CN102557166A - Process for producing purified water by adopting sewage - Google Patents

Process for producing purified water by adopting sewage Download PDF

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Publication number
CN102557166A
CN102557166A CN201010597035XA CN201010597035A CN102557166A CN 102557166 A CN102557166 A CN 102557166A CN 201010597035X A CN201010597035X A CN 201010597035XA CN 201010597035 A CN201010597035 A CN 201010597035A CN 102557166 A CN102557166 A CN 102557166A
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CN
China
Prior art keywords
sewage
chamber
liquid
heat exchange
water
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Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201010597035XA
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Chinese (zh)
Inventor
藏树正
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Individual
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Individual
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Publication date
Application filed by Individual filed Critical Individual
Priority to CN201010597035XA priority Critical patent/CN102557166A/en
Publication of CN102557166A publication Critical patent/CN102557166A/en
Pending legal-status Critical Current

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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

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  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

The invention relates to a process for producing purified water by adopting sewage. The process comprises a vaporization chamber (6), a liquefaction chamber (13) and a liquid heat exchange tank (15), and is characterized in that the vaporization chamber (3) and the liquefaction chamber (13) both carry out circulating heat exchange in a closed vacuum insulating layer (5); a heat storage body (8), a heater (2) and a temperature control probe (9) are arranged in the vaporization chamber (6); a heat exchanger (7), a forcible circulating inlet (12) and a liquid level controller (14) are arranged in the liquefaction chamber (13); and a methane tank (20) is arranged for sewage treatment of large cities.

Description

Sewage system pure water technology
Affiliated technical field
A kind of sewage disposal technology, particularly a kind of sewage system pure water technology.
Background technology
Sewage water treatment method has membrane technique; Quick-fried gas of mud and thermal treatment learn a skill, and wherein the quick-fried gas technology of membrane technique and mud is applied to be mostly to obtain middle water in the extensive water treatment, accomplishes qualified discharge; And can not accomplish recycle, and heat treatment technics is applied to the water treatment of torrid areas country more.
Summary of the invention
The invention provides water quality such as a kind of use heat treatment technology Treating Municipal Sewage, chemical engineering sewage, seawater, make water quality after the processing reach the degree of the drinkable recycling of high-quality pure water.Difficult in order to solve town water, marine, family uses the high-quality shipwreck of drinking, the problem that the chemical plant WWT is difficult.
Its technical scheme is: after sewage is vaporized, make solid-liquid separation, all solids material in the liquid is all separated out; Gas carries out heat exchange with sewage again; Its solution is to make sewage pass through to get into liquid heat exchange pond (15) behind the filter screen, pass through automatic control pump (29) then and get into liquefied room (13), heat exchanger (7) in and high temperature purification water and high-temperature steam get into vaporizing chamber (6) after carrying out heat exchange and in chamber (6), spray high temperature sewage liquid to vapour through spray thrower (10); Make liquid vaporization fully in vaporizing chamber; Solid matter is through thermal store (8), and well heater (2) falls, and discharges through solid matter relief outlet (1).Gas through steam export mouth (11) get into liquefied room (13) again with heat exchanger (7) in sewage carry out heat exchange; And liquefaction simultaneously; And then import liquid liquid interchanger (16) and sewage in the liquid heat exchange pond (15) and carry out flowing into water purification underpressure chamber (17) after the big area heat exchange completely and flow out through water purification valve (18); Accomplish sewage purification process; If then sewage is behind multilayer sewage filter net (28) in the urban sewage purification, throw out, mud etc. flow into methane-generating pit (26) naturally and in methane-generating pit, behind about 50 ℃ high temperature 2-3 hour aerogenesis, discharge the natural pond slag; The natural pond slag through settling chamber (22) air-dry or oven dry filtrating flow into get into once more after the reservoir (23) sewage inlet (19) natural pond slag through the natural pond slag derive machine (21) and derive and be used for fertilizer, fuel etc.; Biogas is derived by biogas export mouth (20), and (27) are the methane-generating pit well heaters, finally accomplishes the green whole process of handling of municipal effluent.Above equipment all is enclosed in vacuum heat-insulating layer (5) and the thermal insulation layer (3,4), and the 30th, the pump circulation outlet.
Its beneficial effect is: treatment effect is good, can become tap water to sewage, cycling and reutilization; Solve the not enough problem of Urban water supply, WWT is energy-conservation, and is efficient; Floor space is few, and treatment facility is changeable, can be used for boats and ships, seawater system tap water, recycled water in family system pure water; Unmanageable chemical engineering sewage such as paper mill, chemical plant is handled, and can obtain solid material and high-quality water simultaneously.
Description of drawings
Accompanying drawing is the synoptic diagram of sewage system pure water technology
1 is the solid matter relief outlet among the figure; The 2nd, well heater; 3 and 4 is thermal insulation layers; The 5th, vacuum heat-insulating layer; The 6th, vaporizing chamber; The 7th, heat exchanger; The 8th, thermal store; The 9th, temperature probe; The 10th, spray thrower; The 11st, the steam export mouth; The 12nd, the pump circulation inlet; The 13rd, liquefied room; The 14th, LLC; The 15th, the liquid heat exchange pond; The 16th, liquid liquid interchanger; The 17th, the water purification underpressure chamber; The 18th, the water purification valve; The 19th, sewage inlet; The 20th, the biogas export mouth; The 21st, the natural pond slag is derived machine; The 22nd, the settling chamber; The 23rd, the natural pond liquid pool; The 24th, the natural pond slag is derived machine; The 25th, the natural pond slag bath; The 26th, methane-generating pit; The 27th, the methane-generating pit well heater; The 28th, sewage filtering net; The 29th, the automatic control pump; The 30th, the pump circulation outlet.
Specific embodiment
A kind of sewage becomes the pure water technology; In conjunction with accompanying drawing this paper the treatment process that a kind of municipal effluent becomes pure water is described; Its structure is made up of solid matter relief outlet 1, well heater 2, thermal insulation layer 3,4, vacuum heat-insulating layer 5, vaporizing chamber 6, heat exchanger 7, thermal store 8, temperature probe 9, spray thrower 10, steam export mouth 11, pump circulation inlet 12, liquefied room 13, LLC 14, liquid heat exchange pond 15, liquid liquid interchanger 16, water purification underpressure chamber 17, water purification valve 18, sewage inlet 19, biogas export mouth 20, natural pond slag derivation machine 21, settling chamber 22, natural pond liquid pool 23, natural pond slag derivation machine 24, natural pond slag bath 25, methane-generating pit 26, methane-generating pit well heater 27, sewage filtering net 28, automatic control pump 29, pump circulation outlet 30; Its operational process is that municipal effluent is through bottom, sewage inlet (19) influent heat exchange pond (15); After the abundant heat exchange of pure water big area after sewage filtering net (28) filters in sewage and the liquid liquid interchanger (16); Import through automatic control pump (29); Liquefied room (13); Import in the vaporizing chamber (6) after in heat exchanger (7), carrying out heat exchange with high temperature pure water and hot steam, through spray thrower (10) ejection and vaporization, solid matter falls after solid relief outlet (1) discharge through thermal store (8) well heater (2); Steam flows into water purification underpressure chamber (17) after water purification valve (18) flows out after after steam export mouth (11) gets into liquefied room (13) liquefaction, importing liquid-liquid heat exchanger (16) heat exchange; Mud after the filtration flows in the methane-generating pit (26), after in 50 ℃ high temperature pond, steaming 2-3 hour, enters natural pond slag bath (25); After natural pond slag derivation machine (24) importing settling tank (22) natural pond flow is gone into natural pond liquid pool (23), import slag derivation machine (24) derivation of sewage inlet (19) natural pond slag through the natural pond; (3,4) are thermal insulation layers, and (5) are vacuum heat-insulating layers, and (9) are that temperature probe (12) is that pump circulation inlet (14) is a LLC.

