CN101279156A - In-situ regeneration method of polluted filtering material - Google Patents
In-situ regeneration method of polluted filtering material Download PDFInfo
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- CN101279156A CN101279156A CNA2007103034917A CN200710303491A CN101279156A CN 101279156 A CN101279156 A CN 101279156A CN A2007103034917 A CNA2007103034917 A CN A2007103034917A CN 200710303491 A CN200710303491 A CN 200710303491A CN 101279156 A CN101279156 A CN 101279156A
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- situ regeneration
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- 238000011069 regeneration method Methods 0.000 title claims abstract description 48
- 239000000463 material Substances 0.000 title claims abstract description 45
- 238000011065 in-situ storage Methods 0.000 title claims abstract description 43
- 238000001914 filtration Methods 0.000 title claims description 32
- 230000008929 regeneration Effects 0.000 claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000010865 sewage Substances 0.000 claims abstract description 27
- 239000002245 particle Substances 0.000 claims abstract description 26
- 230000001172 regenerating effect Effects 0.000 claims abstract description 16
- 238000000034 method Methods 0.000 claims abstract description 11
- 238000004062 sedimentation Methods 0.000 claims abstract description 7
- 230000008569 process Effects 0.000 claims abstract description 4
- 239000000706 filtrate Substances 0.000 claims description 83
- 239000003245 coal Substances 0.000 claims description 12
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 7
- 235000009496 Juglans regia Nutrition 0.000 claims description 7
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 7
- QCCKPZOPTXCJPL-UHFFFAOYSA-N dodecyl(dimethyl)azanium;hydroxide Chemical compound [OH-].CCCCCCCCCCCC[NH+](C)C QCCKPZOPTXCJPL-UHFFFAOYSA-N 0.000 claims description 7
- 239000000194 fatty acid Substances 0.000 claims description 7
- 229930195729 fatty acid Natural products 0.000 claims description 7
- 239000003208 petroleum Substances 0.000 claims description 7
- 229920001495 poly(sodium acrylate) polymer Polymers 0.000 claims description 7
- 150000003839 salts Chemical class 0.000 claims description 7
- 229910052708 sodium Inorganic materials 0.000 claims description 7
- 239000011734 sodium Substances 0.000 claims description 7
- NNMHYFLPFNGQFZ-UHFFFAOYSA-M sodium polyacrylate Chemical compound [Na+].[O-]C(=O)C=C NNMHYFLPFNGQFZ-UHFFFAOYSA-M 0.000 claims description 7
- 235000020234 walnut Nutrition 0.000 claims description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- WERKSKAQRVDLDW-ANOHMWSOSA-N [(2s,3r,4r,5r)-2,3,4,5,6-pentahydroxyhexyl] (z)-octadec-9-enoate Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO WERKSKAQRVDLDW-ANOHMWSOSA-N 0.000 claims description 6
- 230000009471 action Effects 0.000 claims description 6
- 150000004665 fatty acids Chemical class 0.000 claims description 6
- 239000000919 ceramic Substances 0.000 claims description 5
- 239000000470 constituent Substances 0.000 claims description 5
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- 230000007246 mechanism Effects 0.000 claims description 5
- JHZICVAIDBTSOQ-UHFFFAOYSA-N [O-2].[Na+].[Ar].[Na+] Chemical compound [O-2].[Na+].[Ar].[Na+] JHZICVAIDBTSOQ-UHFFFAOYSA-N 0.000 claims description 4
- 239000002828 fuel tank Substances 0.000 claims description 4
- JKQOBWVOAYFWKG-UHFFFAOYSA-N molybdenum trioxide Chemical compound O=[Mo](=O)=O JKQOBWVOAYFWKG-UHFFFAOYSA-N 0.000 claims description 4
- 239000012530 fluid Substances 0.000 claims description 3
- 239000002689 soil Substances 0.000 claims description 3
- 239000006004 Quartz sand Substances 0.000 claims description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 2
- 230000005540 biological transmission Effects 0.000 claims description 2
- 240000007049 Juglans regia Species 0.000 claims 1
- 238000003780 insertion Methods 0.000 claims 1
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- DQMUQFUTDWISTM-UHFFFAOYSA-N O.[O-2].[Fe+2].[Fe+2].[O-2] Chemical compound O.[O-2].[Fe+2].[Fe+2].[O-2] DQMUQFUTDWISTM-UHFFFAOYSA-N 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
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- PHYFQTYBJUILEZ-IUPFWZBJSA-N triolein Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OCC(OC(=O)CCCCCCC\C=C/CCCCCCCC)COC(=O)CCCCCCC\C=C/CCCCCCCC PHYFQTYBJUILEZ-IUPFWZBJSA-N 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Filtering Materials (AREA)
Abstract
The invention discloses an in-situ regeneration method particularly applied to polluted filter materials of a water treatment system in the ferrous metallurgy industry, which does not need displacement, wherein, a spiral tube is drilled into the filter materials of a filter to cause both ends of a composite tube which is installed with ultrasonic resonators to be spread and extend out of the wall of the filter, and then to be inserted into the filter materials. In the process of the materials in-situ regeneration, compressed air is intermittently blasted into the composite tube and an in-situ regenerating medium passes through a regenerating medium input tube and then is inputted into the composite tube. The compressed air and the in-situ regenerating medium generate synergistic reactions of gas and liquid mixture in the composite tube in sequence to speed up the elimination of dirt of the polluted filter materials. A sewage pump is started and sewage in the filter passes through a drain outlet and then is sent to a front end sedimentation tank of the water treatment for water treatment. The situ regeneration method of the polluted filter materials can completely dispose the dirt at the particle surface of the polluted filter materials and the dirt inside the particles and no displacement processing is required, thus obtaining great economic and environmental benefits and being capable of popularizing for the enterprises having water treatment systems which require cleaning of the polluted filter materials.
Description
Technical field
The present invention relates to the in situ regeneration method of polluted filtering material in a kind of all water circulation systems or the water treatment system; relate in particular to a kind of in situ regeneration method that is used for industry water treatment systems such as Ferrous Metallurgy, petrochemical industry, generating, papermaking or water circulation system polluted filtering material, the method is of value to the environmental protection and the ecological balance.
Background technology
The handling problem of the contaminated filtrate of the filter in enterprise such as Ferrous Metallurgy or petrochemical industry or generating, papermaking water treatment system or the water circulation system (pond) is being perplexed gently always, the development and the existence of heavy industry, after using one section, filter (pond) needs backwash, but greasy filth dirt composition complexity, strong adhesion because of contaminated filtrate adhesion, the backwash effect is not good enough, makes the water yield and the effluent characteristics of filter (pond) not reach production requirement.In order to solve this difficult problem, one of least responsible way is contaminated filtrate in the filter (pond) to be drawn (digging) go out to discard in the strange land, becomes industrial refuse, pollutes.
The foreign oil industry adopts " pump is washed formula " filtrate treatment technology to replace " stirring-type " filtrate processing mode from the eighties in last century, filtrate is carried out backwash handle." pump is washed formula " technology is comparative maturity, domesticly introduces this technology in 1989, but this technology is only applicable to the processing of oil field walnut shell filtering material, and its processing mode is divided into two kinds by its structure difference: outer circulation mode and inner loop mode.The outer circulation mode is a kind of " displacement " processing method, and this method utilization liquefaction pump is sent walnut shell filtering material into the outer Scrubbing apparatus of filter body, to the filtrate processing of regenerating, then filtrate is sent into filter, discharges greasy dirt simultaneously.Be characterized in that filtration device structure is simple, be convenient to make, but increased pipeline and attached valve member, make the system pipeline complexity, increased the difficulty of control system, increased whole investment, if control bad, be easy to cause the migration of filtrate between filter, directly influence filters out water quality.Inner loop mode also is a kind of " displacement " processing method, and its utilizes liquefaction pump that walnut shell filtering material is sent in the Scrubbing apparatus in the filter, directly finishes the processing to filtrate in filter.The characteristics of this endless form are that backwash is abundant, and equipment mainly is made up of tank body, motor, liquefaction pump, Scrubbing apparatus and manifold, valve member etc.In Scrubbing apparatus when work,, oil-containing and impure filtrate enter Scrubbing apparatus from tangential direction under the effect of high-velocity flow, and high velocity impact friction in the inner small space of Scrubbing apparatus reaches the purpose of backwash " regeneration ".
Once the relevant report of handling relevant for the filtrate of getting dirty because of interior petroleum industry, but it mainly uses chemical method to finish, and must transform existing equipment, even need to change original filter.Before the present invention, it is investigated that 1. publication number is CN1772859A " filter material in oil field sewage filtering tank regeneration cleaning agent and a regeneration washing process ", it is the method that the contaminated filtrate of a kind of petroleum industry adopts displacement regeneration to handle; What 2. publication number was that CN1672770A " sewage water filtration jar useless filtrate reclaim cleaning " relates to is the recovery cleaning that useless filtrate adopts displacement regeneration to handle in the oil recovery field, a kind of oil field.
The employed processing mode of home and overseas all must discarded existing filter plant, and new equipment is installed, and these two kinds of processing modes still use cleaning agent that filtrate is carried out chemical washing, still can't remove the greasy filth of filtrate filter intragranular portion.
Both at home and abroad the filtrate in the steel industry filter (pond) mostly is the cleaned coal filtrate, and the filtrate after contaminated is continued to use back-washing method always and carried out halfway processing, and filtrate promptly loses filter capacity after a period of time, have to periodically more renew filtrate.Point out according to " scientific and technological novelty assessment report " that the Scientific and Technical Information Institute, Hunan Province provided on December 17th, 2007: " not looking into identical steel industry water treatment system filtrate in-situ regeneration technical research of new projects' complex art feature and the reported in literature of applying both at home and abroad at present " with this.
Summary of the invention
The object of the present invention is to provide a kind of especially iron and steel metallurgical industry to remove the surface of contaminated filtrate in the sewage treatment pot and the polluted filtering material in situ regeneration method of filtering material particle internal contamination thing, the in-situ regeneration that this in situ regeneration method is equally applicable to polluted filtering material in the industry sewage disposal such as petrochemical industry, generating, papermaking or the circulatory system cleans.
To achieve these goals, the present invention is achieved by the following technical solution: beginning to place successively particle diameter at the inner chamber of filter from bottom is that 20-50mm, particle diameter are that 10-20mm and particle diameter are the filtrate of 5-10mm, and the thickness of each filter material layer is in the 1.5-3m scope.Start the motor that links to each other with speed changer that is positioned on the installing rack, motor transmits power by decelerator to drive shaft, the drive drive shaft is rotated, drive shaft drives planetary gear rotates the spiral tube, the spiral tube is moved downward pierce successively in the interior filtrate of filter, and make the bottom of the top in shape head arrival lower floor filtrate of the spiral tube that is processed with the thread groove edge of a knife on its with drill bit function.Clutch on the Clutch Control line traffic control, make clutch " leave " planetary driven wheel, be that drive shaft breaks away from the drive connection between the planetary gear, warp clutch down makes drive shaft be meshed with bevel gear, drive the action of more piece pipe and stretch out the spiral barrel and go in the filtrate by bevel gear, rotate around self simultaneously.Primer fluid press pump, hydraulic oil drive telescoping mechanism through first petroleum pipeline and stretch out.The ultrasonic wave that supersonic generator produces is passed to oscillator through line makes oscillator produce vibration, connect compressed air hose with compressed air in universal joint blasts the more piece pipe, to account for the dodecyldimethylammonium hydroxide inner salt of gross weight 25-45% from the regenerating medium input pipe, account for the sodium humate of gross weight 5-15%, account for the shrink sorbitol monooleate of gross weight 10-15%, account for the fatty acid amide of gross weight 2-5%, account for the Sodium Polyacrylate of gross weight 2.5-5.0%, account for the sodium hydroxid of gross weight 3.0-5.0% and account for in-situ regeneration medium that the water of gross weight 25-35% is re-dubbed in universal joint is input to the more piece pipe, its input quantity is controlled at 10-50kg/min.Both can be that compressed air also can be compressed oxygen in universal joint blasts the more piece pipe, the pressure of the compressed air that batch (-type) blasts to the more piece pipe (or oxygen) be controlled at the 0.09-0.11MPa scope.Stretch out or the more piece pipe of the spiral drum outer wall of withdrawing on N (integer of N＞1) individual oscillator and the individual water jet of N ' (integer of N '＞1) are housed, entering the compressed air in the more piece pipe by compressed air hose and making oscillator produce vibration and loosening filtrate by supersonic generator, the surface of contaminated filtrate and the pollutant in the internal capillary such as greasy dirt and dust are all cleaned (being in-situ regeneration), finish the cleaning of the filtrate of certain one deck.Start the sewage pump be installed on the installing rack, sewage is sent into water treatment front end sedimentation basin through soil pick-up water pipe and blow-off pipe carry out sewage disposal.Wherein sewage pump can be selected the sewage pump of 10-60t/h for use.The actuating motor backward rotation, make the telescoping mechanism action of more piece pipe make the withdrawal of more piece bar by bevel gear, engagement between the bevel gear is thrown off, clutch makes the meshing disengaging between drive shaft and the planetary gear in the control, simultaneously drive shaft is meshed with bevel gear, cleans the filtrate of an aspect again.
