TW200302329A - System and method for delivering reactive fluids to remote application sites - Google Patents

System and method for delivering reactive fluids to remote application sites Download PDF

Info

Publication number
TW200302329A
TW200302329A TW091137491A TW91137491A TW200302329A TW 200302329 A TW200302329 A TW 200302329A TW 091137491 A TW091137491 A TW 091137491A TW 91137491 A TW91137491 A TW 91137491A TW 200302329 A TW200302329 A TW 200302329A
Authority
TW
Taiwan
Prior art keywords
fluid
internal gear
cable
crescent
flow rate
Prior art date
Application number
TW091137491A
Other languages
Chinese (zh)
Inventor
James L Birdsall
David H Johnson
Original Assignee
Neopoxy 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 Neopoxy Corp filed Critical Neopoxy Corp
Publication of TW200302329A publication Critical patent/TW200302329A/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J4/00Feed or outlet devices; Feed or outlet control devices
    • B01J4/02Feed or outlet devices; Feed or outlet control devices for feeding measured, i.e. prescribed quantities of reagents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00164Controlling or regulating processes controlling the flow
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00191Control algorithm

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
  • Nozzles (AREA)
  • Pipeline Systems (AREA)
  • Protection Of Pipes Against Damage, Friction, And Corrosion (AREA)

Abstract

Reactive fluids that react upon contact and are intended to be combined only at a site of application that is remote or not easily accessible are transported to the site by separate crescent internal gear pumps whose pump rates are governed by a control loop that uses individual mass flow rates and a common automatic controller. In preferred embodiments, a multi-lumen cable is used to convey the pump outputs individually to the application site, and an application head at the distal end of the cable both combines the individual flows and dispenses them to the site. The invention is useful for a variety of reactive systems and applications, but particularly for applying two-component epoxy linings to underground pipes.

Description

200302329200302329

玖、發明說明: (發明說明應敘明:發明所屬 之技術領域、先前技術 實施方式及圖式簡單説明) 發明背景 I.技術領域 本心月ί7:關於流體傳遞系統的領域,以在控制流量及流 量比率下供應多種物質至遠距端。 2.先前技藝 在迕多建造地點及各種商業操作型式,二或更多流體需 被個別傳邈至遂距端並在控制流量或流量比率下。這些操 作的貫例為以施用内襯於管線内部表面或灌漿管壁裂口進 行地下管子的修護。其他的實例為供應流體或流體化物質 至然法直接到達的地點如建築物或建造地點如橋、停車場 結構、及建築物地基。其他的實例為供應物質至礦區、人 孔、地下儲槽或儲存器、海面下位置、及水壩。須被個別 供應並在岔控制比率下傳遞的物質實例為反應性成份, 於此必須避免提早反應且保持反應化學計量。聚合物系統 ,如環氡類、聚氨酯類、聚尿類及聚丙烯醯類,為主要實 例。 傳遞水、污水、或排放水的地下管線為說明性實例。這 些官線易因腐、有機成長、生根;參入、流量負載、地面 運動、及一般退化而變差。此退化在經過管線的流體造成 阻礙且在某些情況造成管線的崩潰。如追化的污水管可導 致污水漏出並污染地上水及土壤形成,或是其$導致地上 水滲入並因此不必要地增加至處理工廠的流體。 地下管線修護非常昂貴且置換常需要顯著的地上中斷。 200302329 ⑺ 辕袁: 為避免這些中斷,已發展一些地下管線修護方法,其不带 自地面移除管線成挖管溝’而是使用遠距控制方法以施用 内襯於管線内部。就地内襯的一個方法包括插入_軚的、 可撓曲的管狀内襯(含可熟化樹脂)於管線,一旦插入,、 以 流體或空氣施壓於内襯,以將内襯壓向管子内壁,於此被 熱化’此步驟為困難的步驟,因未熟化的内襯管無法於管 子内被操作’且較無法完全確保管子被適當放置或沿其全 部長度被均勻施壓以達到所欲修護程度。 藉由遠距裝置施用内層的另一個方法為插入一長的軟質 辱官於管内並在管線末端經由噴嘴噴出樹脂以塗覆於管子 内壁’使樹脂在被噴霧後可就地熟化。許多以此方式施用 的樹脂為兩成份樹脂如環氧類、聚氨酯類、及聚脲類。為 達最大效果’這些反應性樹脂系統的兩成份必須維持分開 的,直到它們到達管子内部的應用點,且因此它們必須被 刀別栗达。目前此種應用型式的泵送方法為使用機械副往 復比例泵。 般兩成份反應性樹脂系統及多成份樹脂系統的一個困 難為各種成份係在特定化學計量比值下反應,且任何一個 义ί/7的過i會造成在樹脂熟化後未反應物質的存在。除未 ^的進料物貝之不良效率外’未反應成份仍留在樹脂内 =灸内概σσ貝降級’此外,未反應成份會緩慢地渡取内襯 二亏&通4^言線的流體。故為達最大效率、内襯品質、及 有^女全’在應用點維持兩成份的正確化學計量比值是重 要的。 200302329 (J) 發明說辑繽翼 ~^ 當使用比例泵時’可接受的控制及流量比例的穩定性僅 能在低於泵容量的泵流量達到,因大部份的脈衝(其為這些 泵的特性)可由在泵及噴嘴間的軟質導管之累積壓力及喷 霧噴嘴本身而在下一個衝程完成前被消除。當在導管末端 僅少量或沒有背壓時,此問題為特別敏感的。然而比例粟 的典型容量為低於3加侖每分鐘(0.7立方公尺每小時)。如此 ,為減少此種泵的脈衝,泵流量須被限制於約1加侖每分鐘 (0.23立方公尺每小時),此對小内徑管子是可接受的,但對 在許多下水道系統及其他水傳遞系統典型的大管子則否, 比例泵亦具有限的比值調整的變化性,因它們主要由泵哪 筒比值所控制。 兩成份反應系統的另一個困難為成份流量隨黏度、溫度 及影響成份密度的其他因素及泵磨損程度及用做導管之軟 管情況的差異而不同。流量一般由差壓測量,且黏度、溫 度及上述的其他因素會影響流動路徑沿線差壓且由此提供 與質量流量變化無關的讀數。 已揭示為僅在遠距位置接觸而被放置的許多成份可在高 程度的成份流量比率控制及廣銘阁 一 干彳工利汉Μ祀圍的流量(包括高體積流 置)下被傳遞至該位置。此發頊右田士 夕 &現有用於由多種成份内襯物質 形成的管子内襯的原地應用及可用 J用於任何指定地點位置, 包括建造位址、地下位址、海面 > 位址、及其他上速的退 距位置。此結果由一種丰蛴;素忐 禋'7、,、,疋遠成,其包括個別反應成份的 個別新月形内部齒輪泵及含測量每一 里兮成伤的筲量流率的流 (4) 200302329 量計及比較測得值與預先嗅擇 以修正與預先選擇值的偏差之 此方式控制的流動可藉由個別 個別腔的一種多腔纜線傳送至 無法到達的建造位址或上述的 管末端合併,於此它們可在所 或分散。 發明說稱繽真 值並產生訊號以調整泵速度 自動控制器之控制迴路。以 V營’較佺為含個別成份的 遠距位置,可為管線内部、 任何其他應用,成份係在導 欲位址合併及沉積、分配、 新月形内部齒輪袞挺Μ > 泵挺供媒脈衝的穩定流動,及流量比值 的連續變化性以允碑曰 α宁連、,的流置調整以修正與所欲比率的 微小偏差而不需在今周蚊 W疋上考慮基於設備的限制。此質量流 Ϊ 0十允命乐統以曾吾 貝里而非差壓提供比率控制,質量流量控 制允許反應化學計蚕^^& 卞里的連續及精確保持並避免基於影響成 份岔度或壓降而非暂Θ 千叩非貝罝的因素之調整。 在某些應用’可包括除主要反應成份外的系統成份以改 良要I和、物貝的待性,如内襯的物理及化學特性(在管線内 概的情況),或是加速反應速率、或是一般為改良方法的任 何爷數或特性。本發明系統可藉由個別泉送它們及使它們 在興主要成份相同方式控制的流量下傳遞炱應用位址來選 擇性地使用這些額外成份。 本發明的這些及其他特性、優點、及具體實施例更詳細 說明於本專利說明書的後續章節。 實施方式 新月形内部#輪泵具兩個圓形齒輪,亦即,一具向内延 伸的齒之外部齒輪,其與内部齒輪的向外延伸的齒相嚙合 200302329 ' 發嘯嘯頁. ,兩個齒輪皆在同一個外殼但在不同的平行輛(其使齒輪為 偏心關係)上旋轉,在其間留下新月形狀的空間。大部份新 月形狀的空間由新月形狀的插入物佔據,其提供其本身與 齒輪的齒尖之間的鄰近間隙。任一個齒輪可用做驅動齒輪 ,雖然較佳為以内部齒輪做為驅動齒輪。當齒輪的齒自嚙 合處離開時,它們產生空隙,當齒輪旋轉時空隙擴張以產 生吸力’以吸引流體進入齒輪間的空間並因此進入泵。當 齒輪回到嚙合處時,在齒附近的體積減少,由此增加壓力 並使流體經由排出端流出,由此流量可由齒輪旋轉速度決 定典型的新月形内部齒輪泵在内部齒輪具十三個齒且在 外部齒輪具十七個齒,操作在自約400至約6,000轉每分鐘 的速度,較佳為自約700轉每分鐘至約3,6〇〇轉每分鐘,且 具有母轉目約0.3平方寸至約15平方寸(約〇 〇〇5升至約〇以 升)的位移。較佳的泵為具自約2,〇〇(^f/平方寸至約6,〇〇〇磅 /平方寸範圍的連續額定壓力且自約3,〇〇〇磅/平方寸至約 5,0〇〇磅/平方寸的尖峰壓力之泵。可使用單程或多程(典型 為雙权)泵。新月形内部齒輪泵揭示於美國專利第丨,8 號(Tmninger為發明者,頒於…川年以%日卜第5,36〇325 號(亨利(Henry)等為發明者,美國海軍為受讓人,頒於Η% 年1 1月丨曰)’及第5,605,45 1號(Saitoh為發明者,Toky〇 Sintered N/丨etal Company Limited為受讓人,頒於 1997年2 月 25曰)。上述每一專利的揭示内容在此併入本文做為參考。 新月形内部齒輪泵可購自泵供應商,例如化〇 門羅、 北卡維萊納州、美國。 200302329 v ; p明說萌繽賀 每一個新月形内部齒輪泉矸由具習知可變或可調頻率驅 動的馬達所驅動,此種型式的頻率驅動器可容易地講自供 應商,如美國富士電機公司Saddle Brook,紐澤西州 美國q 特別設計以使用頻率驅動馬達的泵可購自通用電子工業系 統,Plainville,康乃迪克州,美國及BaldorElectncC〇mpany ’ Fort Smith,阿肯色州,美國。典型的頻率驅動器為型號 AF-3 00 G1 1,購自富士電機公司及通用電子工業系統q 根據本發明所測量之質量流率係藉由使用測量質量流率 之已知結構及操作原則的流量計,而非簡單的體積或線性 流率’且不會深受影響壓降的因素或與質量流率無關的其 他流量參數之因素所影響。各種形式的質量流量計為已知 且可商業購得,任何一種可用於本發明應用。這些形式的 流量計包括熱感式溫度計、電子流量計、及科氏型流量計。 科氏型流量計為較佳的。 在科氏型流量計中,質量流率要被測量的流體通過一管 子’其因來目電磁驅動器的正弦波電壓之導入而振盡。該 流動流體施以一科氏力於管子以修改振盪,通常使得沿管 子的點與沿管子的其他點異相振盪。差值直接與通過管子 的質量流率相關且被用做測量質量流率的方法。科氏型流 量計被揭示於文獻,例如美國專利第4,89 1,99 1號(Mattar等 為發明者,頒於1 9 9 0年1月9日),第4,9 1 1,0 2 0號(T h 〇 m p s ο η 為發明者,頒於1 990年3月27日),第5,048,350號(Hussain 等為發明者,頒於1991年9月17曰),及第5,054,3 26號(Mat tar 等為發明者,頒於1991年丨〇月8曰),所有受讓給Foxboro 200302329 發明說齊;繽罵发明 Description of the invention: (The description of the invention should state: the technical field to which the invention belongs, the prior art embodiments and the simple description of the drawings) Background of the invention I. Technical field Primitive month 7: In the field of fluid transfer systems, in order to control the flow And flow rate supply a variety of substances to the remote end. 2. Previous Skills At the construction sites and various types of commercial operations, two or more fluids need to be individually transmitted to the end of the tunnel and under controlled flow or flow rate. Examples of these operations are the repair of underground pipes by lining the inner surface of the pipeline or cracks in the wall of the grouting pipe. Other examples are places where the fluid or fluidized substance is supplied directly, such as buildings or construction sites such as bridges, parking lot structures, and building foundations. Other examples are the supply of materials to mines, manholes, underground tanks or reservoirs, subsea locations, and dams. An example of a substance that must be supplied individually and delivered under a bifurcation control ratio is a reactive component, where an early reaction must be avoided and the reaction stoichiometry must be maintained. Polymer systems, such as cymbals, polyurethanes, polyurethanes, and polypropylenes, are the main examples. Underground pipelines that carry water, sewage, or drainage are illustrative examples. These official lines are susceptible to deterioration due to decay, organic growth, rooting; participation, flow loading, ground movement, and general degradation. This degradation causes obstruction to the fluid passing through the pipeline and in some cases causes the pipeline to collapse. For example, the sewage pipe in the recovery can cause the sewage to leak out and pollute the surface water and soil formation, or it may cause the surface water to infiltrate and thus unnecessary increase the fluid to the treatment plant. Underground pipeline repairs are very expensive and replacement often requires significant ground disruption. 200302329 ⑺ 辕 Yuan: In order to avoid these interruptions, some underground pipeline repair methods have been developed that do not take the pipeline from the ground into a trench, and instead use remote control methods to apply the lining inside the pipeline. One method of lining in situ involves inserting a flexible tube lining (containing curable resin) into the pipeline. Once inserted, the lining is pressurized with fluid or air to press the lining against the inner wall of the pipe. , This is heated 'this step is a difficult step, because the uncured lining pipe cannot be operated in the pipe' and it is less complete to ensure that the pipe is properly placed or evenly pressed along its entire length to achieve the desired Repair degree. Another method of applying the inner layer by a remote device is to insert a long soft scum in the tube and spray the resin at the end of the pipeline through a nozzle to coat the inner wall of the tube 'so that the resin can be cured in place after being sprayed. Many of the resins applied in this way are two-component resins such as epoxy, polyurethane, and polyurea. To achieve the greatest effect, the two components of these reactive resin systems must be kept separate until they reach the point of application inside the tube, and therefore they must be cut off. The current type of pumping for this type of application is the use of a mechanical pair of proportional pumps. One of the difficulties of general two-component reactive resin systems and multi-component resin systems is that various components react at specific stoichiometric ratios, and any one of the meaning of / 7 will cause the presence of unreacted substances after the resin is matured. In addition to the unsatisfactory efficiency of the unreceived feed, 'the unreacted components remain in the resin = the moxibustion in the moxibustion is degraded'. In addition, the unreacted components will slowly pass through the two losses of the lining & pass 4 ^ speech line Of fluid. It is therefore important to maintain the correct stoichiometric ratio of the two components at the point of application in order to achieve maximum efficiency, quality of the lining, and women's quality. 