CN105601017B - The near-zero release processing system and method for a kind of high concentrated organic wastewater and sludge - Google Patents
The near-zero release processing system and method for a kind of high concentrated organic wastewater and sludge Download PDFInfo
- Publication number
- CN105601017B CN105601017B CN201610136458.9A CN201610136458A CN105601017B CN 105601017 B CN105601017 B CN 105601017B CN 201610136458 A CN201610136458 A CN 201610136458A CN 105601017 B CN105601017 B CN 105601017B
- Authority
- CN
- China
- Prior art keywords
- sludge
- oxygen
- liquid
- organic wastewater
- zero release
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/727—Treatment of water, waste water, or sewage by oxidation using pure oxygen or oxygen rich gas
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
- C02F2201/007—Modular design
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Sludge (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The invention discloses the near-zero release processing system and method for a kind of high concentrated organic wastewater and sludge, belong to chemical industry and environmental technology field.Using supercritical Water Oxidation Technology as core, waste water and sludge first pass around sludge Homogenizing pump and are ground, then pressurizeed using high-pressure plunger pump, be transported to follow-up pipeline preheat and and oxygen mix, supercritical water oxidation occurs in reactor.Fluid is after dropping equipment is depressured after reaction, the separation of insoluble solid, gas is carried out by self-cleaning filter, gas-liquid separator successively, mechanical steam recompression technology (MVR) crystallization is subsequently entered, carries out the crystallization of soluble-salt, realizes the near-zero release processing of feed.At the same time, SCWO technologies are aided in using conventional water treatment technology (such as coagulating sedimentation, membrane-biotechnology, membrane technology etc.), the appropriate operating parameter for reducing SCWO reactors, will remain a part of COD and transfers at conventional water technology to handle, effectively reduce operating cost.
Description
Technical field
The invention belongs to chemical industry and environmental technology field, and in particular to a kind of height using supercritical Water Oxidation Technology as core
The near-zero release processing system and method for concentration organic wastewater and sludge.
Background technology
Under normal conditions, water exists with steam, liquid water and the common state of three kinds of ice, and liquid water is polar solvent, its
Density changes little with the rise of pressure, can dissolve most of electrolyte including salt, to gas and most of
Organic matter then slightly soluble or insoluble.Supercritical water refers to that temperature, pressure are above the spy of its critical point (374.15 DEG C, 22.1MPa)
Water under different state.The property of supercritical water can occur greatly to change, its density, dielectric constant, diffusion coefficient and thermal conductivity
Rate is all different from light water.Moreover, the solubility of organic matter and gas in supercritical water significantly improves.
Supercritical Water Oxidation Technology (SCWO technologies) is exactly that make use of water possessed special nature in the supercritical state,
Oxidant and organic matter is set to be dissolved completely in supercritical water and homogeneous oxidation reaction occurs, rapidly, thoroughly by organic matter
It is converted into the micromolecular compounds such as harmless carbon dioxide, nitrogen and water.Traditional highly difficult, bio-refractory have with other
The treatment technology of machine waste water is compared, and supercritical Water Oxidation Technology has the advantage that：
1st, oxidation efficiency is high, and the theoretical removal rate of organic matter is up to more than 99.9%；
2nd, the reaction time is short, and device structure is simple, and floor space is small；
3rd, after organic matter mass concentration reaches 3%, system can realize self-heating.
Supercritical Water Oxidation Technology has at home and abroad been applied, but when process object is petrochemical sludge, still
There are the problem of several respects to need to solve, and is mainly manifested in：
Although theoretically seeing, the COD removal rates that can make organic wastewater (sludge) using SCWO technologies are up to 99.9%,
But this data is realized under very good reaction environment, including higher coefficient of oxidation (3~10 times), higher is anti-
Answer condition (600~700 DEG C, 27~29MPa), longer reaction time (100~150s).Like this, system pipeline
Selection, the quantity delivered of oxygen and the size of reactor will improve, this needs high raising to be realized into original, SCWO skills
The economy of art treated sewage will have a greatly reduced quality.Therefore need to aid in SCWO technical finesses by other sewage disposal means.
