EP3165678B1 - Ground improvement method - Google Patents
Ground improvement method Download PDFInfo
- Publication number
- EP3165678B1 EP3165678B1 EP15799627.3A EP15799627A EP3165678B1 EP 3165678 B1 EP3165678 B1 EP 3165678B1 EP 15799627 A EP15799627 A EP 15799627A EP 3165678 B1 EP3165678 B1 EP 3165678B1
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- EP
- European Patent Office
- Prior art keywords
- ground
- jet device
- solidification material
- slurry
- stable liquid
- Prior art date
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- 238000000034 method Methods 0.000 title claims description 37
- 239000000463 material Substances 0.000 claims description 189
- 238000007711 solidification Methods 0.000 claims description 118
- 230000008023 solidification Effects 0.000 claims description 118
- 239000007788 liquid Substances 0.000 claims description 82
- 239000002002 slurry Substances 0.000 claims description 76
- 238000005192 partition Methods 0.000 claims description 71
- 239000002689 soil Substances 0.000 claims description 69
- 239000000203 mixture Substances 0.000 claims description 44
- 238000005553 drilling Methods 0.000 claims description 24
- 108090000790 Enzymes Proteins 0.000 claims description 19
- 102000004190 Enzymes Human genes 0.000 claims description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 19
- 239000004568 cement Substances 0.000 claims description 14
- 238000005520 cutting process Methods 0.000 claims description 14
- 238000000354 decomposition reaction Methods 0.000 claims description 8
- 239000012530 fluid Substances 0.000 claims description 8
- 229910021536 Zeolite Inorganic materials 0.000 description 41
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 41
- 239000010457 zeolite Substances 0.000 description 41
- 238000000926 separation method Methods 0.000 description 35
- 239000003673 groundwater Substances 0.000 description 22
- 229940088598 enzyme Drugs 0.000 description 17
- 239000012857 radioactive material Substances 0.000 description 15
- 238000009792 diffusion process Methods 0.000 description 11
- 239000002440 industrial waste Substances 0.000 description 10
- 239000011259 mixed solution Substances 0.000 description 8
- 239000001913 cellulose Substances 0.000 description 7
- 229920002678 cellulose Polymers 0.000 description 7
- 238000010276 construction Methods 0.000 description 7
- 229910052792 caesium Inorganic materials 0.000 description 6
- TVFDJXOCXUVLDH-UHFFFAOYSA-N caesium atom Chemical compound [Cs] TVFDJXOCXUVLDH-UHFFFAOYSA-N 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 5
- 229920002907 Guar gum Polymers 0.000 description 4
- 239000000665 guar gum Substances 0.000 description 4
- 229960002154 guar gum Drugs 0.000 description 4
- 235000010417 guar gum Nutrition 0.000 description 4
- 238000011065 in-situ storage Methods 0.000 description 4
- 239000002861 polymer material Substances 0.000 description 4
- 229920003169 water-soluble polymer Polymers 0.000 description 4
- 108010059892 Cellulase Proteins 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 229940106157 cellulase Drugs 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 238000011109 contamination Methods 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 239000004014 plasticizer Substances 0.000 description 2
- 238000010791 quenching Methods 0.000 description 2
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 2
- 239000004115 Sodium Silicate Substances 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 235000019353 potassium silicate Nutrition 0.000 description 1
- 229910052911 sodium silicate Inorganic materials 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Classifications
-
- E—FIXED CONSTRUCTIONS
- E02—HYDRAULIC ENGINEERING; FOUNDATIONS; SOIL SHIFTING
- E02D—FOUNDATIONS; EXCAVATIONS; EMBANKMENTS; UNDERGROUND OR UNDERWATER STRUCTURES
- E02D3/00—Improving or preserving soil or rock, e.g. preserving permafrost soil
- E02D3/12—Consolidating by placing solidifying or pore-filling substances in the soil
-
- E—FIXED CONSTRUCTIONS
- E02—HYDRAULIC ENGINEERING; FOUNDATIONS; SOIL SHIFTING
- E02D—FOUNDATIONS; EXCAVATIONS; EMBANKMENTS; UNDERGROUND OR UNDERWATER STRUCTURES
- E02D2250/00—Production methods
- E02D2250/003—Injection of material
-
- E—FIXED CONSTRUCTIONS
- E02—HYDRAULIC ENGINEERING; FOUNDATIONS; SOIL SHIFTING
- E02D—FOUNDATIONS; EXCAVATIONS; EMBANKMENTS; UNDERGROUND OR UNDERWATER STRUCTURES
- E02D2300/00—Materials
- E02D2300/0004—Synthetics
- E02D2300/0018—Cement used as binder
-
- E—FIXED CONSTRUCTIONS
- E02—HYDRAULIC ENGINEERING; FOUNDATIONS; SOIL SHIFTING
- E02D—FOUNDATIONS; EXCAVATIONS; EMBANKMENTS; UNDERGROUND OR UNDERWATER STRUCTURES
- E02D2300/00—Materials
- E02D2300/0004—Synthetics
- E02D2300/0018—Cement used as binder
- E02D2300/0023—Slurry
Definitions
- the ratio of water to a solidification material (a cement) to be fed (W/C) be low, or the solidification material be so called "rich-mixed.”
- Patent Document 1 JP-A-7-331652
- a lower end portion of the jet device 1 is provided with a discharge port 11 (a jetting port) of a solidification material.
- a portion which is vertically higher than the lower end portion of the jet device 1 is provided with a plurality of jetting ports 12such as nozzles (2 jetting ports in Fig. 1 ).
- a high plasticizer is added to the solidification material (W/C ranges from 26% to 40%).Addition of a high plasticizer can reduce an increase in the viscosity of a rich-mixed solidification material whose W/C ranges from 26% to 40%, and it is possible to carry the rich-mixed solidification material (W/C ranges from 26% to 40%) by using a conventional pump for carrying a lean-mixed solidification material.
- the partition forming material, the stable liquid and the solidification material can be controlled in feed/feed-quenching by ON-OFF control of a pump of the partition forming material feed source 7 (not shown), a pump of the stable liquid feed source 8 (not shown), a pump of the solidification material feed source 9 (not shown).
- discharge of the (rich-mixed) solidification material delivered (injected) in the soil by the layer L D (the separation layer) of the partition forming material above the ground is reduced.
- a slurry discharged (subjected to reverse flow)above the ground contains the stable liquid and the cut soil, discharge of the solidification material above the ground as a slurry can be reduced.
- the slurry fed to the slurry treating structure 4 is a mixed solution of the stable liquid and the cut soil to prevent the solidification material from being contained. Therefore, in Fig. 1 , when a cellulose decomposition enzyme is added to the slurry fed to a slurry treating structure 4, guar gum (a natural water-soluble polymer material) in the stable liquid is degraded by the cellulose decomposition enzyme and the slurry will turn into a mixed solution of water and soil. This type of solution does not correspond to an industrial waste, and it is thus not necessary to transport the mixed solution to an treating facility as an industrial waste.
