, to reduce subsequent place The processing load of reason system.Subsequent filter further carries out the polluters such as particulate matter, pearl of floaing, floating ash, SS in waste water Processing, meets bottom ash water requirement.In process flow, dosing coagulant, flocculation aid before filter, equal energy intensive filtration device Treatment effect improves pearl of floaing, floating grey removal rate.Meanwhile bottom ash has higher requirements to water temperature with water, filter water outlet is using setting The cooling tower on treating stations roof is set, as far as possible reduction cooling tower leaving water temperature, to reduce bottom ash treatment water water to greatest extent Amount, to reduce the power output of entire bottom ash overflow water treatment system.If bottom ash overflow water needs to adjust pH value, overflow in bottom ash A pH value regulating device is set above flowing water reception tank, pH value in wastewater treatment process is avoided to fluctuate to equipment, corrosive pipeline.

Claims (2)

1. a kind of thermal power plant bottom ash overflow water process cooling and cyclic utilization system, including bottom ash overflow water reception tank, mistake Filter, cooling tower, it is characterised in that:Connecting pipe chemical-dosing mixer, filter between bottom ash overflow water reception tank and filter Intermediate pool is connected, intermediate pool connects cooling tower, and cooling tower connects water purifying tank, and connection one is grabbed above bottom ash overflow water reception tank Struggle against crane.
2. thermal power plant bottom ash overflow water process according to claim 1 is cooling and cyclic utilization system, feature exist In:PH value regulating device is connected above the bottom ash overflow water reception tank.
CN201820304072.9U 2018-03-05 2018-03-05 The cooling of thermal power plant bottom ash overflow water process and cyclic utilization system Active CN208104088U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820304072.9U CN208104088U (en) 2018-03-05 2018-03-05 The cooling of thermal power plant bottom ash overflow water process and cyclic utilization system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820304072.9U CN208104088U (en) 2018-03-05 2018-03-05 The cooling of thermal power plant bottom ash overflow water process and cyclic utilization system

Publications (1)

Publication Number Publication Date
CN208104088U true CN208104088U (en) 2018-11-16

Family

ID=64126597

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201820304072.9U Active CN208104088U (en) 2018-03-05 2018-03-05 The cooling of thermal power plant bottom ash overflow water process and cyclic utilization system

Country Status (1)

Country Link
CN (1) CN208104088U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112225358A (en) * 2020-11-09 2021-01-15 西安热工研究院有限公司 Slag water self-circulation utilization system of thermal power plant

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112225358A (en) * 2020-11-09 2021-01-15 西安热工研究院有限公司 Slag water self-circulation utilization system of thermal power plant

Similar Documents

Publication Publication Date Title
CN204939112U (en) A kind of waste disposal plant
CN101417841B (en) Process for treating revolving furnace flue gas dedusting water from steel mill by low hardness method
CN102491598B (en) Sewage disposal system
CN208104088U (en) The cooling of thermal power plant bottom ash overflow water process and cyclic utilization system
CN201817499U (en) Water processing system for blast-furnace slag granulation
CN102795715A (en) Treatment system for thermal power plant circulating water blowdown water
CN203768187U (en) Continuous loop aerated domestic sewage treatment device
CN202369475U (en) Sewage treatment system
CN204607769U (en) A kind of desalination Zero discharging system
CN201445834U (en) Ash water concentration and separation tank
CN101612489B (en) Cinder soaking water concentrating and separating tank
CN207210041U (en) A kind of modular construction of sludge circulation clarification cell system
CN216890433U (en) Converter hot-stewing slag wastewater treatment system
CN209797650U (en) zero-discharge system for waste water of gas power plant based on zero-pollution discharge of cooling tower
CN206069908U (en) A kind of blast furnace ironmaking water circulation system
CN201835379U (en) Water-saving operation device
CN214115172U (en) Energy-saving adjusting device of circulating water system
CN114291936A (en) Converter hot-stewing slag wastewater treatment system
CN210528705U (en) Complete equipment for recycling and treating sewage of water-jet loom
CN208949003U (en) A kind of thermal power plant, steam power plant's waste water hierarchical synthesis processing system
CN109836000A (en) A kind of plant gas wastewater zero discharge system and method based on cooling tower zero blowdown
CN221071233U (en) Water saving device of smelting rolling circulating water system
CN214990734U (en) Acid-base regeneration waste water decrement system of waste water zero release project
CN204550280U (en) Vitriol works's process water supernatant treatment system
CN212016839U (en) Cooling water recycling and saving device for industrial silicon smelting furnace

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant