CN205762937U - Water layer heating treatment system - Google Patents
Water layer heating treatment system Download PDFInfo
- Publication number
- CN205762937U CN205762937U CN201620435392.9U CN201620435392U CN205762937U CN 205762937 U CN205762937 U CN 205762937U CN 201620435392 U CN201620435392 U CN 201620435392U CN 205762937 U CN205762937 U CN 205762937U
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- CN
- China
- Prior art keywords
- water layer
- processing system
- water
- groundwater
- pollution
- 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.)
- Expired - Fee Related
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 64
- 238000010438 heat treatment Methods 0.000 title abstract description 10
- 239000003673 groundwater Substances 0.000 claims abstract description 10
- 238000012545 processing Methods 0.000 claims description 24
- 229920001903 high density polyethylene Polymers 0.000 claims description 8
- 239000004700 high-density polyethylene Substances 0.000 claims description 8
- 238000012544 monitoring process Methods 0.000 claims description 4
- 229910001220 stainless steel Inorganic materials 0.000 claims description 4
- 239000010935 stainless steel Substances 0.000 claims description 4
- 239000005416 organic matter Substances 0.000 claims description 3
- 229920000915 polyvinyl chloride Polymers 0.000 claims 2
- 239000004800 polyvinyl chloride Substances 0.000 claims 2
- 230000005611 electricity Effects 0.000 claims 1
- 239000002689 soil Substances 0.000 abstract description 17
- 239000003344 environmental pollutant Substances 0.000 abstract description 5
- 231100000719 pollutant Toxicity 0.000 abstract description 5
- 238000003895 groundwater pollution Methods 0.000 abstract 1
- 239000002957 persistent organic pollutant Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 22
- 239000012071 phase Substances 0.000 description 12
- 230000008569 process Effects 0.000 description 9
- 230000000694 effects Effects 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 230000033228 biological regulation Effects 0.000 description 5
- 239000000356 contaminant Substances 0.000 description 4
- 238000013461 design Methods 0.000 description 4
- 239000000284 extract Substances 0.000 description 4
- 230000001590 oxidative effect Effects 0.000 description 4
- 239000003209 petroleum derivative Substances 0.000 description 4
- 238000003911 water pollution Methods 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 239000002680 soil gas Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- 230000001133 acceleration Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 239000007800 oxidant agent Substances 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 230000000246 remedial effect Effects 0.000 description 2
- OQVYMXCRDHDTTH-UHFFFAOYSA-N 4-(diethoxyphosphorylmethyl)-2-[4-(diethoxyphosphorylmethyl)pyridin-2-yl]pyridine Chemical compound CCOP(=O)(OCC)CC1=CC=NC(C=2N=CC=C(CP(=O)(OCC)OCC)C=2)=C1 OQVYMXCRDHDTTH-UHFFFAOYSA-N 0.000 description 1
- -1 Biological Substances 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000008034 disappearance Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920001596 poly (chlorostyrenes) Polymers 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000009738 saturating Methods 0.000 description 1
- 231100000241 scar Toxicity 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 238000005063 solubilization Methods 0.000 description 1
- 230000007928 solubilization Effects 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000013022 venting Methods 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The utility model relates to a water layer heating treatment system, which is a treatment system applied to groundwater pollution, a pipe body which can be correspondingly placed into the ground bottom is mainly arranged on the ground surface, a plurality of through holes are distributed on the surface of the pipe body, at least one temperature control device is arranged in the pipe body, and the temperature control device is connected with a heating device arranged at the groundwater level of the pipe body so as to drive the heating device to generate temperature to heat groundwater by utilizing the temperature control device controlled by constant temperature; therefore, the underground water containing volatile organic pollutants is heated, so that the volatilization efficiency of the organic matters can be accelerated, and the project of soil and underground water restoration is achieved. When the DNAPL phase does not exist in the groundwater due to low-concentration pollution, pollutants dissolved in the water can be treated, and the volatilization efficiency is improved; when the DNAPL phase is suspected to exist in the groundwater due to high-concentration pollution, the volatilization efficiency can be improved, the solubility of the groundwater is increased, the movement of pollutants is accelerated, and the purpose of accelerating the treatment of the pollution adsorbed on the stratum is achieved.