200302329 (J) Invented by Binyi ~ ^ When using proportional pumps, 'acceptable control and flow ratio stability can only be achieved at pump flows below pump capacity, since most of the pulses (which are these pumps) Characteristics) can be eliminated by the accumulated pressure of the soft conduit between the pump and the nozzle and the spray nozzle itself before the next stroke is completed. This problem is particularly sensitive when there is little or no back pressure at the end of the catheter. However, typical millet capacity is less than 3 gallons per minute (0.7 cubic meters per hour). Thus, in order to reduce the pulsation of such pumps, the pump flow rate must be limited to about 1 gallon per minute (0.23 cubic meters per hour). This is acceptable for small diameter pipes, but for many sewer systems and other water The large pipe of the transfer system is not true. Proportional pumps also have limited variability in ratio adjustment, because they are mainly controlled by the pump ratio. Another difficulty of the two-component reaction system is that the component flow rate varies with viscosity, temperature, other factors affecting the component density, the degree of wear of the pump, and the condition of the flexible tubing used as the conduit. Flow is generally measured by differential pressure, and viscosity, temperature, and other factors described above affect differential pressure along the flow path and thus provide readings that are independent of changes in mass flow. It has been revealed that many components placed for contacting only at a remote location can be delivered to the component at a high degree of component flow rate control and the flow (including high volume flow) surrounding the Guangming Pavilion-Gonglihan M Temple. position. This hairpin Shida & existing in-situ application for pipe linings formed from multi-component lining materials and can be used at any designated location, including construction site, underground site, sea surface > site , And other high-speed backlash positions. This result consists of a kind of abundance; Su Yuan'7 ,,,, and Yuan Yuancheng, which includes individual crescent-shaped internal gear pumps with individual reaction components and a stream containing a volumetric flow rate that measures each mile's injury ( 4) 200302329 The flow rate controlled by measuring and comparing the measured value with the pre-selected value to correct the deviation from the pre-selected value can be transmitted to the unreachable construction site or the above by a multi-cavity cable for each individual cavity. The ends of the tubes are merged, where they can be dispersed. It is said that the control circuit of the automatic controller is called the bin truth value and generates a signal to adjust the pump speed. Taking V Camp 'as the remote location with individual components, it can be used inside the pipeline and any other applications. The components are merged and deposited and distributed at the inductive address. The crescent-shaped internal gears are provided. M > The stable flow of the medium pulse and the continuous variability of the flow rate are adjusted by allowing the flow rate of α and α to allow the correction of small deviations from the desired ratio without the need to consider device-based restrictions on this week . This mass flow is controlled by Zengwu Baili instead of differential pressure. Mass flow control allows the reaction chemistries to be maintained continuously and accurately and avoids the influence of components based on bifurcation or Adjustment of pressure drop rather than temporary Θ factor. In some applications, it may include system components in addition to the main reaction components to improve the properties of chemicals and materials, such as the physical and chemical characteristics of the liner (in the case of pipelines), or to accelerate the reaction rate, Or any number or characteristic of the improved method. The system of the present invention can selectively use these additional components by sending them individually and passing them under application-controlled flows in the same manner as the main components. These and other features, advantages, and specific embodiments of the present invention are described in more detail in subsequent sections of this patent specification. Implementation of the crescent-shaped internal #wheel pump with two circular gears, that is, an external gear with inwardly extending teeth that meshes with the outwardly extending teeth of the internal gear 200302329 ' Both gears rotate on the same casing but on different parallel vehicles (which make the gears eccentric), leaving a crescent-shaped space in between. Most of the crescent-shaped space is occupied by a crescent-shaped insert, which provides an adjacent gap between itself and the tooth tip of the gear. Either gear can be used as the drive gear, although internal gears are preferred as the drive gear. When the teeth of the gear leave from the meshing place, they create a gap, and when the gear rotates, the gap expands to generate suction ' to attract fluid into the space between the gears and thus into the pump. When the gear returns to the meshing position, the volume near the teeth decreases, thereby increasing the pressure and allowing the fluid to flow out through the discharge end. From this, the flow rate can be determined by the gear rotation speed. A typical crescent-shaped internal gear pump has thirteen internal gears. There are seventeen teeth in the external gear, operating at a speed from about 400 to about 6,000 revolutions per minute, preferably from about 700 to about 3,600 revolutions per minute, and with female rotation A displacement of about 0.3 square inches to about 15 square inches (about 0.05 liters to about 0 liters). The preferred pump is a continuous rated pressure with a range from about 2,000 psi / square inch to about 6,000 pounds per square inch and from about 3,000 pounds per square inch to about 5, A pump with a peak pressure of 1000 psi. One-way or multi-pass (typically double weight) pumps can be used. Crescent internal gear pumps are disclosed in US Patent No. 丨 8 (Tmninger is the inventor and was issued in … In the year of the year, No. 5,36,0325 (Henry, etc. as the inventor, the United States Navy as the assignee, awarded in January 1 年%), and No. 5,605,45 1 (Saitoh is the inventor and Toky〇Sintered N / 丨 etal Company Limited is the assignee, issued on February 25, 1997.) The disclosure of each of the above patents is incorporated herein by reference. Crescent interior Gear pumps can be purchased from pump suppliers, such as Chemicals Monroe, North Carolina, United States. 200302329 v; p said that every crescent-shaped internal gear spring of Meng Binhe is variable or adjustable by the conventional Driven by a frequency-driven motor, this type of frequency driver can be easily spoken from a supplier, such as Fuji Electric, Saddle Brook, New York A pump specifically designed to use a frequency-driven motor in the Western United States is available from General Electronic Industries, Plainville, Connecticut, USA and BaldorElectnccomany Fort Fort, Arkansas, USA. A typical frequency driver is model AF- 3 00 G1 1, purchased from Fuji Electric Corporation and General Electronic Industrial System q The mass flow rate measured according to the present invention is a flow meter using a known structure and operating principle for measuring mass flow rate, rather than a simple volume or 'Linear flow rate' without being deeply affected by factors such as pressure drop or other flow parameters that are not related to mass flow rate. Various forms of mass flow meters are known and commercially available, and any of them can be used in the present invention Applications. These types of flowmeters include thermal thermometers, electronic flowmeters, and Coriolis flowmeters. Coriolis flowmeters are preferred. In Coriolis flowmeters, the fluid whose mass flow rate is to be measured By a tube, which is completely vibrated by the introduction of the sine wave voltage of the electromagnetic drive of the eye. The flowing fluid exerts a Coriolis force on the tube to modify the oscillation, Often the points along the pipe are oscillated out of phase with other points along the pipe. The difference is directly related to the mass flow rate through the pipe and is used as a method of measuring the mass flow rate. Coriolis type flowmeters are disclosed in the literature, such as US patent No. 4,89 1,99 1 (Mattar and others are inventors, issued on January 9, 1990), and No. 4,9 1 1, 0 2 0 (T h 〇mps ο η is the inventor , Issued on March 27, 1990), No. 5,048,350 (Hussain and others are inventors, issued on September 17, 1991), and No. 5,054,3 26 (Mat tar and others are inventors, awarded in 1991丨 〇 8 月 年), all transferees to Foxboro 200302329 inventions are all here;