Contain the organic matter of more easy coking in sludge, if be fed by traditional method using heating furnace to sludge
Preheated, the extreme temperatures of pipe heating, the organic matter in water-containing sludge has higher coking tendency on high-temperature wall surface.Such as
Fruit monitors not in time, and wall occurs coking and causes wall temperature to ascend to heaven, and causes to block in wall overtemperature tube burst or pipe.
When the treating capacity of sludge is larger, whole system flow is longer, if reactor inlet temperature deficiency needs to mend temperature,
If heated using gas-fired heater, heating amount is unable to control.If using electric furnace, it is electrically heated startup the time compared with
Long, thermal inertia is strong, can not realize quick concurrent heating.Therefore a kind of device that can control heating power quick concurrent heating at the same time is needed.
SCWO processes are an exothermal reaction process, and studies have shown that after organic matter mass concentration reaches 3%, put by reaction
The heat gone out preheats the material into before reactor enough.But since SCWO reactions are that high temperature, high pressure, a hyperoxia contain
The strong corrosive environment of amount, it is high for the equipment choice requirement in system, nickel-base alloy is typically chosen as cores such as reactors
The material of equipment, the higher price of nickel-base alloy, many materials even not yet realize throwing in advance that is domestic, therefore can causing higher
Money.
The content of the invention
In order to overcome the problems of the above-mentioned prior art, it is an object of the invention to provide a kind of high concentrated organic wastewater
And the near-zero release processing system and method for sludge, the present invention up to standard can handle waste material and carry out effective material recycling, solve
Certainly corrosion and mineralization problem, improve economy, realize near-zero release.
The present invention is to be achieved through the following technical solutions：
A kind of near-zero release processing system of high concentrated organic wastewater and sludge, including waste water sending unit, reaction member,
Supply oxygen unit and post-processing unit；
Waste water sending unit includes sludge storage tank and sludge surge tank, the pipeline between sludge storage tank and sludge surge tank
It is equipped with homogenizing emulsifying pump；Reaction member includes heat exchanger and tubular reactor, in the pipe that sludge surge tank is connected with heat exchanger
Road is equipped with high-pressure frequency-conversion plunger pump, and the pipe side outlet end of heat exchanger is connected with the arrival end of tubular reactor, tubular reactor
The port of export be connected with the shell-side inlet end of heat exchanger；Oxygen supply unit is connected with tubular reactor；
Post-processing unit includes reducing transformer, self-cleaning filter, gas-liquid separator MVR crystalline elements and deep processing unit；
The shell-side outlet end of heat exchanger is connected with the arrival end of reducing transformer, the port of export of reducing transformer and the arrival end phase of self-cleaning filter
Even, the clean fluid port of export of self-cleaning filter is connected with gas-liquid separator, and exhaust outlet is equipped with the top of gas-liquid separator,
Bottom is equipped with liquid outlet, and the liquid outlet end of gas-liquid separator bottom is connected with the arrival end of MVR crystalline elements, MVR crystallizations
The port of export of unit is connected with the arrival end of advanced treatment unit.
The oxygen supply unit includes liquid oxygen storage tank, Low Temperature Liquid oxygen pump, liquid oxygen carburetor, oxygen surge tank and oxygenation mixing
Device；The port of export of liquid oxygen storage tank is connected with the arrival end of Low Temperature Liquid oxygen pump, the port of export and the liquid oxygen carburetor shell of Low Temperature Liquid oxygen pump
Side entrance end is connected, and the shell-side outlet end of liquid oxygen carburetor is connected with the arrival end of oxygen surge tank, the outlet of oxygen surge tank
End is connected with the arrival end of oxygenation mixer, and oxygenation mixer is connected with the gas access end of tubular reactor.
Advanced treatment unit (11) uses activated carbon adsorption device, ultrafiltration apparatus or film condensing device.
Self-cleaning filter uses rotary cutter self-cleaning filter.
The solute of MVR crystalline element entrances is the soluble-salts such as sodium chloride, sodium sulphate or sodium carbonate.
The invention also discloses a kind of near-zero release processing that high concentrated organic wastewater and sludge are carried out based on said system
Method, comprise the following steps：
1) organic wastewater and sludge are stored in sludge storage tank, until particle diameter is less than setting after homogenizing emulsifying pump is ground
Value, meets the deposition that salt will not occur in the case where setting flow velocity, and the water-containing sludge after grinding enters sludge surge tank and carries out particle diameter inspection
Survey；
2) water-containing sludge after step 1) processing is squeezed into heat exchanger through high-pressure frequency-conversion plunger pump, is 500 DEG C with temperature
Medium occur heat exchange, subsequently into tubular reactor；
3) oxygen that unit provides is supplied oxygen in tubular reactor with the organic matter in the waste water that handle through step 2) to surpass
Homogeneous reaction occurs under critical condition, organic matter is CO by oxygenolysis2、N2And H2O, the high temperature fluid after reaction enter heat exchange
Device, carries out heat exchange with WATER AS FLOW MEDIUM, is cooled to 80 DEG C；
4) fluid handled through step 3) enters in reducing transformer and is depressured, and is then discharged through self-cleaning filter insoluble
Solid, then gas-liquid separation is carried out through gas-liquid separator, the gas isolated puts idle discharge, and the fluid isolated is crystallized into MVR
Unit；
5) fluid removes soluble-salt through MVR crystalline elements, subsequently into advanced treatment unit, realizes industrial treatment waste water
And the near-zero release of sludge.
In step 3), it is that the liquid oxygen in liquid oxygen storage tank is entered liquid by Low Temperature Liquid oxygen pump that oxygen supply unit, which provides oxygen,
Oxygen vaporizer is changed into gaseous state, subsequently into oxygen surge tank, finally enters in tubular reactor；
Super critical condition described in step 3) is 560 DEG C of temperature, pressure 26MPa.
Reducing transformer outlet condition is 80 DEG C of temperature in step 4), pressure 0.4MPa；The temperature of self-cleaning filter is set to 80
DEG C, pressure is set to 0.4MPa, and filtering accuracy is 10 μm.
The disposal ability of MVR crystalline elements is 2.13t/h, evaporation capacity 2t/h.
Compared with prior art, the present invention has technique effect beneficial below：
The near-zero release processing system of high concentrated organic wastewater and sludge disclosed by the invention, including waste water sending unit,
Reaction member, oxygen supply unit and post-processing unit；Waste water and sludge are first passed around homogenizing emulsifying pump and carried out by waste water delivery unit
Grinding, can be ground to design particle diameter first by the insoluble solid in sludge, prevent occurring mineralization in follow-up pipeline and make
Into blocking；Then be transported to follow-up pipeline after being pressurizeed using high-pressure frequency-conversion plunger pump and preheated, and with from oxygen supply unit
Oxygen mix, occurs supercritical water oxidation in tubular reactor in the reaction cell, utilizes post processing after reaction
After the dropping equipment of unit is depressured, insoluble solid, gas are carried out by self-cleaning filter, gas-liquid separator successively
Separation, subsequently enters the crystallization treatment that MVR (mechanical recompression) crystalline element carries out soluble-salt, realizes the nearly zero-emission of feed
Put processing.Pass through the system of the present invention so that the solid containing heavy metal that SCWO processing produces can efficiently separate, and realize stabilization
Change landfill or entrust qualified processing unit safe to fill；The inorganic salts that MVR crystallizations produce are returned by glass factory, sodium sulphate factory
Receive, the gas produced in whole processing procedure is based on carbon dioxide and nitrogen, it is possible to achieve idle discharge is put or systematic collection.This
Invention also novelty uses advanced treatment unit in post-processing unit, and the outlet liquid of advanced treatment unit can row up to standard
Put.Advanced treatment unit uses conventional water treatment technology, such as activated carbon adsorption, film concentration or membrane-biotechnology.Manage depths
Unit can aid in SCWO technologies, and the appropriate operating parameter for reducing SCWO reactors, will remain a part of COD and transfer to often
Technology is handled at rule water, effectively reduces operating cost, and passes through two stage treatment, reduces water outlet possibility not up to standard.
Therefore, waste water (sludge) processing system using SCWO as core of the present invention can fully achieve the near of industrial treatment waste water and sludge
Zero-emission.
Processing method disclosed by the invention based on said system, the waste water and sludge handled by SCWO, using from clearly
Washed filter removes out the insoluble solid in fluid after reaction, is further dehydrated the solid filtered out with filter press is followed by.Adopt
Gas after removing out reaction with gas-liquid separator in fluid.Crystallized again by mechanical steam recompression technology (MVR).Pass through
Above separate mode, the solid containing heavy metal that SCWO processing produces can efficiently separate, and realize stabilisation landfill or commission
Qualified processing unit safe landfill；The inorganic salts that MVR crystallizations produce are recycled by glass factory, sodium sulphate factory, whole treated
The gas produced in journey is based on carbon dioxide and nitrogen, it is possible to achieve idle discharge is put or systematic collection.This SCWO is core
Waste water (sludge) processing system can fully achieve the near-zero release of industrial treatment waste water and sludge.
Brief description of the drawings
Fig. 1 is the structure diagram of the near-zero release processing system of high concentrated organic wastewater of the present invention and sludge.
Wherein, 1 is sludge storage tank；2 be homogenizing emulsifying pump；3 be sludge surge tank；4 be high-pressure frequency-conversion plunger pump；5 be to change
Hot device；6 be tubular reactor；7 be reducing transformer；8 be self-cleaning filter；9 be gas-liquid separator；10 be MVR crystalline elements；11
For advanced treatment unit；12 be liquid oxygen storage tank；13 be Low Temperature Liquid oxygen pump；14 be liquid oxygen carburetor；15 be oxygen surge tank, and 16 are
Oxygenation mixer.
Embodiment
With reference to specific embodiment, the present invention is described in further detail, it is described be explanation of the invention and
It is not to limit.
Referring to Fig. 1, it is of the invention it is a kind of using supercritical Water Oxidation Technology as core organic wastewater with high concentration and sludge it is near
Zero-discharge treatment system, whole system include waste water sending unit, reaction member, oxygen supply unit and post-processing unit.
Waste water sending unit includes sludge storage tank 1 and sludge surge tank 3, between sludge storage tank 1 and sludge surge tank 3
Pipeline is equipped with homogenizing emulsifying pump 2；Reaction member includes heat exchanger 5 and tubular reactor 6, in sludge surge tank 3 and heat exchanger 5
Connected pipeline is equipped with high-pressure frequency-conversion plunger pump 4, and the pipe side outlet end of heat exchanger 5 is connected with the arrival end of tubular reactor 6,
The port of export of tubular reactor 6 is connected with the shell-side inlet end of heat exchanger 5；Oxygen supply unit is connected with tubular reactor 6；
Post-processing unit includes reducing transformer 7, self-cleaning filter 8, gas-liquid separator 9 and MVR crystalline elements 10；Heat exchanger
5 shell-side outlet end is connected with the arrival end of reducing transformer 7, the port of export of reducing transformer 7 and the arrival end phase of self-cleaning filter 8
Even, the clean fluid port of export of self-cleaning filter 8 is connected with gas-liquid separator 9, and exhaust is equipped with the top of gas-liquid separator 9
Mouthful, bottom is equipped with liquid outlet, and the liquid outlet end of 9 bottom of gas-liquid separator is connected with the arrival end of MVR crystalline elements 10.Afterwards
Processing unit further includes deep processing unit 11, and the outlet of MVR crystalline elements 10 is connected with the entrance of advanced treatment unit 11.
The oxygen supply unit includes liquid oxygen storage tank 12, Low Temperature Liquid oxygen pump 13, liquid oxygen carburetor 14, oxygen surge tank 15 and adds
Oxygen mixer 16；The port of export of liquid oxygen storage tank 12 is connected with the arrival end of Low Temperature Liquid oxygen pump 13, the port of export of Low Temperature Liquid oxygen pump 13
It is connected with 14 shell-side inlet end of liquid oxygen carburetor, the shell-side outlet end of liquid oxygen carburetor 14 and the arrival end phase of oxygen surge tank 15
Even, the port of export of oxygen surge tank 15 is connected with the arrival end of oxygenation mixer 16, oxygenation mixer 16 and tubular reactor 6
Gas access end is connected.
The solute component of 10 entrance of MVR crystalline elements is sodium chloride, sodium sulphate or sodium carbonate.
Self-cleaning filter 8 uses rotary cutter self-cleaning filter, and filtering accuracy is high, can accomplish continuous and band
There is the operation under pressure condition.It is the insoluble solid filtered in water outlet that it, which is acted on,.
The advanced treatment unit 11 uses conventional water technology, can be active carbon adsorption, and film is given birth to
Thing technology or membrane technology etc..It is to handle the COD that supercritical water oxidation is not disposed that it, which is acted on, so as to suitably drop
The temperature of low supercritical water oxidation, pressure parameter, reduce selection quality and running temperature, reduce cost.
A kind of near-zero release processing that high concentrated organic wastewater and sludge are carried out based on said system disclosed by the invention
Method, comprises the following steps：
1) organic wastewater and sludge are stored in sludge storage tank, until particle diameter is less than setting after homogenizing emulsifying pump is ground
Value, the water-containing sludge after grinding enter sludge surge tank and carry out droplet measurement；
2) water-containing sludge after step 1) processing is squeezed into heat exchanger through high-pressure frequency-conversion plunger pump, is 500 DEG C with temperature
Medium occur heat exchange, subsequently into tubular reactor；
3) oxygen that unit provides is supplied oxygen in tubular reactor with the organic matter in the waste water that handle through step 2) to surpass
Homogeneous reaction occurs under critical condition, organic matter is CO by oxygenolysis2、N2And H2O, the high temperature fluid after reaction enter heat exchange
Device, carries out heat exchange with WATER AS FLOW MEDIUM, is cooled to 80 DEG C；
4) fluid handled through step 3) enters in reducing transformer and is depressured, and is then discharged through self-cleaning filter insoluble
Solid, then gas-liquid separation is carried out through gas-liquid separator, the gas isolated puts idle discharge, and the fluid isolated is crystallized into MVR
Unit；
5) fluid removes soluble-salt through MVR crystalline elements, subsequently into advanced treatment unit, realizes industrial treatment waste water
And the near-zero release of sludge.
The concrete operating principle of said system and method is as follows：
(1) organic wastewater and sludge store in sludge storage tank 1, and particle diameter setting is reached after the grinding of homogenizing emulsifying pump 2
Value, sets the insoluble mud granule of solid of particle diameter according to setting flow rate, it is ensured that in system under normal flow less than this
Smooth outflow does not deposit in each pipe.Water-containing sludge after grinding carries out further droplet measurement into sludge surge tank 3.Then
By high-pressure frequency-conversion plunger pump 4, heat exchanger 5 is made it into, cold sludge is carried out with the intermediate medium that one inlet temperature is 500 DEG C
Heat exchange, subsequently enters in tubular reactor 6.Liquid oxygen in liquid oxygen storage tank 12 first passes around Low Temperature Liquid oxygen pump 13 and enters liquid oxygen
Vaporizer 14 is changed into gaseous state and enters oxygen surge tank 15, is mixed subsequently into tubular reactor 6 with organic wastewater, instead
Should.
(2) (560 DEG C, 26MPa) occurs oxygen under super critical condition in tubular reactor 6 with the organic matter in waste water
Phase reaction, organic matter resolve into CO by rapid, exhaustive oxidation2、N2、H2O, the high temperature fluid after reaction enter heat exchanger, are cooled
To 80 DEG C, the type of cooling is to exchange heat with intermediate medium water.It is depressured afterwards into reducing transformer 7, the outlet work of reducing transformer 7
Condition is (80 DEG C, 0.4MPa).