Description
Technical field
This utility model is related to a kind of water layer and heats processing system, carries out water layer and heat control in espespecially one is used in pipe
System, with proper temperature heating and can effectively decompose volatility organic dirt in water layer, reach soil educate again, subsoil water whole
First the effect controlled for creating utilization.
Background technology
After domestic formulation soil and underground water pollution regulation method, the environmental protection relevant with underground water pollution to soil is asked
Topic is gradually paid attention to, in the middle of numerous pollution cases, again with chloride containing by government, enterprise and each side personage such as among the people
The contamination accident that compound and petroleum Hydrocarbon are caused accounts at most, and environment and human body are good for by aforesaid organic solvent
Kang Douhui causes high risks.Therefore, soil and the regulation of subsoil water have been instant necessary work.But,
Aforesaid organic solvent pole is difficult to be decomposed by Institute of Micro-biology, the most often need to artificially get involved and actively renovate.
And a lot of in the regulation common method of subsoil water with regard to current industry, with know-why be categorized as physical property, chemical,
Biological, and soil gas can be divided to extract method (SVE) with physics remedial technology, air injection method (AS), two-phase extract
Method ... etc.；This soil gas extracts method (SVE) and mainly utilizes vacuum suction, makes the pollution produce being present in soil
Raw volatilization, it is gas phase that pollutant are shifted by solid phase or liquid phase, waves in unsaturated layer (Vadose Zone) soil
Send out contact scar thing to process.And air injection method (Air Sparging) is that unpolluted cleaned air is injected underground
In water contaminated area (zone of saturation), by aeration effect in water so that organic substance blows out from the liquid phase dissolved and removes,
In it arrives the soil horizon of unsaturated layer, soil gas pumping and removing equipment such as SVE (Soil Vapor Extraction) can be passed through
Etc. extracting.And two-phase extract method also known as extract method (multi-phase extraction) and biology sobs suction method for heterogeneous
(bioslurping), it belongs to one of existing ground processing mode, mainly above contaminated area soil, digs a recovery whole
Control well, well arrange pump, by pumping from, remove the polluter existed in soil and subsoil water with different kenels, its
Include oil slick phase (free product), dissolve in phase, and unsaturated soil layer, have with the volatility that gas phase exists
The materials such as machine thing.
And chemical remedial technology point oxidizing process (ISCO), interfacial agent can rush row's method (SEAR) ... etc.；Existingization
Learning oxidizing process is to utilize different chemical oxidant in now, injects in soil or Water table, is oxidized in environment exist
Pollutant so that it is Non-toxic or mineralising (water and carbon dioxide), conventional oxidant includes that ozone, hydrogen peroxide are with high
Potassium manganate.And interfacial agent punching row's rule is to utilize solubilising (solubilization) or the mobile of interfacial agent
(mobilization) effect, accelerates soil or the dissolution of Organic Chemicals In Groundwater, then is removed, and this method
Pollutant are only the transfer of phase, and its follow-up taking back and process equipment cost also may be at a relatively high.
And biological regulation method promotes the growth of existing geomicrobes of saturated aqueous layer the most exactly, strengthening is raw
Thing decomposition, and this technology can effectively process the organic species being dissolved in subsoil water, such as oil product class is polluted
Thing etc..But, when the regulation of underground aquatic organism is also to have a little disappearance, as in high concentration, material with low solubility may
Bio-toxicity can be caused, or cannot be bioavailable, or the water-bearing layer (< 10 in low permeability matter-4Cm/sec) more difficult
Reach treatment effect, and Degradation is likely to be limited only to the region that water penetration in contaminated area is higher.
In view of this utility model people, adheres to the abundant of these relevant industries for many years and designs and develops and actual fabrication experience, pin
Prior art gives research design again, and a kind of water layer of special offer heats processing system, to reaching more preferably practical value
The purpose of property.
Utility model content
Main purpose of the present utility model is to be to provide a kind of water layer to heat processing system, refers in particular to one and is used in
Carry out water layer in pipe and heat control, can effectively decompose volatility organic dirt in water layer with proper temperature heating (or total
Petroleum hydrocarbon), reach the purpose of effect that soil is educated again, subsoil water is renovated.