Claims (1)

1. a sewage system pure water is technological; Forming its special feature by vaporizing chamber (6) liquefied room (13) liquid heat exchange pond (15) is that vaporizing chamber (6) liquefied room (13) all carries out the cycling hot exchange and in vaporizing chamber, be provided with thermal store (8) well heater (2) temperature probe (9) in liquefied room (13), being provided with heat exchanger (7) in vacuum heat-insulating layer (5) inside of sealing; Pump circulation inlet (12) pump circulation outlet (30), LLC (14) large size city WWT is provided with methane-generating pit (20).
CN201010597035XA 2010-12-19 2010-12-19 Process for producing purified water by adopting sewage Pending CN102557166A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201010597035XA CN102557166A (en) 2010-12-19 2010-12-19 Process for producing purified water by adopting sewage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201010597035XA CN102557166A (en) 2010-12-19 2010-12-19 Process for producing purified water by adopting sewage

Publications (1)

Publication Number Publication Date
CN102557166A true CN102557166A (en) 2012-07-11

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201010597035XA Pending CN102557166A (en) 2010-12-19 2010-12-19 Process for producing purified water by adopting sewage

Country Status (1)

Country Link
CN (1) CN102557166A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106967589A (en) * 2017-06-01 2017-07-21 段国昌 A kind of full automatic high efficiency processing sewage, excrement and the device for producing biogas

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106967589A (en) * 2017-06-01 2017-07-21 段国昌 A kind of full automatic high efficiency processing sewage, excrement and the device for producing biogas

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Application publication date: 20120711