- the jet device 1 injects the jet flow J of the partition forming material to cut the ground G, and moves (pulls up) in a vertical direction by rotating the same. Consequently, a layer L D (a separation layer) of a mixture of the partition forming material and a cut soil is formed.
- the partition forming material is injected to form a separation layer L D composed of the partition forming material so as not to mix but separate an layer L W of a mixture of the stable liquid and the cut soil and a layer L C of a solidification material.
- a slurry as a mixture of the partition forming material and a cut soil is generated and subjected to reverse flow above the ground. Slurry subjected to reverse flow above the ground is collected by the slurry collecting structure 2.
- the stable liquid is injected from the jet device 1 as a jet flow J to cut a ground G.
- the jet device 1 is pulled up in an upward vertical direction by rotating the same.
- a slurry collected by a slurry collecting structure 2 is enzyme-degraded by the slurry treating structure 4, and it will turn into a mixture of soil and water. Accordingly, the trouble of treating the same by using a dedicated treating facility can be saved as an industrial waste.
- Fig. 7 is a flow chart showing steps shown in Figs. 2 to 6 .
- step S1 a change-over valve 10 is switched to open only a feed line 17 from a partition forming material feed source 7 to the jet device 1, and a feed line 18 from a stable liquid feed source 8 and a feed line 19 from a solidification material feed source 9 are closed to feed a partition forming material to the jet device 1.
- a partition forming material is injected underground from jetting ports 12, the jet device 1 is pulled up in a vertical direction by rotating the same, thereby forming a separation layer L D composed of the partition forming material.
- the process proceeds to step S2.
- stepS5 a change-over valve 10 is switched to close a feed line 18 from a stable liquid feed source 8 to the jet device 1 and a feed line 19 from a solidification material feed source 9 to the jet device 1 to quench the feeding of a stable liquid and a solidification material to the jet device 1.
- step S3 Since a passage from the partition forming material feed source 7 to the jet device 1 is closed in step S3, the partition forming material is not fed by the jet device 1even in step S5.
- a step S1 for injecting the partition forming material to form a separation layer L D composed of the partition forming material is implemented prior to step S3 for cutting soil with a stable liquid, a layer L W of a mixture of the stable liquid and the cut soil and a rich-mixed layer L C of the solidification material are divided by a separation layer L D . Accordingly, contact of a rich-mixed solidification material with a mixed fluid of the stable liquid and the cut soil(a mixed liquid comprising a layer L W ) is reduced, and only a mixed fluid of the stable liquid and the cut soil(a mixed liquid composed of a layer L W ) is discharged above the ground as a slurry. Therefore, since the rich-mixed solidification material is scarcely discharged above the ground, consumption of the solidification material can be reduced compared to a conventional level.
- the slurry collected by the slurry collecting structure 2 (a mixture of the stable liquid and the cut soil) is carried to a slurry treating structure 4 to add a cellulose decomposition enzyme from an enzyme feed source 5, thereby turning the slurry into a mixed solution of only water and soil as non-industrial waste.
- a slurry treating structure 4 to add a cellulose decomposition enzyme from an enzyme feed source 5, thereby turning the slurry into a mixed solution of only water and soil as non-industrial waste.
- a continuous wall 22 e.g. a frozen soil wall
- the flow of the ground water WG1 containing a radioactive material subjected to outflow and diffusion underground from the reactor building 21 is cut off by using the continuous wall 22. Accordingly, outflow and diffusion of the ground water WG1contaminated to the outside thereof through the frozen soil wall 22 is prevented.
- the thickness B of the zeolite bottom slab L Z , while the ground water WG2contaminated with the radioactive material passes (transmits) the zeolite bottom slab L Z , is determined at a value so that cesium contained in the ground water WG2 can sufficiently be adsorbed by zeolite of the zeolite bottom slab L Z .
- the thickness depends on the degree of contamination and several working conditions.
- the ground water WG2 subjected to outflow (leakage) and diffusion underground in a direction just beneath the reactor building 21 from the same passes the zeolite bottom slab L Z to adsorb and remove cesium.
- zeolite has a chemical property of adsorbing cesium as a main component of the radioactive material.
- cesium is a major component of the radioactive material, and if cesium can be removed, the radioactive material concentration in the ground water WG2 is reduced to a safety value (or a standard value or less).
- Fig. 10 shows formation of the zeolite bottom slab L Z extending in a horizontal direction.
- a layer L W of a mixture of the stable liquid and the cut soil and the layer L D (the separation layer) of a mixture of the partition forming material and the cut soil are formed.
- a layer L Z of zeolite is formed.
- Across sectional shape of the layer L Z of zeolite (i.e. the range of the zeolite bottom slab L Z in a horizontal direction) is circular like in the embodiments shown in Figs. 1 to 7 .
- the shape of the zeolite bottom slab L Z can be non-circular (e.g. a semicircle or a sector) in case contaminated water is diffused.
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Structural Engineering (AREA)
- Agronomy & Crop Science (AREA)
- Environmental & Geological Engineering (AREA)
- Soil Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Mining & Mineral Resources (AREA)
- Paleontology (AREA)
- Civil Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Consolidation Of Soil By Introduction Of Solidifying Substances Into Soil (AREA)
Description
- The present invention relates to a ground improvement technology that forms an underground consolidated body by cutting (in-situ) soil in the ground to be improved and mixing water and a solidification material such as cement and agitating a mixture thereof, such as generally known from and disclosed by document
DE 101 54 201 A , disclosing the features according to the preamble ofclaim 1. - A technology for forming an underground consolidated body of a cylindrical shape by drilling a drilling hole in a ground to be improved, moving (pulling up or pushing down) a jet device in a vertical direction by rotating the same while the jet device is inserted into the drilling hole and a high-pressure fluid such as water is injected in an outward radial direction from the jet device to cut an in-situ soil, and by mixing the cut soil and a solidification material such as a cement and agitating a mixture thereof by injecting or delivering the solidification material to the soil has widely been known (e.g. Patent Document 1).
- In order to improve the strength (quality) of an underground consolidated body formed, it is preferable that the ratio of water to a solidification material (a cement) to be fed (W/C) be low, or the solidification material be so called "rich-mixed."
- However, a lower W/C might lead to more viscosity of a mixture of water and a cement, thereby blocking a carrying passage from a cement feed source to a jet device. Thus, it is difficult to carry a solidification material to the jet device.
- In addition, all of a solidification material injected from a jet device is not solidified underground and large amounts of the solidification material are discharged above the ground as a slurry. In fact, such a solidification material must be treated as an industrial waste. Also, if a solidification material is "rich-mixed" with a low W/C, large amounts of the solidification material will be treated as an industrial waste, resulting in an increase in construction costs accordingly.
- From the above described reasons, use of a "lean-mixed" solidification material with a W/C of 100% or more has been essential in a prior art.
- Patent Document 1:
JP-A-7-331652 - The present invention was created in view of the above situation, and has an object to provide a method for improving ground being capable for improving the strength or quality of an underground consolidated body formed by reducing the ratio of water to a "rich-mixed" solidification material (a cement) (W/C), assuredly carrying the solidification material from a feed source to a jet device, and reducing the amount of the solidification material treated as an industrial waste.
- The above mentioned problem is solved by the method of improving ground according to
claim 1. - According to
claim 2, method for improving ground of the present invention preferably comprises: a step of collecting a mixture of the stable liquid discharged above the ground and a cut soil (S: slurry) by a slurry collecting structure (2); and a step of carrying the slurry (S) collected by the slurry collecting structure (2) to a slurry treating structure (4) and adding an enzyme (E: a cellulose decomposition enzyme such as "cellulase") from an enzyme feed source (5). - The method for improving ground of the present invention comprising the above steps can improve the strength(quality)of an underground consolidated body formed from a rich-mixed solidification material whose ratio of water to a cement (W/C) ranges from 26% to 40%, compared to the strength of an underground consolidated body formed with a conventional lean-mixed solidification material.
- Herein, a solidification material (a rich-mixed solidification material whose W/C ranges from 26% to 40%) contains a high fluidity, and an increase in the viscosity of even a rich-mixed solidification material is reduced. Thus, the method for improving ground of the present invention can carry a rich-mixed solidification material by means of a pump for carrying a lean-mixed solidification material used in a prior art.
- According to the present invention, a partition forming material is injected prior to a step of cutting soil with a stable liquid, a separation layer (LD) composed of the partition forming material is formed between a layer (LW) of a mixture of the stable liquid and a cut soil and a layer (LC) of a rich-mixed solidification material.
- By using the separation layer (LD: the layer composed of the partition forming material), the rich-mixed solidification material injected underground can reduce contact with the mixture of the stable liquid and the cut soil.
- Therefore, only the mixture of the stable liquid and the cut soil is discharged above the ground as a slurry (S), and the rich-mixed solidification material is scarcely discharged above the ground. Specifically, the layer of the partition forming material(LD: the separation layer) can reduce discharge of the solidification material injected underground above the ground.
- Since discharge of the solidification material above the ground as a slurry (S) is reduced, the method for improving ground of the present invention can reduce the amount of a solidification material discharged above the ground as a slurry (S) in comparison with a prior art, thereby saving construction costs accordingly.
- The method for improving ground of the present invention can collect a mixture of a stable liquid and a cut soil (S: slurry)ejected above the ground by including a step of collecting the slurry (S) discharged above the ground by a slurry collecting structure (2).Therefore, it is possible to prevent the slurry (S) from dispersing around a construction site and working conditions from deteriorating.
- In addition, by including a step of carrying the slurry (S) collected by the slurry collecting structure (2) to a slurry treating structure (4) and adding an enzyme (E: a cellulose decomposition enzyme such as "cellulase") from an enzyme feed source (5), the slurry (S) as a mixed solution of the stable liquid and the cut soil will turn into a mixed solution of only water and soil after guar gum (a natural water-soluble polymer material) in the stable liquid is degraded by the cellulose decomposition enzyme (E). Herein, since the method for improving ground of the present invention is not required to treat a slurry as an industrial waste, if it is a mixed solution of only water and soil, it is not necessary to transport by land the slurry to a treating facility accordingly, as opposed to a prior art.
- In a step of moving (pulling up) a jet device (1) in a vertical direction by rotating or pivoting the same while a fluid for cutting the ground(G)(a stable liquid or a partition forming material) is injected from the jet device (1) according to the present invention, zeolite is injected from the jet device (1) to form a zeolite layer (LZ: a zeolite bottom slab)underground.
- When said zeolite bottom slab (LZ) is placed underground at an outflow (leakage)passage or a diffusion passage of a ground water (WG)contaminated with a radioactive material in an adjacent facility such as a reactor building (21),the ground water (WG)contaminated with the radioactive material that flows out or diffuses underground from the reactor building (21) or others comes into said zeolite bottom slab (LZ) in the process of underground outflow or diffusion and passes (or transmits)said zeolite bottom slab (LZ).
- In the process of the ground water (WG) to pass (transmit) the zeolite bottom slab (LZ), most cesium mainly contained in the radioactive material is adsorbed by zeolite to be removed from the ground water. Consequently, the concentration of the radioactive material in the ground water that passes (transmits) said zeolite bottom slab (LZ) is significantly reduced to a "standard value" or less. Specifically, the method for improving ground of the present invention also serves as a method for purifying ground water contaminated with a radioactive material.
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Fig. 1 is a schematic view showing an embodiment of the present invention; -
Fig. 2 is a process drawing showing a first step for implementing an embodiment; -
Fig. 3 is a process drawing showing a step following a step shown inFig. 2 ; -
Fig. 4 is a cross sectional view of a jet device taken from line A-A ofFig. 3 ; -
Fig. 5 is a process drawing showing a step following a step shown inFig. 3 ; -
Fig. 6 is process drawing showing a step following a step shown inFig. 5 ; -
Fig. 7 is a flow chart showing the procedures shown inFigs. 2 to 6 ; -
Fig. 8 is a view showing the problem to be solved by the another embodiment of the present invention; -
Fig. 9 is a schematic view showing another embodiment of the present invention; and -
Fig. 10 is a process drawing showing a step of another embodiment of the present invention. - An embodiment of the present invention will be described with reference to the drawings.