Company, Foxboro,麻州,美國,及美國專利第4,49 1,〇25號 (史密司等為發明者’頒於1 985年1月1曰)及Re 3丨,450(史密 司等為發明者’頒於1982年2月11日),二者受讓給Micro Motion, Inc, Boulder,科羅拉多州,美國。此章節的每一個專 利的揭示内容在此併入本文做為參考。科氏型質量流量計 可購自儀為供應商’如En dr ess + Hauser, Inc.,Greenwood, 印第女納州,美國及美國Y〇k〇gawa公司,Newnan,喬治亞 州,美國。 自動程序控制可由習知軟體達到,其可由熟知化學程序 電fe控制之使用的任何人容易地程式化。可有效使用的軟Company, Foxboro, Massachusetts, United States, and U.S. Patent No. 4,49 1,025 (Smith and others are inventors' issued on January 1, 1985) and Re 3, 450 (Smith Etc. was awarded by the inventor on February 11, 1982), and both were transferred to Micro Motion, Inc, Boulder, Colorado, USA. The disclosure of each patent in this section is incorporated herein by reference. Coriolis-type mass flowmeters are available from suppliers ’such as En dress + Hauser, Inc., Greenwood, Indiana, USA and Yokogawa Corporation, Newnan, Georgia, USA. Automatic program control can be achieved by conventional software, which can be easily programmed by anyone familiar with the use of chemical programs. Effectively used software

