CN1743284A - Sewage-refuse treatment clean-production system at the center of generating plant - Google Patents

Sewage-refuse treatment clean-production system at the center of generating plant Download PDF

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Publication number
CN1743284A
CN1743284A CN 200410155264 CN200410155264A CN1743284A CN 1743284 A CN1743284 A CN 1743284A CN 200410155264 CN200410155264 CN 200410155264 CN 200410155264 A CN200410155264 A CN 200410155264A CN 1743284 A CN1743284 A CN 1743284A
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China
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water
coal
flue gas
gas
pipe
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CN 200410155264
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Chinese (zh)
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徐宝安
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徐宝安
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Publication of CN1743284A publication Critical patent/CN1743284A/en

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Abstract

This sewage and garbage treatment system centrally designed for power plant includes sewage treatment unit, fuel processing unit, garbage combustion boiler, fly ash processing unit, smoke processing unit, the de-oxygenating draining steam of turbine steam-extraction heat-supply boiler and circulated water cooling unit. The effluent of sewage treatment unit with coal as filter is led into magnetic water strainer, and condensed water from the domestic garbage dehydration-drying condensed water-recovering combustion-supporting device is cleared by the coal filtration and normal water treatment system to feedback the circulated water-cooling system, the steam condensed water is heated and delivered into the de-oxygenating device. Treated sewage is introduced into multi-medium condenser and the distillation-desalination device; discharged smoke from fly ash incineration device is led into garbage combustion boiler; acid water discharged from distillation unit and alkaline water from coal filter are neutralized and discharged. Water distillation system and the circulation cooling water of the steam turbine condensator are led to the air- water cooling tower.

Description

A kind of is the sewage-refuse treatment clean-production system at center with the power station
Affiliated technical field
The present invention be a kind of be the sewage-refuse treatment clean-production system at center with the power station, relate to a kind of with coal as the waste disposal plant of filtrate.Gases such as separation and Extraction sulfur dioxide in flue gas utilize flue gas to handle and add hot water, produce the method and the device of steam.Hot gas heating thermosyphon circulation submergence tubular type multiple-effect evaporation desalting plant.Hot gas heat hot siphon circulating evaporator surface film multi-effect distilling desalting plant.Domestic refuse dehydrates and reclaims water of condensation tail gas auxiliary combustion equipment.Calcine method and device that the burning boiler that removes rubbish contains the Dioxins flying dust.Apparatus systems such as air cooled water composite cooling tower etc. belong to the energy environment protection field.
Background technology
Along with Chinese economic development, problems such as municipal sewage treatment, refuse treatment, sulfur dioxide emissions, Dioxins poisonous substance have had a strong impact on the Sustainable development of Urbanization in China and China.
At present, the filtrate of known raw water filtration device mainly contains two kinds, and a kind of is non-adsorptivity, i.e. quartz sand, pottery, plastics etc., and another kind has adsorption function, as carbon leaching material.Yet, filtering material for above two kinds of former water all is to use under the situation relatively preferably in the water quality of former water, and the amount of dirt is big inadequately in the filtering water, and the cycle of operation is shorter relatively, therefore, the rejection rate for some undesirable substances such as the pathogenic bacterium in the water, organism, heavy metals is lower.And conventional domestic sewage processing system, the cost of water treatment height, water quality inferiority, and its sediment contains a large amount of pathogenic bacterium and toxic substance, makes mud cause secondary pollution.
And because the present handled mode of domestic refuse is to fill out and modes such as waste incineration and generating electricity are handled by burying, rubbish bury occupy with a large amount of soils in addition its existence of oozing drop liquid underground water and surrounding environment have been constituted severe contamination, and waste incineration and generating electricity can produce the flying dust of a large amount of Dioxins poisonous substances, environment is caused serious secondary pollution, known garbage burning boiler can produce a large amount of flying dusts that contains the Dioxins poisonous substance, and the Dioxins poisonous substance is difficult to decompose under normal temperature condition, and this poisonous substance has seriously formed second environmental pollution.
The condition that produces Dioxins in waste incineration is: (1) combustion instability.(2) combustion temperature in hearth is inhomogeneous.(3) temperature of combustion<850 ℃.(4) metal catalytic.
Though the fluidized bed garbage combustion boiler is the superior burning mode of a kind of over-all properties, especially be fit to the characteristics that China's rubbish is low with the seasonal variation calorific value, composition is complicated.Fluidized bed refuse incinerator adopts quartz sand as thermal barrier, and heat storage capacity is big, and combustion stability is good, and combustion reaction temperature is even.The fluidized-bed combustion temperature has effectively been contained the existence of Dioxins in ashes between 850 ℃-950 ℃.Yet, but can not stop the later stage of Dioxins in boiler systems synthetic.In addition, the rubbish water content is big, and the combustion power generation economic benefit is not high.The core of consumer waste incineration treatment technology is the rational proportion of fuel and the control of incendiary control rationally and secondary pollution.Domestic refuse is because its water content is big, and directly throwing being thrown and burning in the boiler and will the stable burning and the raising furnace temperature of boiler be had a negative impact.Influence boiler stable burning owing to domestic refuse is moisture, temperature is subjected to the influences of a large amount of heat absorptions of water evaporation in addition, and furnace temperature reduces, and boiler operatiopn will be moved in the temperature range that can produce a large amount of Dioxins poisonous substances.And increased the vapour content of flue gas greatly, because the water vapor heat content is big, not only absorbed the heat energy that can do work in a large number, the boiler temperature that makes is elevated to the decomposable temperature of Dioxins and makes flue-gas temperature be reduced to the difficulty of Dioxins resynthesis temperature rapidly all very big.And the reduction of the high moisture and temperature of flue gas will make HCl gas that the harm of garbage incinerating system is increased, and can cause the high temperature corrosion damage of furnace heating surface and the low temperature corrosion of back-end surfaces.This safe operation to boiler will produce greatly and threaten.
Fuel is most of to be coal because China's heat power station uses, and the coal sulfur-bearing of China is higher, and known power industry is to cause SO 2The main industries of pollution and acid rain, SO 2A large amount of dischargings cause the atmospheric pollution of Chinese city very serious.SO 2Discharging has caused serious acid rain to pollute and ecological damage, thereby its environmental influence has received very big concern.The portion report " clear water blue sky Zhao is looked forward to the Chinese environmental of 21 century " of the World Bank has estimated that Chinese topsoil and water pollute the influence to environment.According to the estimation of willingness to pay value method, China's loss of (1995) big G﹠W pollution at present accounts for 8% of GDP.If adopt the human capital technique of estimation, its loss is equivalent to 3.5% of GDP.Along with SO 2The increase of quantity discharged, the loss cost that is caused increases sharply.According to relevant research, nineteen ninety-five, China was because acid rain and SO 2It is more than 1,100 hundred million yuan that pollution causes the financial loss of aspects such as farm crop, forest and HUMAN HEALTH, and 2.0% of approaching gross national product then becomes the important factor that restricts China's economy and social development.Therefore, to SO 2The control of discharging is imperative.
At present, the SO 2 from fume system of removing generally is divided into (a) dry washing system and (b) wet scrubbing system, and in the dry washing system, the solution of reagent or slurries are sprayed in hot flue gas, its moisture is evaporated, collects the quite dried byproduct that helps handling then.In the wet scrubbing system, make reagent for example the solution or the slurries of alkali reagent or alkaline earth reagent contact with gas, collect and handle wet mud then.Yet, adopt conventional sulfur removal technology to make boiler efficiency reduce, cost of electricity-generating significantly improves, and the solid waste quantity discharged increases.
A large amount of good water sources has been consumed in known thermal power generation, utilize the former water desalination technology of hot gas as thermal source, mostly be utilize the pump circulation, realize by evaporation or flash distillation, but because its equipment scaling is serious, be difficult to long-term trouble free reliability service, by adding modes such as acid water is carried out pre-treatment mostly, therefore, the cost height, dangerous, comparatively serious to the corrosion of equipment.Because of its circulation needs water pump, big energy-consuming is difficult to realize the scale operation of fresh water.Limit the application of hot gas thermal source aspect former water desalination greatly, be difficult to extensively carry out popularization.
At present, known cooling tower is cold water formula and two kinds of principal modes of air-cooled type.These two kinds of cooling towers have natural draft cooling tower and mechanical-draft cooling tower again.Because water cooling tower mainly is subjected to the influence of air ' s wet bulb temperature, be to dispel the heat, so its consumption to water is very big by evaporation of water and conduction.And atmospheric cooling tower is to utilize conduction that air is absorbed heat to realize heat radiation mainly being subjected to the influence of air dry-bulb temperature.Because air dry-bulb temperature is higher, specific heat is little, and heat absorption capacity is limited, and cooling efficiency is low, therefore, needs air-cooler that very big surface-area is arranged, and the air-cooler cost height that makes makes its popularization be subjected to restriction serious.Above problem has produced serious challenge to the cleaner production and the Sustainable development of China.
Summary of the invention
The purpose of this invention is to provide a kind of with sanitary sewage, municipal wastes, the system of the sulfur-bearing resource utilization in the coal: it is by the waste disposal plant of a kind of usefulness coal completely newly as filtrate, utilize coal the various impurity in the water all to be had the characteristics of very strong filtering ability, for the pathogenic bacterium in the water, organism, some undesirable substances such as heavy metal carry out filtering, by the electromagnetic filter deironing, utilize the submerged floating wet land aeration to hold concurrently the oxygen pool except that the nitrogen in anhydrating, nutritions such as phosphorus, filter Sewage treatment systems by coal, the magnetic filtering system, ozone sterilization, ultra-violet sterilization, water is further purified, by the electrolytic process water treatment system water is softened processing, provide power plant used water of productive use in conjunction with conventional water treatment device.By a kind of dewatered drying rubbish being provided and reclaiming the moisture of rubbish by condensation, and the airtight feeding boiler preheating of the dehydration fever air device that will dry rubbish heats and uses as combustion air.By reducing the water ratio of rubbish, reclaim the moisture of rubbish, the water yield of injecting burner hearth is reduced, eliminate the peculiar smell of gas simultaneously, be beneficial to of the corrosion of the synthetic and hydrogen chloride gas of minimizing Dioxins, the thermo-efficiency and the security that improve boiler to boiler.By a kind of apparatus and method with the sulfurous gas in the boiler smoke, carbonic acid gas, water vapor and used heat resource utilization are provided, utilize chemical method to realize the purification of flue gas, utilize the different characteristics of all gases density in the flue gas, the separation and Extraction with physics method realization all gases makes its resource utilization.By hot gas heat hot siphon circulating evaporator surface film multi-effect distilling desalting plant is provided, or provide a kind of hot gas heating thermosyphon circulation submergence tubular type multiple-effect evaporation desalting plant, realize well heater non-scaling, self-circulation, multiple-effect evaporation, the efficient height, safe and reliable, power consumption is few, the level of automation height, and the novel hot gas that expense is low adds the pyrogen water desalination apparatus.By providing a kind of calcining burning boiler that removes rubbish to contain the method and the device of Dioxins flying dust, make it can thoroughly remove Dioxins in the flying dust, and less investment, it is low to consume energy, safety and environmental protection.By a kind of air cooled water composite cooling tower is provided, make full use of water when water cooling tower cools off and the heat exchange of air, atmospheric moisture is increased, heat absorption capacity improves (water vapor specific heat is near 2 times of air specific heat) and characteristics that air dry-bulb temperature reduces are cooled off air-cooler with it.Because design needs refrigerative hot water at first to enter air-cooler, with the air inversion heat exchange of high humidity, low dry-bulb temperature, the water in the cooling air water cooler.Simultaneously, air-cooler has heated the air of high humidity, and its density is reduced, and has reduced the pressure in the water cooling tower air duct, has improved the speed of air ascension, has increased the cooling air output of cooling tower.Water temp through the air-cooler precooling reduces, and is distributed on the water distribution cooling heat exchange filler of water cooling tower cooling heat dissipation again through the cloth water spray system, reduced evaporation of water, simultaneously, reduce the dry-bulb temperature of air, made air-cooler that good cooling heat transferring effect is arranged again.Because the water temp that spray equipment is distributed on the water cooling tower water distribution cooling heat exchange filler is low, therefore, can reduce a large amount of evaporations of water, thereby reduce scattering and disappearing and blowdown of water, formed and made full use of that air is done, wet-bulb temperature, the air cooled water composite cooling tower of complementary heat radiation.Air cooled water composite cooling tower can be realized the independent operating of air-cooler when temperature is low, realize water saving to greatest extent.Native system has been eradicated the Dioxins in the flying dust in operational process, filter cleaning sanitary sewage, reduced the consumption of power plant to the cleaning water source, can utilize the sour water of its discharging simultaneously, in and the alkaline water of paper mill discharging make it innoxious, reclaim sulfurous gas and make its resource utilization.
The present invention is a kind of to be that the purpose of the sewage-refuse treatment clean-production system at center is achieved in that to be the sewage-refuse treatment clean-production system at center with the power station, to comprise compositions such as water treatment system, fuel processing system, flying dust treating system, smoke processing system, circulating water cooling system, garbage burning boiler system, steam turbine generator system, extraction for heat supply boiler deoxidizing method draining system a kind of with the power station.Other that relates to the relevant power plant of applicant applied for a patent: the method for descaling of ash removal pipe of power plant and device (application number: 95110474.8), improved power plant water and ash treatment system (application number: 95112258.4), multimedium distiller (application number: 95235083.1), hot gas heat hot siphon circulating evaporator surface film multi-effect distilling desalting plant (application number: 02160361.8), a kind of hot gas heating thermosyphon circulation submergence tubular type multiple-effect evaporation desalting plant (application number: 02160360.X), a kind of device and installation method (application number: 03103219.2) that is used for the multimedium distiller hydroecium of recovery of heat, a kind of method of sea water desaltination and device (application number: 95112245.2), a kind of electrolytic process water treatment device (application number: 200310120032.7), a kind of with the waste disposal plant (application number: 03101146.2) of coal as filtrate, a kind of floating combined modules environmental protection landscape wetland device (application number: 200310101151.8) of diving, a kind of floating composite module constructed wetland device (application number: 200410044486.5) of diving, a kind of module combined type bearing coal filtering waste disposal plant (application number: 200310113946.0), a kind of with the bearing sewage treating apparatus (application number: 200310113950.7) of charcoal coal as filtrate, air cooled water composite cooling tower (application number: 02131789.5), method and the device (application number: 03103694.5) that carbon used heat is produced steam carried in the desulfurization of a kind of smoke density method, a kind of cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit (application number: 200310124006.1), a kind of cold-water solution method flue gas desulfurization (FGD) unit (application number: 200310124007.6), a kind of domestic refuse dehydrates and reclaims water of condensation tail gas auxiliary combustion equipment (application number: 03103221.4), a kind of calcining burning boiler that removes rubbish contains the method and the device (application number: 03103982.0) of Dioxins flying dust, a kind of power generation and heat supply cleaning system (application number: 03108558.X) with municipal sewage as a resource.
Above patent is carried out different combinations with conventional power plant, can form different systems.95110474.8), improved power plant water and ash treatment system (application number: 95112258.4) wherein, the wet ash disposal system in coal-powder boiler power station can be selected patent for use: the method for descaling of ash removal pipe of power plant and device (application number:.
A, water treatment system comprise: pipeline, coarse rack, fine fack, sedimentation basin, settling tank, water reservoir, pump house, coal filtrate sewage water filtration adsorption treatment device, coal pulverizer, electromagnetism water filter, ultraviolet radiation for sterilizing and disinfecting device, solar energy housing, aerating apparatus, aeration distributing trough, the cloth water channel that confluxes, submerged floating wet land aeration facultative lagoon, demudding device, ozone sterilization sterilizing unit, sludge dehydration device, pipeline, e Foerderanlage, the electrolytic process water treatment device, compositions such as boiler:
1), devices such as coarse rack, fine fack, sedimentation basin, settling tank, water pump, pipeline, valve connect the composition pretreatment system for sewage successively.
2), be filled with coal filtrate sewage water filtration adsorption treatment device, electromagnetism water filter, ultraviolet radiation for sterilizing and disinfecting device, the connection successively of device such as water pump, pipeline, valve, composition sewage one-level treatment system through the broken coal of coal pulverizer.
3) place the aeration distributing trough that is equipped with water temperature regulation device and aerating apparatus in the solar energy housing, the submerged floating wet land aeration facultative lagoon of the one-level at least in the cloth water channel that confluxes, solar energy housing, device such as water pump, pipeline, valve connects successively, forms the sewage second-level treatment system.
4), be filled with coal filtrate sewage water filtration adsorption treatment device through the broken coal of coal pulverizer, the electromagnetism water filter, the ozone sterilization sterilizing unit, device such as ultraviolet radiation for sterilizing and disinfecting device, water pump, pipeline, valve connects successively, forms the tertiary sewage treatment system.
5), comprise that the electrolytic process water treatment device that devices such as direct supply control device, water supply and sewage device, electrolysis cathode slot device, electrolytic cathode assembly, conductive separator plate device, precipitation of scales device, electrolytic anode slot device, electrolytic anode device are formed is a fourth stage Sewage treatment systems.
More than Sewage treatment systemss at different levels or dispose of sewage for independent operating, or for successively step by step combined running dispose of sewage, or dispose of sewage for being used in combination with the above Sewage treatment systems of conventional one-level.Or be one to dispose of sewage to level Four Sewage treatment systems series operation successively.
From pretreating sewage treatment system to the level Four Sewage treatment systems or be centralized configuration, or be decentralized configuration.Coarse rack, fine fack, sedimentation basin, settling tank, water reservoir, the aeration distributing trough, the mud of submerged floating wet land aeration facultative lagoon is through the dehydration of demudding device input sludge dehydration device, through e Foerderanlage output, send into boiler combustion, sludge dehydration device removes sewage backflow sewage pretreatment unit.Coal filtrate sewage water filtration adsorption treatment device heating water vapor condensation water reclaims, send boiler auxiliary combustion after the coal filtrate sewage water filtration adsorption treatment device discharge vaporization waste gas heat exchange dehydration, the coal of coal filtrate sewage water filtration adsorption treatment failure of apparatus by e Foerderanlage output, is sent into boiler combustion after drying.The ferromagnetic substance of electromagnetism water filter absorption reclaims.Domestic refuse dehydrates and reclaims the water of condensation device, and flue gas reclaims the water of condensation device, conventional water pre-treatment means, distillation desalting plant.The cooling circulating water water dispensing apparatus, Water Treatment device, industrial sewage processing unit.
B, fuel processing system comprise that domestic refuse stores shredder assembly, and domestic refuse dehydrates and reclaims water of condensation tail gas auxiliary combustion equipment, and coal stores shredder assembly, coal filtrate drying and dewatering e Foerderanlage, coal and domestic garbage mixing device.
C, garbage burning boiler system comprise garbage burning boiler, calcine the device that the burning boiler that removes rubbish contains the Dioxins flying dust.
D, flying dust treating system comprise the flying dust collection device, flying dust prilling granulator, fly ash granule e Foerderanlage, fly ash granule roasting assembly.
E, smoke processing system comprise fume dust remover, the flue gas heat recovery dewatering unit, and the desulfurization of smoke density method is carried carbon used heat and is produced distilled water device, heating fume emission device.Or for smoke processing system comprises fume dust remover, the flue gas heat recovery dewatering unit, dissolution method flue gas desulfurization used heat is produced the method and the device of distilled water, heating fume emission device.
F, extracted steam from turbine heating boiler deoxygenation draining system comprise boiler deoxidizing method vapour, rubbish oven dry vapour, coal filtrate oven dry vapour, heat supply is with vapour etc., and wherein rubbish oven dry, coal filtrate hydrophobic with the vapour condensation dried and fed deoxygenator with the vapour condensation is hydrophobic by water pump.
G, circulating water cooling system comprise steam turbine multimedium condenser device, distillation desalination condenser device, the compound cooling tower of air cooling cold water.