- First, an apparatus required for implementing an embodiment for the method for improving ground will be described with reference to
Fig. 1 . - In
Fig. 1 , the ground to which the method for improving ground of the present invention is applied is denoted by a symbol G. A rod-shaped jet device 1 is inserted into a drilling hole H drilled in a ground G. - Herein, a
installing mechanism 6 shown by dotted line inFig. 1 is an apparatus for inserting (installing) thejet device 1 into the drilling hole H. - The
jet device 1 is a double-pipe structure (Fig. 4 , not shown inFig. 1 in detail). InFig. 4 , an inner space of aninner pipe 15 provides a flow passage for feeding a rich-mixed solidification material. An annular space between theinner pipe 15 and anouter pipe 16 provides a flow passage for feeding as table liquid or a partition forming material. - In
Fig. 1 , a lower end portion of thejet device 1 is provided with a discharge port 11 (a jetting port) of a solidification material. A portion which is vertically higher than the lower end portion of thejet device 1 is provided with a plurality of jetting ports 12such as nozzles (2 jetting ports inFig. 1 ). - On a horizontal cross section of the
jet device 1, a plurality of jetting ports 12 (2 jetting ports inFig. 1 ) are disposed so as to be symmetrical with respect to the central axis in a vertical direction (not shown). A plurality ofjetting ports 12 are provided to inject the stable liquid or the partition forming material. - The stable liquid and the partition forming material are not simultaneously injected from a plurality of the jetting ports 12.As shown in
Figs. 5 and6 and later descriptions, the partition forming material is injected from thejetting ports 12 prior to a step of cutting soil by injecting the stable liquid from a plurality of saidjetting ports 12. - As shown in
Fig. 1 , a separation layer LD composed of a mixture of the partition forming material and a cut soil is formed between a layer LW of a mixture of the stable liquid and the cut soil and a layer LC of a (rich-mixed) solidification material. - In
Fig. 1 , the separation layer LD composed of the partition forming material is formed after a step of forming a separation layer LD by injecting the partition forming material, and soil is cut by injecting a jet flow J of the stable liquid from the jetting ports 12.Herein, the solidification material is delivered (injected)from thedischarge port 11 at a lower end of thejet device 1 to form the layer LC of the solidification material. - In an illustrative example as presented in the drawings, a solution containing 5% by weight of a viscosity improver such as guar gum of a natural water-soluble polymer material is injected from the
jet device 1 and a plurality of thejetting ports 12 as the stable liquid to drill soil. - In a further illustrative example presented in drawings, the partition forming material is a solution containing 5% by weight of a viscosity improver such as guar gum of a natural water-soluble polymer material and 5% by weight of sodium silicate (water glass).The partition forming material is then injected in the soil and mixed with field soil to provide a separation layer LD.
- The solidification material is a mixture of water and a rich-mixed cement in an embodiment shown in drawings, such as a mixture whose W/C ranges from 26% to 40%.The theoretical value of W/C is determined at 26% and a lower limit. On the other hand, inventors of the present invention experimentally failed to obtain a desired strength (quality) on an underground consolidated body when W/C was over 40%.
- In an illustrative example presented in drawings, a high plasticizer is added to the solidification material (W/C ranges from 26% to 40%).Addition of a high plasticizer can reduce an increase in the viscosity of a rich-mixed solidification material whose W/C ranges from 26% to 40%, and it is possible to carry the rich-mixed solidification material (W/C ranges from 26% to 40%) by using a conventional pump for carrying a lean-mixed solidification material.
- In an illustrative example presented in the drawings,
3to 7% by weight of polycarboxylic acid-based compound (e.g. Product from TAKEMOTO OIL&FAT Co., Ltd. "Chu-po-ru" series) is added to a cement as a high fluidity. Inventors of the present invention experimentally added 5% by weight of a polycarboxylic acid-based compound to a cement, and found that it is preferable in carrying a solidification material of an underground consolidated body. - Inventors of the present invention experimentally found that a mixture obtained by mixing 100parts by weight of a cement, 25parts by weight of water and 5parts by weight of a polycarboxylic acid-based compound and agitating a mixture thereof can be carried by using a conventional pump for carrying a lean-mixed solidification material (W/C is 100% or more).
- In
Fig. 1 , thejet device 1 is connected to a partition formingmaterial feed source 7 via anintroduction portion 14 and afeed line 17, and connected to a stableliquid feed source 8 via theintroduction portion 14 and afeed line 18. Thejet device 1 is connected to a solidificationmaterial feed source 9 via theintroduction portion 13 and afeed line 19. - A change-over
valve 10 is placed on feed lines17, 18 and 19.By switching the change-overvalve 10, the partition forming material, the stable liquid and the solidification material are each fed to thejet device 1 or feeding is quenched. - As shown in
Fig. 1 , formation of a separation layer LD is completed. Soil is cut by injecting the stable liquid, and the solidification material is delivered (injected) to form a layer LC of the solidification material. Thus, inFig. 1 , while the change-overvalve 10 cuts off feeding of the partition forming material from a partition formingmaterial feed source 7 to thejet device 1, the change-overvalve 10 is at a switching position for feeding the stable liquid from the stableliquid feed source 8 to thejet device 1 and the solidification material from the solidificationmaterial feed source 9 to thejet device 1. - In place of the change-over
valve 10, the partition forming material, the stable liquid and the solidification material can be controlled in feed/feed-quenching by ON-OFF control of a pump of the partition forming material feed source 7 (not shown), a pump of the stable liquid feed source 8 (not shown), a pump of the solidification material feed source 9 (not shown). - As described above, the jet device is moved(e.g. pulled up)in a vertical direction by rotating the same (i.e. rotating a inject nozzle in a injecting direction) while high-pressure water and a solidification material are injected from the jet device. In this case, a conventional method for improving ground subjects a solidification material to reverse flow above the ground as a slurry of a mixture of water, soil and a solidification material and to discharge above the ground.
- On the other hand, as shown in
Fig. 1 , a layer LW of a mixture of the stable liquid and the cut soil and a layer LC of a rich-mixed solidification material are divided by a layer LD (a separation layer) of a mixture of the partition forming material and the cut soil. Therefore, the layer LD of the stable liquid for cutting soil hardly mixes with the layer LC of the rich-mixed solidification material via the separation layer LD. - As the rich-mixed solidification material is injected and the size of the solidification material layer LC in a vertical direction increases (becomes thick), the layer LD (the separation layer) of the partition forming material will move upward.
- Consequently, the mixture of the stable liquid and the cut soil is discharged above the ground(as a slurry), and excess of the solidification material on the solidification material layer LC via the separation layer LD to be discharged above the ground is reduced or removed.
- Specifically, as shown in drawings, discharge of the (rich-mixed) solidification material delivered (injected) in the soil by the layer LD (the separation layer) of the partition forming material above the ground is reduced. Thus, in an embodiment shown in drawings, while a slurry discharged (subjected to reverse flow)above the ground contains the stable liquid and the cut soil, discharge of the solidification material above the ground as a slurry can be reduced.
- Herein, the thickness of the layer LD(the separation layer) of the partition forming material is equal to a distance L in a vertical direction between the
discharge port 11 of the solidification material (the discharge port at a lower end portion of the jet device 1) and the jettingports 12 for ejecting the stable liquid or the partition forming material (a plurality of jetting ports provided upward from the discharge port 11). - The vertical distance L between said
discharge port 11 and the jettingports 12 is defined as a thickness (the size in a vertical direction)required for dividing the layer LW of the mixture of the stable liquid and the cut soil and the layer LC of the rich-mixed solidification material by the separation layer LD composed of the partition forming material and preventing the rich-mixed solidification material from mixing with the mixture of the stable liquid and the cut soil. - In an embodiment shown in drawings, the thickness L (the distance in a vertical direction) is determined at 1m.
- A surface portion of the drilling hole H is provided with a
slurry collecting structure 2. - In
Fig. 1 , a slurry is ejected above the ground via a sectional annular space between an inner wall surface of the drilling hole H and thejet device 1. - In
Fig. 1 , theslurry collecting structure 2 collects slurry discharged above the ground. Thus, dispersion of the slurry around a construction site and deterioration of working conditions can be prevented. - A known technology may be applied as for the
slurry collecting structure 2. - Slurry collected in the
slurry collecting structure 2 is fed to theslurry treating structure 4 via aslurry carrying line 3. An enzyme (a cellulose decomposition enzyme such as "cellulase") is added from anenzyme feed source 5 to the slurry fed to theslurry treating structure 4. - Herein, since a prior art shows that a slurry discharged above the ground contains a solidification material, the slurry must be treated as an industrial waste. Nevertheless, as described above with reference to
Fig. 1 , the slurry fed to theslurry treating structure 4 is a mixed solution of the stable liquid and the cut soil to prevent the solidification material from being contained. Therefore, inFig. 1 , when a cellulose decomposition enzyme is added to the slurry fed to aslurry treating structure 4, guar gum (a natural water-soluble polymer material) in the stable liquid is degraded by the cellulose decomposition enzyme and the slurry will turn into a mixed solution of water and soil. This type of solution does not correspond to an industrial waste, and it is thus not necessary to transport the mixed solution to an treating facility as an industrial waste. - Subsequently, with reference to
Figs. 2 to 7 , operational processes of the above-mentioned method for improving ground will be described. -
Fig. 2 shows that a drilling hole H is drilled in a ground G to be improved. Ajet device 1 is inserted into the drilling hole H. - In
Fig. 2 , an internal diameter DH of the drilling hole H is larger than an external diameter of the jet device 1to be inserted. Herein, when soil of the ground G is cut with a stable liquid, a slurry is discharged (subjected to reverse flow)above the ground via a sectional annular space between an inner wall surface of the drilling hole H and an outer peripheral surface of thejet device 1. The internal diameter DH of the drilling hole H is determined at a value so that the slurry is smoothly discharged above the ground. - The depth of the drilling hole H (LH) is determined according to the depth of the soil to be improved.
- In
Fig. 3 showing a step following a step shown inFig. 2 , a rod-shapedjet device 1 is inserted into a drilling hole H. When thejet device 1 is inserted into the drilling hole H, a knowninstalling mechanism 6 is employed. -
Fig. 4 is a cross sectional viewshowing jetting ports 12 of thejet device 1 taken from line A-A ofFig. 3 .Fig. 4 shows only thejet device 1, not a sectional view of the drilling hole H. As shown inFig. 4 , thejet device 1 is a double-pipe structure composed of aninner pipe 15 and anouter pipe 16. A solidification material flows inside theinner pipe 15, and a stable liquid or a partition forming material flows via a space between theinner pipe 15 and theouter pipe 16. - In fact, the stable liquid or the partition forming material is not simultaneously injected. Either of them is injected according to a corresponding step. An
introduction portion 14 of the stable liquid or the partition forming material is connected to a plurality of jettingports 12 via an annular space (Fig. 4 ) between theinner pipe 15 and theouter pipe 16 of thejet device 1 and a pipe (not shown). -
Fig. 3 shows that thejet device 1 is inserted into the drilling hole H, and none of the solidification material, the stable liquid or the partition forming material are injected or delivered in the soil. - Upon injecting of the stable liquid or the partition forming material, in order to pull upwardly the
jet device 1 by rotating the same on a central axis in a longitudinal direction, structures (a rotating structure and a lifting structure, not-shown in drawings) are provided in theinstalling mechanism 6. - In
Fig. 3 , aslurry collecting structure 2 provided at a surface portion of the drilling hole H is connected to an annular space between an inner wall surface of the drilling hole H and an outer peripheral surface of thejet device 1 to collect a slurry ejected above the ground. Theslurry collecting structure 2 is operated by a drive mechanism (not shown). -
Fig. 5 is a process drawing showing a step following a step shown inFig. 3 and shows that a partition forming material is injected to cut a ground G. InFigs. 5 and6 , ainstalling mechanism 6 is not shown. - In
Fig. 5 , the partition forming material is introduced at anintroduction portion 14 to thejet device 1 from a partition formingmaterial feed source 7 via a change-overvalve 10 and a feed line 17.The partition forming material is injected underground from a plurality of jetting ports 12in an outward radial direction as a jet flow J via an annular space (Fig. 4 ) between aninner pipe 15 and anouter pipe 16. - Thereafter, the
jet device 1 injects the jet flow J of the partition forming material to cut the ground G, and moves (pulls up) in a vertical direction by rotating the same. Consequently, a layer LD(a separation layer) of a mixture of the partition forming material and a cut soil is formed. As described with reference toFig. 1 , prior to a step of cutting the soil by injecting the stable liquid, the partition forming material is injected to form a separation layer LD composed of the partition forming material so as not to mix but separate an layer LW of a mixture of the stable liquid and the cut soil and a layer LC of a solidification material. - As shown in
Fig. 5 , in a step of cutting a ground G by injecting the partition forming material, a change-overvalve 10 is opened only in afeed line 17 from a partition formingmaterial feed source 7 to thejet device 1 and closed in feed lines18 and 19 from a stableliquid feed source 8 and a solidificationmaterial feed source 9 to the jet device 1.Thus, only the partition forming material is fed to thejet device 1, and the stable liquid and the solidification material are not fed to thejet device 1. - Herein, in a step of cutting the ground G by injecting the partition forming material, a slurry as a mixture of the partition forming material and a cut soil is generated and subjected to reverse flow above the ground. Slurry subjected to reverse flow above the ground is collected by the
slurry collecting structure 2. - If the
jet device 1 is pulled up until the thickness of the layer LD(the separation layer)of the partition forming material comes to a specific size L (the thickness required for dividing the layer LW of a mixture of the stable liquid and the cut soil and a rich-mixed layer LC of the solidification material and reducing mixture with a mixture of the stable liquid and the cut soil by the rich-mixed solidification material: 1m in an embodiment shown in drawings), a step shown inFig. 5 will be completed and a step shown inFig. 6 will be started. - In a step shown in
Fig. 6 , the solidification material is injected while the ground G is cut by injecting the stable liquid. In a step shown inFig. 6 , while the change-over valve 10cuts off afeed line 17 from the partition formingmaterial feed source 7 to thejet device 1, it opens afeed line 18 from the stableliquid feed source 8 to thejet device 1 and afeed line 19 from a solidificationmaterial feed source 9 to thejet device 1. - Accordingly, the stable liquid fed via the change-over
valve 10 in thefeed line 18 from the stableliquid feed source 8 is injected in an outward radial direction in underground from a plurality of jettingports 12 via an annular space (Fig. 4 ) between aninner pipe 15 and anouter pipe 16 from anupper introduction portion 14 of thejet device 1. The solidification material is introduced into thejet device 1 from an solidificationmaterial introduction portion 13 upward from thejet device 1 via afeed line 19 and the change-overvalve 10 from the solidificationmaterial feed source 9, and delivered underground from adischarge port 11 via an internal space of the inner pipe 15 (Fig. 4 ). - The stable liquid is injected from the
jet device 1 as a jet flow J to cut a ground G. Thejet device 1 is pulled up in an upward vertical direction by rotating the same. - Meanwhile, the solidification material is delivered (injected) from the
discharge port 11 provided at a lower end of thejet device 1. Thereafter, an in-situ soil and the solidification material are mixed to form an underground consolidated body. - The stable liquid is injected underground from the
jet device 1 to cut and agitate the ground G, and thejet device 1 is pulled up in a vertical direction by rotating the same on an axis of thejet device 1 to form the layer LW of a mixture of the stable liquid and the cut soil. Then, the solidification material is delivered (injected) underground from thejet device 1 to form the layer LC of the solidification material (an underground consolidated body). - As described above, since the separation layer LD composed of the partition forming material is placed between the layer LW of a mixture of the stable liquid and the cut soil and the layer LC of the solidification material, mixture of the layer LW of a mixture of the stable liquid and the cut soil and the layer LC of the solidification material are not mixed.
- As the solidification material is continuously delivered (injected) from the
jet device 1 and the size of the layer LC of the solidification material in a vertical direction increases (becomes thick), the layer of the partition forming material (the separation layer LD) will move upward. - Thus, a slurry (a mixture of the stable liquid and the cut soil) is discharged above the ground only from an upper region of the separation layer LD composed of the partition forming material, or the layer LW of a mixture of the stable liquid and the cut soil. A rich-mixed solidification material in the layer LC of the solidification material is scarcely discharged above the ground.
- Since the solidification material is not discharged above the ground in a step shown in
Fig. 6 , a slurry collected by aslurry collecting structure 2 is enzyme-degraded by theslurry treating structure 4, and it will turn into a mixture of soil and water. Accordingly, the trouble of treating the same by using a dedicated treating facility can be saved as an industrial waste. - The step shown in
Fig. 6 is continued until the layer LC of the solidification material (the underground consolidated body) comes above the ground and a size of an underground consolidated body in a vertical direction reaches a predetermined value. -
Fig. 7 is a flow chart showing steps shown inFigs. 2 to 6 . - With reference to the flow chart in
Fig. 7 in particular andFigs. 2 to 6 , construction procedures of the embodiment shown in drawings will be described. - In
Fig. 7 , in step S1, a change-overvalve 10 is switched to open only afeed line 17 from a partition formingmaterial feed source 7 to thejet device 1, and afeed line 18 from a stableliquid feed source 8 and afeed line 19 from a solidificationmaterial feed source 9 are closed to feed a partition forming material to the jet device 1.Then, while a partition forming material is injected underground from jettingports 12, thejet device 1 is pulled up in a vertical direction by rotating the same, thereby forming a separation layer LD composed of the partition forming material. Thereafter, the process proceeds to step S2. - In stepS2, whether the thickness of the separation layer LD composed of the partition forming material reaches a required thickness (a size in a vertical direction L: predetermined size) or not is determined. In other words, in stepS2, whether the amount of pulling up the
jet device 1 is a predetermined size L or more or not is determined. - If the amount of pulling up the jet device 1 (the thickness of the separation layer LD) is less than the thickness L required for the separation layer LD(step S2 is determined "NO"), the process will return to step S1 to continue a step of injecting the partition forming material and cutting the ground G to form the separation layer LD.
- On the other hand, the amount of pulling up the jet device 1 (the thickness of the separation layer LD)is the thickness L required for the separation layer LD or more (step S2 is determined "YES"), the process will proceed to step S3.
- In stepS3, the change-over
valve 10 is switched to close afeed line 17 from a partition formingmaterial feed source 7 to thejet device 1 and to open afeed line 18 from a stableliquid feed source 8 to thejet device 1 and afeed line 19 from a solidificationmaterial feed source 9 to the jet device 1.Accordingly, injecting of the partition forming material is quenched, and the stable liquid is injected in a horizontal direction to deliver a solidification material. - Thereafter, the
jet device 1 is pulled up in a vertical direction by rotating the same while the stable liquid is injected to cut the ground G. At the same time, the solidification material is delivered (injected) from a discharge port 11provided at a lower end of thejet device 1, and it is mixed with a cut in-situ soil to form an underground consolidated body. - A slurry (a mixed fluid of the stable liquid and the cut soil) generated in step S3 is collected above the ground by using a collecting
structure 2, carried to aslurry treating structure 4 by using aslurry carrying line 3, and an enzyme is added from anenzyme feed source 5 in theslurry treating structure 4 to provide a mixed solution only composed of water and soil. Therefore, it is not necessary to transport the same to a treating facility as an industrial waste. - Then, the process will proceed to step S4.
- In stepS4, whether a layer LC of the solidification material reaches above the ground so that the size of an underground consolidated body in a vertical direction is a desired size to complete the formation of an underground consolidated body or not is determined.
- If the layer LC of the solidification material (the underground consolidated body)does not reach a desired thickness and the formation of the underground consolidated body is not completed (step S4 is determined "NO"), the process will return to step S3 to continue a step of delivering (injecting) the solidification material while the stable liquid is injected to cut the ground G.
- If the layer LC of the solidification material reaches a desired size in a vertical direction and the formation of the underground consolidated body is completed (step S4 is determined "YES"), the process will proceed to step S5.
- In stepS5, a change-over
valve 10 is switched to close afeed line 18 from a stableliquid feed source 8 to thejet device 1 and afeed line 19 from a solidificationmaterial feed source 9 to thejet device 1 to quench the feeding of a stable liquid and a solidification material to thejet device 1. - In addition, an operation for rotating the
jet device 1 and an operation for pulling up the same above the ground at a predetermined speed are quenched. - Since a passage from the partition forming
material feed source 7 to thejet device 1 is closed in step S3, the partition forming material is not fed by the jet device 1even in step S5. - Thereafter, operations of a
slurry collecting structure 2, aslurry carrying line 3 and aslurry treating structure 4 are quenched, and the process will proceed to step S5 to complete the operations. - According to the embodiment shown in drawings, use of a rich-mixed solidification material (C) whose ratio of water to a cement (W/C) ranges from 26% to 40% can improve the strength (quality) of an underground consolidated body formed, compared to a solidification material of a conventional lean-mixed solidification material (W/C is 100% or more).
- Herein, since a solidification material (C: a rich-mixed solidification material whose W/C ranges from 26% to 40%) contains a high fluidity, an increase in the viscosity of the solidification material (C) is reduced, and it can be carried by using a conventional solidification material carrying pump (a pump for carrying a lean-mixed solidification material in a prior art).