(3) insoluble solid is separated and discharged, then by self-cleaning filter 8 (80 DEG C, 0.4MPa) by fluid after reacting
Fluid enters gas-liquid separator 9 and carries out gas-liquid separation, and separated gas is with CO2And N2Based on, directly idle discharge can be put, separated
Liquid enter MVR crystalline elements 10, the disposal abilities of MVR crystalline elements 10 is 2.13t/h, evaporation capacity 2t/h, and system can be with
Realize continuous feed.Soluble-salt in solution is divided (based on sodium chloride, sodium sulphate, sodium carbonate) after evaporative crystallization
From.Subsequent fluid enters advanced treatment unit 11, its effect is the residual organic substances that advanced treating SCWO is not disposed, depth
Processing unit 11 for conventional water treatment facilities, can be active carbon adsorption, membrane-biotechnology or membrane technology etc..
Claims (10)
- A kind of 1. near-zero release processing system of high concentrated organic wastewater and sludge, it is characterised in that including waste water sending unit, Reaction member, oxygen supply unit and post-processing unit；Waste water sending unit includes sludge storage tank (1) and sludge surge tank (3), sludge storage tank (1) and sludge surge tank (3) it Between pipeline be equipped with homogenizing emulsifying pump (2)；Reaction member includes heat exchanger (5) and tubular reactor (6), in sludge surge tank (3) pipeline being connected with heat exchanger (5) is equipped with high-pressure frequency-conversion plunger pump (4), and the pipe side outlet end of heat exchanger (5) and tubular type are anti- The arrival end of device (6) is answered to be connected, the port of export of tubular reactor (6) is connected with the shell-side inlet end of heat exchanger (5)；Supply oxygen unit It is connected with tubular reactor (6)；Post-processing unit includes reducing transformer (7), self-cleaning filter (8), gas-liquid separator (9), MVR crystalline elements (10) and depth Spend processing unit (11)；The shell-side outlet end of heat exchanger (5) is connected with the arrival end of reducing transformer (7), the port of export of reducing transformer (7) It is connected with the arrival end of self-cleaning filter (8), the clean fluid port of export and the gas-liquid separator (9) of self-cleaning filter (8) It is connected, exhaust outlet is equipped with the top of gas-liquid separator (9), bottom is equipped with liquid outlet, the liquid of gas-liquid separator (9) bottom The port of export is connected with the arrival end of MVR crystalline elements (10), the port of export and the advanced treatment unit (11) of MVR crystalline elements (10) Arrival end be connected.
- 2. the near-zero release processing system of high concentrated organic wastewater according to claim 1 and sludge, it is characterised in that institute Stating oxygen supply unit includes liquid oxygen storage tank (12), Low Temperature Liquid oxygen pump (13), liquid oxygen carburetor (14), oxygen surge tank (15) and oxygenation Mixer (16)；The port of export of liquid oxygen storage tank (12) is connected with the arrival end of Low Temperature Liquid oxygen pump (13), Low Temperature Liquid oxygen pump (13) The port of export is connected with liquid oxygen carburetor (14) shell-side inlet end, shell-side outlet end and the oxygen surge tank of liquid oxygen carburetor (14) (15) arrival end is connected, and the port of export of oxygen surge tank (15) is connected with the arrival end of oxygenation mixer (16), oxygenation mixing Device (16) is connected with the gas access end of tubular reactor (6).
- 3. the near-zero release processing system of high concentrated organic wastewater according to claim 1 and sludge, it is characterised in that deep Degree processing unit (11) uses activated carbon adsorption device or film condensing device.
- 4. the near-zero release processing system of high concentrated organic wastewater according to claim 1 and sludge, it is characterised in that from Cleaning filter (8) uses rotary cutter self-cleaning filter.
- 5. the near-zero release processing system of high concentrated organic wastewater according to claim 1 and sludge, it is characterised in that The solute of MVR crystalline elements (10) entrance is sodium chloride, sodium sulphate or sodium carbonate.