This utility model water layer heats the purpose of processing system and is realized by following technology with effect:
For a kind of processing system applying to underground water pollution, mainly it is provided with a pipe that corresponding can insert the end, ground by earth's surface
Body, this tube surfaces is distributed multiple open-work, is provided with at least one attemperating unit, and this attemperating unit links one and installs
Heater at body level of ground water, with the attemperating unit utilizing constant temperature to control, orders about heater and produces temperature
Heating subsoil water；Thereby, allow the subsoil water containing volatile organic contaminant (or total petroleum hydrocarbon) through adding
Heat treatment so that it is decomposable asymmetric choice net Organic substance and purify water, and earth's surface can be moistened via the open-work of body, with reach soil and
The engineering that subsoil water is educated again.
Water layer as above heats processing system, power-off immediately after wherein this attemperating unit has arrival design temperature
The effectiveness of supply；And at least one attemperating unit can set point temperatures respectively and supply different volatile organic contaminant to make
With, or as taking precautions against the mechanism that attemperating unit damages.
Water layer as above heats processing system, and wherein the supply of electric power of this heater is generally from civil power；It addition,
A solar power current collection device can be further provided with, utilize this solar power current collection device provisioning heater electric power, and through temperature
Control device performs temperature and controls.
Water layer as above heats processing system, is provided with exhaust apparatus the most further in this body, and this aerofluxus fills
Put for additional discharge volatile organic matter gas.
Water layer as above heats processing system, and wherein the employing of this exhaust apparatus Negative pressure machine or pressure fan etc. can the rows of extraction
The equipment of venting body.
Water layer as above heats processing system, wherein this body can use further underground water well, monitoring well casing,
Stainless steel tube, polrvinyl chloride (PVC) pipe or high density polyethylene (HDPE) (HDPE) pipe.
This utility model has the advantage that
1. this utility model water layer heats processing system, there is not DNAPL phase time in subsoil water in low concentration pollution,
Polluter soluble in water can be processed, reach to promote volatilization efficiency, promote polluter volatilization.
2. this utility model water layer heats processing system, doubtful in subsoil water in high density pollution there is DNAPL phase
Time, volatilization efficiency can be promoted, promote polluter volatilization, make subsoil water dissolubility increase, accelerate polluter and move,
Reach acceleration and process the pollution being adsorbed in stratum.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or the required accompanying drawing used is briefly described in description of the prior art, it should be apparent that, attached in describing below
Figure is only embodiments more of the present utility model, for those of ordinary skill in the art, is not paying creativeness
On the premise of laborious, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is the cross-sectional schematic of this utility model overall architecture.
Fig. 2 is another embodiment cross-sectional schematic of this utility model.
Drawing reference numeral:
1 body
11 open-works
2 attemperating units
3 heaters
4 solar power current collection devices
5 exhaust apparatus
Detailed description of the invention
By the technology contents making this utility model be used, creation purpose and effect of reaching has more completely and clearly
Disclose, hereby in lower detailed description, and see also the graphic and figure number taken off:
First, referring to shown in Fig. 1～Fig. 2, the framework section view heating processing system for water layer of the present utility model is shown
Being intended to, it consists predominantly of:
One body 1, for being inserted the hollow tube at the end, ground by earth's surface, this body 1 surface distributed has multiple open-work 11；
At least one attemperating unit 2, this attemperating unit 2 is for being used for setting certain value temperature, vertical after arriving point temperatures
The i.e. equipment of power-off supply；
One heater 3, corresponding links with attemperating unit 2, and is arranged at body 1 level of ground water and carries out water layer increasing
The equipment of temperature.
Refer to shown in Fig. 1～Fig. 2, when, in time using, its underground water pollution processes main in the scope of suitable distance
Dig and set pipe laying body 1, and this body 1 can use underground water well, monitoring well casing, stainless steel tube, polychlorostyrene second further
Alkene (PVC) pipe or high density polyethylene (HDPE) (HDPE) pipe.When body 1 stretches into the end, ground, and its subsoil water can saturating on tube wall
Hole 11 flows in pipe, and is provided with heater 3 at level of ground water, and this heater 3 links attemperating unit 2, temperature
Control device 2 connects input electric power in correspondence and supplies heater 3 electric power；And typically electric power uses civil power, it is possible to enter
One step arranges a solar power current collection device 4, utilizes this solar power current collection device 4 to supply heater 3 electric power, then warp
Attemperating unit 2 performs temperature control, and this attemperating unit 2 mainly has and arrives the supply of power-off immediately after design temperature
Effectiveness, and at least one attemperating unit 2 can be set in this utility model, mainly can set different point temperatures respectively and come
For different volatile organic contaminants, or as taking precautions against the mechanism that attemperating unit 2 damages.