More than seven kinds of apparatus systems and known power generation and heat supply conventional system device mutually combine, forming a kind of is the sewage-refuse treatment clean-production system at center with the power station.Wherein, device such as A, coarse rack, fine fack, sedimentation basin, settling tank, water pump, pipeline, valve connects successively, forms pretreatment system for sewage.The coal that coal among the fuel processing system B stores the shredder assembly processing places the sewage treatment unit of the usefulness coal of water treatment system A as filtrate, it filters water outlet and inserts in the electromagnetic filter, as the used coal of filtrate, heat by the steam among the extracted steam from turbine heating boiler deoxygenation draining system F, water of condensation is input in the deoxygenator as hydrophobic.After mixing with the rubbish of oven dry, the coal of oven dry burns among the input garbage burning boiler C of system, the water vapor mixing gas that the oven dry of coal filtrate produces imports to domestic refuse and dehydrates in the recovery water of condensation tail gas auxiliary combustion equipment, it is combustion-supporting that the garbage burning boiler system is introduced in its dehydration exhaust, after its water of condensation process coal filtration and conventional water treatment system are filtered clarification, mend among the circulating water cooling system G.Be filled with coal filtrate sewage water filtration adsorption treatment device through the broken coal of coal pulverizer, the electromagnetism water filter, the ultraviolet radiation for sterilizing and disinfecting device, device such as water pump, pipeline, valve connects successively, forms sewage one-level treatment system.Place and be equipped with the water temperature regulation device that is connected with the water outlet of steam turbine condenser recirculated water and the aeration distributing trough of aerating apparatus in the solar energy housing, the cloth water channel confluxes, the submerged floating wet land aeration facultative lagoon of the one-level at least in the solar energy housing, device such as water pump, pipeline, valve connects successively, forms the sewage second-level treatment system.Be filled with coal filtrate sewage water filtration adsorption treatment device through the broken coal of coal pulverizer, the electromagnetism water filter, the ozone sterilization sterilizing unit, device such as ultraviolet radiation for sterilizing and disinfecting device, water pump, pipeline, valve connects successively, forms the tertiary sewage treatment system.Comprise that the electrolytic process water treatment device that devices such as direct supply control device, water supply and sewage device, electrolysis cathode slot device, electrolytic cathode assembly, conductive separator plate device, precipitation of scales device, electrolytic anode slot device, electrolytic anode device are formed is a fourth stage Sewage treatment systems.Coarse rack, fine fack, sedimentation basin, settling tank, water reservoir, the aeration distributing trough, the mud of submerged floating wet land aeration facultative lagoon is through the dehydration of demudding device input sludge dehydration device, through e Foerderanlage output, send into boiler combustion, sludge dehydration device removes sewage backflow sewage pretreatment unit.Coal filtrate sewage water filtration adsorption treatment device heating water vapor condensation water reclaims, send boiler auxiliary combustion after the coal filtrate sewage water filtration adsorption treatment device discharge vaporization waste gas heat exchange dehydration, the coal of coal filtrate sewage water filtration adsorption treatment failure of apparatus by e Foerderanlage output, is sent into boiler combustion after drying.Domestic refuse dehydrates the used steam of recovery water of condensation tail gas auxiliary combustion equipment and derives from extraction for heat supply boiler deoxidizing method draining system F, and the heating steam water of condensation is input in the deoxygenator as hydrophobic.Water after the filtration of sanitary sewage process coal, magnetic filter and the conventional water treatment in the water-treatment system device, insert in multimedium condenser and the distillation desalting plant, the flying dust that flying dust treating system D collects inserts the fly ash granule roasting assembly, the smoke evacuation of flying dust roasting assembly inserts the garbage burning boiler device, and the smoke processing system device is carried carbon device, distillation desalting plant, Smoke-heating device, fume extractor by desulfurization and is formed by combining.Or for smoke processing system comprises fume dust remover, the flue gas heat recovery dewatering unit, dissolution method flue gas desulfurization used heat is produced the method and the device of distilled water, heating fume emission device.The water outlet of distillation desalting plant distilled water, is connected with the Water Treatment device, in the sewer of distillation desalting plant and the filtering alkaline water of industrial sewage coal strainer and discharge, or with liming in and discharge, or with Water Treatment trade effluent dual disposal.Domestic refuse dehydrates and reclaims the water of condensation device, flue gas reclaims water of condensation device, conventional water pre-treatment means, distillation desalting plant, cooling circulating water water dispensing apparatus, Water Treatment device, industrial sewage processing unit, interconnects successively.Equal and the air cooled water composite cooling tower of the recirculated cooling water of distillation desalination system and steam turbine multimedium condenser system, or former water-chilling plant connects.
A kind of is the sewage-refuse treatment clean-production system at center: water treatment system A with the power station: comprise that devices such as coarse rack, fine fack, sedimentation basin, settling tank, water pump, pipeline, valve connect successively, form pretreatment system for sewage.Be filled with coal filtrate sewage water filtration adsorption treatment device through the broken coal of coal pulverizer, the electromagnetism water filter, the ultraviolet radiation for sterilizing and disinfecting device, device such as water pump, pipeline, valve connects successively, forms sewage one-level treatment system.Place the aeration distributing trough that is equipped with water temperature regulation device and aerating apparatus in the solar energy housing, the submerged floating wet land aeration facultative lagoon of the one-level at least in the cloth water channel that confluxes, solar energy housing, device such as water pump, pipeline, valve connects successively, forms the sewage second-level treatment system.Be filled with coal filtrate sewage water filtration adsorption treatment device through the broken coal of coal pulverizer, the electromagnetism water filter, the ozone sterilization sterilizing unit, device such as ultraviolet radiation for sterilizing and disinfecting device, water pump, pipeline, valve connects successively, forms the tertiary sewage treatment system.Comprise that the electrolytic process water treatment device that devices such as direct supply control device, water supply and sewage device, electrolysis cathode slot device, electrolytic cathode assembly, conductive separator plate device, precipitation of scales device, electrolytic anode slot device, electrolytic anode device are formed is a fourth stage Sewage treatment systems.Domestic refuse dehydrates and reclaims the water of condensation device, and flue gas reclaims the water of condensation device, conventional water pre-treatment means, distillation desalting plant, cooling circulating water water dispensing apparatus, Water Treatment device, industrial sewage processing unit.Wherein, coal filtrate sewage water filtration adsorption treatment device or for comprising the sewage water filtration pond, filtrate, the cloth tank, catchment tray, pipeline, by-pass valve control, device such as water pump is formed, the required filtrate of coal filtrate sewage water filtration adsorption treatment device is a coal, the pond group that a plurality of ponds that to be orthogonal separate by pool wall, sewage water filtration pond are formed, one group of relative both sides of filtering basin are mounted with cloth tank and catchment tray, between cloth tank and the sewage water filtration pond, grid all is installed between sewage water filtration pond and the catchment tray, other one group of opposite face in sewage water filtration pond is to fill out the worktable that unloads coal and get the charcoal of coalingging, and waste disposal plant is connected with pipeline, valve, water pump.All be connected with valve and device liaison tube on the connecting tube of cloth tank and catchment tray, interconnect by valve.The sewage water filtration pond is connected with sewer line, contact pipeline, drainage pipeline, fresh water pipeline, the contact pipeline is provided with water pump, the contact pipeline is connected by valve with catchment tray with the cloth tank of filtering basin, by valve, water pump control realization filtering basin being connected with series, parallel between the filtering basin and operation, the draining of filtering basin, getting coal, fill out the carrying out of operations such as coal.Coal filtrate sewage water filtration adsorption treatment device or for comprising pressure-bearing oily water separation cloth tank, pressure-bearing carbon coal water filter vat, the pressure-bearing catchment tray, Scraping device, coal-charcoal filter material, pipeline, by-pass valve control, device such as water pump is formed, coal filtrate sewage water filtration adsorption treatment device is at least one group, by pressure-bearing oily water separation cloth tank, pressure-bearing carbon coal water filter vat, the pressure-bearing catchment tray connects successively, comprises water feeding and draining device, Scraping device, the remittance discharge equipment, the remittance mud discharging device, coal-charcoal filter material, the remittance water-freeing arrangement, the backwash feeding apparatus, air inlet and outlet device, pipeline, by-pass valve control, the device that water pump etc. are formed.Wherein, pressure-bearing oily water separation cloth tank is by the corresponding seal and pressure bearing end cap of bottom land, a cell wall corresponding another side cell wall that keeps at a certain distance away, cell wall corresponding seal and pressure bearing water distribution frame that keeps at a certain distance away is formed the hexahedron groove, water feeding and draining device, the cloth tank, the remittance discharge equipment, Scraping device, the mud discharging device that converges is settled in it and is constituted, the remittance mud discharging device that is positioned at pressure-bearing oily water separation cloth bottom of gullet is connected with slush pump by the spoil disposal pipeline of valve control, the seal and pressure bearing end cap that is positioned at pressure-bearing oily water separation cloth tank top is for converging discharge equipment, be connected with oil-drain pipe by valve control, supplying drainage is by by-pass valve control and sewage feedwater piping, middle contact pipeline and middle contact pump connect.Pressure-bearing carbon coal water filter vat is by the corresponding seal and pressure bearing end cap of bottom land, a cell wall corresponding another side cell wall that keeps at a certain distance away, one group of expanded metals, rigidity grid keep at a certain distance away, and corresponding another organized expanded metals, the rigidity grid is formed the hexahedron groove, the charcoal coal of filling in the groove can be coal, charcoal, the plant ass charcoal of pulverizing, and air inlet and outlet device is installed on the groove.The pressure-bearing catchment tray is by the corresponding seal and pressure bearing end cap of bottom land, a cell wall corresponding another side cell wall that keeps at a certain distance away, seal and pressure bearing charge for remittance frame corresponding cell wall that keeps at a certain distance away is formed the hexahedron groove, catchment tray, seal and pressure bearing charge for remittance frame, filter captation, feeding apparatus are settled in it and are constituted, the remittance drainage pipeline and the fresh water pipeline of valve control are installed on the groove, fresh water pump, middle contact pipeline, middle contact pump, the contact pipe valve connects, the backwash feeding apparatus are connected with the backwash feedwater piping by by-pass valve control, the backwash feedwater piping is connected with fresh water pump, and the intake and exhaust pipeline that is connected on the seal and pressure bearing end cap connects atmosphere by valve.Coal filtrate sewage water filtration adsorption treatment device has the worktable of filling and unloading coal-charcoal and taking and loading carbon coal.All be connected with valve and device contact on the connecting tube of cloth tank and catchment tray, interconnect by valve.Coal filtrate sewage water filtration adsorption treatment device is by realizing filter vat and be connected with series, parallel between the filter vat and the carrying out of operations such as the operation of filter vat, coal-charcoal taking process, coal-charcoal filling process to valve, water pump control.Coal filtrate sewage water filtration adsorption treatment device or for comprising pressure-bearing oily water separation settling vessel, pressure-bearing oily water separation water distributor, Scraping device, pressure-bearing carbon coal water strainer, coal-charcoal filter material, pressure-bearing charge for remittance device, pressure sealer, pipeline, by-pass valve control, device such as water pump is formed, coal filtrate sewage water filtration adsorption treatment device is at least one group, by pressure-bearing oily water separation settling vessel, pressure-bearing oily water separation water distributor, pressure sealer, pressure-bearing carbon coal water strainer, pressure sealer, pressure-bearing charge for remittance device connects successively, comprises water feeding and draining device, Scraping device, the remittance discharge equipment, the remittance mud discharging device, coal-charcoal filter material, the remittance water-freeing arrangement, the backwash feeding apparatus, air inlet and outlet device, pipeline, by-pass valve control, the device that water pump etc. are formed.Wherein, pressure-bearing oily water separation settling vessel is by pressure resistant vessel, water distributor, the seal and pressure bearing end cap, the remittance discharge equipment, oily water separation remittance mud plate, precipitation inclined tube plate, water wheels or motorized motions Scraping device, the remittance mud discharging device, the connection of lifting group frame constitutes, the remittance mud discharging device that is positioned at pressure-bearing oily water separation settling vessel bottom is connected with slush pump by the spoil disposal pipeline of valve control, the seal and pressure bearing end cap that is positioned at pressure-bearing oily water separation settling vessel top is for converging discharge equipment, be connected with oil-drain pipe by valve control, supplying drainage is by by-pass valve control and sewage feed main, female pipe of middle contact and middle contact pump connect.Pressure-bearing oily water separation water distributor is by pressure resistant vessel, water distributor, water-freeing arrangement, remittance discharge equipment, Scraping device, remittance mud discharging device are settled in it and are constituted, the remittance mud discharging device that is positioned at pressure-bearing oily water separation water distributor bottom is connected with slush pump by the spoil disposal pipeline of valve control, the cavity volume that is higher than pressure-bearing carbon coal water strainer that is positioned at pressure-bearing oily water separation water distributor top is for converging discharge equipment, be connected with oil-drain pipe by valve control, supplying drainage is connected with sewage feed main, the female pipe of middle contact and middle contact pump by by-pass valve control.Pressure sealer is connected with the pipeline that charges into, emits gas or liquid by valve control, and pipe connection charges into the pump of medium.Pressure-bearing carbon coal water strainer is an expanded metals by at least one bottom surface, the rigidity grid is formed the cavity that the two double buckle of opening lumps together composition, built-in coal-charcoal filter material, or the coal-charcoal filter material in the pressure-bearing carbon coal water strainer is the corresponding seal and pressure bearing end cap of a wall that adds in by able to turn on or off button with lock, a wall corresponding another side wall that keeps at a certain distance away, one group of expanded metals, rigidity grid corresponding another group expanded metals that keeps at a certain distance away, the rigidity grid is formed container, hanger is arranged on the container, add the water filter of charcoal coal by hanging device, the charcoal coal of filling in the water filter can be the coal of pulverizing, charcoal, the plant ass charcoal, pressure-bearing carbon coal water filter bottom can be provided with well heater.Pressure-bearing charge for remittance device is by pressure resistant vessel, charge for remittance device, seal and pressure bearing charge for remittance frame, filtration captation, feeding apparatus are settled in it and are constituted, remittance drainage pipeline and the clear water mother that valve control is installed on the pressure resistant vessel manages, fresh water pump, the female pipe of middle contact, middle contact pump, the contact pipe valve connects, the backwash feeding apparatus are connected with the backwash feed main by by-pass valve control, and the backwash feed main is connected with fresh water pump, and the intake and exhaust pipeline that is connected on the pressure resistant vessel connects atmosphere by valve.Coal filtrate sewage water filtration adsorption treatment device has the lifting worktable of filling and unloading coal-charcoal and taking and loading carbon coal.All be connected with valve and device contact on the connecting tube of water distributor and charge for remittance device, interconnect by valve.Coal filtrate sewage water filtration adsorption treatment device is by realizing strainer and be connected with series, parallel between the strainer and the carrying out of operations such as the operation of strainer, draining, coal-charcoal taking process, coal-charcoal filling process to valve, water pump control.Coal has water vapour heating, drying device as the waste disposal plant bottom of filtrate, this device can evaporate strong sewage in the waste disposal plant of coal as filtrate, the water vapour that makes generation is linked into domestic refuse by pipeline and dehydrates and reclaim water of condensation tail gas auxiliary combustion equipment, or carries carbon used heat in the desulfurization of smoke density method and produce condensation in the device of steam.
Charcoal is a most important moiety in the coal, and it has constituted the basic screen work of coal, and the carbon content of coal changes with the difference of degree of coalification and coal petrography component, and coal is a kind of uneven organic-fuel, mainly is to be decomposed rotten mutually and formed by the part of plant.Because the coal surface has been covered with micropore, surface-area is very big, and therefore, coal has very strong adsorptive power.In addition, there is a large amount of functional groups on the surface of coal, can carry out chemisorption and electrostatic attraction effect to the organic substance of various character, and coal can be removed the deleterious material of ion-exchanger, can remove colloidalmaterial and organic substance.The receptivity of utilizing the coal vesicular structure to reach organism, suspended substance can make water be filtered clarification.
Is with coal in special idle pond as the waste disposal plant of filtrate, unloads coal through coal tripper, and it is full to push away plain cloth, feeds that sewage realizes raw water filtration is handled.Utilize coal porous short texture, automatic distribution according to hydraulic pressure, the layered multi-stage series, parallel adsorbs the dirt in the former water, realizes that not dosing carries out pre-treatment to the more abominable former water of water quality, then pretreated former water is used as the required former water of other water treating equipment.Whole device is with the length of filtration time, and water permeable ability will change, and water level also along with to the influence of water resistance and change, changes the filtering cross section of coal synchronously, therefore, has remained the good filtration to sewage.Sewage is incorporated in the sewage water filtration pond of containing coal,, makes sewage pass the coal seam and obtain filtering by the combination utilization of water-distributing device and water collector.As required, but sewage water filtration pond one-level operation or the operation of multistage series and parallel.Can and be located at recycle pump in the system by contact pipeline, by-pass valve control in the system, make system realize series, parallel, single seat, many switchover operation.
Fuel processing system:
Comprise that domestic refuse stores shredder assembly, domestic refuse dehydrates and reclaims water of condensation tail gas auxiliary combustion equipment, and coal stores shredder assembly, coal filtrate drying and dewatering e Foerderanlage, coal and domestic garbage mixing device.Wherein, domestic refuse dehydrates and reclaims water of condensation tail gas auxiliary combustion equipment, by housing, blower fan, airheater, holder drying materials chain net, the material dispenser, fly upward material collection chain net, fly-ash separator, the air heat exchange condensers, the wash spray device, water-recovering device, induced draft fan, compositions such as air preheater, domestic refuse dehydrates recovery water of condensation tail gas auxiliary combustion equipment and is connected with gas blower in turn by pipeline, airheater, holder drying materials chain net, the material dispenser, fly upward material collection chain net, the dilatation chamber, fly-ash separator, the air heat exchange condensers, the wash spray device, water-recovering device, induced draft fan, devices such as air preheater, coagulate water collection water tank and be connected with the air heat exchange condensers, holder drying materials chain net by pipeline, the material that flies upward the discharging of material collection chain net and fly-ash separator imports material bin by e Foerderanlage.Gas blower blasts well heater with air heating with wind, imports the drying garbage storehouse, with the online drying materials of holder drying materials chain in the dryness storehouse.Blown the material that flies upward and collect by flying upward material collection chain net, dust is collected by fly-ash separator, and the dust of collecting with fly-ash separator by the isolating oven dry rubbish of separation cleaning wheel is pooled on the device for transporting objects, imports the garbage fuel storehouse, the boiler of feeding burning.Through the mixed gas of fly-ash separator, through the air heat exchange condensers
Condensation by the gas after the water-recovering device dehydration, blasts the air preheater heating and imports boiler auxiliary combustion.Water of condensation and the spray washing water collected from the air heat exchange condensers import water reservoir.Whole device is a closed system.
Flying dust treating system:
A kind of calcining burning boiler that removes rubbish contains the method and the device of Dioxins flying dust, compound being equipped with calcined the rotary calcining stove that contains Dioxins poisonous substance flying dust on garbage burning boiler, and the structure of rotary calcining stove is made up of burner, rotation calcining compartment, fly ash granule import, cooling air import, exhanst gas outlet, air intlet, fly ash granule outlet, cooling blower, separation fly-ash separator, insulation flue, supporting mechanism, transmission rig, garbage burning boiler, fly ash granule shaper, e Foerderanlage etc.The employed body of heater of calcining furnace mainly is made up of three parts, and a part is the burning feed stage, and another part is rotation calcining section, and third part is the dedusting cooling section.It is the high-temperature flue gas that the burning of burner body of heater produces, the fly ash granule that mixed e Foerderanlage feeds, introduce in the rotation calcining compartment, the fly ash granule that is passed to the rotation calcining compartment is carried out high-temperature calcination, by the cyclonic separator of installing at rotation calcining compartment afterbody, the part flying dust in incinerating fly ash granule and the flue gas to be collected by tornado dust collector, flue gas is introduced into garbage burning boiler, tornado dust collector are equipped with air cooling apparatus, the part flying dust in cooling fly ash granule and the flue gas and with its discharge.Its temperature control can keep the weighing apparatus of cigarette temperature fixed by control fuel input and the air amount of feeding, rotation calcining compartment body tilts to install at a certain angle, after containing the flying dust calcining of Dioxins, collect by tornado dust collector, flue gas after the calcining is connected in the burner hearth of garbage burning boiler by utilidor, fly ash granule after slag and the calcining can be by the interchanger air cooling, or cool off by water and water vapour, the capacity of this calcining burner reaches 850 ℃ ~ 1050 ℃ that no Dioxins exists and is as the criterion to satisfy calcining fly ash granule temperature.
Burner can be conventional fuel oil, combustion vapour burner, can be coal-fired combusting device, wherein, and coal-fired combusting device or coal-powder boiler or material casting formula chain furnace or fluid bed furnace or Circulation fluidized-bed furnace etc.The fuel of burner can be fuel oil, combustion vapour, coal, needs according to the various type of furnaces can be provided with the water-cooled or the refrigerating unit of air cooling on stove, flue-gas temperature is remained in 850 ℃ ~ 1050 ℃ scopes, smoke evacuation is directly introduced in the garbage burning boiler by rotation calcining compartment, separation fly-ash separator, utilizes the dust removal installation and the fume extractor operation of garbage burning boiler.
The rotation calcining compartment is the cylinder that steel plate is made, liner thermal insulation fire-resistant material, by the chamber head that burner is connected with the fly ash granule handling machinery, the chamber tail that is connected with fly-ash separator, partly form with the cylinder that has transmission mechanism etc., the size of its inclination is generally 2% ~ 5% of rotation calcining compartment body length overall.