- 6. the near-zero release of high concentrated organic wastewater and sludge is carried out based on the system described in any one in Claims 1 to 5 The method of processing, it is characterised in that comprise the following steps：1) organic wastewater and sludge are stored in sludge storage tank (1), until particle diameter is less than setting after homogenizing emulsifying pump (2) grinding Value, the water-containing sludge after grinding enter sludge surge tank (3) and carry out droplet measurement；2) water-containing sludge after step 1) processing is squeezed into heat exchanger (5) through high-pressure frequency-conversion plunger pump (4), is 500 with temperature DEG C medium occur heat exchange, subsequently into tubular reactor (6)；3) oxygen that unit provides is supplied oxygen in tubular reactor (6) with the organic matter in the waste water that handle through step 2) to face surpassing Homogeneous reaction occurs under the conditions of boundary, organic matter is CO by oxygenolysis2、N2And H2O, the high temperature fluid after reaction enter heat exchanger (5), heat exchange is carried out with WATER AS FLOW MEDIUM, is cooled to 80 DEG C；4) fluid handled through step 3) enters in reducing transformer (7) and is depressured, and is then discharged through self-cleaning filter (8) insoluble Property solid, then carry out gas-liquid separation through gas-liquid separator (9), the gas isolated puts idle discharge, and the fluid isolated enters MVR Crystalline element (10)；5) fluid through MVR crystalline elements (10) remove soluble-salt, subsequently into advanced treatment unit (11) processing rest COD and NH3- N, realize industrial treatment waste water and sludge nearly zero, qualified discharge.
- 7. the method for the near-zero release processing of high concentrated organic wastewater according to claim 6 and sludge, it is characterised in that In step 3), it is that the liquid oxygen in liquid oxygen storage tank (12) is entered liquid by Low Temperature Liquid oxygen pump (13) that oxygen supply unit, which provides oxygen, Oxygen vaporizer (14) is changed into gaseous state, subsequently into oxygen surge tank (15), finally enters in tubular reactor (6).
- 8. the method for the near-zero release processing of high concentrated organic wastewater according to claim 6 and sludge, it is characterised in that Super critical condition described in step 3) is 560 DEG C of temperature, pressure 26MPa.
- 9. the method for the near-zero release processing of high concentrated organic wastewater according to claim 6 and sludge, it is characterised in that Reducing transformer (7) outlet condition is 80 DEG C of temperature in step 4), pressure 0.4MPa；The temperature of self-cleaning filter (8) is set to 80 DEG C, Pressure is set to 0.4MPa.
- 10. the method for the near-zero release processing of high concentrated organic wastewater according to claim 6 and sludge, its feature exist In the disposal ability of MVR crystalline elements (10) is 2.13t/h, evaporation capacity 2t/h.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610136458.9A CN105601017B (en) | 2016-03-10 | 2016-03-10 | The near-zero release processing system and method for a kind of high concentrated organic wastewater and sludge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610136458.9A CN105601017B (en) | 2016-03-10 | 2016-03-10 | The near-zero release processing system and method for a kind of high concentrated organic wastewater and sludge |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105601017A CN105601017A (en) | 2016-05-25 |
| CN105601017B true CN105601017B (en) | 2018-04-17 |
Family
ID=55981449
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610136458.9A Active CN105601017B (en) | 2016-03-10 | 2016-03-10 | The near-zero release processing system and method for a kind of high concentrated organic wastewater and sludge |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105601017B (en) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106316023A (en) * | 2016-09-21 | 2017-01-11 | 重庆赛迪热工环保工程技术有限公司 | Supercritical water gasification and recycling method and apparatus for steel mill high-oil-content iron-containing sludge |
| CN108447581A (en) * | 2018-04-23 | 2018-08-24 | 何辉 | A kind of Radioactive myocardial damage processing unit and its method |
| CN108911103A (en) * | 2018-07-10 | 2018-11-30 | 西安交通大学 | A kind of maintenance clean system for supercritical water oxidation treatment system |
| CN109399893B (en) * | 2018-10-23 | 2020-05-22 | 西安交通大学 | Waste heat gradient utilization system and method for supercritical water oxidation sludge treatment |
| CN109534616A (en) * | 2018-12-26 | 2019-03-29 | 常茂生物化学工程股份有限公司 | The processing method of Aspartame production waste water |