體的一個貫例為在個人電腦(如IBM相容電腦)的LabvIEW 程序控制軟體。 個別反應成份至應用位址的傳遞(可為管線内部或其他 退距或然法到達的位置)可由使用習知流體流動導管達到 導管維持成份分開 直到它們到達應用位址。在管線内 部的情況下,齡估沾嗜泣& ^ 一 毕乂仏的夺官為能藉由遠距驅動器在控制速度An example of this is LabvIEW program control software on a personal computer (such as an IBM compatible computer). The transfer of individual reaction components to the application site (which can be inside the pipeline or other back-off or otherwise reachable locations) can be achieved using conventional fluid flow conduits to maintain the components separated until they reach the application site. In the case of the inside of the pipeline, the age is estimated to be somber & ^ 1 Bi Bi's win is to control the speed by a long-range drive

以使所欲厚度的塗層可沿管壁被沉積 官的末端合併,於此它們以混合物向外 址沉積並同時彼此反應。可使用個別導 一種多腔纜線(在工業界一般稱為“臍帶 道料管線。較佳的多腔纜線含用於内襯 用於溫度控制的額外腔,例如熱水或任 質的循環,亦可包括其他腔以用做其他 力至在纜線末端的電力設施集管,容納 (8) 200302329So that the coatings of the desired thickness can be merged along the tube wall by the ends of the deposition officers, where they are deposited as a mixture to the outside and simultaneously react with each other. A multi-cavity cable can be used individually (commonly referred to in the industry as the "umbilical dosing line." A preferred multi-cavity cable contains additional cavities for lining for temperature control, such as hot water or any kind of circulation , Can also include other cavities for other forces to the power facility header at the end of the cable, to accommodate (8) 200302329

溫度及壓力傳感器,自溫度及壓力傳感器接收及 ,日 α 琴虎 ,提供訊號傳輸如影像訊號以使得設施的位 " 且〜彳冢可於遠 處(如地上)監視器觀看,提供在纜線末端的機械器具的允 制,及供應f力至光源以加強影響傳送器^ 、 在多腔纜線末端的器具可為合併成份並將它們導入所於 應用位址的任何裝置。在本發明施用管線内襯的具體實施 例中,為具可為噴霧噴嘴,可為無空氣的或是空氣輔助的 ,通風裝置、離心鑄塑裝置、或能導引混合物均勻分佈於 管線周圍的任何其他射出裝置。對需要36〇度施用的本發明 應用,旋轉噴霧器為較佳的,特別是具兩個同時以反方向 轉動的轉子之噴霧器。在管線内部應用中,其避免或最小 化任何塗層厚度變化,其可能沿突起或在管壁表面的不規 鬌 則處形成。噴霧器可裝設於觸輪上’此處使用的此名稱表Temperature and pressure sensors, received from the temperature and pressure sensors, and Japanese α 琴 虎, provide signal transmission such as image signals so that the location of the facility " and ~ 彳 tsuka can be viewed from a distant (such as above ground) monitor, provided on the cable Allowance of mechanical devices at the end of the line, and the supply of f-forces to the light source to enhance the effect of the transmitter ^, the devices at the end of the multi-cavity cable can be components that incorporate and direct them to any device at the application site. In the specific embodiment of the application of the pipeline lining of the present invention, the nozzle may be a spray nozzle, may be airless or air-assisted, a ventilating device, a centrifugal casting device, or one capable of guiding the mixture to be evenly distributed around the pipeline. Any other injection device. For applications of the present invention that require a 360 degree application, a rotary sprayer is preferred, especially a sprayer with two rotors rotating in opposite directions simultaneously. In pipeline applications, it avoids or minimizes any change in coating thickness, which may form along protrusions or irregularities on the surface of the pipe wall. The sprayer can be mounted on the touch wheel ’This name list used here

不任何可移動的支撐物’其可以最少阻力沿管子長度移動 並固定噴霧器於約管線中心,以當導管被拉引通過管線時 ’噴霧器沿管軸移動。 本發明可應用於由二或更多成份反應所形成的組合物之 沉積,且因此成份在接觸時反應,故必須避免接觸直到它 們到達施用點’以避免提早反應,此敘述應用於許多聚合 物°實例為雨成份聚合物系統,包括,但不限於,環氡類 、聚氨酯類、聚脲類、及聚酯類,環氧類為特別重要的, 特別是於管線内襯施用。為達最適性能,維持個別成份在 預先選擇範圍内的溫度以控制黏度及維持均勻的一致性。 根據本發明系統亦可包括額外泵及傳遞管線以供應額外 -13 - 200302329 唠軸績薦 成份至地面上的混合點或經由在多腔纜線的個別腔至施用 位址。對聚合物系統,此種額外成份包括調節劑如膠凝劑 、促進劑、觸媒、及稀釋劑、或任何可被用來控制反應速 率或聚合物塗層的物理或化學特性之成份。 維然本發明可以許多不同結構及安裝進行,於圖1說明的 系統表示管線内襯系統且用做說明用途。在此系統中,兩 成份聚合物的兩個成份被儲存於個別的調節槽1丨及1 7,每 一個為套層容器,套層以來自鍋爐1 3的熱水供應,熱水自 銷爐13以個別的水泵14、15送至套層。容器亦以惰性氣體 盍覆。形成聚合物的兩個成份自調節槽以初步泵1 6、‘ 1 7引 出,在此實例中其為習知的三螺旋槳泵,合適實品可講自 I πι ο P u m p及其他泵供應商。螺旋槳粟經由循環迴路1 8J 9 將成份經由調節槽循環。 每一成份流體再由新月形内部齒輪泵2 1、2 2自循環管線 引出’粟將成份送至多腔或“齡帶纟覽線2 3的個別腔。由新 月形内部齒輪泵產生的質量流率由個別科氏型流量計24 、2 5偵測。在每^一個新月形内部齒輪栗出口管線的三向闕 26、27使得泵輸出可被導引回循環迴路18、19或至臍帶缓 線。 臍帶纜(線2 3的地上部份裝設於捲軸2 8並由線型纟覽線晕引 裝置29(其控制纜線的直線速度)引至捲軸或自捲軸弓丨出。 缓線溫度由自鋼爐1 3以水泵3 0個別供應之熱水控制。或是 ’纜線溫度亦可由沿纜線長度延伸的電加熱器(未示出)控 制。在臍帶纜線的末端為影像照相機3 4、靜態或動態混合 -14 - 200302329Without any movable support, it can move along the length of the pipe with minimum resistance and fix the sprayer about the center of the pipeline so that when the catheter is pulled through the pipeline, the sprayer moves along the axis of the tube. The present invention can be applied to the deposition of a composition formed by the reaction of two or more ingredients, and therefore the ingredients react when contacted, so contact must be avoided until they reach the point of application 'to avoid early reactions. This statement applies to many polymers ° Examples are rain component polymer systems, including, but not limited to, cyclic, polyurethane, polyurea, and polyester. Epoxy is particularly important, especially for line lining applications. For optimum performance, maintain the temperature of individual ingredients in a preselected range to control viscosity and maintain uniform consistency. The system according to the present invention may also include additional pumps and transfer lines to supply additional -13-200302329 stern shaft recommended components to a mixing point on the ground or via individual cavities in a multi-cavity cable to the application site. For polymer systems, such additional components include modifiers such as gelling agents, accelerators, catalysts, and diluents, or any component that can be used to control the rate of reaction or the physical or chemical characteristics of the polymer coating. Although the present invention can be carried out in many different structures and installations, the system illustrated in Figure 1 represents a pipeline lining system and is used for illustrative purposes. In this system, the two components of the two-component polymer are stored in individual adjustment tanks 1 and 17; each is a jacketed container, and the jacket is supplied with hot water from the boiler 13; 13 is sent to the jacket by individual pumps 14,15. The container is also covered with an inert gas. The two components that form the polymer are self-adjusting tanks that are led out by the preliminary pumps 16 and '17. In this example, they are the conventional three-propeller pumps. The suitable products can be said from I π Pump and other pump suppliers. . The propeller mill circulates the ingredients through a regulating tank via a circulation circuit 1 8J 9. Each component fluid is drawn from the crescent-shaped internal gear pump 2 1, 2 2 from the circulation line to send the component to the multi-chamber or individual cavity of the "age band view line 2 3". Produced by the crescent-shaped internal gear pump The mass flow rate is detected by individual Coriolis flowmeters 24, 25. The three-way 阙 26, 27 of each crescent-shaped internal gear pump outlet line allows the pump output to be directed back to the circulation circuit 18, 19 or To the umbilical cord. The umbilical cable (the above-ground part of the line 23 is installed on the reel 28 and guided by the linear view line halo guide 29 (which controls the linear speed of the cable) to the reel or from the reel bow. The temperature of the slow line is controlled by hot water supplied separately from the steel furnace 13 and the pump 30. Alternatively, the temperature of the cable can also be controlled by an electric heater (not shown) extending along the length of the cable. At the end of the umbilical cable For Image Camera 3 4, Static or Dynamic Mix-14-200302329

