JP2023021209A - Cyclone device - Google Patents

Cyclone device Download PDF

Info

Publication number
JP2023021209A
JP2023021209A JP2022166971A JP2022166971A JP2023021209A JP 2023021209 A JP2023021209 A JP 2023021209A JP 2022166971 A JP2022166971 A JP 2022166971A JP 2022166971 A JP2022166971 A JP 2022166971A JP 2023021209 A JP2023021209 A JP 2023021209A
Authority
JP
Japan
Prior art keywords
sand
specific gravity
liquid
stable liquid
sand content
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2022166971A
Other languages
Japanese (ja)
Inventor
康晴 和知
Yasuharu Wachi
智貴 森下
Tomoki Morishita
俊彦 三浦
Toshihiko Miura
和哲 吉本
Kazunori Yoshimoto
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Obayashi Corp
Original Assignee
Obayashi Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Obayashi Corp filed Critical Obayashi Corp
Priority to JP2022166971A priority Critical patent/JP2023021209A/en
Publication of JP2023021209A publication Critical patent/JP2023021209A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E30/00Energy generation of nuclear origin
    • Y02E30/30Nuclear fission reactors

Abstract

PROBLEM TO BE SOLVED: To provide a cyclone device that separates sand contained in a stabilization solution for efficiently measuring a percentage of sand contained in the stabilization solution for evaluation.
SOLUTION: An evaluating device 20 comprises a first specific gravity measuring part 21, a second specific gravity measuring part 22, and a control part 31. The first specific gravity measuring part 21 measures a first measurement value which is a specific gravity of a stabilization solution supplied to a cyclone device 25 which removes sand contained in the stabilization solution. The second specific gravity measuring part 22 measures a second measurement value which is a specific gravity of the stabilization solution having the sand ejected from the cyclone device 25 removed therefrom. The control part 31 calculates a percentage of sand in the stabilization solution, from a value based on a result of comparison between the first measurement value and the second measurement value.
SELECTED DRAWING: Figure 1
COPYRIGHT: (C)2023,JPO&INPIT

Description

本発明は、場所打ちのコンクリート杭や地中連続壁の工事等で使われる安定液中に含まれる砂分を分離するサイクロン装置に関する。 TECHNICAL FIELD The present invention relates to a cyclone device for separating sand contained in a stabilizing liquid used in the construction of cast-in-place concrete piles and diaphragm walls.

掘削した孔の孔壁崩壊防止のために安定液(ベントナイト泥水)が用いられる。この安定液の性状は、孔内に構築する杭体コンクリートの品質に影響することがあるため、安定液の性状を測定している。一般に、安定液の粘度、比重及び砂分率は、ファンネル粘度計、マッドバランス及び砂分計をそれぞれ用いて計測される。更に、安定液の性状を定期的に測定する技術もある(例えば、特許文献1参照。)。この文献に記載の泥水の性状測定方法では、安定液の比重、粘度及び砂分率を計測する。この場合、砂分率は、泥水測定容器から流出させた泥水に含まれる砂分を分級し、分級した砂分の重量を測定する。 A stabilizing liquid (bentonite mud) is used to prevent collapse of the wall of the drilled hole. Since the properties of the stabilizing liquid may affect the quality of the pile concrete built in the hole, the properties of the stabilizing liquid are measured. Generally, the viscosity, specific gravity and sand content of the stable liquid are measured using a funnel viscometer, mud balance and sand content meter respectively. Furthermore, there is also a technique for periodically measuring properties of a stable liquid (see, for example, Patent Document 1). In the method for measuring properties of muddy water described in this document, the specific gravity, viscosity and sand content of the stable liquid are measured. In this case, the sand content is determined by classifying the sand contained in the muddy water discharged from the muddy water measuring container and measuring the weight of the classified sand.

特開平8-35924号公報JP-A-8-35924

しかしながら、砂分率等の安定液の性状を測定するには、何れも、時間と手間が掛かっていた。 However, it takes time and effort to measure the properties of the stable liquid such as the sand content.

上記課題を解決するサイクロン装置は、安定液中に含まれる砂分を分離するサイクロン装置であって、孔の内部に充填された前記安定液が流れる供給管が接続され、前記供給管を介して供給された前記安定液から分離した砂分を下方から排出し、上部に接続された排出管を介して、前記砂分を分離して除去した安定液を排出し、前記安定液において除去対象となる砂粒子の直径及び前記安定液の粘度に応じて、周速度及び前記安定液の流入速度を調整する。 A cyclone device that solves the above problems is a cyclone device that separates sand contained in a stabilizing liquid, wherein a supply pipe through which the stabilizing liquid filled inside the hole is connected is connected, and through the supply pipe, The sand separated from the supplied stabilizing liquid is discharged from below, and the stabilizing liquid from which the sand is separated and removed is discharged through the discharge pipe connected to the upper part, and the stabilizing liquid to be removed is discharged. The peripheral speed and the inflow speed of the stabilizing liquid are adjusted according to the diameter of the sand particles and the viscosity of the stabilizing liquid.

本発明によれば、安定液の砂分率を効率的に計測して安定液の性状を評価することができる。 ADVANTAGE OF THE INVENTION According to this invention, the sand content rate of a stable liquid can be measured efficiently and the property of a stable liquid can be evaluated.

実施形態における評価装置のシステム構成を説明する説明図。Explanatory drawing explaining the system configuration|structure of the evaluation apparatus in embodiment. 実施形態における比重差を説明する説明図であって、(a)は従来用いられていた砂分計を示し、(b)は、空気、水及び土粒子の関係を説明する説明図。BRIEF DESCRIPTION OF THE DRAWINGS It is explanatory drawing explaining the specific gravity difference in embodiment, Comprising: (a) shows the sand content meter currently used, (b) is explanatory drawing explaining the relationship between air, water, and a soil particle. 実施形態における従来法による砂分率と換算砂分との関係を説明する説明図であって、(a)は各安定液の計測値、(b)は(a)の数値を示したグラフ。FIG. 4 is an explanatory diagram for explaining the relationship between the sand content and the equivalent sand content according to the conventional method in the embodiment, where (a) is a measured value of each stable liquid and (b) is a graph showing the numerical value of (a).

以下、図1~図3を用いて、サイクロン装置を具体化した一実施形態を説明する。ここでは、杭孔から排出して回収する安定液の砂分率等の性状を計測して評価する。 An embodiment of a cyclone device will be described below with reference to FIGS. 1 to 3. FIG. Here, properties such as the sand content of the stable liquid discharged from the pile hole and collected are measured and evaluated.