| CN115806367A (en) * | 2022-12-16 | 2023-03-17 | 湖南汉华京电清洁能源科技有限公司 | Organic wastewater treatment system |
| CN116179232A (en) * | 2023-03-06 | 2023-05-30 | 西安交通大学 | System for improving reliability of preparation of liquid fuel by sludge liquefaction coupling upgrading |
| CN117682717B (en) * | 2024-01-05 | 2024-06-07 | 舒俭 | Supercritical water-based high-salinity wastewater circulating treatment method and system |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4543190A (en) * | 1980-05-08 | 1985-09-24 | Modar, Inc. | Processing methods for the oxidation of organics in supercritical water |
| CN103626364A (en) * | 2013-11-06 | 2014-03-12 | 西安交通大学 | Supercritical water oxidation treatment and generation system of municipal sludge having high-solid content |
| CN104030427A (en) * | 2014-06-16 | 2014-09-10 | 西安交通大学 | Supercritical water oxidation treatment system for printing and dyeing wastewater and sludge |
| CN105293856A (en) * | 2015-10-10 | 2016-02-03 | 西安交通大学 | Supercritical water oxidation treatment system and supercritical water oxidation treatment system process for high-concentration dyeing sludge |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000126798A (en) * | 1998-10-22 | 2000-05-09 | Hitachi Plant Eng & Constr Co Ltd | Waste treatment apparatus by supercritical hydroxylation method |
-
2016
- 2016-03-10 CN CN201610136458.9A patent/CN105601017B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4543190A (en) * | 1980-05-08 | 1985-09-24 | Modar, Inc. | Processing methods for the oxidation of organics in supercritical water |
| CN103626364A (en) * | 2013-11-06 | 2014-03-12 | 西安交通大学 | Supercritical water oxidation treatment and generation system of municipal sludge having high-solid content |
| CN104030427A (en) * | 2014-06-16 | 2014-09-10 | 西安交通大学 | Supercritical water oxidation treatment system for printing and dyeing wastewater and sludge |
| CN105293856A (en) * | 2015-10-10 | 2016-02-03 | 西安交通大学 | Supercritical water oxidation treatment system and supercritical water oxidation treatment system process for high-concentration dyeing sludge |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105601017A (en) | 2016-05-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105601017B (en) | The near-zero release processing system and method for a kind of high concentrated organic wastewater and sludge | |
| US10370276B2 (en) | Near-zero-release treatment system and method for high concentrated organic wastewater | |
| CN102249461B (en) | Supercritical water oxidation treatment system for high-salt high-chlorine organic wastewater | |
| CN101607772B (en) | Supercritical water treatment and resource utilization system for waste organic matter | |
| CN205442932U (en) | Near zero emission processing system of high concentration organic waste water and mud | |
| WO2012151795A1 (en) | Supercritical water oxidation reaction system using auxiliary fuel to supply energy | |
| WO2012051875A1 (en) | Supercritical water treatment system for organic waste water with high salt content | |
| CN114838369B (en) | Inorganic salt online desorption system and method based on supercritical hydrothermal combustion treatment | |
| US9718717B2 (en) | Optimised hydrothermal carbonisation method and facility for implementing same | |
| CN205590487U (en) | Chemistry nickel liquid waste processing system | |
| CN207259186U (en) | A kind of coal chemical industry strong brine technique of zero discharge special equipment | |
| CN105601016A (en) | Chemical nickel waste liquid integrated processing system | |
| JP2010207700A (en) | Methane fermentation apparatus and methane fermentation method | |
| JP2004033910A (en) | Treatment method for organic acid washing waste liquid and apparatus therefor | |
| JP2000126798A (en) | Waste treatment apparatus by supercritical hydroxylation method | |
| CN107651801B (en) | High-salt high-organic-matter wastewater thermal membrane coupling zero-emission treatment process | |
| RU2704193C1 (en) | Oxidation by moist air at low temperatures | |
| CN205151821U (en) | Freezing sewage treatment plant of low temperature | |
| CN206556030U (en) | Brine waste processing system | |
| CN207313348U (en) | A kind of shale gas produced water treatment system | |
| CN107324578A (en) | A kind of shale gas produced water treatment system and method | |
| CN111533351B (en) | Salt-containing and difficult-to-oxidize organic matter separation treatment system and process | |
| Mustakeem et al. | Desalination by Membrane Distillation | |
| CN114514203A (en) | Apparatus and method for treating waste cleaning liquid | |
| CN205133320U (en) | Salt -containing wastewater treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |