JPS6225413B2 - - Google Patents

Info

Publication number
JPS6225413B2
JPS6225413B2 JP54061532A JP6153279A JPS6225413B2 JP S6225413 B2 JPS6225413 B2 JP S6225413B2 JP 54061532 A JP54061532 A JP 54061532A JP 6153279 A JP6153279 A JP 6153279A JP S6225413 B2 JPS6225413 B2 JP S6225413B2
Authority
JP
Japan
Prior art keywords
mixing
tank
liquid
chemical
measuring
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP54061532A
Other languages
Japanese (ja)
Other versions
JPS55155734A (en
Inventor
Masuo Shimazaki
Yasuo Takaku
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.)
SHIMAZAKI MIXING EQUIP
Original Assignee
SHIMAZAKI MIXING EQUIP
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 SHIMAZAKI MIXING EQUIP filed Critical SHIMAZAKI MIXING EQUIP
Priority to JP6153279A priority Critical patent/JPS55155734A/en
Publication of JPS55155734A publication Critical patent/JPS55155734A/en
Publication of JPS6225413B2 publication Critical patent/JPS6225413B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80Mixing plants; Combinations of mixers

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Accessories For Mixers (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

この発明は、例えば、土質安定液に使用される
土質硬化液、土質硬化促進液等の複数の薬液に対
する計量槽と混合槽と貯液槽とが直列に配管接続
されて各々独立に系列配備され各配管に介装され
た電磁弁が同期作動回路により接続されている薬
液混合供給装置に関するものであり、特に、上記
各計量槽に付設されたレベル検知装置に連動する
ポンプの電磁弁を上記各計量槽、前記混合槽付設
予備混合装置に各々対設させると共に上記混合槽
に付設された他のレベル検知装置に連動する他の
電磁弁を前記貯液槽に対設させて、連続混合供給
可能な薬液混合供給装置に係るものである。 従来、例えば地盤安定材の薬液混合供給装置と
して、複数の薬液に対する計量混合槽とバツチ式
貯液槽とが直列に配管接続された複数の系が各々
独立に配備され、各配管に手動弁が設けられると
共に上記計量混合槽に目視レベル計が付設された
態様が一般に採用されていた。 而して、上記薬液混合供給装置は予め、混合し
た一種類の薬液混合液等を注入する1シヨツト方
式に対しては優れた機能を奏しはする。 さりながら、例えば、薬液としての土質安定液
は一般に硬化プロセスに於ける圧縮強度及び公害
対処等の見地から速硬性ゲルタイムコントロール
が重視され、例えば、ゲルタイム5〜6秒の瞬結
タイプでは該ゲルタイム内に混合注入する1.5シ
ヨツト或は2シヨツトの方式が採用使用される様
になつて来ているが、これらのシヨツト方式に対
し、バツチ式貯液槽を有している上記薬液混合供
給装置の適用は不可能であつた。 蓋し、土質安定液の地盤注入に際し、大量の土
質安定液を要し、短ゲルタイム内に大量の薬液混
合を生成し得ないので、予め、大量の薬液混合を
生成しておく必要が有し、従つて、上記在来タイ
プの薬液混合供給装置はそのキヤパシテイが大と
なり、高コストとなる不利点があるのみならず、
運搬等の管理に対しても煩瑣となる難点があつ
た。 又、原液から稀釈薬液、或は、混合した薬液は
大量な為1.5シヨツト注入等を行おうとすると長
時間貯液槽にて貯留することになり、該薬液はゲ
ル化又は劣化する可能性が有し、複数の該薬液同
志は所定に化学反応され得ない不利点もあつた。 更に、計量混合槽に付設されるレベル計は目視
による為弁操作等が手動になり現場誤動作が避け
られず、正確な当量反応が出来ず、確実な化学反
応プロセスに対し決定的な欠陥となる場合がある
デメリツトもあつた。 特に近時極めて小量で敏感に反応時間、末成物
の化学性が異なる反応材が製造される様になると
手動操作では反応コントロールが出来ない不具合
があつた。 この発明の目的は上記従来技術に基づくバツチ
タイプ薬液混合供給装置の問題点に鑑み、複数の
薬液に対する計量槽と混合槽と貯液槽とが直列に
配管接続して系をなし、各複数系が各々独立に系
列配備させ、各給排配管に各槽付設レベル検知装
置に連動する電磁弁を同期回路に接続して介装さ
せてフロー式にすることにより、上記欠点を除去
し、難点を解消し、不利点やデメリツトを無く
し、優れた機能を有する新規な薬液混合供給装置
を提供せんとするものである。 上記目的に沿うこの発明の構成は独立系列に配
備された各系列の複数薬液に対して計量槽付設レ
ベル検知装置により、該計量槽給排管に介装した
ポンプ、電磁弁を同期連動させて、各々設定時間
内に連続計量し、予備混合装置を経、混合槽に各
系列で供給混合した後、混合槽排管に介装した同
期作動する電磁弁を介して更に貯液槽に貯留し、
該各貯液槽より、供給工程中、或は、次段反応工
程中に於て正確に設定反応する様に連続供給する
様にしたことを要旨とするものである。 次に、上記目的に沿うこの発明の1実施例を図
面に基づき説明すれば以下の通りである。 第1,3図に於て、1はこの発明の要旨をなす
地盤安定材としての薬液混合供給装置であり、該
薬液混合供給装置1は複数の薬液、例えば、ゲル
タイム5〜6secの土質安定液を2シヨツトにて反
応生成せしめる組成液として水ガラス原液2を所
定稀釈した水ガラス稀釈液としてA液3、土質硬
化液B液4と土質硬化促進液C液5との混合稀釈
液としてのD液5′を各個にフロー裡に連続生成
供給せしめるために供されるものである。 而して、上記薬液混合供給装置1に原液2の稀
釈水に対する計量槽6、B液4に対する計量槽
7、C液5に対する計量槽8が併設裡に上設され
ており、該計量槽8は上記他の計量槽6,7に比
し底面積小にて小容量とされ、又、該各計量槽
6,7,8に適宜周知の複段定位レベル検知装置
9,10及びフロート式無段レベル検知装置11
が各々内装されている。 又、上記各計量槽6及び7,8に対しては各々
混合槽12及び13が下設されており、該混合槽
12,13は内部側方に各々前記同様周知の複段
レベル検知装置14,15を、他の内部側方にミ
キサ16,17を、又、中央に予備混合装置とし
ての周知のインジエクタ18,19を各々付設さ
せている。 更に、上記混合槽12,13に各々同様複段の
レベル検知装置20,21,22を有する貯液槽
23,24が下設されている。 尚、25は該貯液槽23,24に併設された水
タンクである。 而して、第1図図上26はポンプ室であり、該
ポンプ室26にポンプ27,28,29,30及
び電磁弁31,32……38が内装され、該ポン
プ室2にタンク室39が併設され、該タンク室3
9に前記水ガラス原液2、B液4、C液5に対す
る貯留用タンク40,41,42が各々内装され
ている。 又、43は水に対する配管であり、該配管43
は前記ポンプ29、電磁弁34,35,38を介
装させて図示しない水供給パイプより計量槽6、
貯液槽25、インジエクタ19に接続させ、同様
に水ガラス原液2、B液4、C液5に対する配管
44,45,46はポンプ30,27,28を介
装して上記タンク40,41,42より、各々イ
ンジエクタ18、計量槽7,8に接続させてい
る。 而して、47,48……51は中間配管であ
り、該配管47,48……51は、電磁弁33,
31,32,36,37を各々介装させて計量槽
6とインジエクタ18とを、計量槽7,8とイン
ジエクタ19とを、混合槽12,13と貯液槽2
3,24とを各々系列接続させてある。 又、52は制御盤であり、第1図に示す様にプ
ラントフレームの前面に適宜装備され、該制御盤
52はその前面に第2図に示す操作盤53を付設
させると共に第4図図上のシーケンス同期回路5
4を内装する。 尚、バルブ55,56,57を介装させた配管
58,59,60は貯液槽23,24,25に
各々下設させると共に該配管58,59先端を図
示しない地盤注入用2重管の内管、外管に接続す
る圧送ポンプに接続させ、連続2シヨツト注入が
可能にされている。 上記構成に於て、ゲルタイム5〜6secの瞬結タ
イプ土質安定液を2重管を介して所定深度地盤に
対し2シヨツト注入態様にて反応させるに組成液
としてのA液3、B液4とC液5との混合稀釈D
液5′を各々2重管の内管、外管に供給するに際
し、予め、注入せんとする所定深度地盤に対する
圧縮強度、ゲルタイムを設定し、例えば下記する
ゲルタイム5〜6secの瞬結タイプ土質安定液の圧
縮強度と組成液割合との関係データが予め得られ
ていたとすればそのデータにもとづいて組成液割
合を決定する。
In the present invention, for example, a measuring tank, a mixing tank, and a liquid storage tank for a plurality of chemical solutions such as a soil hardening liquid used as a soil stabilizing liquid, a soil hardening accelerating liquid, etc. are connected in series with piping and each is arranged in series independently. This relates to a chemical liquid mixing and supplying device in which solenoid valves installed in each piping are connected by a synchronous operation circuit, and in particular, the solenoid valves of the pumps linked to the level detection devices attached to each of the measuring tanks are connected to each of the above. A measuring tank and a premixing device attached to the mixing tank are respectively provided opposite to each other, and another electromagnetic valve linked to another level detection device attached to the mixing tank is provided opposite to the liquid storage tank to enable continuous mixing and supply. The present invention relates to a chemical liquid mixing and supplying device. Conventionally, for example, as a chemical liquid mixing supply device for ground stabilizing materials, multiple systems in which metering mixing tanks and batch-type liquid storage tanks for multiple chemical liquids are connected in series with piping are each independently installed, and each piping is equipped with a manual valve. Generally, a visual level meter is attached to the metering and mixing tank. Therefore, the above-mentioned chemical liquid mixing and supplying device exhibits an excellent function for a one-shot system in which a single type of chemical liquid mixture or the like that has been mixed in advance is injected. However, for example, for soil stabilizing liquids as chemicals, quick curing gel time control is generally important from the viewpoint of compressive strength in the curing process and pollution control. For example, for instant setting type with gel time of 5 to 6 seconds, The 1.5-shot or 2-shot system, which mixes and injects the chemical into the liquid, has come into use, but it is difficult to apply the above-mentioned chemical liquid mixing and supply device having a batch-type liquid storage tank to these shot systems. was impossible. When the soil stabilizing solution is injected into the ground, a large amount of soil stabilizing solution is required, and a large amount of the chemical mixture cannot be generated within a short gel time, so it is necessary to generate a large amount of the chemical mixture in advance. Therefore, the above-mentioned conventional type chemical liquid mixing and supplying device not only has the disadvantage of large capacity and high cost, but also
There were also some troublesome problems with the management of transportation, etc. In addition, since the drug solution diluted from the original solution or the mixed drug solution is a large amount, if you try to inject 1.5 shots, it will be stored in a storage tank for a long time, and the drug solution may gel or deteriorate. However, there was also a disadvantage that the plurality of chemical solutions could not be subjected to a predetermined chemical reaction. Furthermore, since the level meter attached to the metering and mixing tank is visually checked, valve operations, etc. must be done manually, making on-site malfunctions inevitable, making it impossible to perform accurate equivalent reactions, which is a decisive flaw in ensuring a reliable chemical reaction process. There were some disadvantages as well. Particularly in recent years, when reactants have been manufactured in extremely small quantities with sensitively different reaction times and chemical properties of final products, there has been a problem in that the reaction cannot be controlled manually. An object of the present invention is to solve the problems of the batch-type chemical liquid mixing and supplying device based on the above-mentioned prior art, and to form a system in which a measuring tank, a mixing tank, and a liquid storage tank for a plurality of chemical liquids are connected in series with piping, and each of the plural systems is The above-mentioned drawbacks are eliminated by installing each independently in series and installing a solenoid valve linked to the level detection device attached to each tank in each supply/discharge pipe by connecting it to a synchronous circuit to create a flow type system. However, it is an object of the present invention to provide a novel chemical liquid mixing and supplying device that eliminates disadvantages and disadvantages and has excellent functions. The structure of the present invention in accordance with the above object is to synchronize and interlock pumps and solenoid valves interposed in the metering tank supply and discharge pipes for multiple chemical solutions arranged in independent lines using a level detection device attached to a measuring tank. The liquid is continuously weighed within a set time, supplied to the mixing tank in each series through a premixing device, and mixed.Then, the liquid is further stored in a storage tank via a synchronously operated solenoid valve installed in the mixing tank discharge pipe. ,
The gist of this is that the liquid is continuously supplied from each of the liquid storage tanks so that the reaction can be set accurately during the supply process or during the next reaction process. Next, one embodiment of the present invention that achieves the above object will be described below based on the drawings. In FIGS. 1 and 3, reference numeral 1 denotes a chemical solution mixing and supplying device as a soil stabilizing material, which is the gist of the present invention. As a composition liquid to be reacted and produced in two shots, A solution 3 is a water glass diluted solution obtained by diluting the water glass stock solution 2 to a predetermined value, and D is a mixed diluted solution of soil hardening solution B solution 4 and soil hardening accelerator solution C solution 5. This is provided to continuously generate and supply the liquid 5' to each individual in a flow manner. Therefore, a measuring tank 6 for diluting water of the stock solution 2, a measuring tank 7 for the B liquid 4, and a measuring tank 8 for the C liquid 5 are installed above the chemical mixing supply device 1, and the measuring tank 8 has a smaller bottom area and smaller capacity than the other measuring tanks 6, 7, and each measuring tank 6, 7, 8 is equipped with a well-known multi-stage localization level detecting device 9, 10 and a float type non-contact device. Step level detection device 11
Each one is decorated individually. Also, mixing tanks 12 and 13 are provided below each of the measuring tanks 6, 7, and 8, and each of the mixing tanks 12, 13 has a well-known multi-stage level detection device 14 on the inside side. , 15, mixers 16, 17 on the other internal sides, and well-known injectors 18, 19 as premixing devices in the center, respectively. Further, liquid storage tanks 23 and 24 having multi-stage level detection devices 20, 21 and 22 are provided below the mixing tanks 12 and 13, respectively. Note that 25 is a water tank attached to the liquid storage tanks 23 and 24. 1 is a pump chamber, in which pumps 27, 28, 29, 30 and solenoid valves 31, 32...38 are installed, and a tank chamber 39 is installed in the pump chamber 2. is attached, and the tank room 3
Storage tanks 40, 41, and 42 for the water glass stock solution 2, B solution 4, and C solution 5 are installed inside the tank 9, respectively. Further, 43 is a pipe for water, and the pipe 43
The metering tank 6 is connected to the water supply pipe (not shown) by interposing the pump 29 and the solenoid valves 34, 35, and 38.
Similarly, the pipes 44, 45, 46 for the water glass stock solution 2, B solution 4, and C solution 5 are connected to the liquid storage tank 25 and the injector 19, with pumps 30, 27, 28 interposed, and connected to the tanks 40, 41, 42 are connected to the injector 18 and the measuring tanks 7 and 8, respectively. Thus, 47, 48...51 are intermediate pipes, and the pipes 47, 48...51 are connected to the solenoid valves 33,
31, 32, 36, and 37, respectively, to connect the measuring tank 6 and the injector 18, the measuring tanks 7, 8 and the injector 19, and the mixing tanks 12, 13 and the liquid storage tank 2.
3 and 24 are connected in series. Further, 52 is a control panel, which is appropriately installed on the front of the plant frame as shown in FIG. 1, and the control panel 52 has an operation panel 53 shown in FIG. Sequence synchronization circuit 5
Interior 4. The pipes 58, 59, 60 with valves 55, 56, 57 are installed below the liquid storage tanks 23, 24, 25, respectively, and the tips of the pipes 58, 59 are connected to a double pipe for ground injection (not shown). It is connected to a pressure pump connected to the inner and outer tubes, allowing continuous two-shot injection. In the above configuration, the instant setting type soil stabilizing solution with a gel time of 5 to 6 seconds is reacted with two shot injection mode into the ground at a predetermined depth through a double pipe, and the composition liquids A liquid 3 and B liquid 4 are reacted. Mixing dilution D with C liquid 5
When supplying the liquid 5' to the inner and outer pipes of the double pipe, set the compressive strength and gel time for the specified depth of the ground to be injected in advance. If the relationship data between the compressive strength of the liquid and the liquid composition ratio is obtained in advance, the liquid composition ratio is determined based on that data.

【表】 又、併せて次の表に示す様な同じく予め分て
いるとするデータよりC液5が極めて微小量にて
ゲルタイムに及ぼす影響大であることから極微小
設定ゲルタイム内にてA液3、D液5′貯液槽2
3,24に連続供給し、常時一定量貯留すること
を要し、従つて、以下の計量混合プロセスを設計
しておく。
[Table] In addition, as shown in the table below, from the data that is also known in advance, it is found that liquid C 5 has a large influence on the gel time even in an extremely small amount. 3. D liquid 5' liquid storage tank 2
3 and 24, and it is necessary to always store a certain amount. Therefore, the following measuring and mixing process is designed.

【表】 即ち、例えば、ゲルタイム5〜6secで圧縮強度
6Kg/cm2の土質安定液を2シヨツト注入するに際
し、操作盤53にて強度選択の所定摘みを6に一
致させて自動スタートするとレベル検知装置9,
10,11が設定レベルにて検知可能に自動選定
すると共にポンプ27,28,29及び電磁弁3
4開動させて、水及びタンク41,42貯留の
B、C液4,5は同時併工程に各々一定流量にて
計量槽6,7,8に同時供給貯留される。 而して、計量槽6,7,8貯留液面が所定レベ
ルに達すると第4図に示す制御システムによりレ
ベル検知装置9,10,11はレベル検知作用に
より、リレーの適宜自で保持作用を介してポンプ
27,28を停止させ、ポンプ30を所定時間稼
動させると共に電磁弁33,31,32,35を
開作動させ、電磁弁34を停止して各計量槽6,
7,8にて所定短時間に所定計量された水、B液
4、C液5の中、水とタンク40貯留水ガラス2
をインジエクタ18に所定量比で供給混合して一
次予備撹拌し、混合槽12に貯留し、常時稼動の
ミキサ16を介して二次撹拌し、一方、上記所定
計量のB液4、C液5は、上記電磁弁31,32
の開動によつて、又、水は上記電磁弁35の所定
時間開動にて計量されて各々インジエクタ19に
所定量比で3者供給混合されつつ、上記混合槽1
2と同時プロセス裡に混合槽12に貯留撹拌され
る。 又、混合槽12,13混合撹拌液が各々所定レ
ベルに達すると、レベル検知装置14,15はそ
のレベル検知作用により図示しないリレーを介し
て電磁弁36,37を同時開動させ、貯液槽2
3,24にA液3、D液5′として貯留する。 而して、上記計量、混合撹拌プロセスが次述制
御により連続反復され、貯液槽23,24に順次
供給貯留される一方、該貯液槽23,24貯留A
液3、D液5′はバルブ55,56の開動を介し
て地盤に対する二重管の内管、外管に個別的に供
給されノズルにて噴射する際A液3、D液5′は
混合反応し土質安定液として地盤中に注入されゲ
ルタイム5〜6sec経過後ゲル化し所定深度地盤の
改良安定が図れることとなる。 而して、レベル検知装置36,37のレベル検
知作用により、貯液槽23,24の在液が設定レ
ベルより昇降するとその前後のプロセスの発停が
制御され、貯液槽23,24貯留A液3、D液
5′、は常時所定レベルに維持される。 尚、貯液槽25貯留水は、注入終了後上記2重
管の洗浄作用に使用される。 又、この発明の実施例は上記実施態様に限るこ
となく、又、実施例も種々の設計変更可能である
ことは勿論可能であり、例えば、使用する薬液は
土質安定液混合薬液に限れることなく他の薬液に
対しても適用出来るのである。 上記の様にこの発明によれば、複数の薬液に対
する計量槽と、予備混合装置を付設する混合槽と
貯液槽とが直列に配管接続して各々独立に系列配
備され、各槽に付設したレベル検知装置に連動す
る電磁弁、ポンプを同期的に各給排配管に介装さ
れているので、基本的に微小量正確に計量出来、
計量、混合撹拌プロセスの同期的サイクル化が可
能になり、従つて、該混合撹拌プロセスと併せて
処理済に貯液槽貯留液を次段処理に供給出来る極
めて優れた効果がある。 又、複数の大量薬液を混合供給するに際し、フ
ローシステムで混合撹拌し供給出来るので、従来
技術の如く予めから貯留する大容量の貯液槽を要
せず、レベル平衡を得るに足る容量の貯液槽でプ
ラントが構成出来、従つて、貯留液は劣化するこ
ともなく、薬液混合装置のコンパクト化も図れ、
運搬等の管理が容易になると共に該装置の低廉を
も図れる優れた利点があり、少量供給で反応に敏
感な影響を与え、他の薬液との当量反応、生成物
の特性に影響を与える場合、自動的に計量計供出
来、その点から自動計量設計が出来る優れた効果
がある。 又、計量槽にレベル検知装置が付設されている
ので自動的に高精度の計量が出来、化学プロセス
に対し絶対に詳されない誤動作も皆無となり、特
に、土質硬化促進液の如く、微小量微変がゲルタ
イムを左右する混合撹拌に対し、微量供給が正確
に計量出来、反応時間、反応生成物の性質コント
ロールが所望で可能である等顕著な効果がある。 更に、混合槽に予備混合装置が付設されている
ので、混合槽に複数の薬液を投入する際に予備混
合され混合槽に於ける混合撹拌を迅速にし、次段
混合槽の負担を軽くし、従つて、全体的に効率良
く混合撹拌が行えその上、混合撹拌プロセスの連
続サイクルを可能にするメリツトもある。加え
て、複数の薬液原液用タンクが各々付設されてい
るので、従来の如く、予め、工場等で稀釈混合し
た大容量の稀釈混合液等の現場までの大量輸送が
省略される等薬液供給準備が簡素となる具合さも
ある。
[Table] That is, for example, when injecting two shots of a soil stabilizer with a compressive strength of 6 kg/cm 2 with a gel time of 5 to 6 seconds, if the predetermined knob for strength selection is set to 6 on the operation panel 53 and automatic start is started, the level will be detected. device 9,
10 and 11 are automatically selected to be detectable at the set level, and the pumps 27, 28, 29 and the solenoid valve 3
4, water and B and C liquids 4 and 5 stored in tanks 41 and 42 are simultaneously supplied and stored in measuring tanks 6, 7, and 8 at constant flow rates, respectively, in a simultaneous process. When the level of the liquid in the measuring tanks 6, 7, 8 reaches a predetermined level, the control system shown in FIG. pumps 27 and 28 are stopped, pump 30 is operated for a predetermined time, and solenoid valves 33, 31, 32, and 35 are opened, and solenoid valve 34 is stopped and each measuring tank 6,
Water measured in a predetermined time in a predetermined time at steps 7 and 8, liquid B 4, liquid C 5, water and tank 40 stored water glass 2
are supplied to the injector 18 at a predetermined ratio and mixed for primary pre-stirring, stored in the mixing tank 12, and secondly stirred via the constantly operating mixer 16. Meanwhile, the predetermined amounts of B liquid 4 and C liquid 5 are is the above-mentioned solenoid valve 31, 32
The water is metered by the opening of the electromagnetic valve 35 for a predetermined period of time, and the water is supplied to the injector 19 at a predetermined ratio and mixed in the mixing tank 1.
2 and is stored and stirred in the mixing tank 12 during the same process. Further, when the mixed stirring liquid in the mixing tanks 12 and 13 reaches a predetermined level, the level detection devices 14 and 15 simultaneously open and operate the solenoid valves 36 and 37 via a relay (not shown) by their level detection action, and the liquid storage tank 2
3 and 24 as A liquid 3 and D liquid 5'. The above-mentioned measuring, mixing and stirring processes are continuously repeated under the following control, and the liquid is sequentially supplied and stored in the liquid storage tanks 23 and 24, while the liquid storage tanks 23 and 24 storage A
Liquids 3 and D 5' are individually supplied to the inner and outer pipes of the double pipe connected to the ground through the opening of valves 55 and 56, and liquids A 3 and D 5' are mixed when injected from the nozzle. It reacts and is injected into the ground as a soil stabilizing liquid, which gels after a gel time of 5 to 6 seconds, improving and stabilizing the ground at a predetermined depth. By the level detection action of the level detection devices 36 and 37, when the liquid in the liquid storage tanks 23 and 24 rises and falls below the set level, the start and stop of processes before and after that are controlled, and the liquid storage A in the liquid storage tanks 23 and 24 is controlled. Liquid 3 and D liquid 5' are always maintained at predetermined levels. Incidentally, the water stored in the liquid storage tank 25 is used for cleaning the double pipe after the injection is completed. Further, the embodiments of the present invention are not limited to the embodiments described above, and it is of course possible to make various design changes to the embodiments. For example, the chemical solution used may be limited to a soil stabilizing solution mixed chemical solution. It can also be applied to other chemical solutions. As described above, according to the present invention, a measuring tank for a plurality of chemical solutions, a mixing tank equipped with a premixing device, and a liquid storage tank are connected in series by piping and arranged independently in series, and Since solenoid valves and pumps linked to the level detection device are synchronously installed in each supply and discharge pipe, it is basically possible to accurately measure minute amounts.
It is possible to perform a synchronous cycle of measuring and mixing and stirring processes, and therefore, there is an extremely excellent effect that the treated liquid stored in the storage tank can be supplied to the next stage of processing in conjunction with the mixing and stirring process. In addition, when mixing and supplying multiple large amounts of chemical solutions, the flow system can mix and agitate them before supplying them, so there is no need for a large-capacity storage tank that stores the liquids in advance as in the conventional technology, and the storage tank has a sufficient capacity to achieve level balance. The plant can be configured with a liquid tank, so the stored liquid will not deteriorate, and the chemical mixing device can be made more compact.
It has the excellent advantage of being easy to manage transportation, etc. and also making the equipment inexpensive, and it has a sensitive effect on reactions when supplied in small quantities, and when it affects equivalence reactions with other chemical solutions and the properties of products. , it is possible to automatically provide a weighing meter, which has an excellent effect of allowing automatic weighing design. In addition, since the measuring tank is equipped with a level detection device, it is possible to automatically measure with high precision, and there are no malfunctions that are not known in detail in the chemical process. Compared to mixing and stirring, which influences the gel time, this method has remarkable effects such as being able to accurately measure small amounts of feed, and making it possible to control the reaction time and the properties of the reaction product as desired. Furthermore, since the mixing tank is equipped with a pre-mixing device, when multiple chemical solutions are added to the mixing tank, they are pre-mixed, speeding up mixing and agitation in the mixing tank, and reducing the burden on the next-stage mixing tank. Therefore, there is an advantage that mixing and agitation can be carried out efficiently as a whole, and furthermore, a continuous cycle of the mixing and agitation process can be performed. In addition, since multiple tanks for chemical liquid concentrate are attached to each tank, preparation for chemical liquid supply is eliminated, such as eliminating the need to transport large volumes of diluted mixtures diluted and mixed in advance at factories, etc. to the site, as in the past. In some cases, it becomes simple.

【図面の簡単な説明】[Brief explanation of the drawing]

図面はこの発明の実施例を示すものであり、第
1図は薬液混合装置の概略斜視説明図、第2図は
操作盤の平面図、第3図は薬液混合装置の作用プ
ロセス図、第4図は制御盤内装の制御回路概略説
明図である。 6,7,8……計量槽、12,13……混合
槽、23,24……貯液槽、31,32,33…
…電磁弁、9,10,11……レベル検知装置、
18,19……予備混合装置、36,37……他
の電磁弁、1……薬液混合装置。
The drawings show an embodiment of the present invention, and FIG. 1 is a schematic perspective view of the chemical liquid mixing device, FIG. 2 is a plan view of the operation panel, FIG. 3 is a working process diagram of the chemical liquid mixing device, and FIG. The figure is a schematic explanatory diagram of the control circuit inside the control panel. 6,7,8...Measuring tank, 12,13...Mixing tank, 23,24...Liquid storage tank, 31,32,33...
...Solenoid valve, 9,10,11...Level detection device,
18, 19... Premixing device, 36, 37... Other solenoid valves, 1... Chemical liquid mixing device.

Claims (1)

【特許請求の範囲】[Claims] 1 複数の薬液に対する計量槽と混合槽と貯液槽
とが直列に配管接続して、各々独立に系列配備さ
れ各配管に介装された電磁弁が同期作動回路によ
り接続されている薬液混合供給装置において、レ
ベル検知装置が付設された上記各計量槽と前記混
合槽に接続する予備混合装置とが上記レベル検知
装置に連動する電磁弁を付設した配管を介して接
続され、而して上記混合槽は該混合槽に付設され
た他のレベル検知装置に連動する他の電磁弁を付
設した配管を介して貯液槽に接続されていること
を特徴とする薬液混合供給装置。
1 A chemical liquid mixed supply in which a measuring tank, a mixing tank, and a liquid storage tank for multiple chemical liquids are connected in series with piping, each independently arranged in series, and the solenoid valves installed in each piping are connected by a synchronous operation circuit. In the apparatus, each of the measuring tanks equipped with a level detection device and a premixing device connected to the mixing tank are connected via piping equipped with a solenoid valve that operates in conjunction with the level detection device, and the mixing A chemical liquid mixing and supplying device, characterized in that the tank is connected to a liquid storage tank via a pipe provided with another electromagnetic valve that is linked to another level detection device attached to the mixing tank.
JP6153279A 1979-05-21 1979-05-21 Chemical liquid mixing and feeding device Granted JPS55155734A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6153279A JPS55155734A (en) 1979-05-21 1979-05-21 Chemical liquid mixing and feeding device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6153279A JPS55155734A (en) 1979-05-21 1979-05-21 Chemical liquid mixing and feeding device

Publications (2)

Publication Number Publication Date
JPS55155734A JPS55155734A (en) 1980-12-04
JPS6225413B2 true JPS6225413B2 (en) 1987-06-03

Family

ID=13173802

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6153279A Granted JPS55155734A (en) 1979-05-21 1979-05-21 Chemical liquid mixing and feeding device

Country Status (1)

Country Link
JP (1) JPS55155734A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2313221B (en) * 1995-11-28 1999-02-24 Fujitsu Ltd Automatic immigration card preparation system,airline ticket issuance apparatus,automatic immigration card preparation apparatus and airline ticket

Also Published As

Publication number Publication date
JPS55155734A (en) 1980-12-04

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