The fly ash granule import is installed on burner apparatus and rotation calcining compartment junction, and its outlet can be transported to fly ash granule in the rotation calcining compartment.
The cooling air import of air cooling apparatus be located at respectively on the burner and fly-ash separator on, to slag and fly ash granule heat exchange cooling, combustion-supporting respectively to burner.
Exhanst gas outlet is placed in and separates on the fly-ash separator, is connected with garbage burning boiler by the insulation flue, and the circulating fluidized bed combustion device is provided with the front and back stages separation cyclone scrubber, and exhanst gas outlet is placed on the back level separation fly-ash separator.
Separating fly-ash separator is made up of housing, thermal insulation fire-resistant material, flue dust import, exhanst gas outlet, fly ash granule outlet, air cooled heat exchanger, cooling air import etc., separate fly-ash separator and be installed in rotation calcining compartment tail end, combine with the rotation calcining compartment, after the flue dust of burner and the generation of rotation calcining compartment enters and separates fly-ash separator separation dedusting, system enters garbage burning boiler by flue gas exhaust, and the fly ash granule of fly-ash separator separated and collected is discharged through air cooled heat exchanger cooling back.
The fly ash granule shaper is the flying dust of fly-ash separator dischargings at different levels to be processed by conventional universal machine make it form fly ash granule, is convenient to carry, calcines, separates dedusting.
The e Foerderanlage import is connected with the fly ash granule shaper, and outlet is connected with rotation calcining compartment material inlet on the burner apparatus, can be conventional belt conveyor or other e Foerderanlage.
Supporting mechanism, transmission rig be with the rotation calcining compartment by rotatable supporting mechanism positioning supports on pedestal, make the rotation calcining compartment according to the rotation of certain rotating speed by transmission rig.
Feed intake and the fuel of downflow system rotary kiln enter at same end, burn back gas and solid residue, discharge at the stove the other end, and its technical process is as follows:
Mixing such as fly-ash separator ash discharge, air preheater ash discharge, other ash discharges is after after the granulation of fly ash granule shaper, is input in the rotation calcinatory by the ash particle e Foerderanlage and calcines.Fuel and warm air are blended in the burner internal combustion, the flue gas that burning produces, by separator or directly enter the rotation calcinatory fly ash granule is calcined, flue gas after the calcining enters separator with fly ash granule to be separated, flue gas is imported into garbage burning boiler, fly ash granule enters into the preheating of air ash ejector and carries out heat exchange with the freezing air that blasts, and it is combustion-supporting that heated air is guided to burner, and the refrigerative fly ash granule is discharged.
The fluidized bed coal roasting kiln is the box hat vertical cylindrical type heater, inner lining refractory block and insulating brick, and the stove bottom is provided with airflow-distribution board with holes, is covered with certain thickness layer carrier particle on the grid distributor.The feeding high-pressure hot air blows afloat the carrier on the plate below the plate, it is suspended in presents boiling state in the burner hearth.Use stoker this moment, with the coal input, mixes with the ebullient carrier and to burn.The thin ash that burnouts is discharged with flue gas, enters the rotation calcining compartment fly ash granule is calcined, and enters garbage burning boiler after fly-ash separator captures.From this body structure of stove, there is not mechanical driving part, simple in structure, easy to maintenance.And technological operation is required higher than common mechanical.
Smoke processing system:
Comprise fume dust remover, flue gas heat-recovering device, the desulfurization of smoke density method is carried carbon used heat and is produced distilled water device, heating fume emission device.Wherein, method and the device that carbon used heat is produced steam carried in the desulfurization of smoke density method, connected to form by devices such as flue, dilatation cavity, induced draft fan, chimney, well heater, water pump, gas extraction device, ponds.
To be the chemical property of utilizing sulfur in smoke, sulfur trioxide gas, nitrogen protoxide, nitrogen dioxide gas, hydrogen chloride gas and carbon dioxide make water vapour heat release condensation in the flue gas by the heat exchange cooling to flue gas to apparatus system, the dewfall atomizing, absorb acidic gas in flue gas and form acid solution, alkaline dust in acid solution and the flue gas produces chemical reaction, generate the hydrochlorate mixing solutions, reclaim acid condensate water and dwindle flue gas volume.Utilize the different characteristics of all gases density in the flue gas, reduce the flow velocity of flue gas by dilatation, make the dust in flue gas sedimentation, the all gases natural layering, by being installed on the air supporting collector in each gas-bearing formation, separation and Extraction with all gases in the physics method realization flue gas with flue gas ash removal, purification, makes its resource utilization.
Cavity is built-in with flue gas heater, the feedwater of flue gas heater bottom, and the top water outlet is parallel six cube structures.Flue gas heater has enough surface-area, and is corrosion-resistant, and the top layer is an electrically insulating material, and the centre is a conductor, and the internal skin is an electrically insulating material, is three-decker, and the centre is a conductor, and both sides are isolator.The top water outlet of flue gas heater has a tilted tube, the incondensable gas discharge equipment is installed on herein, there is thermosiphon water to be delivered on the up-set type vaporizer of certain altitude, base of evaporator is connected with downtake and is connected with the water inlet pipe of well heater, feedwater after the adjustment acidity, be placed in the flue gas heater water-cooled preheating water-recovering device afterwards by the pipeline input, the water of heating feeds the flue gas heater filling pipe.Conventional water-recovering device is installed after the water-cooled preheating water-recovering device.Lowest part at flue gas heater is connected with the blow-off line of controlling by valve, leans on the water supply of the pressure realization of internal system to the distillation Demineralized Water Production device in downstream.Flue gas heater water inlet pipe and rising pipe are flow path structures such as diagonal lines.The top of interchanger is useful on the atomizing spray water distributor of flushing heat exchanging device, water distribution wave tank along gradient direction is arranged at the bottom in pond, certain distance apart from pool wall has catchment tray, catchment tray has constant slope, and the buck that compiles is drawn by the pipeline that places trench bottom, is connected with settling tank, on catchment tray choke manifold wall, there is an inverted-loop tube to pick out, place the pneumatic trough lowest part in catchment tray downstream,, extract the gas of pneumatic trough bottom by the negative pressure that its flow velocity produces.The pneumatic trough bottom is mounted with the air-flotation type collector that charges into hydrogen or helium in the light tough and tensile encloses container of a thin-walled body, another air-flotation type collector is installed on the top of pneumatic trough, be equipped with on the pipeline of collector and get the gas blower fan, be connected with gas deep processing system by pipeline.The exhaust of deep processing device is discharged to gas in the dilatation cavity device by the negative pressure ventilation blower fan.The settling tank bottom pipe is connected with slush pump, and mud is realized the separation of water, slurry by mud concentrate drying device.Mud is imported ash treatment system by e Foerderanlage, separates the clear water backflow precipitation of separating out.The water that settling tank overflows enters clean water basin, divides two-way to confess by water pump, and the valve of leading up to control enters the grey water flushing device of cavity device bottom, and another road enters strainer, filters the back and divides two-way to confess, and one the tunnel enters well heater spray Cleaning for High Capacity water distribution pipe.Another road enters distilled water by pipeline and handles former pond and adjust former acidity of water.Air-pressure balancing device is connected with the dilatation cavity with the top vent of settling tank by pipeline, realizes the sealing settling tank is overflowed the absorption circulation of gas.The conductor part of flue gas heater is connected with the negative pole of direct supply by insulated conductor, and the positive pole of direct supply is connected with the bottom and the flue gas heater in pond by corrosion-resistant electrode, forms electrostatic anti-scaling
The dedusting circuit.End at flue gas heater is equipped with water-recovering device, to collect the water droplet in the flue gas.The top afterbody has flue gas discharge opening on the dilatation cavity, and flue gas is drawn wind by induced draft fan and sent to hot tube heat exchanger, and flue gas heating is heated up, and discharges by flue.The longitudinal cross-section of flue gas heater is a parallelogram sturcutre, and the bottom of flue gas heater is parallel consistent with the bottom of dilatation cavity, and progressively separate on the top blind flange plane of the upper top of flue gas heater and dilatation cavity, and width progressively increases, and forms the flue gas collection chamber.
The dilatation cavity is furnished with sulfurous gas, carbonic acid gas and flue gas exhaust mouth from low to high successively, and the flue gas of discharge blasts the flue gas heater heating by induced draft fan, enters smoke stack emission.The fume emission mouth places one jiao at the top, top in pond, and the bottom air inlet in pond is put at the smoke air inlet diagonal angle, and there are enough degree of depth, enough sectional area and enough volumes in the pond, makes flue gas that lower flow velocity be arranged, and is convenient to flue gas according to the proportion AUTOMATIC ZONING.Spray thrower sprays the top of interchanger with water, and the catchment tray at the bottom of the pond imports the collection pipe discharging.
Through the dust separating flue gas of fly-ash separator, temperature is higher, belong to dust, carbonic acid gas, sulfurous gas, oxygen, nitrogen, carbon monoxide, nitrogen oxide, water vapor, the mixed gas of gases such as dust, gas flow velocity in flue is very fast, belong to turbulent state, the pyritous flue gas is introduced the flue gas flash vessel that the long-pending and volume of enough sections is arranged, the flow velocity of flue gas descends rapidly in flash vessel, and according to the different AUTOMATIC ZONING of density, heavy sulfurous gas, sulphur trioxide, gases such as nitrogen peroxide are sunken to the bottom in pond, and the lighter nitrogen oxide of proportion, hydrogenchloride, nitrogen, carbon monoxide, gases such as water vapor float the top in flue gas, carbonic acid gas places the middle level of container flue gas, because smoke air inlet places the bottom discharging of container, and the bigger dust of proportion is in the container that has reduced flow velocity, natural subsidence, also be sunken to the bottom in pond, the spray equipment on top sprays in interchanger and cavity water with the water smoke form, spray into and absorbed the heat in the flue gas, temperature raises, the dissolving of soluble gas in the flue gas is absorbed, and and flue gas in the dust and the acidic gas in flue gas of apparent alkalescence react, most of heat of water vapour in the flue gas and flue gas is by placing the intravital interchanger absorption in chamber and producing water vapour by the thermal siphon self-circulation mode in vaporizer, water vapour as the water vapour of next stage interchanger, is realized multiple-effect evaporation again.Water vapor condensation in the flue gas of heat release, dirty along heat exchanger wall, converge with the water of spray, because device is equipped with static good antiscale property device and makes the interchanger top layer induce positive charge, flue gas is under effect of electric field, dust and gas adsorption are in heat exchanger surface, under current, and at the bottom of the pond slope, come together in the catchment tray, enter settling tank with the dust collection that reclaims in the flue gas, because flue gas flow velocity in flash vessel is slow, the volume that is cooled shrinks, and water vapor condensation, the flue gas volume that makes is dwindled greatly, Pen Lin water shows acid in addition, and dust in flue gas shows alkalescence, has under the big contact area condition, the sulfur in smoke that makes, sulphur trioxide, gases such as hydrogenchloride are all soluble in water, and and flue gas in the dust of alkalescence react, change salt or acid into, become the saturated solution of saturated sour gas, emit carbonic acid gas simultaneously, this water pumps into former water treating equipment and uses as the moisturizing of flue gas heater behind sedimentation and filtration.Undissolved sulfurous gas, carbonic acid gas, nitrogen, oxygen, carbon monoxide and water vapour pass through the different natural layerings of proportion separately, the sulfurous gas of bottom is compiled in the pneumatic trough that is lower than at the bottom of the pond, be mounted with in the pneumatic trough and get tracheae, get gas tube orifice by the balloon type float with get tracheae and be connected to make and get gas tube orifice and place in the sulfur dioxide gas, on sulfur dioxide gas, have with the carbonic acid gas of carbon dioxide gas volume density correspondence and get tracheae, place in the carbonic acid gas gas-bearing formation, top in the pond, the flue gas exhaust mouth is installed, the flue gas of discharging blasts flue gas heating heat pipe-type well heater or steam heater well heater through induced draft fan, with the flue gas temperature raising, discharge, according to sulfurous gas as raw material, difference according to following step process is connected with the sulfurous gas of routine, carbon dioxide is connected with conventional carbon dioxide and is utilized, and sulfurous gas that overflows and carbon dioxide place the inlet mouth place of flue gas again by conduit, carry out layering again.
The flue gas that boiler combustion is discharged enters into the heat absorbing end heat absorption of the self-declining type heat pipe that is provided with the spray deashing device after by the fly-ash separator dedusting, reduce the temperature of flue gas, dwindle the volume of flue gas, make flue gas further form negative pressure, dust on the water cleaning heat pipe of spray equipment ejection, heat pipe is kept clean and high heat exchange efficiency, what spray equipment sprayed can be water, can be high pressure steam.After the flue gas heat release, density increases, sink, sedimentary flying dust washes through water-freeing arrangement, enters in the heat exchange cavity, and the gas flue gas is by cloth vapour device, according to layering in the dilatation chamber that do not coexist of gas autologous density, the water vapor of light specific gravity, nitrogen, oxygen, nitrogen protoxide, etc. gas in the chamber intravital top, carbonic acid gas, chlorine, hydrogen chloride gas place the intravital middle part of cavity gas, sulfurous gas, sulphur trioxide, nitrogen peroxide etc. place the lower bottom part of cavity.The water of the spraying gun ejection of interchanger top spray, interchanger is cleaned, form the abundant heat exchange of water smoke and flue gas simultaneously, the heat content that absorbs other gas in the flue gas becomes water vapor and rises, easy to be molten gas in the water droplet dissolving flue gas, hydrogen chloride gas, nitrogen protoxide, nitrogen dioxide gas, gases such as sulphur trioxide, improve the dewfall point of water vapor, form enough temperature difference with the water in the interchanger that heats, and condensation is dirty along exchanger tube wall, the wave-shaped trench of falling the bottom is interior extremely low in ash-pit from height, acidic gas in flue gas is washed, and dust is by the globule and have the electrostatic of having interchanger absorption to sweep away with water to enter into grey tank internal exchange collection, enter in the catchment tray.And sulfurous gas, carbonic acid gas and other flue gas, AUTOMATIC ZONING, difference according to weight density, layering as cocktail, behind water-recovering device, filtering water droplet wherein, enter into dilatation flue gas demixing zone, the lighter flue gas of proportion is on the top layer, discharge through induced draft fan, the release end of heat heating that enters into the heat pipe-type well heater is discharged by flue, and the sulfurous gas of bottom is extracted out by the induced draft fan on the air-flotation type gas barrier, enters into the sulfur dioxide treatment device, the air-flotation type collector is the density difference according to different flue gases, float among the flue gas, its air hatch places the bottom of air-flotation type gas barrier, can guarantee the purity of exhaust sulfurous gas.The carbonic acid gas collector also is according to than being refitted among the carbonic acid gas, and the air hatch of collector is in the bottom of air-flotation type collector.Bottom at the gas collection cavity, sulfur trioxide gas is because proportion is the heaviest, the foot of pneumatic trough will be come together in, throttling set by collection pipe, by placing the inverted-loop tube air extractor on the throttling set, water that it is inner or sulfur trioxide gas extract, discharge, in pumping process, also there is sulfur dioxide gas to be drawn out of, this air-water mixture enters into settling tank, the ash of buck, alkali components and the acid in the water form salt, soluble in water, and saturated sour gas such as sulfurous gas will overflow the top that is full of encloses container.Ash is extracted out by the slurry pump of settling tank, arrives the Ash Water Separator device, after the ash dehydration, through grey e Foerderanlage, is mixed in the boiler ash discharge treatment unit with the boiler ash discharge.Because Dioxins is water insoluble, also sinks in the ash, along with ash is imported in the ash handling equipment jointly.And enter into clean water basin from the water that settling tank overflows, and divide the two-way to confess, the one tunnel enters filtration unit, forms the water of acid characteristics, enters into the filling pipe of interchanger, and as the moisturizing of interchanger, another road enters into cavity by valve and throttling set
The bottom flushing arrangement, simultaneously, throttling set has extraction pipe to be connected with the top bleeding point of airtight settling tank, and the sour gas that will overflow is drained in the heat exchange cavity again, realizes recirculation.Sulfur dioxide gas and carbon dioxide, treated device overflows, and extracts out by pump to enter in the layering cavity, realizes the separation once more of gas, and be added in the interchanger through the water that has absorbed sour gas, can prevent the generation of the incrustation scale on the interchanger inwall.The water vapor that vaporizer produces is introduced the distillation desalting plant in downstream.The draining of interchanger enters into the water replanishing device in downstream, and discharge the final back that concentrates.
Or be a kind of cold-water solution method flue gas desulfurization (FGD) unit: by flue, the flue gas heat exchange device, heat pipe evaporator, flash vessel, the flue gas heating distiller, spray washing fume and dust device, water-cooled flue gas device, the cold-water solution flue gas desulfurization device, cold-water sprinkler, water-recovering device, induced draft fan, the gas compression condenser, water cooler, interchanger, heat pipe condenser, gas-liquid separator, gas cooler, refrigerator, cooling tower, chimney, deposition filter, store up grey pond, pump, water collecting basin, devices such as pipeline connect to form.A kind of cold-water solution method flue gas desulfurization (FGD) unit, its method principle is: cold water has powerful dissolving power to sulfur dioxide gas, and heating for dissolving has the water of sulfur dioxide gas, and sulfur dioxide gas cognition is disengaged from water.
Sulfurous gas (sulphurous anhydride) physico-chemical property:
Colourless gas.The intense stimulus smell is arranged.Molecular formula: SO 2Molecular weight 64.07.Relative density 2.264 (0 ℃).Fusing point-72.7 ℃.Boiling point-10 ℃.Vapour pressure 338.32kPa (21.11 ℃ of 2538mmHg).Solubleness 8.5% in water (25 ℃).At 1 normal atmosphere, 0 ℃, 1 premium on currency, the meltage of sulfur dioxide gas is: 79.789 liters.At 1 normal atmosphere, 20 ℃, 1 premium on currency, the meltage of sulfur dioxide gas is: 40 liters.
The solubleness of sulfurous gas in water
Temperature (℃) ??0 ??5 ??10 ??15 ??20 ??25 ??30 ??40
Solubleness (gso2/100gH2O) ??22.83 ??18.31 ??16.21 ??13.54 ??11.29 ??9.41 ??7.86 ??6.47
A kind of cold-water solution method flue gas desulfurization (FGD) unit, its technical process is: use the interchanger cooled flue gas, water vapor condensation in the flue gas is removed, with flash vessel, water spray system with flue gas ash removal, water cold flue gas device reduces the cigarette temperature, with the cold water spray, and dissolving sulfur in smoke gas, to being dissolved with the cold water heating of sulfur dioxide gas, sulfur dioxide gas is disengaged from water.Its process system comprises: be disposed in order the flue gas system that assemblies cold-water solution method flue gas desulfurization (FGD) unit by parts such as flue, flue gas heat exchange device, heat pipe evaporator, flash vessel, flue gas heating distiller, spray washing fume and dust device, water-cooled flue gas device, cold-water solution flue gas desulfurization device, cold-water sprinkler, water-recovering device, induced draft fan, gas compression condenser, water cooler, flue gas heat exchange device, chimneys.Be disposed in order the process water system that assemblies cold-water solution method flue gas desulfurization (FGD) unit by parts such as water-recovering device, cold-water sprinkler, cold-water solution flue gas desulfurization device, water collecting basin, pipeline, water pump, water-cooled flue gas device, deposition filter, water cooler, interchanger, heat pipe condenser, gas-liquid separator, interchanger, cooling tower, refrigerator, cold-water sprinklers.Be disposed in order the sulfur dioxide gas gathering system that assemblies cold-water solution method flue gas desulfurization (FGD) unit by parts such as gas-liquid separator, gas cooler, gas compression condensers.Be disposed in order the flue gas cool-down heat recovery water that assemblies cold-water solution method flue gas desulfurization (FGD) unit by parts such as flue gas heating distiller, cooling towers and handle desalination system.Be disposed in order the washing fume and dust system that assemblies cold-water solution method flue gas desulfurization (FGD) unit by parts such as spray washing fume and dust device, buck collecting tank, grey water pump, deposition filter, recycle pump, spray washing fume and dust devices.Be disposed in order the wet dust removing system that assemblies cold-water solution method flue gas desulfurization (FGD) unit by parts such as deposition filter, slurry pump, mortar pool, removing ash pipelines.Devices such as flue gas heat exchange device, heat pipe evaporator, flue gas heating distiller are furnished with ash exhauster clearly, and the dilatation cavity bottom has devices such as deashing flushing water distributor, and the dilatation cavity bottom has catchment tray, and catchment tray is connected with settling tank.That complete assembly has is corrosion-resistant, insulation, sealing characteristics.