- In the embodiment shown in drawings, a step S1 for injecting the partition forming material to form a separation layer LD composed of the partition forming material is implemented prior to step S3 for cutting soil with a stable liquid, a layer LW of a mixture of the stable liquid and the cut soil and a rich-mixed layer LC of the solidification material are divided by a separation layer LD. Accordingly, contact of a rich-mixed solidification material with a mixed fluid of the stable liquid and the cut soil(a mixed liquid comprising a layer LW) is reduced, and only a mixed fluid of the stable liquid and the cut soil(a mixed liquid composed of a layer LW) is discharged above the ground as a slurry. Therefore, since the rich-mixed solidification material is scarcely discharged above the ground, consumption of the solidification material can be reduced compared to a conventional level.
- Furthermore, in the embodiment shown in drawings, since a mixture of the stable liquid and the cut soil discharged above the ground is collected by a
slurry collecting structure 2, no contamination around a construction site from a slurry ejected above the ground is found. - The slurry collected by the slurry collecting structure 2 (a mixture of the stable liquid and the cut soil) is carried to a
slurry treating structure 4 to add a cellulose decomposition enzyme from anenzyme feed source 5, thereby turning the slurry into a mixed solution of only water and soil as non-industrial waste. Thus, it is not necessary to transport the same to a treating facility, which can save costs for treating a slurry. - Herein, diffusion of ground water contaminated with a radioactive material (e.g. around a reactor building) has recently become a problem in society. Another embodiment as opposed to the ones described in
Figs. 1 to 7 is capable of solving the problem. - Herein, with reference to
Fig. 8 , the above described problem (diffusion of ground water contaminated with a radioactive material) will be described. - In
Fig. 8 , in cases where a ground water WG1contaminated with a radioactive material from a reactor building 21 (including a storage facility for a radioactive material and ground water: the same as above) flows out (leaks) in the ground G, a continuous wall 22 (e.g. a frozen soil wall) is formed so as to surround the reactor building 21.Specifically, the flow of the ground water WG1 containing a radioactive material subjected to outflow and diffusion underground from thereactor building 21 is cut off by using thecontinuous wall 22. Accordingly, outflow and diffusion of the ground water WG1contaminated to the outside thereof through thefrozen soil wall 22 is prevented. - A
symbol 23 inFig. 8 represents a device for forming a frozen soil wall. - However, use of only the
continuous wall 22 fails to prevent diffusion of the contaminated ground water WG2 subjected to outflow (leakage) underground in a direction just below thereactor building 21 from the same. - As obviously shown in
Fig. 8 , this is because that the flow of the contaminated ground water WG22 running underground more deeply than thecontinuous wall 22 cannot be prevented. - An embodiment for solving the problem will be described with reference to
Figs. 9 and10 . - As shown in
Fig. 9 , according to the construction method of an embodiment shown inFigs. 1 to 7 , a layer of zeolite (LZ: a zeolite bottom slab) extending in a horizontal direction is formed in the ground G and below thereactor building 21. - The thickness B of the zeolite bottom slab LZ, while the ground water WG2contaminated with the radioactive material passes (transmits) the zeolite bottom slab LZ, is determined at a value so that cesium contained in the ground water WG2 can sufficiently be adsorbed by zeolite of the zeolite bottom slab LZ. The thickness depends on the degree of contamination and several working conditions.
- In addition, the range of the zeolite bottom slab LZ in a horizontal direction is determined so that passages for outflow and diffusion of the ground water WG2 contaminated with the radioactive material subjected to outflow (leakage) from the from
reactor building 21 can assuredly pass the zeolite bottom slab LZ. - When the zeolite bottom slab LZ shown in
Fig. 9 is formed, the ground water WG2 subjected to outflow (leakage) and diffusion underground in a direction just beneath thereactor building 21 from the same passes the zeolite bottom slab LZ to adsorb and remove cesium. This is because zeolite has a chemical property of adsorbing cesium as a main component of the radioactive material. Herein, since cesium is a major component of the radioactive material, and if cesium can be removed, the radioactive material concentration in the ground water WG2 is reduced to a safety value (or a standard value or less). - The ground water WG1 running upward from the zeolite bottom slab LZ is cut off by a
continuous wall 22, resulting in no diffusion. - In order to prevent diffusion of the contaminated ground water WG2, the
continuous wall 22 and the zeolite bottom slab LZ are connected to each other. - According to similar procedures of embodiments shown in
Figs. 1 to 7 ,Fig. 10 shows formation of the zeolite bottom slab LZ extending in a horizontal direction. - As shown in
Fig. 10 , a step of drilling a drilling hole H in the ground G and a step of moving (pulling up) ajet device 1 in a vertical direction by rotating the same while a fluid (a partition forming material) for cutting the ground G is injected from thejet device 1 are the same as those shown inFigs. 1 to 7 . - The
jet device 1 injects a jet flow J of the partition forming material to cut the ground G, and pulled up in an upward vertical direction by rotating the same. Like in the embodiments inFigs. 1 to 7 , a layer LD (a separation layer) of a mixture of the partition forming material and a cut soil is formed. - In a step shown in
Fig. 10 , zeolite is delivered underground from adischarge port 11 provided at a lower end of thejet device 1, in place of a solidification material according to embodiments shown inFigs. 1 to 7 . - Since the separation layer LD is placed in this process, the zeolite delivered does not mix with a stable liquid injected from discharge ports12 and a cut soil by a jet flow of a stable liquid to form a zeolite bottom slab LZ extending in a horizontal direction.
- In other words, by pulling up the
jet device 1 in a vertical direction by rotating the same on an axis thereof while the stable liquid is injected underground from thejet device 1 to cut and agitate the ground G, like in the embodiments shown inFigs. 1 to 7 , a layer LW of a mixture of the stable liquid and the cut soil and the layer LD (the separation layer) of a mixture of the partition forming material and the cut soil are formed. Thereafter, by delivering (injecting) zeolite underground from thejet device 1, a layer LZ of zeolite (a zeolite bottom slab) is formed. - Since the separation layer LD composed of the partition forming material is placed between the layer LW of a mixture of the stable liquid and the cut soil and the layer Lz of the zeolite (the zeolite bottom slab), mixture of the stable liquid of and the cut soil in the layer LW with the layer LZ of zeolite (the zeolite bottom slab) is reduced, thereby maintaining a separate situation.
- A step shown in
Fig. 10 is continued until the layer LZ of zeolite (the zeolite bottom slab) has a predetermined depth at a predetermined position (depth) in a vertical direction underground. - Across sectional shape of the layer LZ of zeolite (the zeolite bottom slab) (i.e. the range of the zeolite bottom slab LZ in a horizontal direction) is circular like in the embodiments shown in
Figs. 1 to 7 .However, the shape of the zeolite bottom slab LZ can be non-circular (e.g. a semicircle or a sector) in case contaminated water is diffused. -
- 1
- Jet device
- 2
- Slurry collecting structure
- 3
- Slurry carrying line
- 4
- Slurry treating structure
- 5
- Enzyme feed source
- 6
- Installing mechanism
- 7
- Partition forming material feed source
- 8
- Stable liquid feed source
- 9
- Solidification material feed source
- 10
- Change-over valve
- 11
- Discharge port
- 12
- Jetting port
- 13
- Solidification material introduction portion
- 14
- Stable liquid introduction portion and partition forming material introduction portion
- 15
- Inner pipe (jet device)
- 16
- Outer pipe (jet device)
- 17
- Pipe
- G
- Ground
- H
- Drilling hole
- LC
- Layer of solidification material
- LD
- Layer of partition forming material(separation layer)
- LW
- Layer of mixture of stable liquid and cut soil
- 21
- Reactor building
- 22
- Continuous wall
- WG1, WG2
- Contaminated ground water
- LZ
- Layer of zeolite (zeolite bottom slab)
Claims (2)
- A method for improving ground comprising:- a step of drilling a drilling hole (H) in a ground (G) to be improved;- a step of moving a jet device (1) in a vertical direction by rotating the same while the jet device (1) is inserted into the drilling hole (H) and a fluid for cutting the ground (G) is injected from the jet device (1); and- a step of injecting a solidification material from the jet device (1) from a discharge port (11) at a lower end of the jet device, characterised in that said step of moving the jet device (1) in a vertical direction by rotating the same while the fluid for cutting the ground (G) is injected from the jet device (1) comprises the steps of:o cutting the ground (G) by injecting a partition forming material from a plurality of jetting ports (12) at a portion which is vertically higher than the lower end portion of the jet device (1); ando after having cut the ground by injecting the partition forming material, injecting the solidification material from the discharge port (11)while the ground (G) is cut by injecting a stable liquid from the plurality of jetting ports (12), and in that the solidification material is a rich-mixed solidification material comprising a cement and having a ratio of water to cement in the range of 26% to 40%.
- The method according to claim 1, wherein the method for improving ground further comprises- a step of collecting a mixture of the stable liquid discharged above the ground (G) and a cut soil by a slurry collecting structure (2); and- a step of carrying the slurry collected by the slurry collecting structure (2) to a slurry treating structure (4) and adding a decomposition enzyme from an enzyme feed source.
Applications Claiming Priority (3)
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JP2014109733 | 2014-05-28 | ||
JP2014166456A JP6415897B2 (en) | 2014-05-28 | 2014-08-19 | Ground improvement method |
PCT/JP2015/065174 WO2015182635A1 (en) | 2014-05-28 | 2015-05-27 | Ground improvement method |
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EP3165678A1 EP3165678A1 (en) | 2017-05-10 |
EP3165678A4 EP3165678A4 (en) | 2017-11-15 |
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EP (1) | EP3165678B1 (en) |
JP (1) | JP6415897B2 (en) |
AU (1) | AU2015266559B2 (en) |
CA (1) | CA2950562C (en) |
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WO (1) | WO2015182635A1 (en) |
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GB2537317B (en) * | 2014-04-07 | 2020-02-12 | Halliburton Energy Services Inc | Soil and rock grouting using a hydrajetting tool |
CN108519477B (en) * | 2018-04-24 | 2023-10-13 | 西南科技大学 | Seasonal frozen soil area roadbed model test system |
CN110284487B (en) * | 2019-06-04 | 2020-11-27 | 东南大学 | Method for treating collapsible loess foundation by vibrating rod compacting method |
CN111410465B (en) * | 2020-04-26 | 2020-11-24 | 四川颐千石油工程有限公司 | Environment-friendly water-based rock debris curing agent and application thereof |
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JPS56125530A (en) * | 1980-03-06 | 1981-10-01 | Kubota Ltd | Driving of pile |
US5141366A (en) * | 1989-10-04 | 1992-08-25 | Nitto Chemical Industry Co., Ltd. | Method of improving ground and apparatus used therefor |
US20150132824A1 (en) * | 2012-05-07 | 2015-05-14 | Novozymes A/S | Polypeptides Having Xanthan Degrading Activity and Polynucleotides Encoding Same |
Family Cites Families (6)
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DE3737259C1 (en) * | 1987-11-03 | 1989-03-16 | Bauer Spezialtiefbau | Apparatus and method for high-pressure injection |
JP2000290991A (en) * | 1999-04-02 | 2000-10-17 | Nit Co Ltd | Soil improvement method |
JP2001232344A (en) * | 2000-02-23 | 2001-08-28 | Kurita Water Ind Ltd | Method for forming sand layer in contaminated soil and treating method of contaminated soil |
DE10154201A1 (en) * | 2001-11-07 | 2003-05-22 | Frank Otto | Underground foundation procedure mixes suspension of fiber aggregates and binder for injection into ground already worked out by cutting fluid jets. |
JP2004195387A (en) * | 2002-12-19 | 2004-07-15 | Toko Corp | Soil purification method and hardening material used for it |
JP3964904B2 (en) * | 2004-11-11 | 2007-08-22 | 栄興産業株式会社 | Jet stirring method and jet stirring device |
-
2014
- 2014-08-19 JP JP2014166456A patent/JP6415897B2/en active Active
-
2015
- 2015-05-27 EP EP15799627.3A patent/EP3165678B1/en active Active
- 2015-05-27 WO PCT/JP2015/065174 patent/WO2015182635A1/en active Application Filing
- 2015-05-27 US US15/314,145 patent/US20170204580A1/en not_active Abandoned
- 2015-05-27 CA CA2950562A patent/CA2950562C/en active Active
- 2015-05-27 AU AU2015266559A patent/AU2015266559B2/en active Active
- 2015-05-27 SG SG11201609037UA patent/SG11201609037UA/en unknown
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56125530A (en) * | 1980-03-06 | 1981-10-01 | Kubota Ltd | Driving of pile |
US5141366A (en) * | 1989-10-04 | 1992-08-25 | Nitto Chemical Industry Co., Ltd. | Method of improving ground and apparatus used therefor |
US20150132824A1 (en) * | 2012-05-07 | 2015-05-14 | Novozymes A/S | Polypeptides Having Xanthan Degrading Activity and Polynucleotides Encoding Same |
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JP2016006270A (en) | 2016-01-14 |
JP6415897B2 (en) | 2018-10-31 |
EP3165678A1 (en) | 2017-05-10 |
SG11201609037UA (en) | 2016-12-29 |
AU2015266559A1 (en) | 2016-12-15 |
CA2950562A1 (en) | 2015-12-03 |
AU2015266559A8 (en) | 2017-01-05 |
WO2015182635A1 (en) | 2015-12-03 |
EP3165678A4 (en) | 2017-11-15 |
US20170204580A1 (en) | 2017-07-20 |
CA2950562C (en) | 2019-12-31 |
AU2015266559B2 (en) | 2019-05-02 |
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