The in situ regeneration method that adopts a kind of polluted filtering material that as above technical scheme provides compared with prior art, technique effect is:
1. described polluted filtering material in situ regeneration method collection ultrasonic wave, compressed air, special-purpose regenerating medium monotechnics, necessary physical chemistry means have been used, needn't shift (i.e. displacement) polluted filtering material, need not transform existing filter (pond) or filtrate jar yet, by an orderly operation that can enter the spiral tube in filter or the filtrate jar, directly the polluted filtering material in filter or the filtrate jar is handled, the dirt of polluted filtering material particle surface and micropore inside is decomposed fast, thoroughly remove and reach the purpose of regeneration, saved equipment investment.
2. polluted filtering material in-situ regeneration technology, abandoned the anti-cleaning method that the polluted filtering material in employed filter (pond) or the filtrate jar in the iron and steel metallurgical industry water filtration treatment system is continued to use always, need not periodically more to renew filtrate, need not transform the structure of filter (pond) or filtrate jar, additionally not add solid mechanical equipment.The present invention adopts multiple monotechnics, directly polluted filtering material is carried out processing such as physicsization at filter (pond) or filtrate jar inside, make it to regenerate and reuse, thereby realize solid waste waste resource, energy-saving and emission-reduction, promote recycling economy development, great economic benefit and environmental benefit are arranged.
3. to a China that produces 5.0 hundred million tons of steel per year, if all adopt in situ regeneration method to handle to the polluted filtering material in the water treatment circulatory system, can reduce the discharging of ten thousand tons of pollutants of 60-70 every year, and can reduce by 1,000,000 m every year
2Above throwing out without care huddles land area, saved valuable arable land or greenery patches.
4. the filtrate mud more than 98% contains the di-iron trioxide of 35-40% and the grease of 0.3-8.0% after in situ regeneration method is handled, and has to recycle to be worth.
Description of drawings
Accompanying drawing also is a Figure of abstract of the present invention for implementing the device schematic diagram of a kind of polluted filtering material in situ regeneration method of the present invention.
The specific embodiment
Below in conjunction with drawings and Examples the specific embodiment of the present invention is described in further detail.
As shown in drawings, begin to place successively the filtrate 11 that filtrate 17 that particle diameter is 20-50mm, filtrate 15 that particle diameter is 10-20mm and particle diameter are 5-10mm at the inner chamber of the barrel-shaped filter 7 of drum shape or side from bottom, the stacking thickness of filtrate 17, filtrate 15 and filtrate 11 can be chosen between the 1.5-3.0m, and described filtrate 17,15,11 can be selected from quartz sand filter media or walnut shell filtering material or ceramic filter material or activated carbon filtrate or cleaned coal filtrate.Start and to be positioned on the installing rack 3 and motor 1 speed changer 1 ' link to each other, by decelerator 1 ' drive drive shaft 5 rotations to drive shaft 5 transmission power.Through Clutch Control line 12 ' make clutch 12 and driven wheel 13 engagements, control clutch (12A) down allows flat bevel gear 31 and perpendicular bevel gear 10 break away from meshing relations.Primer fluid press pump 20, hydraulic oil makes spiral tube 6 descending through fuel tank 21 and second petroleum pipeline 8 ' driving travel mechanism 22, and driven wheel 13 drives planetary gears 14 and makes spiral tube 6 rotate and make the top in shape head of the spiral tube 6 that is processed with the thread groove edge of a knife on its with drill bit function pierce filtrate 11, filtrate 15 and the filtrate 17 in the filter 7 successively and arrive the bottom of filter 7.Clutch 12 in the 12 ' control of Clutch Control line allows clutch 12 leave driven wheel 13, the drive connection that promptly allows drive shaft 5 break away between the planetary gear.Clutch 12A makes flat bevel gear 31 and perpendicular bevel gear 30 engagements under Clutch Control line 12A ' control, be drive shaft 5 and bevel gear engagement, rotation by drive shaft 5 drives flat bevel gear 31 and perpendicular bevel gear 30 actions, more piece pipe 18 self is rotated, hydraulic oil inserts in the filtrate 17 or 15 or 11 through the outer wall that fuel tank 21 and first petroleum pipeline 8 make 18 actions of more piece pipe and stretch out spiral tube 6, again allow clutch 12 and driven wheel 13 mesh thereafter, control clutch 12A down allows flat bevel gear 31 and perpendicular bevel gear 30 break away from meshing relation, and being rotated further of drive shaft 5 rotated more piece pipe 18 in a plane.The ultrasonic wave that sends with supersonic generator 24 connects warp 26 makes oscillator 25 produce vibration, and the vibration that oscillator 25 is produced by supersonic generator 24 can be accelerated the cleaning of filtrate.In universal joint 29 blasted more piece pipe 18, the compressed-air actuated pressure that blasts in more piece pipe 18 in filtrate " in-situ regeneration " process discontinuous formula was 0.09-0.11MPa to connection compressed air hose 9 compressed air.Regenerating medium input pipe 10 is communicated with more piece pipe 18 through universal joint 28, by the dodecyldimethylammonium hydroxide inner salt that accounts for gross weight 25-45%, account for the sodium humate of gross weight 5-15%, account for the shrink sorbitol monooleate of gross weight 10-15%, account for gross weight 2-5% fatty acid amide, gross weight 2.5-5.0% Sodium Polyacrylate, account for the NaOH of gross weight 3.0-5.0% and account for in-situ regeneration medium that the water of gross weight 25-35% is re-dubbed and be input in the more piece pipe 18 with the amount of 10-50kg/min, each constituent content sum of this in-situ regeneration medium is 100%, also can be referred to as efficient composite regenerated medium.Wherein the dodecyldimethylammonium hydroxide inner salt in the in-situ regeneration medium, sodium humate, shrink sorbierite list olein, fatty acid acyl gastral cavity, Sodium Polyacrylate, NaOH all are activating agent, all tool deoil, the de-sludging function, for buying product in market.The in-situ regeneration medium of compressed air with enter more piece pipe 18 from regenerating medium input pipe 10 in that enters in the more piece pipe 18 from compressed air hose 9 produces the synergy that liquid gas mixes in more piece pipe 18, they are ejected in from the individual water jet 19 of the N ' on the more piece pipe 18 and form violent turbulent flow in the filter 7, the chemistry effectiveness of in-situ regeneration medium is obtained fast, fully play, help the removing of dirt on contaminated filtrate 17 or 15 or 11, simultaneously because N the vibrative oscillator 25 of energy under the effect of supersonic generator 24 arranged on the more piece pipe 18 in inserting filtrate 17 or 15 or 11, it is under compressed-air actuated mating reaction, " cavitation " effect that contaminated filtrate is had cleaning action, under the ultrasonic wave effect, use the in-situ regeneration medium that the particle surface of contaminated filtrate 17 or 15 or 11 and inner dirt can both thoroughly be removed, obtain " in-situ regeneration ".In " in-situ regeneration " process later stage, suitably to adjust from compressed air hose 9 and blast the compressed-air actuated pressure in the more piece pipe 18 and blast the position and the direction of filtrate, the one-tenth bed of the filtrate that helps regenerating recovers.After the filtrate of certain one deck has cleaned, allow motor 1 reverse, and make clutch 12 and driven wheel 13 break away from meshing relation, flat bevel gear 31 and perpendicular bevel gear 30 engagements allow the telescoping mechanism of more piece pipe 18 move, 18 withdrawals of more piece pipe, thereafter clutch 12 is gone up in control allows 6 counter-rotatings of spiral tube rise with driven wheel 13 engagements, after arriving a certain position, repeat as above to operate, this metafiltration material is cleaned.When the sewage disposal in the filter 7 intact and filtrate all cleaned after, start sewage pump 2, sewage through soil pick-up water pipe 4 and blow-off pipe 4 ' send into water treatment front end sedimentation basin 23, carry out sewage disposal, described sewage pump 2 can be selected the sewage pump of 10-60t/h for use, and 1-4 platform sewage pump 2 can be installed on installing rack 3.