The flue gas system of cold-water solution method flue gas desulfurization (FGD) unit, it is the water vapor that utilizes in the flue gas, sulfur dioxide gas, hydrogen chloride gas, the physical property of carbon dioxide, by flue flue gas is introduced the flue gas heat exchange device, heat pipe evaporator, flash vessel, the flue gas heating distiller, flue gas heat exchange is lowered the temperature, make the water vapor heat release condensation in the flue gas, the dewfall atomizing, acidic gas in flue gas forms acid solution, and the alkaline dust in acid solution and the flue gas produces chemical reaction, generates the hydrochlorate mixture, with the flue gas dilatation, reduce the flow velocity of flue gas, make the dust in flue gas sedimentation, flue gas is introduced spray washing fume and dust device, make the flue gas washing dedusting, flue gas is introduced water-cooled flue gas device, flue gas is further lowered the temperature, flue gas is introduced the cold-water solution flue gas desulfurization device, cold water with the cold-water sprinkler spray, dissolving sulfur in smoke gas, the flue gas after the desulfurization dewaters through water-recovering device, pass through induced draft fan, through water cooler, the heating of flue gas heat exchange device is discharged by chimney.
The process water system of cold-water solution method flue gas desulfurization (FGD) unit, be that cold water is guided to cold-water sprinkler, spray on the cold-water solution flue gas desulfurization device, with the flue gas water entrainment that removes through water-recovering device together, the process water that is dissolved with sulfur dioxide gas is come together in water collecting basin, pass through pipeline, water pump, with water pump entry cold flue gas device, flue gas is cooled off, process water after the heat absorption is introduced deposition filter, filters clarifying process water, enter water cooler, interchanger, heat pipe condenser, gas-liquid separator, interchanger, the cooling tower cooling, through middle water reservoir, water pump after process water pumped into refrigerator and cool, is introduced cold-water sprinkler, to cold-water solution flue gas desulfurization device spray, constitute circulation.Refrigerator is an electric heat pump, or lithium-bromide absorption-type refrigerating machine, and thermal source is a steam, or the flue gas heat that transmits of heat pipe, or thermal source is that the flue gas heat that steam and heat pipe transmit heats jointly, heat extraction can first heating process water, after the cold flue gas, through the cooling tower discharging, or directly discharge through cooling tower.
The sulfur dioxide gas gathering system of cold-water solution method flue gas desulfurization (FGD) unit, be the sulfur dioxide gas that gas-liquid separator separates is gone out and the mixture of gases such as water vapor, carbonic acid gas, cool off through gas cooler, make the water vapor dewfall, becoming sulfurous acid extracts, sulfur dioxide gas makes its condensation liquefaction by the gas compression condenser, forms sulfurous gas liquid.But after the heat extraction heating process water of gas compression condenser, the cold flue gas,, or directly discharge through cooling tower through the cooling tower discharging.
The flue gas cool-down heat recovery water is handled desalination system, is disposed in order the cold-water solution method flue gas desulfurization (FGD) unit flue gas cool-down heat recovery water that assemblies by parts such as flue gas heating distiller, cooling towers and handles desalination system.The flue gas heating vaporizer is a parallelepiped structure, the top water outlet of flue gas heating vaporizer connects tilted tube, there is the mouth of pipe to be connected and installed the on-condensable gas discharging apparatus above the tilted tube, tilted tube connects the thermosiphon of vertically arranging, the outlet of thermosiphon upper end connects puts vaporizer, base of evaporator is connected with sewer line and is connected with the bottom water inlet pipe of flue gas heating vaporizer, the vaporizer top is connected with blow-off line, be connected with the water distilling apparatus of flue gas heating distiller, condenser is arranged in the water distilling apparatus, with the recirculated cooling water pump, pipeline is connected with cooling tower, flue gas heating vaporizer water inlet pipe and rising pipe are flow path layouts such as diagonal lines, and the top of flue gas heating vaporizer is equipped with deashing device.The lateral cross section of flue gas heating vaporizer is rectangular configuration or other shape and structure, the longitudinal cross-section is parallelogram sturcutre or other shape and structure, the bottom of flue gas heating vaporizer and the bottom of cavity are parallel consistent or certain space arranged, progressively postpone in the top blind flange plane of upper top and cavity, width increases gradually, or certain space is arranged, and forms the flue gas collection chamber, the flue gas heating vaporizer has enough surface-area, and is corrosion-resistant.
The washing fume and dust system, it is flue gas through the cooling of flue gas heating vaporizer, by spray washing fume and dust device the flue gas through the cooling of flue gas heating vaporizer is sprayed washing fume and dust, buck is through collector groove, come together in the buck collecting tank, pump into the deposition filter clarification through grey water pump, introduce through recycle pump and wash the circulation of cigarette spray thrower formation.The water of spray washing fume and dust device and cold-water solution flue gas desulfurization device is atomizing spray directly, or makes water fogging and spray in corrosion-resistant, and is high temperature resistant, and high surface area has on the filler of flow characteristics of the cigarette G﹠W of getting well.
The wet dust removing system of cold-water solution method flue gas desulfurization (FGD) unit is disposed in order by parts such as deposition filter, slurry pump, mortar pool, removing ash pipelines and assemblies the wet dust removing system of cold-water solution method flue gas desulfurization (FGD) unit.Deposition filter is connected with slurry pump, and slurry pump connects mortar pool, and deposition filter is connected with water pump, is connected with water dispensing apparatus to connect cavity bottom respectively towards grey water pipe, towards grey sprinkler head with wash the cigarette spray thrower.
Devices such as flue gas heat exchange device, hot tube heat exchanger, flue gas heating distiller are furnished with ash exhauster clearly, and the dilatation cavity bottom has devices such as deashing flushing water distributor, and the dilatation cavity bottom has catchment tray, and catchment tray is connected with settling tank.That complete assembly has is corrosion-resistant, insulation, sealing characteristics.Apparatus for ash is installed in the top of flue gas heat exchange device, heat pipe evaporator and flue gas heating vaporizer, water, water vapor or pressurized air spray irrigation, and deashing device has corrosion resistance characteristic.
Heat pipe evaporator and heat pipe condenser are that hair inhales gravity type boat davit natural circulation heat-pipe apparatus, and heat-pipe apparatus heat absorbing end heat pipe evaporator is down, and the release end of heat heat pipe condenser is last, and heat pipe evaporator and heat pipe condenser are by the vertical pipe connection that liquid is flow automatically.
Can be hexahedron structure, the end of dilatation cavity, can be same continuous tilt bottom surface, dilatation cavity bottom surface is the face that extends with certain gradient from high in the end, the bottom of dilatation cavity has along gradient direction, be parallel to domatic damascene trench, the wall of cavity is anticorrosion acid resisting material and makes, and dilatation cavity bottom surface is furnished with deashing flushing water distributor device from high to low in proper order, converges
Tank.Deashing device wash-down water water distributor, flow down along the dilatation cavity bottom from the high-end of bottom of smoke discharging cavity, import the catchment tray of dilatation cavity bottom rear end, catchment tray has constant slope, draw by the pipeline that places catchment tray terminal bottom, be connected with deposition filter.
Or be that a kind of cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit, by flue, the flue gas heat exchange device, heat pipe evaporator, flash vessel, the flue gas heating distiller, spray washing fume and dust device, water-cooled flue gas device, the cold-water solution flue gas desulfurization device, cold-water sprinkler, water-recovering device, induced draft fan, the gas compression condenser, water cooler, interchanger, the electrolytic anode groove, the electrolysis cathode groove, settling vessel, the carbon dioxide injector, storage hydrogen device, direct supply, electrical lead, heat pipe condenser, gas-liquid separator, gas cooler, refrigerator, cooling tower, chimney, deposition filter, store up grey pond, pump, water collecting basin, devices such as pipeline connect to form.A kind of cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit, and its method principle is: cold water has powerful dissolving power to sulfur dioxide gas, and the water in the electrolysis cathode groove shows alkalescence, can increase the absorption of water to sulfur dioxide gas.It is acid that water in the electrolytic anode groove shows, and can make sulfurous acid become sulfur dioxide gas, and heating for dissolving has the water of sulfur dioxide gas, and sulfur dioxide gas cognition is disengaged from water.A kind of cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit, its technical process is: use the interchanger cooled flue gas, water vapor condensation in the flue gas is removed, with flash vessel, water spray system with flue gas ash removal, water cold flue gas device reduces the cigarette temperature, with the cold water spray, and dissolving sulfur in smoke gas, to being dissolved with the cold water heating of sulfur dioxide gas, sulfur dioxide gas is disengaged from water.Its process system comprises: be disposed in order by parts such as flue, flue gas heat exchange device, heat pipe evaporator, flash vessel, flue gas heating distiller, spray washing fume and dust device, water-cooled flue gas device, cold-water solution flue gas desulfurization device, cold-water sprinkler, water-recovering device, induced draft fan, gas compression condenser, water cooler, flue gas heat exchange device, chimneys and assembly the flue gas system that the cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit.Be disposed in order the process water system that the cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit that assemblies by parts such as water-recovering device, cold-water sprinkler, cold-water solution flue gas desulfurization device, water collecting basin, pipeline, water pump, water-cooled flue gas device, deposition filter, water cooler, interchanger, heat pipe condenser, gas-liquid separator, interchanger, cooling tower, refrigerator, cold-water sprinklers.Be disposed in order by parts such as electrolytic anode groove, electrolysis cathode groove, settling vessel, carbon dioxide injector, storage hydrogen device, direct supply, electrical leads and assembly electrolysis that the cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit and remove hard alkali addition process system.Be disposed in order by parts such as gas-liquid separator, gas cooler, gas compression condensers and assembly the sulfur dioxide gas gathering system that the cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit.Be disposed in order by parts such as flue gas heating distiller, cooling towers and assembly the flue gas cool-down heat recovery water that the cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit and handle desalination system.Be disposed in order the washing fume and dust system that the cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit that assemblies by parts such as spray washing fume and dust device, buck collecting tank, grey water pump, deposition filter, recycle pump, spray washing fume and dust devices.Be disposed in order by parts such as deposition filter, slurry pump, mortar pool, removing ash pipelines and assembly the wet dust removing system that the cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit.Devices such as flue gas heat exchange device, heat pipe evaporator, flue gas heating distiller are furnished with ash exhauster clearly, and the dilatation cavity bottom has devices such as deashing flushing water distributor, and the dilatation cavity bottom has catchment tray, and catchment tray is connected with settling tank.That complete assembly has is corrosion-resistant, insulation, sealing characteristics.
The distillation desalting plant:
Comprise compositions such as hot gas heat collector, multiple-effect evaporator, cooler condenser, heat exchanger, fresh water pump well, raw water box, fresh-water tank, pump, valve, pipeline, lagging material, hot gas is a water vapor, or high temperature mixing gas, hot gas heat collector is for importing and exporting the pipeline that is connected with heat collector up and down and constitute hot gas heat collector by being provided with fluid.Wherein, this installs employed hot gas heat collector is the protection against corrosion heat collector, or can be static good antiscale property heat collector.Multiple-effect evaporator is for each other independently, and one-level is above, forms by each cavity of pipe connection.First evaporator is vertically to settle, and connects the thermosyphon circulation vaporizer that the tube chamber of outer wall insulation constitutes by pipeline, valve.First evaporator and second stage vaporizer are by pipe connection, and wherein, the second stage and N level vaporizer are the interchanger of shell structure, are made up of lateral arrangement or vertical tube bundle, tube sheet and housing of arranging.Be that floor plan or folded layer by layer sieve are vertically arranged between the vaporizer, interconnected by pipeline, valve, a plurality of shell cavitys of outer wall insulation constitute.Install used geothermal heat exchanger and be the protection against corrosion heat collector or be static good antiscale property heat exchanger.Heat collector bottom water inlet pipe mouth is connected by utilidor with the first evaporator bottom effluent pipe mouth of multiple-effect evaporator, heat collector top effluent pipe mouth, by being located at the incondensable gas automatic exhaust device on the hot gas heat collector top, be connected with thermosiphon bottom return water pipe in the first evaporator of multiple-effect evaporator.The heating source of hot gas heat collector is that its structure of water vapor is vertical shell heat exchange structure, original water inlet enters from hot gas heat collector bottom, discharges from the top, is connected with thermosiphon, hot gas heat collector heating vapour side has water vapor to insert, and water of condensation is drawn from the bottom.Or the heating source of hot gas heat collector is a high temperature mixing gas, its structure is vertical shell heat exchange structure, original water inlet enters from hot gas heat collector bottom, discharge from the top, be connected with thermosiphon, hot gas heat collector heated side has high temperature mixing gas to insert, and the mixing gas after the heat exchange is discharged, and water of condensation is drawn from the bottom.There is the heat exchanger steam inlet pipe of steam discharge pipe and second stage vaporizer to be connected in the steam chest of first evaporator top.The new water make-up pipe in valve control ground feeds water in its vaporizer.First evaporator and heat collector can be provided with one control air valve.First evaporator steam discharge pipe steam inlet is placed in the steam chest of vaporizer top, and steam discharge pipe is connected with the heat exchanger steam inlet pipe of second stage vaporizer.The water shoot of first evaporator can be connected with feedwater heating apparatus and be connected with second stage vaporizer water distributor by valve control.Second stage vaporizer steam discharge pipe steam inlet is settled
In the vaporizer steam chest, second stage vaporizer steam discharge pipe steam outlet is connected with the interior heat exchanger steam inlet pipe of third evaporator, water of condensation rising pipe in the vaporizer of the second stage can be connected with feedwater heating apparatus draws, be connected with heat exchanger in the third evaporator by U-shaped pipe pressure temperature regulator, the concentrated water drainage water pipe in the vaporizer of the second stage can pass through the control of U-shaped pipe pressure temperature
The system device is connected heat exchange with feedwater heating apparatus draws, and is connected with the third evaporator water-in by the concentrated water drainage water pipe.Third evaporator steam discharge pipe steam inlet is placed in the vaporizer steam chest, third evaporator steam discharge pipe steam outlet is connected with the interior heat exchanger steam inlet pipe of next stage vaporizer, water of condensation rising pipe in the third evaporator can be connected with feedwater heating apparatus draws, be connected with heat exchanger in the next stage vaporizer by U-shaped pipe pressure temperature regulator, concentrated water drainage water pipe in the third evaporator can be connected heat exchange with feedwater heating apparatus by U-shaped pipe pressure temperature regulator draws, and is connected with next stage vaporizer water-in by the concentrated water drainage water pipe.Its system architecture of N level vaporizer is equal to third evaporator.The final evaporator steam discharge pipe is connected with the steam heating feed feeder, final evaporator water of condensation rising pipe is connected with the steam heating feed feeder by feedwater heating apparatus, the former water rising pipe of steam heating feed feeder is connected with feedwater heating apparatus, the dense tank of final evaporator is connected with dense water water storage box, and dense water water storage box is connected with by-pass valve control, blow-off pipe, pump etc.The steam heating feed feeder is by the pipe connection cooler condenser.Wherein, cooler condenser can be former water cooled condenser, or is air-cooled cold water cooler condenser.The bottom of steam heating feed feeder is connected with the fresh water pump well by pipeline, and the rising pipe of fresh water pump well is connected with fresh-water tank by water pump, valve.Former water cooled condenser is placed in the underwater certain depth, places in the tube chamber, and water-in places former water cooled condenser lower bottom part, and the water inlet of cooling raw water tubes is provided with filtration unit, and water outlet communicates with former water body, constitutes closed loop with water body.Air-cooled cold water cooler condenser is that two-layer condenser up and down is installed in the air-cooled tower, and the spray water-distributing device is arranged between the two-layer condenser.Cooler condenser is connected with the fresh water pump well by pipeline.Former water intake filters the back by filtration unit and imports former water water storage box, be provided with former water intake pipe in the former water water storage box, be connected with the multiple-effect evaporator water supply installation, the operation of apparatus system is connected, controls and realize by the reasonable Arrangement of corresponding pipeline, valve, pump and water tank.
Hot gas heat hot siphon circulating evaporator surface film multi-effect distilling desalting plant comprises compositions such as hot gas heat collector, multiple-effect evaporator, cooler condenser, heat exchanger, fresh water pump well, raw water box, fresh-water tank, pump, valve, pipeline, lagging material.Hot gas heat hot siphon circulating evaporator surface film multi-effect distilling desalting plant comprises compositions such as hot gas heat collector, multiple-effect evaporator, cooler condenser, heat exchanger, fresh water pump well, raw water box, fresh-water tank, pump, valve, pipeline, lagging material.Hot gas is a water vapor, or high temperature mixing gas, and hot gas heat collector is for importing and exporting the pipeline that is connected with heat collector up and down and constitute hot gas heat collector by being provided with fluid.This installs employed hot gas heat collector is static good antiscale property heat collector.Wherein, heat collector is to import and export the interchanger that the pipeline that is connected with heat collector constitutes hot gas heat collector up and down by being provided with fluid, and interchanger is placed in the shell chamber, and the shell chamber is provided with inlet pipe, escape pipe and condensate draining pipe.Interchanger top is provided with the water spraying and cleaning apparatus.Heat collector all connects static good antiscale property device makes its good antiscale property, and wherein static is that negative pole by direct supply is connected interval electrical isolation heat-transfer surface between negative pole and the positive pole, dc power anode with the conduction thermal conductor
Connect fluid and the earth, constitute the charging circuit that direct supply, conductor, isolator and conductive fluid are formed.Hot gas heat collector is vertically installed, and the insulate heat switch that is used for heating fluid is the pressure-bearing heat exchanging piece, and hot gas heat collector institute heat-collecting capacity can directly or indirectly conduct to fluid.Intake-outlet equipressure loss is installed or is waited the installation of flow path diagonal angle, and its rising pipe is located at heat collector
The top, be connected with vaporizer by certain angle of inclination.The heat transfer electric conductor of heat collecting element all is electrically connected by the insulation conductance line parallel with the negative pole of direct supply.Multiple-effect evaporator is for each other independently, and one-level is above, forms by each cavity of pipe connection.First evaporator is vertically to settle, and connects the thermosyphon circulation vaporizer that the tube chamber of outer wall insulation constitutes by pipeline, valve.First evaporator and second stage vaporizer are by pipe connection, and wherein, the second stage and N level vaporizer are the interchanger of shell structure, are made up of lateral arrangement or vertical tube bundle, tube sheet and housing of arranging.Be that floor plan or folded layer by layer sieve are vertically arranged between the vaporizer, interconnected by pipeline, valve, a plurality of shell cavitys of outer wall insulation constitute.Install used geothermal heat exchanger and be static good antiscale property heat exchanger.Wherein, static good antiscale property heat exchanger comprises steam heating feed feeder, former water cooled condenser, feedwater heating apparatus, evaporation heat-exchanger etc.The steam heating feed feeder is made up of the heat exchanger and the luminal structure of logical former water.Former water cooled condenser is tubular type or pipe tubular type or tube-sheet type or tube and shell heat exchanger, tubular heat exchanger can be helix tube type, the pipe tube heat-exchanger can be tube and tube and connects and composes, tube-sheet heat exchanger can be pipe and heat exchanger plates connects and composes, tube and shell heat exchanger can be housing, tube sheet, tube bundle and connects and composes, on the interchanger radiating fin can be arranged, be heated air in the interchanger, and interchanger is outer for being heated fluid.In the heat transfer tube or be the steam heating medium in the heat exchanger plates.Feedwater heating apparatus is shell structure interchanger or tubular sheet heat exchanger or pipe tube heat-exchanger, and the inside and outside or tube sheet both sides of pipe can cold and hot each other medium, and heating fluid can be more than one.Heat exchanger is tubular type or pipe tubular type or tube-sheet type or tube and shell heat exchanger, and tubular heat exchanger can be helix tube type, and the pipe tube heat-exchanger can be tube and tube and connects and composes, and tube-sheet heat exchanger can be pipe and heat exchanger plates connects and composes.The static of static good antiscale property heat exchanger is provided by direct supply.Wherein, static good antiscale property heat exchanger heat-transfer surface both sides are isolator, and inside is conductor, or static good antiscale property heat exchanger is under electrical isolation good premise between each fluid medium, on the heat-transfer surface of heat exchange mutually, fluid medium fouling side is an isolator, and fluid medium non-scaling side is a conductor.Can be by accompanying conductor between the two good electrically insulating materials of heat conduction, or compound electric conductor on the electrically insulating material, or method such as composite electrical insulation body realizes on the electrical conductor material.Can be by plating ceramic electrical insulating film or ceramic, plating conducting film on glass on the aluminium alloy.Or pottery, plate electrical insulating film behind the plating conducting film on glass.The negative pole of power supply is electrically connected by the electric conductor of the electrical isolation top layer on the static good antiscale property heat exchanger heat-transfer surface with inside, and anodal access node dirt side water body makes electric conductor and fouling side water body electrical isolation, realizes the static good antiscale property of system.Heat collector bottom water inlet pipe mouth is connected by utilidor with the first evaporator bottom effluent pipe mouth of multiple-effect evaporator, heat collector top effluent pipe mouth, by being located at the incondensable gas automatic exhaust device on the hot gas heat collector top, be connected with thermosiphon bottom return water pipe in the first evaporator of multiple-effect evaporator.Wherein, the incondensable gas automatic exhaust device for being installed in the cavity device of heat collector top or outlet conduit top, has the vapor cock of water float control in the cavity device, and the water float has spacing cavity volume to control its direction of motion, spacing cavity volume open top,
The bottom is porose, be fixed in the chamber receptacle, venting port is on the top of chamber receptacle, and venting port has trim corresponding with the trim on the water float, water-in is positioned at the bottom of chamber receptacle, and the incondensable gas automatic exhaust device has the web member with heat collector top or pipe connection.