図1に示すように、掘削された杭孔10の内部は、安定液11で充填される。杭孔10の底部に、ポンプ15を配置する。このポンプ15には、回収管16が接続される。ポンプ15を駆動させて、回収管16から安定液11を杭孔10の外部に排出する。回収管16は、プラント17に接続される。プラント17は、安定液の砂分を沈降させて除去する複数の水槽を備える。そして、プラント17は、回収した安定液の砂分を各水槽において沈殿させ、砂分を除去した良好な安定液を、杭孔10に供給する。これにより、杭孔10内の安定液を、良好な安定液と置換する。 As shown in FIG. 1 , the inside of the excavated pile hole 10 is filled with a stabilizing liquid 11 . A pump 15 is arranged at the bottom of the pile hole 10 . A recovery pipe 16 is connected to the pump 15 . The pump 15 is driven to discharge the stabilizing liquid 11 from the recovery pipe 16 to the outside of the pile hole 10 . Recovery pipe 16 is connected to plant 17 . The plant 17 comprises a plurality of water tanks for settling and removing sand from the stabilizing liquid. Then, the plant 17 causes sand in the recovered stable liquid to settle in each water tank, and supplies a good stable liquid from which the sand is removed to the pile hole 10 . This replaces the stabilizing liquid in the stake hole 10 with a good stabilizing liquid.

回収管16には、バルブ(図示せず)を介して供給管18が分岐により接続される。この供給管18は、評価装置20に接続され、回収管16を流れる安定液の一部を評価装置20に供給する。ここでは、回収管16を流れる流量に対して、安定液の1/5~1/30程度の量を供給管18に供給する。本実施形態では、供給管18に流す量を、回収管16を流れる安定液の1/15程度に設定する。 A supply pipe 18 is branched and connected to the recovery pipe 16 via a valve (not shown). This supply pipe 18 is connected to the evaluation device 20 and supplies part of the stabilizing liquid flowing through the recovery pipe 16 to the evaluation device 20 . Here, the supply pipe 18 is supplied with an amount of about 1/5 to 1/30 of the stabilizing liquid with respect to the flow rate flowing through the recovery pipe 16 . In this embodiment, the amount of the stable liquid flowing through the supply pipe 18 is set to about 1/15 of the amount of the stable liquid flowing through the recovery pipe 16 .

評価装置20は、第1比重計測部21、第2比重計測部22、泥水槽23、サイクロン装置25及び粘度計測部26を備える。第1比重計測部21、第2比重計測部22及び粘度計測部26にそれぞれに供給された安定液は、泥水槽23に蓄積後、プラント17に供給される。 The evaluation device 20 includes a first specific gravity measuring section 21 , a second specific gravity measuring section 22 , a mud tank 23 , a cyclone device 25 and a viscosity measuring section 26 . The stable liquids supplied to the first specific gravity measuring unit 21 , the second specific gravity measuring unit 22 and the viscosity measuring unit 26 are accumulated in the mud tank 23 and then supplied to the plant 17 .

評価装置20において、供給管18は、砂分除去装置としてのサイクロン装置25に接続される。更に、供給管18の分岐管が、バルブ21vを介して、第1比重計測部21に接続される。この第1比重計測部21は、供給管18を流れる安定液の比重(第1計測値)を測定する。第1比重計測部21は、上面が開口した一定容量の円筒形状の容器21cと、容器21c内の安定液の重量を計測する圧力計21aとを備える。 In the evaluation device 20, the supply pipe 18 is connected to a cyclone device 25 as a sand removing device. Further, a branch pipe of the supply pipe 18 is connected to the first specific gravity measuring section 21 via a valve 21v. The first specific gravity measuring unit 21 measures the specific gravity (first measured value) of the stable liquid flowing through the supply pipe 18 . The first specific gravity measuring unit 21 includes a cylindrical container 21c with an open upper surface and a constant capacity, and a pressure gauge 21a for measuring the weight of the stable liquid in the container 21c.

容器21cの下端には分岐管が接続され、容器21cには下方から安定液が供給される。この供給によって容器21c内部の安定液が上方に流れ、容器21cの上開口から溢れる。更に、第1比重計測部21の容器21cの下方には、バルブを介して、必要に応じて容器21c内部の安定液を排出するためのドレーン管21dが設けられる。 A branch pipe is connected to the lower end of the container 21c, and the stabilizing liquid is supplied to the container 21c from below. By this supply, the stabilizing liquid inside the container 21c flows upward and overflows from the upper opening of the container 21c. Further, below the container 21c of the first specific gravity measuring unit 21, a drain pipe 21d is provided via a valve for discharging the stable liquid inside the container 21c as required.

圧力計21aは、容器21cにおいて上面から所定距離(例えば1m)低い位置(取付位置)に取り付けられる。そして、圧力計21aは、取付位置から上方にある容器21c内の安定液の重量(圧力)を計測し、その計測値を、安定液の比重として管理ユニット30に送信する。 The pressure gauge 21a is mounted at a position (mounting position) a predetermined distance (for example, 1 m) below the upper surface of the container 21c. The pressure gauge 21a measures the weight (pressure) of the stable liquid in the container 21c above the mounting position, and transmits the measured value to the management unit 30 as the specific gravity of the stable liquid.

また、供給管18の分岐管は、粘度計測部26に接続される。この粘度計測部26は、供給管18を流れる安定液の粘度を計測する。本実施形態では、この粘度計測部26として振動式粘度計を用いる。 A branch pipe of the supply pipe 18 is connected to the viscosity measuring section 26 . This viscosity measuring unit 26 measures the viscosity of the stable liquid flowing through the supply pipe 18 . In this embodiment, a vibrating viscometer is used as the viscosity measuring unit 26 .

供給管18に接続されるサイクロン装置25は、安定液中に含まれる砂分(0.075mm以上の粒径の土粒子)を分離する遠心分離器である。このサイクロン装置25は、供給管18を流れる安定液から分離した砂分を、下方から排出する。また、サイクロン装置25は、砂分を分離した安定液を、上部に接続した排出管28を介して、泥水槽23に排出する。このサイクロン装置25の詳細は、後述する。 A cyclone device 25 connected to the supply pipe 18 is a centrifugal separator that separates sand (soil particles having a particle size of 0.075 mm or more) contained in the stable liquid. The cyclone device 25 discharges sand separated from the stable liquid flowing through the supply pipe 18 from below. The cyclone device 25 also discharges the stable liquid from which the sand is separated to the mud tank 23 through the discharge pipe 28 connected to the upper part. Details of the cyclone device 25 will be described later.

排出管28の分岐管は、バルブを介して第2比重計測部22に接続される。第2比重計測部22は、排出管28を流れる安定液の比重を測定する。ここでは、第2比重計測部22は、第1比重計測部21と同じ構成である。この第2比重計測部22も、一定容量の円筒形状の容器22cと、容器22c内の安定液の重量(圧力)を計測する圧力計22aを備える。更に、第2比重計測部22の容器22cの下方には、バルブを介して、ドレーン管22dが設けられる。 A branch pipe of the discharge pipe 28 is connected to the second specific gravity measuring section 22 via a valve. The second specific gravity measuring section 22 measures the specific gravity of the stable liquid flowing through the discharge pipe 28 . Here, the second specific gravity measuring section 22 has the same configuration as the first specific gravity measuring section 21 . The second specific gravity measuring unit 22 also includes a cylindrical container 22c having a constant capacity and a pressure gauge 22a for measuring the weight (pressure) of the stable liquid in the container 22c. Furthermore, below the container 22c of the second specific gravity measuring unit 22, a drain pipe 22d is provided via a valve.

更に、評価装置20は、管理ユニット30を備える。管理ユニット30は、第1比重計測部21、第2比重計測部22及び粘度計測部26に接続され、これらが計測した計測値を取得する。 Furthermore, the evaluation device 20 comprises a management unit 30 . The management unit 30 is connected to the first specific gravity measuring section 21, the second specific gravity measuring section 22, and the viscosity measuring section 26, and acquires the measured values measured by these.

管理ユニット30は、制御部31及び表示部32を備える。
制御部31は、安定液に含まれる砂分率を算出する。砂分率は、泥水(安定液)中に存在する砂の容積の割合である。制御部31は、第1比重計測部21により計測した比重(第1計測値)及び第2比重計測部22により計測した比重(第2計測値)を取得する。そして、制御部31は、第1計測値及び第2計測値と、予め記憶している砂分算出式(後述する(2)式)とを用いて砂分率を算出する。この砂分率の算出の詳細は後述する。そして、制御部31は、算出した砂分率、計測した安定液の比重(第1計測値)、粘度計測部26から取得した粘度を、メモリに記憶する。
The management unit 30 has a control section 31 and a display section 32 .
The control unit 31 calculates the sand content rate contained in the stable liquid. The sand content is the volumetric ratio of sand present in the muddy water (stabilized liquid). The control unit 31 acquires the specific gravity (first measured value) measured by the first specific gravity measuring unit 21 and the specific gravity (second measured value) measured by the second specific gravity measuring unit 22 . Then, the control unit 31 calculates the sand content rate using the first measured value, the second measured value, and a pre-stored sand content calculation formula (formula (2) described later). Details of the calculation of the sand content will be described later. Then, the control unit 31 stores the calculated sand content, the measured specific gravity of the stable liquid (first measured value), and the viscosity acquired from the viscosity measuring unit 26 in the memory.

更に、管理ユニット30は、第1比重計測部21及び第2比重計測部22のバルブ21v,22v、ドレーン管21d,22dのバルブの開閉制御を行なう。
表示部32は、安定液の比重、粘度、砂分率を表示するディスプレイである。
Furthermore, the management unit 30 controls the opening and closing of the valves 21v and 22v of the first specific gravity measuring section 21 and the second specific gravity measuring section 22 and the valves of the drain pipes 21d and 22d.
The display unit 32 is a display that displays the specific gravity, viscosity, and sand content of the stable liquid.

<サイクロン装置25>
次に、砂分を除去するサイクロン装置25の詳細について説明する。
ここで、砂分を分離するためには、サイクロン装置25の有効径と、安定液のサイクロン装置25の滞留時間とから算出する砂の沈降速度を考慮する。
サイクロン装置25における砂の沈降速度(V)は、ストークスの式(以下の(1)式)で示される。
V=(ρs-ρw)gD/18μ=(ρs-ρw)Vt/18μr…(1)
<Cyclone device 25>
Next, details of the cyclone device 25 for removing sand will be described.
Here, in order to separate the sand, the sedimentation velocity of sand calculated from the effective diameter of the cyclone device 25 and the retention time of the stable liquid in the cyclone device 25 is considered.
The sedimentation velocity (V) of sand in the cyclone device 25 is expressed by the Stokes equation (equation (1) below).
V= ( ρs-ρw) gD2 /18μ=(ρs-ρw) Vt2D2 /18μr (1)

ここで、ρsは砂の密度(2.65×103kg/m)、ρwは水の密度(1.00×103kg/m3)、gは重力加速度(9.807m/s2)、μは泥水の粘度(Pa・s)、Dは砂粒子の直径(m)、rは遠心場の半径(m)、Vtは周速度(m/s)である。
上述した(1)式に示したように、砂の沈降速度は、除去対象となる砂粒子の直径、周速度及び粘度の影響を受ける。
where ρs is sand density (2.65×10 3 kg/m 3 ), ρw is water density (1.00×10 3 kg/m 3 ), g is gravitational acceleration (9.807 m/s 2 ), μ is muddy water is the viscosity (Pa·s), D is the diameter of the sand particle (m), r is the radius of the centrifugal field (m), and Vt is the circumferential velocity (m/s).
As shown in the above formula (1), the sedimentation speed of sand is affected by the diameter, peripheral speed and viscosity of sand particles to be removed.

砂の粒径は0.075mm~2mmである。本実施形態では、実際の現場で発生する土砂の性状を考慮して、サイクロン装置25は、安定液中に含まれる砂の粒径を除去できるように設定する。また、杭孔10内の安定液を置換する作業中において、安定液の粘度の変動分を考慮し、サイクロン装置25の周速度を調整する。この周速度は、サイクロン装置25の直径(形状)やサイクロン装置25の流速で決まるため、安定液の速度(流入速度)により調整する。なお、泥水の粘度が更に増加することが考えられる場合には、サイクロン装置25の周速度を更に高くする。 The grain size of sand is 0.075 mm to 2 mm. In the present embodiment, the cyclone device 25 is set so as to be able to remove the particle size of sand contained in the stabilizing liquid, taking into consideration the properties of earth and sand generated at the actual site. Also, during the work of replacing the stabilizing liquid in the pile hole 10, the peripheral speed of the cyclone device 25 is adjusted in consideration of the variation in the viscosity of the stabilizing liquid. Since this peripheral velocity is determined by the diameter (shape) of the cyclone device 25 and the flow velocity of the cyclone device 25, it is adjusted by the velocity (inflow velocity) of the stable liquid. If the viscosity of the muddy water is expected to further increase, the peripheral speed of the cyclone device 25 is further increased.

<砂分率の算出方法>
次に、図2及び図3を用いて、制御部31が実行する砂分率の算出方法について説明する。ここで、本実施形態の算出方法を用いて算出した砂分率(%)を換算砂分と称する。
本実施形態の制御部31は、次の(2)式により換算砂分x(%)を算出する。
x=140×(ρi-ρf)/(2.65-ρf)…(2)
ここで、ρi,ρfは、それぞれ、サイクロン装置25を通過する前の安定液の比重(第1計測値)、通過後の安定液の比重(第2計測値)である。この換算砂分の算出は、比重差が主として砂分に起因するものとして、比重差と砂分の損失の差とから求められる。
<Method for calculating sand content>
Next, a method for calculating the sand content ratio executed by the control unit 31 will be described with reference to FIGS. 2 and 3. FIG. Here, the sand content (%) calculated using the calculation method of the present embodiment is referred to as equivalent sand content.
The control unit 31 of this embodiment calculates the equivalent sand content x (%) by the following equation (2).
x = 140 x (ρi - ρf) / (2.65 - ρf) (2)
Here, ρi and ρf are the specific gravity of the stable liquid before passing through the cyclone device 25 (first measured value) and the specific gravity of the stable liquid after passing through (second measured value), respectively. The equivalent sand content is calculated from the difference in specific gravity and the difference in loss of sand content, assuming that the difference in specific gravity is mainly due to sand content.

具体的には、図2(a)を用いて、砂分計50を用いた従来法による砂分率の計測方法について説明する。この砂分計50では、これに入れた100mLの安定液を用いる。砂分計50は、この中の75μm以下の粒子をフルイで取り除いて水で洗浄し、水51中に残存した砂(75μm以上の土粒子)の積層容積を測定することにより、砂分率を取得する。例えば、砂分率が5%とは、砂分計50に入れた100mLの安定液中に5mLの砂が含まれることを示している。 Specifically, referring to FIG. 2(a), a conventional sand content measurement method using a sand meter 50 will be described. The sand meter 50 uses 100 mL of stabilizing liquid in it. The sand meter 50 removes particles of 75 μm or less in this with a sieve and washes them with water, and measures the lamination volume of the sand (soil particles of 75 μm or more) remaining in the water 51 to determine the sand fraction. get. For example, a sand content of 5% means that 100 mL of the stable liquid contained in the sand meter 50 contains 5 mL of sand.

安定液100mL当りのサイクロン装置25を通過する前後の比重差による質量差は、次の通りに示される。
比重差による質量差=100×(ρi-ρf)…(3)
The mass difference due to the difference in specific gravity before and after passing through the cyclone device 25 per 100 mL of the stable liquid is shown as follows.
Mass difference due to specific gravity difference = 100 x (ρi - ρf) (3)

ここで、図2(b)の土(砂)の構成図に示すように、空気、水及び土粒子の体積を、それぞれVa,Vw,Vsとし、空気と水の合計の体積をVv,空気と水と土粒子の合計の体積をVとする。
そして、サイクロン装置25を通過する前後の砂分の損失による質量差は、砂分計50の砂が堆積する部分の砂52の間隙率をn(=Vv/V×100)、砂の密度をρs(=2.65g/cm)とすると、次の通りに示される。
砂分の損失による質量差=(ρs-ρf)×x×(1-n/100)…(4)
Here, as shown in the configuration diagram of soil (sand) in FIG. Let V be the total volume of water and soil particles.
The difference in mass due to the loss of sand before and after passing through the cyclone device 25 is expressed by n (=Vv/V×100) as the porosity of the sand 52 in the portion where the sand accumulates in the sand meter 50, and as the density of the sand. ρs (=2.65 g/cm 3 ) is shown as follows.
Mass difference due to sand loss = (ρs - ρf) x x x (1 - n/100) (4)

サイクロン装置25を通過した前後の比重による質量差と、砂分の損失による質量差は(概ね)等しいので、上記(3)式及び(4)式から、次式が得られる。
100×(ρi-ρf)=(ρs-ρf)×x×(1-n/100)…(5)
Since the difference in mass due to specific gravity before and after passing through the cyclone device 25 is (generally) equal to the difference in mass due to loss of sand content, the following equation is obtained from equations (3) and (4) above.
100×(ρi−ρf)=(ρs−ρf)×x×(1−n/100)…(5)

この(5)式を、換算砂分xについて変形すると、次式が得られる。
x=100(ρi-ρf)/((ρs-ρf)×(1-n/100))…(6)
The following equation is obtained by transforming this equation (5) with respect to the equivalent sand content x.
x=100(ρi-ρf)/((ρs-ρf)×(1-n/100))…(6)

ここで、評価装置20の特質と、砂52の間隙比を考慮した係数をαとすると、換算砂分xの値は、次式で表される。この係数αは、評価装置20の使用条件ごとに個別に設定可能である。
x=α×(ρi-ρf)/(ρs-ρf)
今回は、実験時の測定値の相関から、α=140とし、また、砂の比重を2.65として、次式で換算した。
x=140×(ρi-ρf)/(2.65-ρf)
Here, the value of the equivalent sand content x is expressed by the following equation, where α is a coefficient that takes into consideration the characteristics of the evaluation device 20 and the void ratio of the sand 52 . This coefficient α can be set individually for each usage condition of the evaluation device 20 .
x=α×(ρi−ρf)/(ρs−ρf)
This time, from the correlation of the measured values at the time of the experiment, α = 140 and the specific gravity of sand is 2.65, and converted by the following formula.
x = 140 x (ρi - ρf) / (2.65 - ρf)

<従来法による砂分率と換算砂分との関係>
図3(a)には、異なる性状の安定液について、砂分計50で計測した(従来法による)砂分率と、本発明の換算砂分とを示している。更に、図3(b)には、従来法よる砂分率の値を横軸に取り、換算砂分を縦軸に取ったグラフを示す。これによれば、従来法による砂分率と換算砂分とがほぼ対応し、換算砂分が従来法とほぼ同じ精度であることを示している。
<Relationship between sand content and equivalent sand content according to the conventional method>
FIG. 3(a) shows the sand content measured by the sand meter 50 (according to the conventional method) and the equivalent sand content of the present invention for stable liquids having different properties. Further, FIG. 3(b) shows a graph in which the value of the sand content by the conventional method is plotted on the horizontal axis and the converted sand content is plotted on the vertical axis. According to this, the sand content ratio and the equivalent sand content obtained by the conventional method almost correspond to each other, indicating that the equivalent sand content has almost the same accuracy as the conventional method.

<評価装置20の計測処理>
次に、図1に示した評価装置20における計測処理について説明する。
まず、杭孔10に配置されたポンプ15を駆動して、杭孔10の安定液を、回収管16を介して、プラント17に排出する。更に、プラント17において、調整された安定液を杭孔10に供給する。
<Measurement processing of the evaluation device 20>
Next, measurement processing in the evaluation device 20 shown in FIG. 1 will be described.
First, the pump 15 arranged in the pile hole 10 is driven to discharge the stable liquid in the pile hole 10 to the plant 17 through the recovery pipe 16 . Furthermore, in the plant 17 a conditioned stabilizing liquid is supplied to the pile hole 10 .

ここで、回収管16の安定液の一部は、供給管18を介して、評価装置20のサイクロン装置25に供給される。この場合、バルブ21vが開いているので、供給管18から第1比重計測部21に安定液を供給する。本実施形態では、評価装置20を流れる安定液の流量の一部(例えば、30%以下)が第1比重計測部21に流れるように調整する。この安定液は、第1比重計測部21の容器21cの下方から供給され、容器21c内の安定液を上へと流して、容器21cの上からオーバーフローさせる。第1比重計測部21の圧力計21aは、定期的に(例えば、5秒毎に)容器21c中の安定液の圧力(比重)を計測する。圧力計21aは、計測した安定液の測定値(第1計測値)を管理ユニット30に送信する。 Here, part of the stabilizing liquid in the recovery pipe 16 is supplied to the cyclone device 25 of the evaluation device 20 via the supply pipe 18 . In this case, since the valve 21v is open, the stable liquid is supplied from the supply pipe 18 to the first specific gravity measuring section 21 . In the present embodiment, adjustment is made so that a portion (for example, 30% or less) of the flow rate of the stabilizing liquid flowing through the evaluation device 20 flows to the first specific gravity measuring section 21 . This stabilizing liquid is supplied from the bottom of the container 21c of the first specific gravity measuring unit 21, and causes the stabilizing liquid in the container 21c to flow upward and overflow the container 21c. The pressure gauge 21a of the first specific gravity measuring unit 21 periodically (for example, every 5 seconds) measures the pressure (specific gravity) of the stable liquid in the container 21c. The pressure gauge 21 a transmits the measured value (first measured value) of the stable liquid to the management unit 30 .

更に、供給管18の分岐管を介して、安定液は粘度計測部26に供給される。粘度計測部26は、安定液の粘度を、定期的に(例えば、5秒毎に)計測し、計測した測定値(粘度)を管理ユニット30に送信する。 Furthermore, the stabilizing liquid is supplied to the viscosity measuring section 26 via the branch pipe of the supply pipe 18 . The viscosity measurement unit 26 measures the viscosity of the stable liquid periodically (for example, every 5 seconds) and transmits the measured value (viscosity) to the management unit 30 .

また、サイクロン装置25で砂分が除去された安定液は、排出管28を介して泥水槽23に排出される。この場合、バルブ22vを開いて、排出管28の安定液を第2比重計測部22に供給する。本実施形態では、第1比重計測部21とほぼ同じ流量の安定液が、第2比重計測部22に流れるように調整する。この安定液は、第2比重計測部22の容器22cの下方から徐々に供給されるので、容器22c内の安定液は上へとゆっくり流れ、容器22cの上からオーバーフローする。第2比重計測部22の圧力計22aは、定期的(例えば、5秒毎)に容器22c中の安定液の圧力(比重)を計測し、計測した安定液の測定値(第2計測値)を管理ユニット30に供給する。 Also, the stable liquid from which sand has been removed by the cyclone device 25 is discharged to the mud tank 23 through the discharge pipe 28 . In this case, the valve 22 v is opened to supply the stable liquid in the discharge pipe 28 to the second specific gravity measuring section 22 . In the present embodiment, adjustment is made so that the stable liquid flows to the second specific gravity measuring section 22 at substantially the same flow rate as the first specific gravity measuring section 21 . Since this stabilizing liquid is gradually supplied from below the container 22c of the second specific gravity measuring unit 22, the stabilizing liquid in the container 22c slowly flows upward and overflows from the top of the container 22c. The pressure gauge 22a of the second specific gravity measuring unit 22 periodically (for example, every 5 seconds) measures the pressure (specific gravity) of the stable liquid in the container 22c, and measures the measured value of the stable liquid (second measured value). to the management unit 30 .

管理ユニット30の制御部31は、取得した第1計測値及び第2計測値と砂分算出式とを用いて、砂分率を算出する。制御部31は、算出した砂分率と、同時期に取得した安定液の比重(第1計測値)及び粘度とを関連付けて、内蔵するメモリに記憶する。そして、管理ユニット30の制御部31は、安定液に関する情報(砂分率、比重及び粘度)を表示部32に表示する。管理者は、表示部32に表示された計測値(安定液の砂分率等)を監視する。 The control unit 31 of the management unit 30 calculates the sand content rate using the obtained first measured value and second measured value and the sand content calculation formula. The control unit 31 associates the calculated sand content with the specific gravity (first measured value) and viscosity of the stable liquid obtained at the same time, and stores them in the built-in memory. Then, the control section 31 of the management unit 30 displays information (sand fraction, specific gravity and viscosity) on the stable liquid on the display section 32 . The administrator monitors the measured values (such as the sand content of the stable liquid) displayed on the display unit 32 .

また、管理ユニット30は、定期的に(例えば、30分毎に)、バルブ21v,22vを閉じて、ドレーン管21d,22dのバルブを開く。これにより、第1及び第2比重計測部(21,22)の容器(21c,22c)の下端から、容器21c,22c内の安定液が排出される。所定時間(例えば数秒)の経過後、ドレーン管21d,22dのバルブを閉じ、かつバルブ21v,22vを開いて、第1及び第2比重計測部(21,22)の容器(21c,22c)を安定液で満たした後、安定液の比重を再び計測する。これにより、一定時間間隔で、評価装置20のキャリブレーションが行なわれる。 Also, the management unit 30 periodically (for example, every 30 minutes) closes the valves 21v and 22v and opens the valves of the drain pipes 21d and 22d. As a result, the stable liquid in the containers 21c, 22c is discharged from the lower ends of the containers (21c, 22c) of the first and second specific gravity measuring units (21, 22). After a predetermined time (for example, several seconds) has passed, the valves of the drain pipes 21d and 22d are closed, the valves 21v and 22v are opened, and the containers (21c and 22c) of the first and second specific gravity measuring units (21 and 22) are After filling with the stabilizing liquid, the specific gravity of the stabilizing liquid is measured again. As a result, the evaluation device 20 is calibrated at regular time intervals.

<具体例>
ここでは、回収液の砂分率について説明する。
例えば、第1比重計測部21の測定値(第1計測値)と第2比重計測部22の測定値(第2計測値)が、以下の表1に示す値であったと仮定する。この場合、換算砂分は、判定値(1.0%)以上であるため、安定液の置換作業を継続する。そして、換算砂分が判定値より小さくなった場合に、安定液の置換作業を停止する。
<Specific example>
Here, the sand content of the recovered liquid will be explained.
For example, assume that the measured value (first measured value) of the first specific gravity measuring unit 21 and the measured value (second measured value) of the second specific gravity measuring unit 22 are the values shown in Table 1 below. In this case, the converted sand content is equal to or higher than the judgment value (1.0%), so the work of replacing the stabilizing solution is continued. Then, when the converted sand content becomes smaller than the judgment value, the replacement work of the stabilizing liquid is stopped.

Figure 2023021209000002
Figure 2023021209000002

本実施形態によれば、以下のような効果を得ることができる。
(1)本実施形態では、サイクロン装置25に供給される安定液の比重(第1計測値)と、サイクロン装置25において砂分を除去した安定液の比重(第2計測値)とを含む式から、安定液の砂分率を算出する。これにより、安定液の砂分率を効率的に計測することができる。
According to this embodiment, the following effects can be obtained.
(1) In the present embodiment, an expression including the specific gravity (first measured value) of the stable liquid supplied to the cyclone device 25 and the specific gravity (second measured value) of the stable liquid from which sand has been removed in the cyclone device 25 , the sand content of the stable solution is calculated. Thereby, the sand content of the stable liquid can be efficiently measured.

(2)本実施形態では、杭孔10からプラント17に回収される安定液の一部を評価装置20に流して、評価装置20において安定液の性状を評価する。これにより、杭孔10からプラント17へ流れる安定液の性状を効率的に評価することができる。 (2) In the present embodiment, part of the stable liquid recovered from the pile hole 10 to the plant 17 is flowed into the evaluation device 20, and the evaluation device 20 evaluates the properties of the stable liquid. Thereby, the properties of the stable liquid flowing from the pile hole 10 to the plant 17 can be efficiently evaluated.

(3)本実施形態では、第1及び第2比重計測部(21,22)の容器(21c,22c)の下端部に供給管18の分岐管が接続される。これにより、容器21c,22cには、下方から安定液が供給されて上方へと流れ、容器21c,22c内の一部を徐々に入れ替えながら、安定液の比重を計測するので、急激な性状変化を生ぜずに、流れる安定液の比重を連続して効率的に計測することができる。更に、第1比重計測部21が接続される供給管18から、第2比重計測部22が接続される排出管28まで、安定液は数秒で流れる。これにより、第1比重計測部21及び第2比重計測部22においては、ほぼ同じ安定液について、ほとんど遅延なく、ほぼ同時に比重を計測することができる。 (3) In the present embodiment, a branch pipe of the supply pipe 18 is connected to the lower ends of the containers (21c, 22c) of the first and second specific gravity measuring units (21, 22). As a result, the stabilizing liquid is supplied to the containers 21c and 22c from below and flows upward. The specific gravity of the flowing stable liquid can be continuously and efficiently measured without causing Furthermore, the stable liquid flows in several seconds from the supply pipe 18 to which the first specific gravity measuring section 21 is connected to the discharge pipe 28 to which the second specific gravity measuring section 22 is connected. As a result, the first specific gravity measuring unit 21 and the second specific gravity measuring unit 22 can measure the specific gravity of almost the same stable liquid almost simultaneously with almost no delay.

(4)本実施形態の第1及び第2比重計測部(21,22)は、容器(21c,22c)において、開口した上端部まで1mとなる位置に設けた圧力計21a,22aを備える。これにより、圧力計21a,22aは、容器21c,22c内の圧力を計測するので、各容器21c,22c内の安定液の比重を効率的に計測することができる。 (4) The first and second specific gravity measuring units (21, 22) of the present embodiment are provided with pressure gauges 21a, 22a provided at positions 1 m from the opened upper end of the container (21c, 22c). As a result, the pressure gauges 21a and 22a measure the pressure inside the containers 21c and 22c, so that the specific gravities of the stable liquids inside the containers 21c and 22c can be efficiently measured.

(5)本実施形態では、管理ユニット30の制御部31は、同時期において計測した安定液の比重、粘度、砂分率の計測値を表示部32に表示する。これにより、安定液の性状管理に必要な複数の性状を同時期に把握することができる。 (5) In the present embodiment, the control section 31 of the management unit 30 displays the measured values of the specific gravity, viscosity, and sand content of the stable liquid measured at the same time on the display section 32 . Thereby, a plurality of properties required for property management of the stable liquid can be grasped at the same time.

(6)本実施形態では、管理ユニット30の制御部31は、定期的に、第1比重計測部21及び第2比重計測部22のドレーン管21d,22dのバルブを開く。これにより、評価装置20のキャリブレーションを、一定時間間隔で行なうことができる。 (6) In this embodiment, the control section 31 of the management unit 30 periodically opens the valves of the drain pipes 21d and 22d of the first specific gravity measuring section 21 and the second specific gravity measuring section 22 . Thereby, the calibration of the evaluation device 20 can be performed at regular time intervals.

本実施形態は、以下のように変更して実施することができる。本実施形態及び以下の変更例は、技術的に矛盾しない範囲で互いに組み合わせて実施することができる。
・上記実施形態では、第1比重計測部21が計測した第1計測値から第2比重計測部22が計測した第2計測値を減算(引き算)した比重差を、砂の比重(2.65)から第2計測値を減算した比重差で除算して、係数(140)を乗算することで砂分率を算出した。安定液の砂分率は、この係数(140)や算出方法に限定されず、例えば、第1計測値を第2計測値で除算した値を、対応する換算テーブルを用いて砂分率を算出する等、第1計測値と第2計測値との比較結果を用いて、砂分率を計測することができればよい。更に、計測した粘度に応じて砂分率を調整して算出してもよい。具体的には、第1計測値と第2計測値とを比較した値を、計測した粘度の値に応じた補正値を用いて補正し、この補正値に応じて砂分率を算出する。
This embodiment can be implemented with the following modifications. This embodiment and the following modified examples can be implemented in combination with each other within a technically consistent range.
In the above embodiment, the specific gravity difference obtained by subtracting (subtracting) the second measured value measured by the second specific gravity measuring unit 22 from the first measured value measured by the first specific gravity measuring unit 21 is calculated from the specific gravity of sand (2.65). The sand content was calculated by dividing the second measured value by the subtracted specific gravity difference and multiplying by a factor (140). The sand content of the stable liquid is not limited to this coefficient (140) or the calculation method. For example, the value obtained by dividing the first measured value by the second measured value is used to calculate the sand content using the corresponding conversion table. It is sufficient if the sand content can be measured using the result of comparison between the first measured value and the second measured value. Furthermore, it may be calculated by adjusting the sand content according to the measured viscosity. Specifically, the value obtained by comparing the first measured value and the second measured value is corrected using a correction value corresponding to the measured viscosity value, and the sand content is calculated according to this correction value.

・上記実施形態では、管理ユニット30の制御部31は、算出した砂分率、計測した比重及び粘度を表示部32に表示した。これに加えて、制御部31が、算出した砂分率が基準値を超えたか否かを判定し、その判定結果を示してもよい。更に、管理ユニット30は、安定液の性状に関する情報であって、砂分率、比重及び粘度以外の情報、例えば、安定液のpHや濾過水量等を管理してもよい。更に、管理ユニット30に通信部を設け、砂分率、比重及び粘度を、管理者の端末に送信してもよい。 - In the above embodiment, the controller 31 of the management unit 30 displays the calculated sand content, the measured specific gravity, and the viscosity on the display 32 . In addition to this, the control unit 31 may determine whether or not the calculated sand content exceeds the reference value, and indicate the determination result. Furthermore, the management unit 30 may manage information other than the sand content, specific gravity, and viscosity, such as the pH of the stable liquid and the amount of filtered water, which are information related to the properties of the stable liquid. Furthermore, a communication section may be provided in the management unit 30 to transmit the sand content, specific gravity and viscosity to the terminal of the manager.

・上記実施形態では、管理ユニット30の表示部32に表示された砂分率を管理者が監視する。これに代えて、管理ユニット30の制御部31が、砂分率が判定基準値以下となった場合に、安定液の回収及び供給を自動的に停止してもよい。この場合、回収管16及び供給管にバルブを設ける。そして、制御部31は、砂分率が判定基準値以下となった場合には、これらバルブを閉鎖する指示信号を出力して安定液の供給及び回収を制御する。 - In the above embodiment, the administrator monitors the sand content displayed on the display section 32 of the management unit 30 . Alternatively, the control section 31 of the management unit 30 may automatically stop the recovery and supply of the stabilizing liquid when the sand content ratio becomes equal to or less than the criterion value. In this case, the recovery pipe 16 and the supply pipe are provided with valves. Then, when the sand content ratio becomes equal to or less than the judgment reference value, the control unit 31 outputs an instruction signal to close these valves to control the supply and recovery of the stable liquid.

・上記実施形態では、杭孔10からプラント17に流れる回収液について評価を行なった。評価する対象となる安定液は、杭孔10から回収される回収液に限らず、杭孔10に供給される供給液であってもよい。この場合には、プラント17から杭孔10に安定液を供給する管路に供給管を介して評価装置20を取り付ける。例えば、次の表2に示されるように、供給される安定液に含まれる砂分率が、基準値(例えば、1.0%)以下の場合には、安定液の供給を継続する。 - In the above-described embodiment, the collected liquid flowing from the pile hole 10 to the plant 17 was evaluated. The stable liquid to be evaluated is not limited to the recovered liquid recovered from the pile hole 10 and may be the feed liquid supplied to the pile hole 10 . In this case, the evaluation device 20 is attached to the pipeline that supplies the stabilizing liquid from the plant 17 to the pile hole 10 via a supply pipe. For example, as shown in Table 2 below, when the sand content in the stabilizing liquid to be supplied is equal to or lower than a reference value (for example, 1.0%), the stabilizing liquid is continued to be supplied.

Figure 2023021209000003
Figure 2023021209000003

そして、供給される安定液に含まれる砂分率が、基準値(例えば、1.0%)以上となる場合には、アラームを表示部32に表示してもよい。更に、このアラームを管理者の端末に送信してもよい。
更に、杭孔10からプラント17に流れる回収液の管路及びプラント17から杭孔10に供給される供給液の管路に、それぞれ評価装置20を設けてもよい。
An alarm may be displayed on the display unit 32 when the sand content rate contained in the supplied stabilizing liquid is equal to or higher than a reference value (for example, 1.0%). Furthermore, this alarm may be sent to the administrator's terminal.
Furthermore, the evaluation device 20 may be provided in each of the pipeline for the recovered liquid flowing from the pile hole 10 to the plant 17 and the pipeline for the feed liquid supplied from the plant 17 to the pile hole 10 .

・上記実施形態では、供給管18を介して評価装置20に供給された安定液は、泥水槽23に一時的に蓄積された後、プラント17に還送する。泥水槽23に安定液を一時的に蓄積する代わりに、評価装置20に供給された安定液を、供給管18を接続した管路(上記実施形態では回収管18)の下流側に戻してもよい。
・上記実施形態では、砂分除去装置としてサイクロン装置25を用いた。砂分を除去することができる装置であれば、サイクロン装置25に限定されない。
- In the above embodiment, the stable liquid supplied to the evaluation device 20 through the supply pipe 18 is temporarily accumulated in the mud tank 23 and then returned to the plant 17 . Instead of temporarily accumulating the stable liquid in the mud tank 23, the stable liquid supplied to the evaluation device 20 may be returned to the downstream side of the pipe line (recovery pipe 18 in the above embodiment) connected to the supply pipe 18. good.
- In the above embodiment, the cyclone device 25 is used as the sand removal device. The device is not limited to the cyclone device 25 as long as it can remove sand.

10…杭孔、11…安定液、15…ポンプ、16…回収管、17…プラント、18…測定供給管、20…評価装置、21…第1比重計測部、21a,22a…圧力計、21c,22c…容器、21d,22d…ドレーン管、21v,22v…バルブ、22…第2比重計測部、23…計測用泥水槽、25…サイクロン装置、26…粘度計測部、28…排出管、30…性状管理部、31…制御部、32…表示部、50…砂分計、51…水、52…砂。 DESCRIPTION OF SYMBOLS 10... Pile hole, 11... Stabilizing liquid, 15... Pump, 16... Recovery pipe, 17... Plant, 18... Measurement supply pipe, 20... Evaluation device, 21... First specific gravity measuring unit, 21a, 22a... Pressure gauge, 21c , 22c... container, 21d, 22d... drain pipe, 21v, 22v... valve, 22... second specific gravity measuring unit, 23... mud tank for measurement, 25... cyclone device, 26... viscosity measuring unit, 28... discharge pipe, 30 ... property management unit, 31 ... control unit, 32 ... display unit, 50 ... sand content meter, 51 ... water, 52 ... sand.

Claims (1)

安定液中に含まれる砂分を分離するサイクロン装置であって、
孔の内部に充填された前記安定液が流れる供給管が接続され、
前記供給管を介して供給された前記安定液から分離した砂分を下方から排出し、
上部に接続された排出管を介して、前記砂分を分離して除去した安定液を排出し、
前記安定液において除去対象となる砂粒子の直径及び前記安定液の粘度に応じて、周速度及び前記安定液の流入速度を調整することを特徴とするサイクロン装置。
A cyclone device for separating sand contained in a stabilizing liquid,
A supply pipe through which the stabilizing liquid filled inside the hole flows is connected,
discharging sand separated from the stable liquid supplied through the supply pipe from below;
Discharge the stable solution from which the sand is separated and removed through the discharge pipe connected to the upper part,
A cyclone device characterized by adjusting a peripheral speed and an inflow speed of the stabilizing liquid according to the diameter of sand particles to be removed in the stabilizing liquid and the viscosity of the stabilizing liquid.
JP2022166971A 2018-12-05 2022-10-18 Cyclone device Pending JP2023021209A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2022166971A JP2023021209A (en) 2018-12-05 2022-10-18 Cyclone device

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2018228251A JP7163747B2 (en) 2018-12-05 2018-12-05 STABLE LIQUID EVALUATION METHOD AND STABLE LIQUID EVALUATION DEVICE
JP2022166971A JP2023021209A (en) 2018-12-05 2022-10-18 Cyclone device

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP2018228251A Division JP7163747B2 (en) 2018-12-05 2018-12-05 STABLE LIQUID EVALUATION METHOD AND STABLE LIQUID EVALUATION DEVICE

Publications (1)

Publication Number Publication Date
JP2023021209A true JP2023021209A (en) 2023-02-10

Family

ID=71013729

Family Applications (3)

Application Number Title Priority Date Filing Date
JP2018228251A Active JP7163747B2 (en) 2018-12-05 2018-12-05 STABLE LIQUID EVALUATION METHOD AND STABLE LIQUID EVALUATION DEVICE
JP2022166972A Active JP7367833B2 (en) 2018-12-05 2022-10-18 Specific gravity measuring device
JP2022166971A Pending JP2023021209A (en) 2018-12-05 2022-10-18 Cyclone device

Family Applications Before (2)

Application Number Title Priority Date Filing Date
JP2018228251A Active JP7163747B2 (en) 2018-12-05 2018-12-05 STABLE LIQUID EVALUATION METHOD AND STABLE LIQUID EVALUATION DEVICE
JP2022166972A Active JP7367833B2 (en) 2018-12-05 2022-10-18 Specific gravity measuring device

Country Status (1)

Country Link
JP (3) JP7163747B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7163747B2 (en) * 2018-12-05 2022-11-01 株式会社大林組 STABLE LIQUID EVALUATION METHOD AND STABLE LIQUID EVALUATION DEVICE

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08117643A (en) * 1994-10-19 1996-05-14 Keisan Kogyo Kk Symmetrical two-barrel liquid cyclone
JP2015178055A (en) * 2014-03-19 2015-10-08 宇部興産機械株式会社 Separation device
JP2020091187A (en) * 2018-12-05 2020-06-11 株式会社大林組 Method and device foe evaluating stabilization liquid

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07104253B2 (en) * 1989-11-03 1995-11-13 株式会社フジタ Stabilizer automatic measuring device
JP3353183B2 (en) * 1994-07-21 2002-12-03 飛島建設株式会社 Mud water property measurement method and device
JPH09133626A (en) * 1995-11-10 1997-05-20 Fujita Corp Measuring apparatus for specific gravity and viscosity of muddy water

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08117643A (en) * 1994-10-19 1996-05-14 Keisan Kogyo Kk Symmetrical two-barrel liquid cyclone
JP2015178055A (en) * 2014-03-19 2015-10-08 宇部興産機械株式会社 Separation device
JP2020091187A (en) * 2018-12-05 2020-06-11 株式会社大林組 Method and device foe evaluating stabilization liquid

Also Published As

Publication number Publication date
JP7163747B2 (en) 2022-11-01
JP7367833B2 (en) 2023-10-24
JP2020091187A (en) 2020-06-11
JP2023002672A (en) 2023-01-10

Similar Documents

Publication Publication Date Title
US9468868B2 (en) Water removing device for extremely high water content three-phase flow, and measurement device and method for extremely high water content three-phase flow
RU2365750C1 (en) Method for measurements of debits, monitoring and control of oil well production technology and installation for its realisation
JP7367833B2 (en) Specific gravity measuring device
RU2415263C2 (en) Procedure for preparing and measurement of production output of oil wells and device for its implementation (versions)
US7966892B1 (en) In line sampler separator
RU2406823C1 (en) Method of differentiated measurement of flow rate of oil wells and device for its implementation (versions)
JP7323035B2 (en) STABLE LIQUID REPLACEMENT METHOD AND STABLE LIQUID REPLACEMENT DEVICE
RU2610745C1 (en) Method of measuring flow rate of oil wells and device for its implementation
WO2013171652A1 (en) Method of controlling a gravity sedimentation device
EP1020713B1 (en) Method and system for determining biphase flow rate
WO2019086918A1 (en) Flow measurement of fluid containing solid by bottom-fed flume
AU2008246228A1 (en) Soil moisture sampling device
RU2657321C1 (en) Bucket meter of liquid and associated petroleum gas in a flowing gas-liquid mixture
CN104763408B (en) A kind of high precision petroleum three-phase automatic metering device and its metering method
RU2541991C1 (en) Method of measuring well flow rate of oil well products and device to this end
CN106526224B (en) A kind of solid-liquid two-phase flow speed measuring device and method
RU2236584C1 (en) Method and device for measuring oil debit
RU155020U1 (en) INSTALLATION FOR MEASURING THE DEBIT OF OIL WELL PRODUCTS
CN103993872B (en) Crude oil volume type measuring sledge
AU2011201556B2 (en) Method for controlling a jigging machine
CN101592509A (en) A kind of automatic measuring system of phreatic water evaporation
RU2552563C1 (en) Portable metering station of extracted well liquid
RU2307249C1 (en) Device for well oil production rate measurement
KR101736678B1 (en) Surface tension type rain gauge and method for measuring a rainfall
RU129554U1 (en) DEVICE FOR DETERMINING OIL AND GAS-WATER FLOW PARAMETERS

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20221018

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20231011

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20231017

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20231213

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20240206

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20240325