Embodiment 1
Place the cleaned coal filtrate 17 that particle diameter is 20-50mm successively at the inner chamber bottom of filter 7, particle diameter is the ceramic filter material 15 of 10-20mm, particle diameter is the walnut shell filtering material 11 of 5-10mm, motor 1 is just changeing the head that makes drive shaft 5 and is arriving cleaned coal filtrate 17 earlier, two of more piece pipe 18 is inserted in the cleaned coal filtrate 17, compressed air hose 9 blasts 0.09MPa compressed air through universal joint 29 to more piece pipe 18 batch (-type)s, import by (weight %) dodecyldimethylammonium hydroxide inner salt=45 to more piece pipe 18 with the amount of 10kg/min through universal joint 28 from regenerating medium input pipe 10, sodium humate=5, shrink sorbitol monooleate=12, fatty acid amide=3, Sodium Polyacrylate=3, argon sodium oxide molybdena=3, the in-situ regeneration medium that water=29 (each constituent content sum is 100%) are re-dubbed, compressed air produces liquid gas immixture with the in-situ regeneration medium in more piece pipe 18.Start the 10t/h sewage pump 2 be installed on the installing rack 3 with sewage through blow-off pipe 4 ' send into water treatment front end sedimentation basin 23, do not contain dirt in in-situ regeneration filtering material particle surface and the granule interior micropore, wherein compressed air hose 9, regenerating medium input pipe 10 and blow-off pipe 4 ' select for use flexible pipe.
Embodiment 2
Place the cleaned coal filtrate 17 that particle diameter is 20-50mm successively at the inner chamber bottom of filter 7, particle diameter is the ceramic filter material 15 of 10-20mm, particle diameter is the activated carbon filtrate 11 of 5-10mm, motor 1 is just changeing the head that makes drive shaft 5 and is arriving cleaned coal filtrate 17 earlier, two of more piece pipe 18 is inserted in the cleaned coal filtrate 17, compressed air hose 9 blasts 0.10MPa compressed air through universal joint 29 to more piece pipe 18 batch (-type)s, imports by (weight %) dodecyldimethylammonium hydroxide inner salt=25 to more piece pipe 18 with the amount of 50kg/min through universal joint 28 from regenerating medium input pipe 10, sodium humate=15, shrink sorbitol monooleate=10, fatty acid amide=5, Sodium Polyacrylate=5, argon sodium oxide molybdena=5, the in-situ regeneration medium that water=35 (each constituent content sum is 100%) are re-dubbed.Compressed air produces liquid gas immixture with the in-situ regeneration medium in more piece pipe 18.Start the 50t/h sewage pump 2 be installed on the installing rack 3 with sewage through blow-off pipe 4 ' send into water treatment front end sedimentation basin 23, do not contain dirt in in-situ regeneration filtering material particle surface and the granule interior micropore, wherein compressed air hose 9, regenerating medium input pipe 10 and blow-off pipe 4 ' select for use flexible pipe.