Circulating water cooling system:
The multimedium condenser is at conventional condenser hydroecium plug-in mounting sleeve or dividing plate, the not connected hydroecium more than two groups will be become between the condenser hydroecium, pass to different heat-eliminating mediums, a kind of heat-eliminating medium is used to reclaim the used heat of condenser discharging, another kind of heat-eliminating medium is connected with cooling tower, is used for the used heat of relief condenser discharging.Air cooled water composite cooling tower is made up of tower body, ventilator, ventilation installation, air distribution device, air-cooler, water distribution system, liquid distribution, water eliminator, water collector, water-in and water-out pipeline and irrigation canals and ditches, other facilities etc.It is characterized in that: wind direction under water distribution heat exchange packing layer in the cooling tower shell and the spray water-distributing device, or outside the water eliminator air outlet, be provided with the air-cooler that has air cooling unit to connect to form that is fixed on the support, support is fixed on the load-bearing supporter of cooling tower.The female pipe of water inlet at first with the cooling tower air duct in the water-in of air-cooler assembly be tightly connected respectively by pipe joint, with hot water introducing air chiller assembly, by water distributor distribution water distribution in the air-cooler assembly.Through air-cooler refrigerative water, collect by the charge for remittance pipeline that is positioned at the air-cooler end, be distributed on the packing layer through water-distributing device, after the heat exchange cooling, conflux in the cooling water reservoir.The air-cooler collection pipe has water outlet, directly is connected with the intake pipe that by-pass valve control is installed of circulating water pool by valve, supplies water for the water circulating pump intake pipe jointly.The air-cooler assembly can be made by good, corrosion resistant other material of metallic substance or heat conductivility and shape.By the pipe of multi-group cooling fins, the section of jurisdiction and the multi-disc section of jurisdiction that connect and compose by water distributor and collection pipe constitute the air-cooler assembly.The air-cooler assembly can by the good section bar of metallic substance or other heat conductivilitys by welding, riveted joint, expanded joint, casting, bonding, technology such as extrude and make moulding.The cooling pipe fitting can be extruded into the section bar processing and fabricating by metal, and the section bar that it processes is threaded fin above.Can be with the metal threaded finned tube of extrusion moulding, by welding fabrication is the section of jurisdiction, many groups by section of jurisdiction and section of jurisdiction are tightly connected, constitute the air-cooler assembly of parallelepiped, its water-in arranges with the water outlet diagonal angle and makes its flow path identical that the sense of rotation of its screw finned pipe can be identical, can be opposite, screw finned pipe between section of jurisdiction and the section of jurisdiction is series arrangement in an identical manner, also direction that can be identical or opposite direction arranged.Support available metal, concrete or plastic-steel and polymer organic composite material are made, and the air-cooler support is fixed on the load-bearing supporter of cooling tower.Hang on the air-cooler fixed support or put on the air-cooler support, also can pass through key, bolt, groove fastening assembly and be fixed.With the air-cooler water-in by pipeline and interface female pipe of intaking with being connected, be arranged in air-cooler water-in next door and fix by the air-cooler stent support.Manage by the charge for remittance mother that pipeline and joint are connected with the air-cooler water outlet, be arranged in air-cooler water outlet next door, fix by the air-cooler stent support.Water eliminator is fixed in the blast inlet place of air-cooler, can be connected with air-cooler the combination or be fixed on the air-cooler fixed support.The valve of control water is installed on the spray water-distributing device.Air-cooler is installed in the following wind direction of natural wind cooling tower and machine power circulation cooling tower water-distributing device or water eliminator, and air-cooler does not have and allows the directly big space of circulation of air.Air-cooler is arranged arrangement with herring-bone, V-arrangement or polyhedron shape by matrix or concentric fan-shaped mode, is fixed on the air-cooler support.Valve on valve on the collection pipe and the cloth water spray system, it is cold to can be used for control air
The but independent operating of device and variable load operation.
The air-cooler working process is as follows: need refrigerative hot water to be fed to respectively on the air-cooler assembly by the female pipe of hot water water delivery, distinguish water distribution on the air-cooler assembly unit by the air-cooler assembly water inlet pipe on the female pipe of hot water water delivery, enter the hot water of air-cooler assembly unit, by flow paths such as air-cooler assembly upper end water distributing pipe and the female pipes of air-cooler assembly upper end hot water water delivery hot water is assigned on the air-cooler assembly cooling unit, by the heat release of screw thread fin cooling tube, conflux on air-cooler section of jurisdiction assembly collection pipe and air-cooler section of jurisdiction and section of jurisdiction assembly collection pipe, finally flow out, conflux in the water coolant of air-cooler assembly lower end confluxes the female pipe of water delivery from cooling water outlet pipe with air-cooler assembly water inlet pipe diagonal angle layout.Cooling air is by the cooling screw finned pipe, water in the cooling tube, and be heated with air behind the water countercurrent flow, density reduces, enter the cooling tower air duct from the discharge of air-cooler assembly ventilation opening, be provided with the air-cooler inter-module between section of jurisdiction and the section of jurisdiction every support, to prevent the distortion of cooling tube chip module, improve its physical strength, air-cooler assembly fin cooling tube cooling fins and cooling tube can be extrusion molding one time, interconnect by modes such as welding, expanded joints between screw thread fin cooling tube and the water distributing pipe.The air-cooler layout design should be convenient to change, safeguard, overhaul when aerodynamic requires.Water temp through the air-cooler precooling reduces, conflux by collecting pipe, again through distribution and the spray flow of water distributor water drenching device by valve regulation and control water coolant, be distributed to through the cloth water spray system on the cellular heat exchange filler of water cooling tower, after the air heat exchange cooling, conflux in the cooling water reservoir.The water eliminator of installing between the air intake of air-cooler and water distributor has been removed the globule in the ascending air, has reduced the windage loss of water.Simultaneously, because the water temp that spray equipment is distributed on the cellular cooling filler of water cooling tower is low, therefore, can reduce a large amount of evaporations of water, thereby reduced scattering and disappearing and blowdown of water, reduced the dry-bulb temperature of air, made air-cooler that good cooling heat transferring effect is arranged again.Formed and made full use of that air is done, wet-bulb temperature, the air cooled water composite cooling tower of complementary heat radiation.Air-cooler collection pipe water outlet directly is connected with the intake pipe that by-pass valve control is installed of circulating water pool by valve, and jointly for the water circulating pump intake pipe supplies water, and by being located at the valve on two pipes, regulation and control are because of different water supply flow in season.To realize air-cooler independent operating when temperature is low of air cooled water composite cooling tower, realize water saving to greatest extent.This cooling tower is suitable for various types of Revamping Cooling Tower and production, and is similar to natural draft cooling tower for its arrangement of mechanical type cooling tower.
Water treatment system:
Industrial sewage processing unit comprises the personal water softening water reclamation system of the reduction of chemical water treatment system, and the reduction discharging acid-base neutralisation water of chemical water treatment system is manually prepared sea water system.Coal is as the papermaking wastewater filtration treatment device of filtrate, and wherein, acid sewer of water distillation desalting plant and coal are as the alkaline blowdown of the papermaking wastewater filtration treatment device discharging of filtrate
The discharging of water neutralizing treatment.
Extraction for heat supply boiler deoxidizing method draining system:
Comprise boiler deoxidizing method vapour, rubbish oven dry vapour, coal filtrate oven dry vapour, externally heat supply vapour.Wherein, rubbish
Drying, coal filtrate hydrophobic with vapour condensation oven dry then mends into deoxygenator by water pump by processing such as magnetic filter, strainers with the vapour condensation is hydrophobic.
The invention has the beneficial effects as follows that the vesicular structure characteristic that has made full use of coal is filtered sanitary sewage.Utilize low-pressure steam oven dry domestic refuse, reclaim that it is moisture, and produce distilled water, and boiler auxiliary combustion is realized that it is innoxious with drying garbage dewatering waste gas with its used heat.Circular fluid bed is added Wingdale less or do not add Wingdale operation, reduce the cindery discharging of solid and improve boiler thermal output and make full use of sulfur-bearing in the coal, effectively control the generation of Dioxins poisonous substance.The Dioxins poisonous substance is calcined under the precursor of elimination in guaranteeing flying dust, and the heat that maximally utilises the flying dust calcining furnace is used to improve boiler efficiency, and the waste heating of ash discharge simultaneously air-breathing is realized the efficient utilization of the coal-fired heat of calcining, and realizes the flying dust resource utilization.Boiler flue gas desulfurization is carried the carbon device and has been reclaimed the used heat in the boiler smoke, sulfurous gas, carbonic acid gas, water vapor and other sour gas, and make flue gas ash removal more thorough, this system utilizes the physical property of flue gas, do not add any Chemical Composition, utilize the heat of self that water is evaporated, oxious component resource utilization with flue gas, realized the desulfurization of flue gas with the simplest method, the purification of carbonic acid gas, the utilization again of used heat, the distillation desalination of waste water, a series of activities such as the processing again of dangerous dust, represented the developing direction of cleaner production, significant.Utilize the heat of flue gas or the low-pressure steam of steam turbine to produce distilled water simultaneously.Realized after the sanitary sewage disposal boiler water feeding and circulating cooling system moisturizing, and can supply water outward, what discharged in the sour water of utilization distillation desalination system discharging and paper mill utilizes in the filtering alkaline sewage of coal and discharging, the coal filtration unit has reclaimed the combustiblesubstance in the papermaking wastewater, improve the thermal value of coal, realized the harmless treatment of power plant emission acid waste water and paper mill discharging alkaline waste water.Air cooled water composite cooling tower can be realized its high-efficiency water-saving under the prerequisite of guaranteeing the system cools effect.More than various facilities by optimum combination, make whole system configuration rationally, less investment, operation cost is low, has realized the cleaner production of power plant fully, has solved the sustainable development of China's power system.
The present invention is further described below in conjunction with accompanying drawing:
Fig. 1 is a system diagram of the present invention;
Fig. 2 is that the submerged floating wet land device that has solar energy housing combines the schematic flow sheet of disposing of sewage with coal as the filtrate bilge strainer.
Among the figure: 1 deoxygenator; 2 sweet-water tanks; 3 desalinations mix bed; the cloudy bed of 4 desalinations; 5 decarburization intermediate water tanks; 6 desalinations sun bed; 7 former water distribution reservoirs; 8 add pyrogen water distribution reservoir; 9 flue gas heaters; 10 flue gas condensing water ash pond; 11 settling ponds; 12 acid condensate water strainers; 13 mortar water traps; 14 carbon dioxide extraction devices; 15 sulfurous gas extractors; 16 flue gas layering grooves; 17 flue gas heat pipe receivers; 18 heat pipe flue gas heaters; 19 induced draft fans; 20 chimneys; 21 incondensable gas vent fans; 22 thermosiphon evaporators; 23 water distillation demineralizer; 24 water distillation demineralizer water circulating pump; 25 fly-ash separators; 26 fly ash granule molding machines; 27 province's coal air backheating devices; 28 material separators; 29 circular fluid beds; 30 circulating fluidized bed gas bags; 31 calcinings fly to be the granule materials separator; 32 fly ash granule rotary calcining kilns; 33 combustion heating furnaces; 34 fuel mix dispensers; 35 boilers are through the wind device; 36 rubbish are pulverized coal mixer; 37 former water multimedium recovery of heat distiller service pumps; 38 rubbish storing grooves; 39 refuse grinders; 40 drying garbage water traps; 41 hot gas distillation demineralizers; 42 hot gas distillation demineralizer water circulating pumps; 43 hot gases reclaim the water of condensation settler; 44 recirculated water water reservoirs; 45 steam turbine; 46 generators; the compound cooling tower of 47 air-cooled cold water; 48 heat-recovery condensers; 49 recirculated water cooling condensers; 50 heat of condensation wells; 51 water of condensation condensate pumps; 52 low pressure heaters; 53 water circulating pumps; 54 coals are as the filtrate bilge strainer; 55 distilled water water reservoirs; 56 neutralizing water tanks; 57 synthetic sea water distribution reservoirs; 58 synthetic sea water water reservoirs; 59 sanitary sewage water service pipes; 60 coarse racks; 61 fine facks; 62 sedimentation basins; 63 settling tanks; 64 pre-treatment anaerobism water reservoirs; 65 pump houses; 66 shore pipes; 67 coal pulverizers; 68 defeated device for coal; 69 electrolytic process water treatment device; 70 pump houses; the facultative water reservoir of 71 submerged floating wet lands; 72 solar energy housings; 73 aeration tubes; 74 submerged floating wet land devices; 75 submerged floating wet land aquatic organisms are cultivated facultative lagoon; 76 aeration distributing troughs; 77 pneumatic pumps; 78 e Foerderanlages; the former water water distributor of 79 power plant; 80 circulating hot water pipes; 81 magnetic sludge collectors; 82 magnetic filters; 83 apparatus for ultraviolet disinfection; 84 coal filtrate adsorption treatment devices; 85 electromagnetism water filters; 86 ozonization plants; 87 apparatus for ultraviolet disinfection; 88 magnetic sludge collectors; 89 recirculated water return water pipes; 90 recirculated water intake pipes; 91 drying garbage device condensate pipes; 92 turbine discharge pipes; 93 low-pressure water vapour pipes; 94 condensate pipes; 95 low pressure heater rising pipes; 96 deoxygenator heating steam pipes; 97 sweet-water tank rising pipes; 98 desalination water pipes; 99 mix sewage pipe in the bed; a 100 cloudy rising pipe; sewage pipe in the 101 cloudy beds; 102 sewage combs; a 103 sun rising pipe; sewage pipe in the 104 sun beds; in 105 and the water comb; 106 adjust water pipe; 107 synthetic sea water combs; 108 synthetic sea waters are failed comb; 109 unboiled water pipes; 110 decarburization intermediate water tank rising pipes; 111 cooling circulating water filling pipes; 112 flue gas thermal source distiller cooling circulating water water inlet pipes; 113 flue gas thermal source distiller cooling circulating water return water pipes; 114 oven dry rubbish hot gas distiller cooling circulating water water inlet pipes; 115 oven dry rubbish hot gas distiller cooling circulating water return water pipes; 116 steam turbine water vapor steam discharge pipes; 117 rubbish oven dry vapour pipe; 118 oven dry rubbish hot gas distiller distillation water pipes; 119 oven dry rubbish hot gas water of condensation filter outlet pipes; 120 oven dry rubbish hot gas water of condensation rising pipes; the dirty pipe of 121 oven dry rubbish hot gas distiller concentrated water drainages; 122 former water water inlet pipes; 123 former hydro-thermal siphon upper hoses; 124 former hydro-thermal siphon downtakes; 125 conveying belt that grind up the refuse; 126 air input tubes; 127 ultraviolet disinfector rising pipes; 128 electromagnetic filter rising pipes; 129 collection pipes; 130 coal filtrates oven dry vapour pipe; 131 boiler main team pipes; 132 2 secondary water pipes; the former water inlet pipe of 133 multimedium condensers; the former water delivery pipe of 134 multimedium condensers; 135 refuse odors input boiler auxiliary combustion pipe; 136 boiler feed pipes; 137 flue gas heating distiller distilled water outlet pipes; 138 flue gas heating thermosyphon circulation vapor pipes; the former water water shoot of 139 flue gas heating; 140 flue gas heating thermal siphon water distilling apparatus downcomers; 141 flue gas heating thermal siphon water distilling apparatus upper hoses; 142 densimetry desulfurization cold smoke device flues; the hot cigarette device of 143 densimetry desulfurization flue; 144 induced draft fan smoke-uptakes; 145 densimetry desulfurization cold smoke device water shoots; 146 sulfurous gas dischargers; 147 settling pond wash-down water water shoots; 148 strainer spray irrigation water pipes; 149 flue gas condensing water ash pond mortar transfer lime; 150 settling pond mortar transfer limes; 151 mortar water trap return water pipes; 152 ash conveying devices; 153 economizer air preheater ash exhausters; 154 boiler flues; 155 fly-ash separator smoke-uptakes; 156 heat pipe smoke-uptakes; the dirty pipe of 157 flue gas heating distiller concentrated water drainages; 158 fly-ash separator ash releasing tubes; 159 coals filter the sewage rising pipe; 160 coals filter inefficacy coal input unit; 161 coal strainer gas barrier; 162 filter broken coal charcoal e Foerderanlage; 163 pretreating sewages are carried distributing pipe line; the 164 coarse racks pipeline of disposing of sewage; the 165 fine facks pipeline of disposing of sewage; the 166 sedimentation basins pipeline of disposing of sewage; the 167 settling tanks pipeline of disposing of sewage; 168 sewage reservoir water pipes; 169 pretreating sewage pipelines; 170 submerged floating wet land sewage disposal outlet conduits; the facultative water reservoir outlet conduit of 171 submerged floating wet lands; 172 pump house rising pipes; 173 coal filtrate adsorption treatment device rising pipes; 174 electromagnetism water filter rising pipes; 175 ozonization plant rising pipes; 176 apparatus for ultraviolet disinfection rising pipes; 177 sludge dehydration device water shoots; 178 ferromagnetic substance dischargers; 179 garbage drying transport pipes; 180 rubbish coal co-fuel delivery pipelines; 181 two-stage electromagnetic strainer ferromagnetic substance output channels; 182 secondary apparatus for ultraviolet disinfection output waterpipe; 183 electrolytic process water treatment device output tubes; 184 rubbish oven dry distiller raw water pipeline; 185 fly ash granule transport pipes; 186 flue gas heater feedwater pipings; 187 acid condensate water water pipes; charcoal concentrating unit vapor pipe is carried in 188 desulfurization; charcoal carbon dioxide extraction pipe is carried in 189 densimetry desulfurization; charcoal carbon dioxide extraction pipe is carried in 190 densimetry desulfurization; 191 heat pipe utilidors; 192 submerged floating wet land demudding devices; 193 waterhead area unboiled water feedwater pipings; 194 coal adsorption filter heating steam condensate draining pipe roads; 195 mix a soft water recovery channel; a 196 cloudy soft water recovery channel
Embodiment
In Fig. 1, sewage enters coarse rack 60, fine fack 61, sedimentation basin 62, settling tank 63, pre-treatment anaerobism water reservoir 64, pump house 65 after sewage water service pipe 59, sludge dehydration device water shoot 177 converge, carry distributing pipe line 163 to enter into coal by pretreating sewage after treatment as in the filtrate bilge strainer 54, mud then enters into shore pipe 66 through sludge-discharge pipe road 169, through the sludge dehydration device drying, by e Foerderanlage 78 outputs, enter in the rubbish storing groove 38.Enter into coal and conflux input magnetic filter 82 through coal filtration sewage rising pipe 159 as the sewage in the filtrate bilge strainer 54.Water outlet through magnetic filter 82 enters apparatus for ultraviolet disinfection 83, and the iron oxide compound is collected through magnetic sludge collector 81.The water outlet of apparatus for ultraviolet disinfection 83 mixes with circulating hot water pipe 80 through ultraviolet disinfector rising pipe 127, enters into aeration distributing trough 76.Coal is handled through coal pulverizer 67, is transported to coal as in the filtrate bilge strainer 54 through defeated device for coal 68, after the inefficacy, filters 160 outputs of inefficacy coal input unit through coal, sends into rubbish and pulverizes coal mixer 36.Water vapour through coal filtrate oven dry vapour pipe 130 enter into coal as filtrate bilge strainer 54 in, water of condensation is 194 outputs through coal adsorption filter heating steam condensate draining pipe road, and coal is exported through coal strainer gas barrier 161 as the waste gas that filtrate bilge strainer 54 produces.The mud that coarse rack 60, fine fack 61, sedimentation basin 62, settling tank 63 produce confluxes in shore pipe 66 through 169 outputs of pretreating sewage pipeline, enters rubbish storing groove 38 through e Foerderanlage 78, sends into boiler combustion behind the drying and dehydrating.Enter into the water in the aeration distributing trough 76, in aeration distributing trough 76 through aeration tube 73, pneumatic pump 77 aerations mix, cultivate in the facultative lagoon 75 by the submerged floating wet land aquatic organism that the submerged floating wet land device is installed that collection pipe 129 enters in the solar energy housing 72, acting in conjunction through aerobic layer Filtration Adsorption layer and anaerobic layer, make the nitrogen in the water, phosphorus, be converted into hydrobiont, be implanted with reed as the next stage kind, beauty Jiao, lotus rhizome and support has hydrobiological submerged floating wet land device 74 submerged floating wet land aeration facultative lagoons and fish hydrocoles eat hydrobiont and algae, nitrogen phosphorus in the water is extracted curing, make hydrobiont carry out omnibearing absorption to the nutrition in the water, water outlet finally enters in the facultative water reservoir 71 of submerged floating wet land.Adjust the water capacity of treatment system with it, its water outlet enters into pump house 70 through the facultative water reservoir outlet conduit of submerged floating wet land, enter into coal filtrate adsorption treatment device 84, electromagnetism water filter 85, magnetic sludge collector 88, ozonization plant 86, apparatus for ultraviolet disinfection 87 by pump house 70, can discharge as three grades of water outlets separately through apparatus for ultraviolet disinfection rising pipe 176 through one tunnel water outlet of apparatus for ultraviolet disinfection 87.Another road water outlet enters into electrolytic process water treatment device 69 through secondary apparatus for ultraviolet disinfection output waterpipe 182, and electrolytic process water treatment device 69 is got rid of the incrustation scale of rejecting, and the good water that electrolytic process water treatment device output tube 183 will be handled is confessed.One the tunnel enters former water distribution reservoir 7 through the former water water distributor 79 of power plant, and another road connects recirculated water intake pipe 90.The sour water that acid condensate water strainer 12 is discharged through acid condensate water water pipe 187 with after primary water in the former water distribution reservoir 7 mixes the adjustment pH value, enter into heat-recovery condenser 48 internal heating through former water multimedium recovery of heat distiller service pump 37, the former water inlet pipe 133 of multimedium condenser, temperature raise after the former water delivery pipe 134 of multimedium condenser enter into add pyrogen water distribution reservoir 8 and sour water that acid condensate water strainer 12 is discharged cooperate the reduction pH value after, be input to flue gas heater 9 internal heating by flue gas heater feedwater piping 186.The water that temperature raises enters into thermosiphon evaporator 22 evaporations by flue gas heating thermal siphon water distilling apparatus upper hose 141, steam enters into multistage distillation desalination in the water distillation demineralizer 23 by flue gas heating thermosyphon circulation vapor pipe 138, and incondensable gas is through 21 dischargings of incondensable gas vent fan.Water distillation demineralizer 23 supplies water and cools off through water distillation demineralizer water circulating pump 24, flue gas thermal source distiller cooling circulating water water inlet pipe 112, by compound cooling tower 47 heat releases of air-cooled cold water.The heat that flue gas heat pipe receiver 17 reclaims enters into heat pipe flue gas heater 18 with flue gas heating by heat pipe utilidor 191, is discharged to discharging in the chimney 20 by the hot cigarette device of densimetry desulfurization flue 143, induced draft fan 19.Carbon dioxide extraction device 14, sulfurous gas extractor 15 are got gas by the collector in the flue gas separator tank 16.The rubbish of rubbish storing groove 38 enters the dehydration of drying garbage water trap 40 inner dryings by the conveying belt 125 that grinds up the refuse after refuse grinder 39 fragmentations, its condensing works absorbs heat distillation desalination in hot gas distillation demineralizer 41 by hot gas and makes distilled water.The recirculated water of water circulating pump 42 supplies absorbs heat, by compound cooling tower 47 dischargings of air-cooled cold water.The rubbish water of condensation that reclaims is after hot gas reclaims 43 clarifications of water of condensation settler, in the discharge cycle water water reservoir 41.Exsiccant rubbish enters rubbish pulverizing coal mixer 36 jointly with exsiccant coal to be mixed, and enters circular fluid bed 29 internal combustion by fuel mix dispenser 34, and rubbish drying unit tail gas blasts boiler auxiliary combustion through boiler induced-draft fan 35.Fly-ash separator 25, economize flying dust that coal air preheater 27 and mortar water trap 13 reclaim through 26 granulations of fly ash granule molding machine after in the fly ash granule transport pipe 185 input fly ash granule rotary calcining kilns 32; calcine through the cigarette that combustion heating furnace 33 produces; separate by material separator 31, calcining materials is discharged.High-temperature flue gas enters in the fluidized-bed combustion boiler, and the high-temperature flue gas that boiler produces separates the reflux cycle fluidized-bed combustion boiler through boiler material separator 28 and burns, and the feedwater of deoxygenator 1 enters province's coal airheater 27 internal heating by boiler feed pipe 136.Discharged flue gas enters flue gas heat pipe receiver 17 through fly-ash separator 25, in flue gas heat pipe receiver 17 enters flue gas heater 9.The steam of circular fluid bed drum superheater 30 discharging enters steam turbine 45 through boiler main team pipe 131 and drives generators 46 generatings, and weary gas enters into heat release condensation in the multimedium distiller that multimedium condensation heat-recovery condenser 48, recirculated water cooling condenser 49, water of condensation condensate pump 51 form by turbine discharge pipe 92.Draw gas and enter drying garbage water trap 40 heating, drying rubbish by steam turbine water vapor steam discharge pipe 116, rubbish oven dry vapour pipe 117, enter coal as filtrate bilge strainer 54 heating, drying coals by steam turbine water vapor steam discharge pipe 116, coal filtrate oven dry vapour pipe 130, and externally heat supply.The recirculated water condensation water that produces is in pipeline is input to deoxygenator 1, the de-mineralized water that water distillation demineralizer 23 is produced enters distilled water water reservoir 55, supply water by 132 pairs of recirculated water water reservoirs 44 of two secondary water pipes with by 109 pairs of desalination sun of unboiled water pipe bed 6, the water outlet of desalination sun bed 6 enters into decarburization intermediate water tank 5 through sun bed rising pipe 103, the water outlet of decarburization intermediate water tank 5 enters into the cloudy bed 4 of desalination, the water outlet of the cloudy bed 4 of desalination enters into desalination and mixes bed 3, and the water outlet that desalination mixes bed 3 enters into sweet-water tank 2.The water of condensation that heat of condensation well 50 produces enters into deoxygenator 1 through water of condensation condensate pump 51, low pressure heater 52.The waste water that desalination sun bed 6, the cloudy bed 4 of desalination, desalination mix bed 3 dischargings enters into neutralizing water tank 56, synthetic sea water distribution reservoir 57, synthetic sea water water reservoir 58.The water that desalination sun bed 6, the cloudy bed 4 of desalination, the mixed bed 3 of desalination reclaim enters into recirculated water water reservoir 44, the water of condensation that flue gas heater 9 produces enters mortar water trap 13 through flue gas condensing water ash pond 10, gas enters in the flue gas heater 9 through flue gas condensing water ash pond 10, its primary water enters settling pond 11, clear water enters in the flue gas heater 9 and washes away, its water enters into acid condensate water strainer 12 and filters clarification, and the water that acid condensate water strainer 12 is produced enters spray in the flue gas heater 9.Another road is divided into two-way, enters distribution reservoir 7 and 8 respectively and adjusts the pH value water distribution.