(ΊΟ) ^ 3 1及位於觸輪3 3上的器具集管3 2。亦包括影像照相機3 4 以在塗覆方法前及期間能觀察管子内部。 裎序避輯控制器4 1接收來自質量流量計24、25及系统中 各個資料收集點的訊號,如溫度計、壓力傳感器、纜線速 度才曰示為、及液體液位指示器(其在圖中未示出),並傳送 訊號至各組件如新月形内部齒輪泵及線型纜線牽引裝置以 控制伴隨這些組件的程序參數。如上所述,可增加額外成 份的額外進料管線以併入臍帶或在進入臍帶前或沿圖中所 示製程流體管線的任何點與系統成份混合。 圖2說明適合輸送兩成份反應聚合物(如本發明應用的環 氧)的臍帶(或多腔)纜線5 1的實例。圖中所示戴面積顯示纜 線包括由植入於聚合物的銅編織線所組成的外部護套5 2。 含有兩個腔5 3、5 4以輸送内襯組合物的個別成份,含有額 外腔55、56以循環熱水,這些為在末端接合的密閉腔,一 個用於進入流,一個用於回流。剩餘的腔由電力線、感應 為線、控制器線、及影像纟覽線所佔據。可增加額外的流動腔 以輸送調節劑或其他添加劑至要施用的聚合物組合物。 先前敘述主要用做說明用途’仍具體化本發明基本元件 的其他變化及修改可容易地為熟知本技藝者所知且包含於 本發明範圍。 圖式簡略說明 圖1為根據本發明的官線内概糸統的程序流程圖。 圖2為多腔纜線的截面圖,其合適用於經由地下管線傳遞 管線内襯組合物的個別成份。 200302329(ΊΟ) ^ 31 and the appliance header 32 on the touch wheel 33. An image camera 3 4 is also included to view the inside of the tube before and during the coating process. The sequence avoidance controller 41 receives signals from mass flow meters 24, 25 and various data collection points in the system, such as thermometers, pressure sensors, cable speeds, and liquid level indicators (which are shown in the figure). (Not shown), and send signals to components such as a crescent-shaped internal gear pump and a linear cable traction device to control the program parameters accompanying these components. As mentioned above, additional feed lines for additional components can be added to incorporate the umbilical cord or mix with system components before entering the umbilical cord or along any point of the process fluid line shown in the figure. Figure 2 illustrates an example of an umbilical (or multi-cavity) cable 51 suitable for transporting a two-component reactive polymer such as the oxygen used in the present invention. The wearing area shown in the figure shows that the cable includes an outer sheath 52 composed of a copper braided wire implanted in a polymer. Contains two cavities 5 3, 5 4 to convey individual components of the lining composition, and additional cavities 55, 56 to circulate hot water. These are closed cavities joined at the ends, one for incoming flow and one for back flow. The remaining cavities are occupied by power lines, sensor lines, controller lines, and image viewing lines. An additional flow chamber may be added to deliver a conditioner or other additive to the polymer composition to be applied. The foregoing description is mainly for illustrative purposes. Other variations and modifications that still embody the basic elements of the present invention can be easily known to those skilled in the art and are included in the scope of the present invention. BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a flow chart of a general system in an official line according to the present invention. Figure 2 is a cross-sectional view of a multi-cavity cable suitable for transferring individual components of a pipeline lining composition via an underground pipeline. 200302329

圖式代表符號說明 11, 12 調節槽 13 鍋爐 14, 15, 30 水泵 16, 17 初步粟 18, 19 循環迴路 21, 22 新月形内部齒輪泵 23, 5 1 臍帶纜線 24, 25 科氏型流量計 26, 27 三向闊 28 1 捲軸 29 線型纜線牽引裝置 3 1 混合器 32 器具集管 3 3 觸輪 3 4 影像照相機 4 1 程序邏輯控制器 52 外部護套 53, 54, 55, 56 腔 發明·翻:·纜頁·Explanation of Symbols in the Drawings 11, 12 Regulating Tanks 13 Boilers 14, 15, 30 Water Pumps 16, 17 Preliminary Mills 18, 19 Circulation Circuits 21, 22 Crescent Internal Gear Pumps 23, 5 1 Umbilical Cables 24, 25 Coriolis Type Flowmeter 26, 27 Three-way wide 28 1 Reel 29 Linear cable traction device 3 1 Mixer 32 Apparatus header 3 3 Touch wheel 3 4 Video camera 4 1 Program logic controller 52 Outer sheath 53, 54, 55, 56 Cavity Invention · Turn: · Cable Sheet ·

-16 --16-

Claims (1)

200302329 拾、申請專利範圍 1 · 一種將許多反應流體在控制流量下傳遞至遠距應用位 址而無提早反應的系統,該系統包括: 許多健槽,每一個儲槽容納一種該反應流體,且每一 個該儲槽具獨立的出口管線以排出該儲槽的内容物; 在每一個該獨立的出口管線有新月形内部齒輪泵以在 每一個該反應流體的選擇流速下分別產生獨立的流動 流體; 質量流率測量裝置以連續測量每一個獨立流動流體的 質量流率及產生由此測得代表每一個質量流率的獨立 訊號; 。單一自動控制器’其接收所有該獨立訊號,比較該訊 號與目標值,並控制每一個新月形内部齒輪泵的速度以 修正與該目標值的偏差; ’個別傳遞該輸出流體至該遠距應用位址,及在該遠距 應用位址合併該輸出流體;及200302329 Patent application scope 1 · A system that transfers a large number of reaction fluids to a remote application site under a controlled flow without early reaction, the system includes: a number of robust tanks, each of which holds one of the reaction fluid, and Each of the storage tanks has an independent outlet line to discharge the contents of the storage tank; there is a crescent-shaped internal gear pump at each of the independent outlet lines to generate independent flows at each selected flow rate of the reaction fluid Fluid; The mass flow rate measuring device continuously measures the mass flow rate of each independently flowing fluid and generates an independent signal representative of each mass flow rate measured thereby; A single automatic controller 'receives all the independent signals, compares the signals with the target value, and controls the speed of each crescent-shaped internal gear pump to correct the deviation from the target value;' individually transfers the output fluid to the long distance An application address, and merging the output fluid at the remote application address; and 傳^衣置以個別接收該新月形内部齒輪泵的輸出流體 弓位址分散該合併的輸出流體。 A系統’其中該質量流率測量 型質量流量計,在每一個該出 統,其中該每一個該出口 自該循環迴路弓丨出反應流體的支流 1形内部齒輪泵裝設在該支流流體。 200302329 申議專刹範圜繽買 4.根據申請專利範圍第1項的系統更包括許多個別的變頻 驅動馬達’每一個該新月形内部齒輪泵由一個該馬達驅 動’該控制器藉由調整該變頻驅動馬達的頻率以控制該 新月形内部齒輪泵的速度。 )·根據申請專利範圍第1項的系統,其中該傳遞裝置針對 每一個輸出流體包括具有個別腔之多腔纜線。 統’其中每一個該新月形The gears receive the output fluid of the crescent-shaped internal gear pump individually, and the combined output fluid is dispersed by the bow address. A system 'wherein the mass flow rate measurement type mass flowmeter is in each of the systems, wherein each of the outlets discharges a branch stream of the reaction fluid from the circulation loop and a 1-shaped internal gear pump is installed in the branch stream. 200302329 Applying for a special brake fan 圜 bin buy 4. The system according to item 1 of the scope of patent application also includes a number of individual variable frequency drive motors 'Each of the crescent-shaped internal gear pump is driven by one of the motors' The controller is adjusted by The frequency drives the frequency of the motor to control the speed of the crescent-shaped internal gear pump. ). The system according to item 1 of the patent application, wherein the delivery device includes a multi-lumen cable with individual lumens for each output fluid. System ’each of the crescents 方寸的尖峰壓力。 6‘根據申請專利範圍第1項的系統 7. 根據申請專利範圍第1項的系 地下管拉引該傳遞裝置。 8. 根據申請專利範圍第5項的系 統更包括牽引裝置以經由 纜線為溫度控制的 cSquare inch spike pressure. 6 ’System according to item 1 of the scope of patent application 7. System according to item 1 of the scope of patent application The underground pipe pulls the transfer device. 8. The system according to item 5 of the scope of patent application further includes a traction device for temperature control via a cable c 該應用裝置間的混合器裝置 統’其中該儲槽及該多腔 ’其中該多腔纜線更包 溫度控制之水循環腔。 t包括在該多腔纜線及The mixer device between the application devices includes the storage tank and the multi-chamber. The multi-chamber cable further includes a temperature-controlled water circulation chamber. t Included in the multi-cavity cable and
TW091137491A 2001-12-27 2002-12-26 System and method for delivering reactive fluids to remote application sites TW200302329A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US10/033,704 US20030124030A1 (en) 2001-12-27 2001-12-27 System and method for delivering reactive fluids to remote application sites

Publications (1)

Publication Number Publication Date
TW200302329A true TW200302329A (en) 2003-08-01

Family

ID=21871972

Family Applications (1)

Application Number Title Priority Date Filing Date
TW091137491A TW200302329A (en) 2001-12-27 2002-12-26 System and method for delivering reactive fluids to remote application sites

Country Status (4)

Country Link
US (1) US20030124030A1 (en)
AU (1) AU2002361888A1 (en)
TW (1) TW200302329A (en)
WO (1) WO2003057357A2 (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6986813B2 (en) * 2003-04-04 2006-01-17 Visuron Technologies, Inc. Sprayed in place pipe lining apparatus and method thereof
US20090207687A1 (en) * 2005-10-03 2009-08-20 Honeywell International Inc. Apparatus and method for preparing ultrapure solvent blends
AU2007219055B2 (en) * 2006-02-23 2011-03-03 David Man Chu Lau An industrial process efficiency method and system
HK1086984A2 (en) * 2006-02-23 2006-09-29 David Man Chu Lau An industrial process efficiency method and system
CH701245B1 (en) * 2009-06-11 2013-05-31 Stefan Schonert Plant for the filling of the liner tubes.
US8925627B2 (en) * 2010-07-07 2015-01-06 Composite Technology Development, Inc. Coiled umbilical tubing
US8522881B2 (en) 2011-05-19 2013-09-03 Composite Technology Development, Inc. Thermal hydrate preventer
CN107850071B (en) * 2015-08-11 2021-01-22 开利公司 Screw compressor economizer plenum for pulsation reduction