Place the cleaned coal filtrate 17 that particle diameter is 20-50mm successively at the inner chamber bottom of filter 7, particle diameter is the ceramic filter material 15 of 10-20mm, particle diameter is the walnut shell filtering material 11 of 5-10mm, motor 1 is just changeing the head that makes drive shaft 5 and is arriving cleaned coal filtrate 17 earlier, two of more piece pipe 18 is inserted in the cleaned coal filtrate 17, compressed air hose 9 blasts 0.11MPa compressed air through universal joint 29 to more piece pipe 18 batch (-type)s, import by (weight %) dodecyldimethylammonium hydroxide inner salt=41 to more piece pipe 18 with the amount of 20kg/min through universal joint 28 from regenerating medium input pipe 10, sodium humate=10, shrink sorbitol monooleate=15, fatty acid amide=2, Sodium Polyacrylate=2.5, argon sodium oxide molybdena=4.5, the in-situ regeneration medium that water=25 (each constituent content sum is 100%) are re-dubbed, compressed air produces liquid gas immixture with the in-situ regeneration medium in more piece pipe 18, start the 60t/h sewage pump 2 be installed on the installing rack 3 with sewage through blow-off pipe 4 ' send into water treatment front end sedimentation basin 23, do not contain dirt in in-situ regeneration granule filter material particle surface and the granule interior micropore, wherein compressed air hose 9, regenerating medium input pipe 10 and blow-off pipe 4 ' select for use flexible pipe.
Apply for utility model patent " a kind of in-situ regeneration device that is applied to polluted filtering material " simultaneously with this case, used accompanying drawing is identical.
Claims (1)
1, a kind of in situ regeneration method of polluted filtering material, the inner chamber of the filter (7) of drum shape from bottom begin to place successively the filtrate that particle diameter is 20-50mm (17), particle diameter is the filtrate (15) of 10-20mm, the filtrate (11) that particle diameter is 5-10mm, it is characterized in that: start the motor (1) that links to each other with speed changer (1 ') that is positioned on the installing rack (3), drive drive shaft (5) by decelerator (1 ') to drive shaft (5) transmission power and rotate; Make clutch (12) and driven wheel (13) engagement through Clutch Control line (12 '), control clutch (12A) down allows flat bevel gear (31) and perpendicular bevel gear (30) break away from meshing relation; Primer fluid press pump (20), hydraulic oil makes spiral tube (6) descending through fuel tank (21) and second petroleum pipeline (8 ') driving travel mechanism (22), driven wheel (13) drives planetary gear (14) rotates spiral tube 6, has the bottom that the top in shape head that is processed with the spiral tube (6) of the thread groove edge of a knife on its of drill bit function arrives filter (7); Clutch (12) in Clutch Control line (12 ') control, allow clutch (12) leave driven wheel (13), clutch (12A) makes flat bevel gear (31) and perpendicular bevel gear (30) engagement under Clutch Control line (12A ') control, more piece pipe (18) self rotates, and hydraulic oil stretches out in the outer wall insertion filtrate (17) or filtrate (15) or filtrate (11) of spiral tube (6) more piece pipe (18) action through fuel tank (21) and first petroleum pipeline (8); Allow clutch (12) and driven wheel (13) mesh, control clutch (12A) down allows flat bevel gear (31) and perpendicular bevel gear (30) break away from meshing relation, and being rotated further of drive shaft (5) rotated more piece pipe (18) in a plane; The ultrasonic wave that sends with supersonic generator (24) makes the oscillator (25) more than 1 produce vibration through connecting (26); Be communicated with compressed air hose (9), compressed air in universal joint (29) blasts more piece pipe (18), in more piece pipe (18), blast the compressed air that pressure is 0.09-0.11MPa in filtrate " in-situ regeneration " process discontinuous formula, regenerating medium input pipe (10) is communicated with more piece pipe (18) through universal joint (28), by the dodecyldimethylammonium hydroxide inner salt that accounts for gross weight 25-45%, account for the sodium humate of gross weight 5-15%, account for the shrink sorbitol monooleate of gross weight 10-15%, account for the fatty acid amide of gross