Fig. 2 technical process is equal to Fig. 1.

Claims (10)

1. one kind is the sewage-refuse treatment clean-production system at center with the power station, comprise compositions such as water treatment system, fuel processing system, flying dust treating system, smoke processing system, circulating water cooling system, garbage burning boiler system, steam turbine generator system, extraction for heat supply boiler deoxidizing method draining system, it is characterized in that:
A, water treatment system comprise: device such as coarse rack, fine fack, sedimentation basin, settling tank, water pump, pipeline, valve connects successively, forms pretreatment system for sewage; Be filled with coal filtrate sewage water filtration adsorption treatment device through the broken coal of coal pulverizer, the electromagnetism water filter, the ultraviolet radiation for sterilizing and disinfecting device, device such as water pump, pipeline, valve connects successively, forms sewage one-level treatment system; Place the aeration distributing trough that is equipped with water temperature regulation device and aerating apparatus in the solar energy housing, the submerged floating wet land aeration facultative lagoon of the one-level at least in the cloth water channel that confluxes, solar energy housing, device such as water pump, pipeline, valve connects successively, forms the sewage second-level treatment system; Be filled with coal filtrate sewage water filtration adsorption treatment device through the broken coal of coal pulverizer, the electromagnetism water filter, the ozone sterilization sterilizing unit, device such as ultraviolet radiation for sterilizing and disinfecting device, water pump, pipeline, valve connects successively, forms the tertiary sewage treatment system; Comprise that the electrolytic process water treatment device that devices such as direct supply control device, water supply and sewage device, electrolysis cathode slot device, electrolytic cathode assembly, conductive separator plate device, precipitation of scales device, electrolytic anode slot device, electrolytic anode device are formed is a fourth stage Sewage treatment systems; Domestic refuse dehydrates and reclaims the water of condensation device, and flue gas reclaims the water of condensation device, conventional water pre-treatment means, distillation desalting plant; The cooling circulating water water dispensing apparatus, the Water Treatment device, industrial sewage processing units etc. are connected successively with the rising pipe of waste disposal plant;
B, fuel processing system comprise that domestic refuse stores shredder assembly, and domestic refuse dehydrates and reclaims water of condensation tail gas auxiliary combustion equipment, and coal stores shredder assembly, coal filtrate drying and dewatering e Foerderanlage, coal and domestic garbage mixing device;
C, garbage burning boiler system comprise garbage burning boiler, calcine the device that the burning boiler that removes rubbish contains the Dioxins flying dust;
D, flying dust treating system comprise flying dust collection device, flying dust prilling granulator, fly ash granule e Foerderanlage, fly ash granule roasting assembly;
E, smoke processing system comprise fume dust remover, the flue gas heat recovery dewatering unit, and the desulfurization of smoke density method is carried carbon used heat and is produced distilled water device, heating fume emission device; Or for smoke processing system comprises fume dust remover, the flue gas heat recovery dewatering unit, dissolution method flue gas desulfurization used heat is produced the method and the device of distilled water, heating fume emission device;
F, extracted steam from turbine heating boiler deoxygenation draining system comprise boiler deoxidizing method vapour, rubbish oven dry vapour, coal filtrate oven dry vapour, heat supply is with vapour etc., and wherein rubbish oven dry, coal filtrate hydrophobic with the vapour condensation dried and fed deoxygenator with the vapour condensation is hydrophobic by water pump;
G, circulating water cooling system comprise steam turbine multimedium condenser device, distillation desalination condenser device, the compound cooling tower of air cooling cold water;
More than seven kinds of apparatus systems and known power generation and heat supply conventional system device mutually combine, forming a kind of is the sewage-refuse treatment clean-production system at center with the power station; Wherein, device such as A, coarse rack, fine fack, sedimentation basin, settling tank, water pump, pipeline, valve connects successively, forms pretreatment system for sewage; Be filled with coal filtrate sewage water filtration adsorption treatment device through the broken coal of coal pulverizer, the electromagnetism water filter, the ultraviolet radiation for sterilizing and disinfecting device, device such as water pump, pipeline, valve connects successively, forms sewage one-level treatment system; The coal that coal among the fuel processing system B stores the shredder assembly processing places the sewage treatment unit of the usefulness coal of water treatment system A as filtrate, it filters water outlet and inserts in the electromagnetic filter, as the used coal of filtrate, heat by the steam among the extracted steam from turbine heating boiler deoxygenation draining system F, water of condensation is input in the deoxygenator as hydrophobic; After mixing with the rubbish of oven dry, the coal of oven dry burns among the input garbage burning boiler C of system, the water vapor mixing gas that the oven dry of coal filtrate produces imports to domestic refuse and dehydrates in the recovery water of condensation tail gas auxiliary combustion equipment, it is combustion-supporting that the garbage burning boiler system is introduced in its dehydration exhaust, after its water of condensation process coal filtration and conventional water treatment system are filtered clarification, mend among the circulating water cooling system G; Place and be equipped with the water temperature regulation device that is connected with the water outlet of steam turbine condenser recirculated water and the aeration distributing trough of aerating apparatus in the solar energy housing, the cloth water channel confluxes, the submerged floating wet land aeration facultative lagoon of the one-level at least in the solar energy housing, device such as water pump, pipeline, valve connects successively, forms the sewage second-level treatment system; Be filled with coal filtrate sewage water filtration adsorption treatment device through the broken coal of coal pulverizer, the electromagnetism water filter, the ozone sterilization sterilizing unit, device such as ultraviolet radiation for sterilizing and disinfecting device, water pump, pipeline, valve connects successively, forms the tertiary sewage treatment system; Comprise that the electrolytic process water treatment device that devices such as direct supply control device, water supply and sewage device, electrolysis cathode slot device, electrolytic cathode assembly, conductive separator plate device, precipitation of scales device, electrolytic anode slot device, electrolytic anode device are formed is a fourth stage Sewage treatment systems; Coarse rack, fine fack, sedimentation basin, settling tank, water reservoir, the aeration distributing trough, the mud of submerged floating wet land aeration facultative lagoon is through the dehydration of demudding device input sludge dehydration device, through e Foerderanlage output, send into boiler combustion, sludge dehydration device removes sewage backflow sewage pretreatment unit; Coal filtrate sewage water filtration adsorption treatment device heating water vapor condensation water reclaims, send boiler auxiliary combustion after the coal filtrate sewage water filtration adsorption treatment device discharge vaporization waste gas heat exchange dehydration, the coal of coal filtrate sewage water filtration adsorption treatment failure of apparatus by e Foerderanlage output, is sent into boiler combustion after drying; Domestic refuse dehydrates the used steam of recovery water of condensation tail gas auxiliary combustion equipment and derives from extraction for heat supply boiler deoxidizing method draining system F, and the heating steam water of condensation is input in the deoxygenator as hydrophobic; Sewage in the water-treatment system device inserts in multimedium condenser and the distillation desalting plant to the level Four sewage disposal through pre-treatment and, the flying dust that flying dust treating system D collects inserts the fly ash granule roasting assembly, the smoke evacuation of flying dust roasting assembly inserts the garbage burning boiler device, and the smoke processing system device is carried carbon device, distillation desalting plant, Smoke-heating device, fume extractor by desulfurization and is formed by combining; Or for smoke processing system comprises fume dust remover, the flue gas heat recovery dewatering unit, dissolution method flue gas desulfurization used heat is produced the method and the device of distilled water, heating fume emission device; The water outlet of distillation desalting plant distilled water, is connected with the Water Treatment device, the sewer of distillation desalting plant or with the filtering alkaline water of industrial sewage coal strainer in and discharge, or with liming in and discharge, or with Water Treatment trade effluent dual disposal; Domestic refuse dehydrates and reclaims the water of condensation device, flue gas reclaims water of condensation device, conventional water pre-treatment means, distillation desalting plant, cooling circulating water water dispensing apparatus, Water Treatment device, waste disposal plant, interconnects successively; Equal and the air cooled water composite cooling tower of the recirculated cooling water of distillation desalination system and steam turbine multimedium condenser system, or former water-chilling plant connects.
2. according to claim 1 a kind of be the sewage-refuse treatment clean-production system at center with the power station, it is characterized in that: water treatment system A: comprise that devices such as coarse rack, fine fack, sedimentation basin, settling tank, water pump, pipeline, valve connect successively, form pretreatment system for sewage; Be filled with coal filtrate sewage water filtration adsorption treatment device through the broken coal of coal pulverizer, the electromagnetism water filter, the ultraviolet radiation for sterilizing and disinfecting device, device such as water pump, pipeline, valve connects successively, forms sewage one-level treatment system; Place the aeration distributing trough that is equipped with water temperature regulation device and aerating apparatus in the solar energy housing, the submerged floating wet land aeration facultative lagoon of the one-level at least in the cloth water channel that confluxes, solar energy housing, device such as water pump, pipeline, valve connects successively, forms the sewage second-level treatment system; Be filled with coal filtrate sewage water filtration adsorption treatment device through the broken coal of coal pulverizer, the electromagnetism water filter, the ozone sterilization sterilizing unit, device such as ultraviolet radiation for sterilizing and disinfecting device, water pump, pipeline, valve connects successively, forms the tertiary sewage treatment system; Comprise that the electrolytic process water treatment device that devices such as direct supply control device, water supply and sewage device, electrolysis cathode slot device, electrolytic cathode assembly, conductive separator plate device, precipitation of scales device, electrolytic anode slot device, electrolytic anode device are formed is a fourth stage Sewage treatment systems; Domestic refuse dehydrates and reclaims the water of condensation device, and flue gas reclaims the water of condensation device, conventional water pre-treatment means, and the distillation desalting plant, the cooling circulating water water dispensing apparatus, Water Treatment device, waste disposal plant connect to form water treatment system successively; Wherein, coal filtrate sewage water filtration adsorption treatment device or for comprising the sewage water filtration pond, filtrate, the cloth tank, catchment tray, pipeline, by-pass valve control, device such as water pump is formed, the required filtrate of coal filtrate sewage water filtration adsorption treatment device is a coal, the pond group that a plurality of ponds that to be orthogonal separate by pool wall, sewage water filtration pond are formed, one group of relative both sides of filtering basin are mounted with cloth tank and catchment tray, between cloth tank and the sewage water filtration pond, grid all is installed between sewage water filtration pond and the catchment tray, other one group of opposite face in sewage water filtration pond is to fill out the worktable that unloads coal and get the charcoal of coalingging, and waste disposal plant is connected with pipeline, valve, water pump; All be connected with valve and device liaison tube on the connecting tube of cloth tank and catchment tray, interconnect by valve; The sewage water filtration pond is connected with sewer line, contact pipeline, drainage pipeline, fresh water pipeline, the contact pipeline is provided with water pump, the contact pipeline is connected by valve with catchment tray with the cloth tank of filtering basin, by valve, water pump control realization filtering basin being connected with series, parallel between the filtering basin and operation, the draining of filtering basin, getting coal, fill out the carrying out of operations such as coal; Coal filtrate sewage water filtration adsorption treatment device or for comprising pressure-bearing oily water separation cloth tank, pressure-bearing carbon coal water filter vat, the pressure-bearing catchment tray, Scraping device, coal-charcoal filter material, pipeline, by-pass valve control, device such as water pump is formed, coal filtrate sewage water filtration adsorption treatment device is at least one group, by pressure-bearing oily water separation cloth tank, pressure-bearing carbon coal water filter vat, the pressure-bearing catchment tray connects successively, comprises water feeding and draining device, Scraping device, the remittance discharge equipment, the remittance mud discharging device, coal-charcoal filter material, the remittance water-freeing arrangement, the backwash feeding apparatus, air inlet and outlet device, pipeline, by-pass valve control, the device that water pump etc. are formed; Wherein, pressure-bearing oily water separation cloth tank is by the corresponding seal and pressure bearing end cap of bottom land, a cell wall corresponding another side cell wall that keeps at a certain distance away, cell wall corresponding seal and pressure bearing water distribution frame that keeps at a certain distance away is formed the hexahedron groove, water feeding and draining device, the cloth tank, the remittance discharge equipment, Scraping device, the mud discharging device that converges is settled in it and is constituted, the remittance mud discharging device that is positioned at pressure-bearing oily water separation cloth bottom of gullet is connected with slush pump by the spoil disposal pipeline of valve control, the seal and pressure bearing end cap that is positioned at pressure-bearing oily water separation cloth tank top is for converging discharge equipment, be connected with oil-drain pipe by valve control, supplying drainage is by by-pass valve control and sewage feedwater piping, middle contact pipeline and middle contact pump connect; Pressure-bearing carbon coal water filter vat is by the corresponding seal and pressure bearing end cap of bottom land, a cell wall corresponding another side cell wall that keeps at a certain distance away, one group of expanded metals, rigidity grid keep at a certain distance away, and corresponding another organized expanded metals, the rigidity grid is formed the hexahedron groove, the charcoal coal of filling in the groove can be coal, charcoal, the plant ass charcoal of pulverizing, and air inlet and outlet device is installed on the groove; The pressure-bearing catchment tray is by the corresponding seal and pressure bearing end cap of bottom land, a cell wall corresponding another side cell wall that keeps at a certain distance away, seal and pressure bearing charge for remittance frame corresponding cell wall that keeps at a certain distance away is formed the hexahedron groove, catchment tray, seal and pressure bearing charge for remittance frame, filter captation, feeding apparatus are settled in it and are constituted, the remittance drainage pipeline and the fresh water pipeline of valve control are installed on the groove, fresh water pump, middle contact pipeline, middle contact pump, the contact pipe valve connects, the backwash feeding apparatus are connected with the backwash feedwater piping by by-pass valve control, the backwash feedwater piping is connected with fresh water pump, and the intake and exhaust pipeline that is connected on the seal and pressure bearing end cap connects atmosphere by valve; Coal filtrate sewage water filtration adsorption treatment device has the worktable of filling and unloading coal-charcoal and taking and loading carbon coal; All be connected with valve and device contact on the connecting tube of cloth tank and catchment tray, interconnect by valve; Coal filtrate sewage water filtration adsorption treatment device is by realizing filter vat and be connected with series, parallel between the filter vat and the carrying out of operations such as the operation of filter vat, coal-charcoal taking process, coal-charcoal filling process to valve, water pump control; Coal filtrate sewage water filtration adsorption treatment device or for comprising pressure-bearing oily water separation settling vessel, pressure-bearing oily water separation water distributor, Scraping device, pressure-bearing carbon coal water strainer, coal-charcoal filter material, pressure-bearing charge for remittance device, pressure sealer, pipeline, by-pass valve control, device such as water pump is formed, coal filtrate sewage water filtration adsorption treatment device is at least one group, by pressure-bearing oily water separation settling vessel, pressure-bearing oily water separation water distributor, pressure sealer, pressure-bearing carbon coal water strainer, pressure sealer, pressure-bearing charge for remittance device connects successively, comprises water feeding and draining device, Scraping device, the remittance discharge equipment, the remittance mud discharging device, coal-charcoal filter material, the remittance water-freeing arrangement, the backwash feeding apparatus, air inlet and outlet device, pipeline, by-pass valve control, the device that water pump etc. are formed; Wherein, pressure-bearing oily water separation settling vessel is by pressure resistant vessel, water distributor, the seal and pressure bearing end cap, the remittance discharge equipment, oily water separation remittance mud plate, precipitation inclined tube plate, water wheels or motorized motions Scraping device, the remittance mud discharging device, the connection of lifting group frame constitutes, the remittance mud discharging device that is positioned at pressure-bearing oily water separation settling vessel bottom is connected with slush pump by the spoil disposal pipeline of valve control, the seal and pressure bearing end cap that is positioned at pressure-bearing oily water separation settling vessel top is for converging discharge equipment, be connected with oil-drain pipe by valve control, supplying drainage is by by-pass valve control and sewage feed main, female pipe of middle contact and middle contact pump connect; Pressure-bearing oily water separation water distributor is by pressure resistant vessel, water distributor, water-freeing arrangement, remittance discharge equipment, Scraping device, remittance mud discharging device are settled in it and are constituted, the remittance mud discharging device that is positioned at pressure-bearing oily water separation water distributor bottom is connected with slush pump by the spoil disposal pipeline of valve control, the cavity volume that is higher than pressure-bearing carbon coal water strainer that is positioned at pressure-bearing oily water separation water distributor top is for converging discharge equipment, be connected with oil-drain pipe by valve control, supplying drainage is connected with sewage feed main, the female pipe of middle contact and middle contact pump by by-pass valve control; Pressure sealer is connected with the pipeline that charges into, emits gas or liquid by valve control, and pipe connection charges into the pump of medium; Pressure-bearing carbon coal water strainer is an expanded metals by at least one bottom surface, the rigidity grid is formed the cavity that the two double buckle of opening lumps together composition, built-in coal-charcoal filter material, or the coal-charcoal filter material in the pressure-bearing carbon coal water strainer is the corresponding seal and pressure bearing end cap of a wall that adds in by able to turn on or off button with lock, a wall corresponding another side wall that keeps at a certain distance away, one group of expanded metals, rigidity grid corresponding another group expanded metals that keeps at a certain distance away, the rigidity grid is formed container, hanger is arranged on the container, add the water filter of charcoal coal by hanging device, the charcoal coal of filling in the water filter can be the coal of pulverizing, charcoal, the plant ass charcoal, pressure-bearing carbon coal water filter bottom can be provided with well heater; Pressure-bearing charge for remittance device is by pressure resistant vessel, charge for remittance device, seal and pressure bearing charge for remittance frame, filtration captation, feeding apparatus are settled in it and are constituted, remittance drainage pipeline and the clear water mother that valve control is installed on the pressure resistant vessel manages, fresh water pump, the female pipe of middle contact, middle contact pump, the contact pipe valve connects, the backwash feeding apparatus are connected with the backwash feed main by by-pass valve control, and the backwash feed main is connected with fresh water pump, and the intake and exhaust pipeline that is connected on the pressure resistant vessel connects atmosphere by valve; Coal filtrate sewage water filtration adsorption treatment device has the lifting worktable of filling and unloading coal-charcoal and taking and loading carbon coal; All be connected with valve and device contact on the connecting tube of water distributor and charge for remittance device, interconnect by valve; Coal filtrate sewage water filtration adsorption treatment device is by realizing strainer and be connected with series, parallel between the strainer and the carrying out of operations such as the operation of strainer, draining, coal-charcoal taking process, coal-charcoal filling process to valve, water pump control; Coal has water vapour heating, drying device as the waste disposal plant bottom of filtrate, this device can evaporate strong sewage in the waste disposal plant of coal as filtrate, the water vapour that makes generation is linked into domestic refuse by pipeline and dehydrates and reclaim water of condensation tail gas auxiliary combustion equipment, or carries carbon used heat in the desulfurization of smoke density method and produce condensation in the device of steam.
3. according to claim 1 a kind of be the sewage-refuse treatment clean-production system at center with the power station, it is characterized in that: fuel processing system B: comprise that domestic refuse stores shredder assembly, domestic refuse dehydrates and reclaims water of condensation tail gas auxiliary combustion equipment, coal stores shredder assembly, coal filtrate drying and dewatering e Foerderanlage, coal and domestic garbage mixing device; Wherein, domestic refuse dehydrates and reclaims water of condensation tail gas auxiliary combustion equipment, by housing, blower fan, airheater, holder drying materials chain net, material dispenser, fly upward material collection chain net, fly-ash separator, air heat exchange condensers, wash spray device, water-recovering device, induced draft fan, air preheater etc. and form; Domestic refuse dehydrates recovery water of condensation tail gas auxiliary combustion equipment and is connected with gas blower, airheater, holder drying materials chain net, material dispenser in turn, flies upward devices such as material collection chain net, dilatation chamber, fly-ash separator, air heat exchange condensers, wash spray device, water-recovering device, induced draft fan, air preheater by pipeline, coagulate water and collect water tank and is connected with the air heat exchange condensers, hold in the palm drying materials chain net, fly upward the material that material collection chain net and fly-ash separator discharge and import material bin by e Foerderanlage by pipeline; Gas blower blasts well heater with air heating with wind, imports the drying garbage storehouse, with the online drying materials of holder drying materials chain in the dryness storehouse; Blown the material that flies upward and collect by flying upward material collection chain net, dust is collected by fly-ash separator, and the dust of collecting with fly-ash separator by the isolating oven dry rubbish of separation cleaning wheel is pooled on the device for transporting objects, imports the garbage fuel storehouse, the boiler of feeding burning; Through the mixed gas of fly-ash separator,,, blast the air preheater heating and import boiler auxiliary combustion by the gas after the water-recovering device dehydration through the condensation of air heat exchange condensers; Water of condensation and the spray washing water collected from the air heat exchange condensers import water reservoir; Whole device is a closed system.
4. according to claim 1 a kind of be the sewage-refuse treatment clean-production system at center with the power station, it is characterized in that: comprise the flying dust collection device among the flying dust treating system D, flying dust prilling granulator, fly ash granule e Foerderanlage, fly ash granule roasting assembly; Wherein, the fly ash granule roasting assembly is that compound being equipped with calcined the rotary calcining stove that contains Dioxins poisonous substance flying dust on garbage burning boiler, and the structure of rotary calcining stove is made up of burner, rotation calcining compartment, fly ash granule import, cooling air import, exhanst gas outlet, air intlet, fly ash granule outlet, cooling blower, separation fly-ash separator, insulation flue, supporting structure, transmission rig, garbage burning boiler, fly ash granule shaper, e Foerderanlage etc.; The employed body of heater of fly ash granule calcining furnace mainly is made up of three parts, and a part is a burning zone, and another part is rotation calcining section, and third part is the dedusting cooling section; Also be that the burning of burner body of heater produces high-temperature flue gas, introduce in the rotation calcining compartment, the fly ash granule that is passed to the rotation calcining compartment is carried out high-temperature calcination, by the cyclonic separator of installing at rotation calcining compartment afterbody, part flying dust in incinerating fly ash granule and the flue gas is collected by tornado dust collector, and flue gas is introduced into garbage burning boiler, and air cooling apparatus is installed in the tornado dust collector, reclaim used heat, the part flying dust in cooling fly ash granule and the flue gas is discharged it; Its controlled temperature can keep the weighing apparatus of cigarette temperature fixed by strengthening the air amount of feeding, coal is fully burnt, for material can be moved in the rotation calcining compartment, rotation calcining compartment body tilts to install, after containing the calcining of Dioxins flying dust, tornado dust collector are used to collect flying dust and the flue dust after the calcining, flue gas after the calcining is connected in the furnace chamber of garbage burning boiler by utilidor, can be with this flue gas as secondary air, fly ash granule after slag and the calcining can be by mending air cooling, also can absorb heat by water and water vapour, use as the boiler replenishing water preheater, the capacity of this calcining burner is as the criterion to satisfy the calcining fly ash granule.
5. according to claim 1 a kind of be the sewage-refuse treatment clean-production system at center with the power station, it is characterized in that: comprise fume dust remover among the smoke processing system E, flue gas heat-recovering device, the desulfurization of smoke density method are carried carbon used heat and are produced distilled water device, heating fume emission device; Wherein, method and the device that carbon used heat is produced steam carried in the desulfurization of smoke density method, connected to form by devices such as flue, dilatation cavity, induced draft fan, chimney, well heater, water pump, gas extraction device, ponds; Device is to utilize chemical method to realize the purification of flue gas, utilizes water vapour heat release condensation in the flue gas, and the different characteristics of all gases density, realizes fume-dehydrating and all gases separation and Extraction with the physics method, makes its resource utilization; This device is the cavity that connects built-in hot tube heat exchanger on the boiler flue behind the fly-ash separator, and hot tube heat exchanger has deashing device; The cavity outlet of hot tube heat exchanger connects another dilatation cavity, and the dilatation cavity has enough degree of depth, enough sectional area and volume; The dilatation cavity bottom has deashing flushing water distributor device, and the dilatation cavity bottom has catchment tray, and catchment tray is connected with settling tank; Flue gas enters the dilatation cavity front portion that is attached thereto from the hot tube heat exchanger cavity, discharges from the open top of dilatation cavity; In the dilatation cavity flue gas heater is installed, the thermosiphon and the sewer line that the incondensable gas discharge equipment are installed on the flue gas heater and vertically arrange, with on put vaporizer and be connected, the vaporizer top is connected with blow-off line, flue gas heater is connected with water shoot, and former water water service pipe is connected with flue gas heater; Water-recovering device is installed after flue gas heater; Be connected with the air pressure balance pipeline between settling tank top and the dilatation cavity, be connected with slush pump and dewatering unit on the settling tank, settling tank is connected with water pump, water pump is connected with water filtering device with dilatation cavity bottom deashing device, and water filtering device is connected with flue gas heater water distribution feeding apparatus with flue gas heater top deashing device; On catchment tray and pipeline that settling tank is connected, throttling set is installed is connected with inverted-loop tube one end, the other end of inverted-loop tube places pneumatic trough bottom lowest part; In the dilatation cavity pneumatic trough, the extraction gas device is installed, the waste gas that leaks that extracts gas device is discharged in the dilatation cavity by gas barrier; The smoke discharge tube at dilatation cavity top is connected with induced draft fan, hot tube heat exchanger, and the heat sink of hot tube heat exchanger and the heat-releasing device of hot tube heat exchanger are by pipe connection, and the hot tube heat exchanger cavity is connected with flue, chimney; That complete assembly has is corrosion-resistant, insulation, sealing characteristics; Or be a kind of cold-water solution method flue gas desulfurization (FGD) unit, connect to form by devices such as flue, flue gas heat exchange device, heat pipe evaporator, flash vessel, flue gas heating distiller, spray washing fume and dust device, water-cooled flue gas device, cold-water solution flue gas desulfurization device, cold-water sprinkler, water-recovering device, induced draft fan, gas compression condenser, water cooler, interchanger, heat pipe condenser, gas-liquid separator, gas cooler, refrigerator, cooling tower, chimney, deposition filter, storage ash pond, pump, water collecting basin, pipelines; The device operating principle is: cold water has powerful dissolving power to sulfur dioxide gas, and heating for dissolving has the water of sulfur dioxide gas, and sulfur dioxide gas cognition is disengaged from water; A kind of cold-water solution method flue gas desulfurization (FGD) unit, its technical process is: use the interchanger cooled flue gas, water vapor condensation in the flue gas is removed, with flash vessel, water spray system with flue gas ash removal, water cold flue gas device reduces the cigarette temperature, with the cold water spray, and dissolving sulfur in smoke gas, to being dissolved with the cold water heating of sulfur dioxide gas, sulfur dioxide gas is disengaged from water; Its process system comprises: arrange the flue gas system that assemblies cold-water solution method flue gas desulfurization (FGD) unit successively by parts such as flue, flue gas heat exchange device, heat pipe evaporator, flash vessel, flue gas heating distiller, spray washing fume and dust device, water-cooled flue gas device, cold-water solution flue gas desulfurization device, cold-water sprinkler, water-recovering device, induced draft fan, gas compression condenser, water cooler, flue gas heat exchange device, chimneys; Arrange the process water system that assemblies cold-water solution method flue gas desulfurization (FGD) unit successively by parts such as water-recovering device, cold-water sprinkler, cold-water solution flue gas desulfurization device, water collecting basin, pipeline, water pump, water-cooled flue gas device, deposition filter, water cooler, interchanger, heat pipe condenser, gas-liquid separator, interchanger, cooling tower, refrigerator, cold-water sprinklers; Arrange the sulfur dioxide gas gathering system that assemblies cold-water solution method flue gas desulfurization (FGD) unit successively by parts such as gas-liquid separator, gas cooler, gas compression condensers; Arrange the flue gas cool-down heat recovery water processing desalination system that assemblies cold-water solution method flue gas desulfurization (FGD) unit successively by parts such as flue gas heating distiller, cooling towers; Arrange the washing fume and dust system that assemblies cold-water solution method flue gas desulfurization (FGD) unit successively by parts such as spray washing fume and dust device, buck collecting tank, grey water pump, deposition filter, recycle pump, spray washing fume and dust devices; Arrange the wet dust removing system that assemblies cold-water solution method flue gas desulfurization (FGD) unit successively by parts such as deposition filter, slurry pump, mortar pool, removing ash pipelines; Devices such as flue gas heat exchange device, heat pipe evaporator, flue gas heating distiller are furnished with ash exhauster clearly, and the dilatation cavity bottom has devices such as deashing flushing water distributor, and the dilatation cavity bottom has catchment tray, and catchment tray is connected with settling tank; That complete assembly has is corrosion-resistant, insulation, sealing characteristics; Or be that a kind of cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit, by flue, the flue gas heat exchange device, heat pipe evaporator, flash vessel, the flue gas heating distiller, spray washing fume and dust device, water-cooled flue gas device, the cold-water solution flue gas desulfurization device, cold-water sprinkler, water-recovering device, induced draft fan, the gas compression condenser, water cooler, interchanger, the electrolytic anode groove, the electrolysis cathode groove, settling vessel, the carbon dioxide injector, storage hydrogen device, direct supply, electrical lead, heat pipe condenser, gas-liquid separator, gas cooler, refrigerator, cooling tower, chimney, deposition filter, store up grey pond, pump, water collecting basin, devices such as pipeline connect to form; The device work principle is: cold water has powerful dissolving power to sulfur dioxide gas, and the water in the electrolysis cathode groove shows alkalescence, can increase the absorption of water to sulfur dioxide gas; It is acid that water in the electrolytic anode groove shows, and can make sulfurous acid become sulfur dioxide gas, and heating for dissolving has the water of sulfur dioxide gas, and sulfur dioxide gas cognition is disengaged from water; A kind of cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit, its technical process is: use the interchanger cooled flue gas, water vapor condensation in the flue gas is removed, with flash vessel, water spray system with flue gas ash removal, water cold flue gas device reduces the cigarette temperature, with the cold water spray, and dissolving sulfur in smoke gas, to being dissolved with the cold water heating of sulfur dioxide gas, sulfur dioxide gas is disengaged from water; Its process system comprises: be disposed in order by parts such as flue, flue gas heat exchange device, heat pipe evaporator, flash vessel, flue gas heating distiller, spray washing fume and dust device, water-cooled flue gas device, cold-water solution flue gas desulfurization device, cold-water sprinkler, water-recovering device, induced draft fan, gas compression condenser, water cooler, flue gas heat exchange device, chimneys and assembly the flue gas system that the cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit; Be disposed in order the process water system that the cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit that assemblies by parts such as water-recovering device, cold-water sprinkler, cold-water solution flue gas desulfurization device, water collecting basin, pipeline, water pump, water-cooled flue gas device, deposition filter, water cooler, interchanger, heat pipe condenser, gas-liquid separator, interchanger, cooling tower, refrigerator, cold-water sprinklers; Be disposed in order by parts such as electrolytic anode groove, electrolysis cathode groove, settling vessel, carbon dioxide injector, storage hydrogen device, direct supply, electrical leads and assembly electrolysis that the cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit and remove hard alkali addition process system; Be disposed in order by parts such as gas-liquid separator, gas cooler, gas compression condensers and assembly the sulfur dioxide gas gathering system that the cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit; Be disposed in order by parts such as flue gas heating distiller, cooling towers and assembly the flue gas cool-down heat recovery water that the cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit and handle desalination system; Be disposed in order the washing fume and dust system that the cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit that assemblies by parts such as spray washing fume and dust device, buck collecting tank, grey water pump, deposition filter, recycle pump, spray washing fume and dust devices; Be disposed in order by parts such as deposition filter, slurry pump, mortar pool, removing ash pipelines and assembly the wet dust removing system that the cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit; Devices such as flue gas heat exchange device, heat pipe evaporator, flue gas heating distiller are furnished with ash exhauster clearly, and the dilatation cavity bottom has devices such as deashing flushing water distributor, and the dilatation cavity bottom has catchment tray, and catchment tray is connected with settling tank; That complete assembly has is corrosion-resistant, insulation, sealing characteristics.