Family Cites Families (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2694367A (en) * 1950-11-01 1954-11-16 Paragon Gear Works Inc Rotary pump
US3491698A (en) * 1966-07-01 1970-01-27 Truninger Ag Gear pump
US4209258A (en) * 1978-02-14 1980-06-24 Oakes W Peter Automatic continuous mixer apparatus
GB2120351B (en) * 1982-05-14 1985-10-30 Ram Services Ltd Pipe linings
FR2587738B1 (en) * 1985-09-25 1988-02-19 Saint Gobain Isover REPAIR OF BONDING COMPOSITIONS FOR MINERAL FIBERS
US5141156A (en) * 1987-12-21 1992-08-25 Union Carbide Chemicals & Plastics Technology Corporation Methods and apparatus for obtaining a feathered spray when spraying liquids by airless techniques
DE3829059A1 (en) * 1988-08-26 1990-03-08 Danfoss As FLOW MEASURING DEVICE WORKING ACCORDING TO THE CORIOLIS PRINCIPLE
US4996940A (en) * 1989-11-17 1991-03-05 Cleary John J Method and apparatus for internally coating and strengthening conduit
US5879499A (en) * 1996-06-17 1999-03-09 Heartport, Inc. Method of manufacture of a multi-lumen catheter
CA2082565A1 (en) * 1991-11-12 1993-05-13 John N. Argyropoulos Polyester particularly suitable for use in coating compositions which are sprayed with compressed fluids as viscosity reducing diluents
US5405218A (en) * 1992-05-05 1995-04-11 Foamseal Inc Method for the repair of existing manholes using elastomeric materials
US5290603A (en) * 1992-12-18 1994-03-01 Union Carbide Chemicals & Plastics Technology Corporation Method for spraying polymeric compositions with reduced solvent emission and enhanced atomization
US5360325A (en) * 1993-09-30 1994-11-01 The United States Of America As Represented By The Secretary Of The Navy Gear pump with reduced fluid-borne noise
DE69530651T2 (en) * 1994-10-31 2004-03-25 Tdk Corp. Manufacturing process of ceramic electronic components and device for manufacturing
JP2654373B2 (en) * 1995-03-14 1997-09-17 東京焼結金属株式会社 Internal gear type fluid device
US5763734A (en) * 1995-10-19 1998-06-09 Nachtman; Thomas J. Method for containing or removing contaminants from a substrate
US6280692B1 (en) * 1996-08-02 2001-08-28 Blentek Systems, Inc. Open-loop apparatus for producing a controlled blend of polyol and blowing agent for use in the manufacture of polyurethane foam
EP0923524A1 (en) * 1996-08-21 1999-06-23 Twenty-First Century Research Corporation Methods and devices for controlling the reaction by adjusting the oxidant consumption rate
US5996650A (en) * 1996-11-15 1999-12-07 Oden Corporation Net mass liquid filler
US6249708B1 (en) * 1997-08-26 2001-06-19 Angeion Corporation Fluted channel construction for a multi-conductor catheter lead
US5925053A (en) * 1997-09-02 1999-07-20 Children's Medical Center Corporation Multi-lumen polymeric guidance channel, method for promoting nerve regeneration, and method of manufacturing a multi-lumen nerve guidance channel
JP3214408B2 (en) * 1997-09-09 2001-10-02 株式会社村田製作所 Method and apparatus for producing ceramic green sheet
US5887975A (en) * 1997-09-30 1999-03-30 The Boeing Company Multiple component in-line paint mixing system
US6149071A (en) * 1998-06-10 2000-11-21 Global Metering Solutions, Llc Flow control system for spray applications
US6231795B1 (en) * 1998-12-04 2001-05-15 The Dow Chemical Company Soft and flexible foams made from blends of alkenyl aromatic polymers and alpha-olefin/vinyl or vinylidene aromatic and/or sterically hindered aliphatic or cycloaliphatic vinyl or vinylidene interpolymers
US6264113B1 (en) * 1999-07-19 2001-07-24 Steelcase Inc. Fluid spraying system

Also Published As

Publication number Publication date
WO2003057357A2 (en) 2003-07-17
WO2003057357A3 (en) 2003-10-23
AU2002361888A8 (en) 2003-07-24
AU2002361888A1 (en) 2003-07-24
US20030124030A1 (en) 2003-07-03

Similar Documents

Publication Publication Date Title
TW200302329A (en) System and method for delivering reactive fluids to remote application sites
CN105643801B (en) A kind of controlling temp type concrete central mix plant
US6632475B1 (en) Method of lining underground pipes and apparatus for performing the method
JP5068756B2 (en) Control system for combining materials
AU2012354278B2 (en) Device and a method for applying a hardenable plastics coating in a tubular construction
JPH01301122A (en) System for feeding and measuring component
EP0094819B1 (en) Pipe linings
WO2019167862A1 (en) Pipeline mixer and method for manufacturing and supplying mixture using same
US6116578A (en) Method for inserting a cable in a duct
US20040243068A1 (en) Apparatus for applying multi-component liquid liner compositions to the inner surfaces of conduits and methods of applying same
CN107387121A (en) The all-hydraulic coupling control system of novel double liquid grout injecting
US9168552B2 (en) Spray system for application of adhesive to a stator tube
JP2012016946A (en) Method for regenerating existing pipe, piping handling machine, pressure pump, and device for supplying back-filling material
CN100412432C (en) Pushing technique capable of reducing friction around pipe
CN1695823A (en) Device system and method for delivering active fluids to remote application sites
FR2715084A1 (en) Method and device for applying a coating in a buried pipe
CN107150014B (en) Method and device for applying paint in pipeline
US20210222817A1 (en) Dry pipe rehabilitation spincaster
RU2015144758A (en) System and method for coating
KR101131338B1 (en) Apparatus for repairing pipelines and facilities having the function of mortar compressive injection and plastering and method for repairing pipelines and facilities using the same
JP2002327597A (en) Method and apparatus for injecting lubricant for jacking method
US20040188538A1 (en) Application head for applying a liquefied liner to a vessel interior
CN117090186A (en) Soil body on-site solidification bidirectional stirring equipment and beach area foundation solidification method
JP2005238176A (en) Apparatus for applying sulfur spray material
JP5770552B2 (en) Pipe making simultaneous backfilling material injection device