weight 2-5%, account for the Sodium Polyacrylate of gross weight 2.5-5%, account for the argon sodium oxide molybdena of gross weight 3-5% and account for in-situ regeneration medium that the water of gross weight 25-35% is re-dubbed and be input in the more piece pipe (18) with the amount of 10-50kg/min, each constituent content sum of this in-situ regeneration medium is 100%; Start the sewage pump (2) that is installed on the installing rack (3), sewage is sent into water treatment front end sedimentation basin (23) through soil pick-up water pipe (4) and blow-off pipe (4 '), opening water discharge valve (27) is discharged the sewage in the filter (7); Wherein filtrate (17,15,11) is selected from a kind of in quartz sand filter media, walnut shell filtering material, ceramic filter material, cleaned coal filtrate, the activated carbon filtrate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200710303491A CN100584422C (en) | 2007-12-29 | 2007-12-29 | The in situ regeneration method of polluted filtering material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200710303491A CN100584422C (en) | 2007-12-29 | 2007-12-29 | The in situ regeneration method of polluted filtering material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101279156A true CN101279156A (en) | 2008-10-08 |
| CN100584422C CN100584422C (en) | 2010-01-27 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200710303491A Expired - Fee Related CN100584422C (en) | 2007-12-29 | 2007-12-29 | The in situ regeneration method of polluted filtering material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100584422C (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101891298A (en) * | 2010-07-30 | 2010-11-24 | Jck株式会社 | In-situ activation modification treatment method for suspended filter material |
| CN102674498A (en) * | 2012-05-18 | 2012-09-19 | 江苏永冠给排水设备有限公司 | Adsorptive water defluorination device for hydroxyapatite filter material |
| CN102784500A (en) * | 2012-08-14 | 2012-11-21 | 湖南娄底泰阳科技有限公司 | General in-situ regeneration device for polluted raw materials |
| CN102886165A (en) * | 2012-10-16 | 2013-01-23 | 抚顺市明尧石油机械有限公司 | Multifunctional purifier |
| CN105647697A (en) * | 2016-02-22 | 2016-06-08 | 潘兴灿 | Multicomponent detergent and application of detergent in cleaning of multi-media filter |
| CN109011737A (en) * | 2018-08-29 | 2018-12-18 | 戚汝常 | It is a kind of for purifying the more filter cylinder filter devices and method of sewage |
| CN113893758A (en) * | 2021-10-20 | 2022-01-07 | 宁波交通工程建设集团有限公司 | Large-capacity industrialized muck stirring device |
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2007
- 2007-12-29 CN CN200710303491A patent/CN100584422C/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101891298A (en) * | 2010-07-30 | 2010-11-24 | Jck株式会社 | In-situ activation modification treatment method for suspended filter material |
| CN101891298B (en) * | 2010-07-30 | 2012-06-20 | Jck株式会社 | In-situ activation modification treatment method for suspended filter material |
| CN102674498A (en) * | 2012-05-18 | 2012-09-19 | 江苏永冠给排水设备有限公司 | Adsorptive water defluorination device for hydroxyapatite filter material |
| CN102784500A (en) * | 2012-08-14 | 2012-11-21 | 湖南娄底泰阳科技有限公司 | General in-situ regeneration device for polluted raw materials |
| CN102784500B (en) * | 2012-08-14 | 2014-08-06 | 湖南娄底泰阳科技有限公司 | General in-situ regeneration device for polluted raw materials |
| CN102886165A (en) * | 2012-10-16 | 2013-01-23 | 抚顺市明尧石油机械有限公司 | Multifunctional purifier |
| CN105647697A (en) * | 2016-02-22 | 2016-06-08 | 潘兴灿 | Multicomponent detergent and application of detergent in cleaning of multi-media filter |
| CN105647697B (en) * | 2016-02-22 | 2018-09-14 | 山东鲁东环保科技有限公司 | A kind of multicomponent cleaning agent and its application in more medium filter cleaning |
| CN109011737A (en) * | 2018-08-29 | 2018-12-18 | 戚汝常 | It is a kind of for purifying the more filter cylinder filter devices and method of sewage |
| CN113893758A (en) * | 2021-10-20 | 2022-01-07 | 宁波交通工程建设集团有限公司 | Large-capacity industrialized muck stirring device |
| CN113893758B (en) * | 2021-10-20 | 2022-09-02 | 宁波交通工程建设集团有限公司 | Large-capacity industrial muck stirring device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100584422C (en) | 2010-01-27 |
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