Then, heat processing system when performing this utility model water layer, with the attemperating unit 2 utilizing constant temperature to control, drive
Make heater 3 produce temperature heating subsoil water, allow containing volatile organic contaminant (or total petroleum hydrocarbon)
The heated process of subsoil water so that it is organic volatilization efficiency can be accelerated, with the engineering reaching soil and subsoil water is educated again.
It addition, when volatile organic gas is volatilized, it is provided with exhaust apparatus 5 further in this body 1, this row
Device of air 5 is used for additional discharge volatile organic matter gas；And this exhaust apparatus 5 can use Negative pressure machine or pressure fan etc.
The equipment of discharge gas can be extracted.
Being made up of above-mentioned element and implement knowable to explanation, with existing structure in comparison, this practicality is new for this utility model
Type has the advantage that
1. this utility model water layer heats processing system, there is not DNAPL phase time in subsoil water in low concentration pollution,
Polluter soluble in water can be processed, reach to promote volatilization efficiency, promote polluter volatilization.
2. this utility model water layer heats processing system, doubtful in subsoil water in high density pollution there is DNAPL phase
Time, volatilization efficiency can be promoted, promote polluter volatilization, make subsoil water dissolubility increase, accelerate polluter and move,
Reach acceleration and process the pollution being adsorbed in stratum.
Above-described detailed description of the invention, is entered the purpose of this utility model, technical scheme and beneficial effect
One step describes in detail, be it should be understood that and the foregoing is only detailed description of the invention of the present utility model, not
For limiting protection domain of the present utility model, all within spirit of the present utility model and principle, that is done any repaiies
Change, equivalent, improvement etc., within should be included in protection domain of the present utility model.
Claims (6)
1. a water layer heats processing system, it is characterised in that it consists predominantly of:
One body, for being inserted the hollow tube at the end, ground by earth's surface, this tube surfaces is distributed multiple open-work；
At least one attemperating unit, this attemperating unit, for being used for setting certain value temperature, breaks after arriving point temperatures immediately
The equipment of electricity supply；
One heater, corresponding links with this attemperating unit, and is arranged in and carries out water layer at this body level of ground water and heat
Equipment.
2. water layer as claimed in claim 1 heats processing system, it is characterised in that set in this body further
There is the exhaust apparatus of an additional discharge volatile organic matter gas.
3. water layer as claimed in claim 1 or 2 heats processing system, it is characterised in that be further provided with one too
Sun energy current collecting equipment, this solar power current collection device provisioning heater electric power.
4. water layer as claimed in claim 1 or 2 heats processing system, it is characterised in that this body is adopted further
By underground water well, monitoring well casing, stainless steel tube, polyvinyl chloride pipe, high density polyethylene pipe one of which.
5. water layer as claimed in claim 2 heats processing system, it is characterised in that this exhaust apparatus is negative for using
Press, pressure fan one of which.
6. water layer as claimed in claim 3 heats processing system, it is characterised in that this body uses ground further
Lower well, monitoring well casing, stainless steel tube, polyvinyl chloride pipe, high density polyethylene pipe one of which.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| TW104207543 | 2015-05-15 | ||
| TW104207543U TWM506146U (en) | 2015-05-15 | 2015-05-15 | Water layer heating treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205762937U true CN205762937U (en) | 2016-12-07 |
Family
ID=54339419
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620435392.9U Expired - Fee Related CN205762937U (en) | 2015-05-15 | 2016-05-13 | Water layer heating treatment system |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN205762937U (en) |
| TW (1) | TWM506146U (en) |
-
2015
- 2015-05-15 TW TW104207543U patent/TWM506146U/en unknown
-
2016
- 2016-05-13 CN CN201620435392.9U patent/CN205762937U/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| TWM506146U (en) | 2015-08-01 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161207 Termination date: 20200513 |