6. according to claim 1 a kind of be the sewage-refuse treatment clean-production system at center with the power station, it is characterized in that: the distillation desalting plant among the water treatment system A comprises compositions such as hot gas heat collector (flue gas heater, oven dry rubbish mixture heat gas), multiple-effect evaporator, cooler condenser, heat exchanger, fresh water pump well, raw water box, fresh-water tank, pump, valve, pipeline, lagging material; Hot gas is a water vapor, or high temperature mixing gas, and hot gas heat collector is for importing and exporting the pipeline that is connected with heat collector up and down and constitute hot gas heat collector by being provided with fluid; Wherein, this installs employed hot gas heat collector is the protection against corrosion heat collector, or is static good antiscale property heat collector; Multiple-effect evaporator is for each other independently, and one-level is above, forms by each cavity of pipe connection; First evaporator is vertically to settle, and connects the thermosyphon circulation vaporizer that the tube chamber of outer wall insulation constitutes by pipeline, valve; First evaporator and second stage vaporizer are by pipe connection, and wherein, the second stage and N level vaporizer are the interchanger of shell structure, are made up of lateral arrangement or vertical tube bundle, tube sheet and housing of arranging; Be that floor plan or folded layer by layer sieve are vertically arranged between the vaporizer, interconnected by pipeline, valve, a plurality of shell cavitys of outer wall insulation constitute; Install used geothermal heat exchanger and be static good antiscale property heat exchanger; Heat collector bottom water inlet pipe mouth is connected by utilidor with the first evaporator bottom effluent pipe mouth of multiple-effect evaporator, heat collector top effluent pipe mouth, by being located at the incondensable gas automatic exhaust device on the hot gas heat collector top, be connected with thermosiphon bottom return water pipe in the first evaporator of multiple-effect evaporator; The heating source of hot gas heat collector is that its structure of water vapor is vertical shell heat exchange structure, original water inlet enters from hot gas heat collector bottom, discharges from the top, is connected with thermosiphon, hot gas heat collector heating vapour side has water vapor to insert, and water of condensation is drawn from the bottom; Or the heating source of hot gas heat collector is a high temperature mixing gas, its structure is vertical shell heat exchange structure, original water inlet enters from hot gas heat collector bottom, discharge from the top, be connected with thermosiphon, hot gas heat collector heated side has high temperature mixing gas to insert, and the mixing gas after the heat exchange is discharged, and water of condensation is drawn from the bottom; There is the heat exchanger steam inlet pipe of steam discharge pipe and second stage vaporizer to be connected in the steam chest of first evaporator top; The new water make-up pipe in valve control ground feeds water in its vaporizer; First evaporator and heat collector can be provided with one control air valve; First evaporator steam discharge pipe steam inlet is placed in the steam chest of vaporizer top, and steam discharge pipe is connected with the heat exchanger steam inlet pipe of second stage vaporizer; The water shoot of first evaporator can be connected with feedwater heating apparatus and be connected with second stage vaporizer water distributor by valve control; Second stage vaporizer steam discharge pipe steam inlet is placed in the vaporizer steam chest, second stage vaporizer steam discharge pipe steam outlet is connected with the interior heat exchanger steam inlet pipe of third evaporator, water of condensation rising pipe in the vaporizer of the second stage can be connected with feedwater heating apparatus draws, be connected with heat exchanger in the third evaporator by U-shaped pipe pressure temperature regulator, concentrated water drainage water pipe in the vaporizer of the second stage can be connected heat exchange with feedwater heating apparatus by U-shaped pipe pressure temperature regulator draws, and is connected with the third evaporator water-in by the concentrated water drainage water pipe; Third evaporator steam discharge pipe steam inlet is placed in the vaporizer steam chest, third evaporator steam discharge pipe steam outlet is connected with the interior heat exchanger steam inlet pipe of next stage vaporizer, water of condensation rising pipe in the third evaporator can be connected with feedwater heating apparatus draws, be connected with heat exchanger in the next stage vaporizer by U-shaped pipe pressure temperature regulator, concentrated water drainage water pipe in the third evaporator can be connected heat exchange with feedwater heating apparatus by U-shaped pipe pressure temperature regulator draws, and is connected with next stage vaporizer water-in by the concentrated water drainage water pipe; Its system architecture of N level vaporizer is equal to third evaporator; The final evaporator steam discharge pipe is connected with the steam heating feed feeder, final evaporator water of condensation rising pipe is connected with the steam heating feed feeder by feedwater heating apparatus, the former water rising pipe of steam heating feed feeder is connected with feedwater heating apparatus, the dense tank of final evaporator is connected with dense water water storage box, and dense water water storage box is connected with by-pass valve control, blow-off pipe, pump etc.; The steam heating feed feeder is by the pipe connection cooler condenser; Wherein, cooler condenser can be former water cooled condenser, or is air-cooled cold water cooler condenser; The bottom of steam heating feed feeder is connected with the fresh water pump well by pipeline, and the rising pipe of fresh water pump well is connected with fresh-water tank by water pump, valve; Former water cooled condenser is placed in the underwater certain depth, places in the tube chamber, and water-in places former water cooled condenser lower bottom part, and the water inlet of cooling raw water tubes is provided with filtration unit, and water outlet communicates with former water body, constitutes closed loop with water body; Air-cooled cold water cooler condenser is that two-layer condenser up and down is installed in the air-cooled tower, and the spray water-distributing device is arranged between the two-layer condenser; Cooler condenser is connected with the fresh water pump well by pipeline; Former water intake filters the back by filtration unit and imports former water water storage box, be provided with former water intake pipe in the former water water storage box, be connected with the multiple-effect evaporator water supply installation, the operation of apparatus system is connected, controls and realize by the reasonable Arrangement of corresponding pipeline, valve, pump and water tank.
7. according to claim 1 a kind of be the sewage-refuse treatment clean-production system at center with the power station, it is characterized in that: the distillation desalting plant among the water treatment system A comprises compositions such as hot gas heat collector (flue gas heater, oven dry rubbish mixture heat gas), multiple-effect evaporator, cooler condenser, heat exchanger, fresh water pump well, raw water box, fresh-water tank, pump, valve, pipeline, lagging material; Hot gas is a water vapor, or high temperature mixing gas, and hot gas heat collector is for importing and exporting the pipeline that is connected with heat collector up and down and constitute hot gas heat collector by being provided with fluid; Wherein, this to install employed hot gas heat collector be static good antiscale property heat collector; In the hot gas heat collector exhaust tube chamber thermal source well heater can be installed; Multiple-effect evaporator is for independently, and one-level is above, vertically settles, and interconnected by pipeline, valve, a plurality of tube chambers of outer wall insulation constitute; Install used geothermal heat exchanger and be static good antiscale property heat exchanger; Heat collector bottom water inlet pipe mouth is connected by utilidor with the first evaporator bottom effluent pipe mouth of multiple-effect evaporator, and heat collector top rising pipe is connected with the thermosiphon bottom return water pipe of first evaporator in the multiple-effect evaporator by the incondensable gas automatic exhaust device that is located on the hot gas heat collector top; The heating source of hot gas heat collector is that its structure of water vapour is vertical shell heat exchange structure, original water inlet enters from hot gas heat collector bottom, discharges from the top, is connected with thermosiphon, hot gas heat collector heating vapour side has water vapor to insert, and water of condensation is drawn from the bottom; Or the heating source of hot gas heat collector is a high temperature mixing gas, its structure is vertical shell heat exchange structure, original water inlet enters from hot gas heat collector bottom, discharge from the top, be connected with thermosiphon, hot gas heat collector heated side has high temperature mixing gas to insert, and the mixing gas after the heat exchange is discharged, and water of condensation is drawn from the bottom; There is steam discharge pipe to be connected in the steam chest of first evaporator top with the heat exchanger steam inlet pipe of vaporizer bottom, the second stage; The new water make-up pipe in valve control ground feeds water in the first evaporator; First evaporator can be provided with one control air valve; The water shoot of valve control is arranged in first evaporator, and water shoot can be connected with feedwater heating apparatus; Second stage vaporizer has the new water make-up pipe in valve control ground that water is fed in it; The steam discharge pipe steam inlet is placed in the steam chest of vaporizer top, and steam discharge pipe is connected with the heat exchanger steam inlet pipe of next stage vaporizer; The heat exchanger bottom condensate water rising pipe of second stage vaporizer picks out pipeline and is connected with the heat exchanger of next stage vaporizer on certain altitude, constitute the pressure and temp controller; Wherein, the heat exchanger bottom condensate water rising pipe of second stage vaporizer can at first connect feedwater heating apparatus, is connected with the heat exchanger of next stage vaporizer after the heat exchange again; Vaporizer top, the second stage is provided with one control air valve; Second stage vaporizer is provided with the water shoot of valve control, and water shoot can be connected with feedwater heating apparatus; In the vaporizer of the second stage, heat exchanger places vertical tube chamber, and the tube chamber lower bottom part has water-in, forms riser waterborne chamber, riser waterborne chamber with fall tube chamber top and bottom under water and communicate; N level vaporizer can be identical with second stage evaporator system apparatus structure; Final evaporator has the dirty pipe of concentrated water drainage, and the dirty pipe of concentrated water drainage is for there being the pipe that water seal is arranged of valve control; The condensate pipe and the steam discharge pipe of the heat exchanger of final evaporator all pick out with setting height, are connected with the steam heating feed feeder; At the final evaporator top one control air valve is installed; The steam heating feed feeder is by the pipe connection cooler condenser; Wherein, cooler condenser can be former water cooled condenser, or is air-cooled cold water cooler condenser; The bottom of steam heating feed feeder is connected with the fresh water pump well by pipeline, and the rising pipe of fresh water pump well is connected with fresh-water tank by water pump, valve; Former water cooled condenser is placed in the underwater certain depth, places in the tube chamber, and water-in places former water cooled condenser lower bottom part, and the water inlet of cooling raw water tubes is provided with filtration unit, and water outlet communicates with former water body, constitutes closed loop with water body; Air-cooled cold water cooler condenser is that two-layer condenser up and down is installed in the air-cooled tower, and the spray water-distributing device is arranged between the two-layer condenser; Cooler condenser is connected with the fresh water pump well by pipeline; Former water intake filters the back by filtration unit and imports former water water storage box, be provided with former water intake pipe in the raw water box, be connected with the multiple-effect evaporator water supply installation, the operation of apparatus system is connected, controls and realize by the reasonable Arrangement of corresponding pipeline, valve, pump and water tank.
8. according to claim 1 a kind of be the sewage-refuse treatment clean-production system at center with the power station, it is characterized in that: comprise steam turbine multimedium condenser device among the circulating water cooling system G, water distiller condenser device, the compound cooling tower of air-cooled cold water; The multimedium condenser is at conventional condenser hydroecium plug-in mounting sleeve or dividing plate, the not connected hydroecium more than two groups will be become between the condenser hydroecium, pass to different heat-eliminating mediums, a kind of heat-eliminating medium is used to reclaim the used heat of condenser discharging, another kind of heat-eliminating medium is connected with cooling tower, is used for the used heat of relief condenser discharging; Air cooled water composite cooling tower is by tower body, ventilator, ventilation installation, air distribution device, air-cooler, water distribution system, liquid distribution, water eliminator, water collector, advance, outlet conduit and irrigation canals and ditches, compositions such as other facilities, it is the water distribution heat exchange packing layer in the cooling tower shell and sprays wind direction under the water-distributing device, or water eliminator air outlet place, be provided with the air-cooler that has air cooling unit to connect to form that is fixed on the support, the air-cooler that is installed on natural wind cooling tower and machine power circulation cooling tower does not have and allows the directly big space of circulation of air, support is fixed on the load-bearing supporter of cooling tower, the female pipe of water inlet at first with the cooling tower air duct in the water-in of air-cooler assembly be tightly connected respectively by pipe joint, with hot water introducing air chiller assembly, by water distributor distribution water distribution in the air-cooler assembly, through air-cooler refrigerative water, collect by the charge for remittance pipeline that is positioned at the air-cooler end, be distributed on the packing layer through water-distributing device, conflux in the cooling water reservoir, air-cooler collection pipe water outlet, directly be connected by valve with the intake pipe that by-pass valve control is installed of circulating water pool, supply water for the water circulating pump intake pipe jointly, the air-cooler assembly can be made by metallic substance or other good material of heat conductivility and shape, and the fin of air-cooler is extruded by metal, expanded joint, welding, technology manufacturings such as casting.
9. according to claim 1 a kind of be the sewage-refuse treatment clean-production system at center with the power station, it is characterized in that: the industrial sewage processing unit among the water treatment system A, industrial sewage processing unit comprises the personal water softening water reclamation system of the reduction of chemical water treatment system, and the reduction discharging acid-base neutralisation water of chemical water treatment system is manually prepared sea water system; Coal is as the papermaking wastewater filtration treatment system device of filtrate, and wherein, acid dense sewer of water distillation desalting plant and coal are as the alkaline discharge water neutralizing treatment discharging of the papermaking wastewater filtration treatment device discharging of filtrate; Or be that water treatment of power plant is partially recycled from water soft water, the spent acid salkali waste is used for ash removal pipe antiscale scale inhibition, and ash removal pipe is installed static good antiscale property device simultaneously, makes spent acid, alkali place Hui Chang to carry out neutralizing treatment; Among the extraction for heat supply boiler deoxidizing method draining system G, comprise boiler deoxidizing method vapour among the system G, rubbish oven dry vapour, coal filtrate oven dry vapour, externally heat supply vapour; Wherein, rubbish oven dry, coal filtrate oven dry hydrophobic with the vapour condensation then mended into deoxygenator by water pump by processing such as magnetic filter, strainers with the vapour condensation is hydrophobic.
10. according to claim 1 a kind of be the sewage-refuse treatment clean-production system at center with the power station, it is characterized in that: be the method and the device (application number: 95110474.8) of power plant's conventional system and descaling of ash removal pipe of power plant, improved power plant water and ash treatment system (application number: 95112258.4), multimedium distiller (application number: 95235083.1), hot gas heat hot siphon circulating evaporator surface film multi-effect distilling desalting plant (application number: 02160361.8), a kind of hot gas heating thermosyphon circulation submergence tubular type multiple-effect evaporation desalting plant (application number: 02160360.X), a kind of device and installation method (application number: 03103219.2) that is used for the multimedium distiller hydroecium of recovery of heat, a kind of method of sea water desaltination and device (application number: 95112245.2), a kind of electrolytic process water treatment device (application number: 200310120032.7), a kind of with the waste disposal plant (application number: 03101146.2) of coal as filtrate, a kind of floating combined modules environmental protection landscape wetland device (application number: 200310101151.8) of diving, a kind of floating composite module constructed wetland device (application number: 200410044486.5) of diving, a kind of module combined type bearing coal filtering waste disposal plant (application number: 200310113946.0), a kind of with the bearing sewage treating apparatus (application number: 200310113950.7) of charcoal coal as filtrate, air cooled water composite cooling tower (application number: 02131789.5), method and the device (application number: 03103694.5) that carbon used heat is produced steam carried in the desulfurization of a kind of smoke density method, a kind of cold-water solution electrolysis removes hard alkali adding method flue gas desulfurization (FGD) unit (application number: 200310124006.1), a kind of cold-water solution method flue gas desulfurization (FGD) unit (application number: 200310124007.6), a kind of domestic refuse dehydrates and reclaims water of condensation tail gas auxiliary combustion equipment (application number: 03103221.4), a kind of calcining burning boiler that removes rubbish contains the method and the device (application number: 03103982.0) of Dioxins flying dust, (application number: 03108558.X) etc. technology is according to the characteristic of its conventional power plant with require to combine successively for a kind of power generation and heat supply cleaning system with municipal sewage as a resource.
CN 200410155264 2004-08-30 2004-08-30 Sewage-refuse treatment clean-production system at the center of generating plant CN1743284A (en)

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Cited By (20)

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CN101805081A (en) * 2010-03-22 2010-08-18 山东电力工程咨询院有限公司 Water treatment system of power plant for combining multi-path water into one path of water
CN101963357A (en) * 2010-09-19 2011-02-02 河北景明循环产业股份有限公司 Method for generating power by using sludge
WO2012122841A1 (en) * 2011-03-16 2012-09-20 上海伏波环保设备有限公司 System for drying sludge by steam extracted from boiler set with thermal compensation
CN102806224A (en) * 2011-06-02 2012-12-05 吴军伟 Integral treating device for urban sludge and household garbage
EP2551025A1 (en) * 2010-03-25 2013-01-30 Hebei Building Materials Industry Design and Research Institute Combined treatment process of domestic garbage and sewage
CN103058440A (en) * 2013-01-17 2013-04-24 孔繁正 Municipal sewage and garbage centralized processor
CN103641255A (en) * 2013-11-26 2014-03-19 邯郸市奥博水处理有限公司 Integrated processing system for industrial flue gas, wastewater, urban regenerated water and circulating cooling water
CN104628237A (en) * 2015-01-23 2015-05-20 广东电网有限责任公司电力科学研究院 Sludge drying incineration system based on thermal power plant
CN104654900A (en) * 2014-03-13 2015-05-27 广西西创自动化有限公司 Descaling method for evaporating pot
CN105240859A (en) * 2015-10-30 2016-01-13 大连科林能源工程技术开发有限公司 Energy-self-supplying type chemical engineering sludge drying and burning system
CN105921484A (en) * 2016-05-04 2016-09-07 扬州市同创再生资源有限公司 Comprehensive utilization method of furnace slag in household garbage incineration power plant
CN106495308A (en) * 2016-12-08 2017-03-15 安徽睿知信信息科技有限公司 A kind of sewage disposal device and its technique
CN107036104A (en) * 2017-04-27 2017-08-11 江苏天楹环保能源成套设备有限公司 A kind of MSW Incineration Plant saves water arrangement system
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CN107487865A (en) * 2017-09-12 2017-12-19 中山大学 A kind of bioelectrochemistry effectively processing phenolic waste water containing chromium and the method produced electricity
CN107585940A (en) * 2017-10-10 2018-01-16 刘惠云 A kind of system that refuse depot sepage is handled using boiler waste gas
CN108726784A (en) * 2018-06-21 2018-11-02 邹福灶 A kind of factory's wastewater treatment reuse means
CN109081489A (en) * 2018-08-03 2018-12-25 江西汇海环保科技有限公司 A kind of highly difficult organic wastewater with difficult degradation thereby treatment process of processing
CN109179832A (en) * 2018-09-06 2019-01-11 清华大学 A kind of public environmentally friendly factory of full resource utilization of industrial high-salt wastewater based on thermal method
CN110304786A (en) * 2018-03-21 2019-10-08 东佑生物株式会社 The processing water of debirs food waste water is without releasing processing equipment for recycling and its processing method

Cited By (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101805081A (en) * 2010-03-22 2010-08-18 山东电力工程咨询院有限公司 Water treatment system of power plant for combining multi-path water into one path of water
EP2551025A4 (en) * 2010-03-25 2015-01-14 Hebei Building Materials Industry Design And Res Inst Combined treatment process of domestic garbage and sewage
EP2551025A1 (en) * 2010-03-25 2013-01-30 Hebei Building Materials Industry Design and Research Institute Combined treatment process of domestic garbage and sewage
CN101963357A (en) * 2010-09-19 2011-02-02 河北景明循环产业股份有限公司 Method for generating power by using sludge
DE112011105039B4 (en) * 2011-03-16 2016-09-15 Shanghai Fubo Environmental Equipment Co., Ltd. System for sludge drying by steam, which is taken from a boiler unit with thermal compensation
WO2012122841A1 (en) * 2011-03-16 2012-09-20 上海伏波环保设备有限公司 System for drying sludge by steam extracted from boiler set with thermal compensation
CN102806224A (en) * 2011-06-02 2012-12-05 吴军伟 Integral treating device for urban sludge and household garbage
CN103058440A (en) * 2013-01-17 2013-04-24 孔繁正 Municipal sewage and garbage centralized processor
CN103641255A (en) * 2013-11-26 2014-03-19 邯郸市奥博水处理有限公司 Integrated processing system for industrial flue gas, wastewater, urban regenerated water and circulating cooling water
CN103641255B (en) * 2013-11-26 2014-12-10 邯郸市奥博水处理有限公司 Integrated processing system for industrial flue gas, wastewater, urban regenerated water and circulating cooling water
CN104654900A (en) * 2014-03-13 2015-05-27 广西西创自动化有限公司 Descaling method for evaporating pot
CN104654900B (en) * 2014-03-13 2016-06-15 广西西创自动化有限公司 The descaling method of evaporator
CN104628237A (en) * 2015-01-23 2015-05-20 广东电网有限责任公司电力科学研究院 Sludge drying incineration system based on thermal power plant
CN105240859A (en) * 2015-10-30 2016-01-13 大连科林能源工程技术开发有限公司 Energy-self-supplying type chemical engineering sludge drying and burning system
CN105921484B (en) * 2016-05-04 2017-12-01 扬州市同创再生资源有限公司 A kind of method of MSW Incineration Plant comprehensive utilization of slag
CN105921484A (en) * 2016-05-04 2016-09-07 扬州市同创再生资源有限公司 Comprehensive utilization method of furnace slag in household garbage incineration power plant
CN106495308A (en) * 2016-12-08 2017-03-15 安徽睿知信信息科技有限公司 A kind of sewage disposal device and its technique
TWI595203B (en) * 2016-12-27 2017-08-11 Jian Liang-Cheng Burning furnace equipment
CN107036104A (en) * 2017-04-27 2017-08-11 江苏天楹环保能源成套设备有限公司 A kind of MSW Incineration Plant saves water arrangement system
CN107487865A (en) * 2017-09-12 2017-12-19 中山大学 A kind of bioelectrochemistry effectively processing phenolic waste water containing chromium and the method produced electricity
CN107585940A (en) * 2017-10-10 2018-01-16 刘惠云 A kind of system that refuse depot sepage is handled using boiler waste gas
CN107585940B (en) * 2017-10-10 2020-08-07 泉州台商投资区国进信息技术有限公司 System for treating leachate of garbage station by using boiler waste gas
CN110304786A (en) * 2018-03-21 2019-10-08 东佑生物株式会社 The processing water of debirs food waste water is without releasing processing equipment for recycling and its processing method
CN108726784A (en) * 2018-06-21 2018-11-02 邹福灶 A kind of factory's wastewater treatment reuse means
CN108726784B (en) * 2018-06-21 2021-06-11 贵港市霖达羽绒制品有限公司 Mill is with effluent treatment device of recycling
CN109081489A (en) * 2018-08-03 2018-12-25 江西汇海环保科技有限公司 A kind of highly difficult organic wastewater with difficult degradation thereby treatment process of processing
CN109179832A (en) * 2018-09-06 2019-01-11 清华大学 A kind of public environmentally friendly factory of full resource utilization of industrial high-salt wastewater based on thermal method

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