Method and equipment to perform controlled access to the projected location inside a storage tank, while it is operated, idle, or undergoing maintenance, to conduct an internal service from outside
20220080474 · 2022-03-17
Inventors
Cpc classification
B08B9/0808
PERFORMING OPERATIONS; TRANSPORTING
B05D7/227
PERFORMING OPERATIONS; TRANSPORTING
B08B13/00
PERFORMING OPERATIONS; TRANSPORTING
B08B9/0813
PERFORMING OPERATIONS; TRANSPORTING
B08B2209/08
PERFORMING OPERATIONS; TRANSPORTING
B08B9/0933
PERFORMING OPERATIONS; TRANSPORTING
International classification
B08B9/08
PERFORMING OPERATIONS; TRANSPORTING
B01D21/00
PERFORMING OPERATIONS; TRANSPORTING
B05D7/22
PERFORMING OPERATIONS; TRANSPORTING
Abstract
Method and equipment to perform controlled access to the projected location inside a storage tank, while it is operated, idle, or undergoing maintenance, to conduct an internal service from outside. This intervention from outside can be performed through an access opening in the wall or roof of the tank. In addition to other innovations, a new coiled tubing (CT) solution for multiple 3D positioning arrangements outside and inside the tank is provided for both positioning, inserting, remote control, and withdrawing the CT with the active head for the controlled accessing of the target area.
Claims
1. Method and equipment to perform the access to the projected location inside a fluid, solids, or the mixture of fluid and solids storage tank, while it is operated, idle, or undergoing maintenance, to make an internal service from outside, which comprises controlled introduction into the tank from the wall or a roof access point outside of the tank through a guide unit placed on the access point and/or beyond it, using the coiled tubing (CT) with the active head on the end, and the CT drive on the other end which provides controlled reciprocating movement of the CT active head inside the tank under different angles in 3D projections set by the variable guide mounted on the access point and/or a diverter inside the tank and/or angled jet nozzles to cover a whole target area.
2. The method as claimed in claim 1 when through the active head as a nozzle agitating or/and cleaning fluid is delivered inside the tank with sediments by means a pump to make a slurry movable or/and pumping out the made slurry by the vacuum unit from the outside source.
3. The method as claimed in claim 2 when fluid is represented by fluid stored in the tank and circulated through the CT from the other access point or drain to the active head.
4. The method as claimed in claim 1 when the CT is used to remove, and recovery treated sludge or dispersed deposits by means of the vacuum unit combined with the CT guiding unit.
5. The method as claimed in claims 2 and 4 when cleaning/agitating fluid is directed to pumping out treated area of the first CT by the other CT through the appropriate tank access point.
6. The method as claimed in claims 3 and 4 when cleaning fluid circulated through double concentric tubing, where inside tubing is CT which used for injection cleaning fluid and annulus to vacuum treated sludge or dispersed deposits.
7. The method as claimed in claims 2, 3, 4, 5, and 6 when cleaning/agitating fluid is heated.
8. The method as claimed in claim 1 when CT intervention monitored and controlled by the measuring of the pressure, vibration, bending stress, and temperature through fiber optic cable, or any other sensors or technology applied on the surface around of the outside tank wall on the height between the tank bottom and the intervention point elevation.
9. The method as claimed in claim 1 when the CT active head represented by the testing end which provides a specific survey of the defined area of the tank.
10. The method as claimed in claim 1 when the CT active head provides a delivery of the repair material to the defined maintain area of the tank.
11. The method as claimed in claims 2, 3, 4, 5, and 6 when cleaning/agitating fluid type and/or composition are customized depending on the nature, composition, chemical and rheological properties of the sediment.
12. The method as claimed in claims 2, 3, 4, 5, and 6 when cleaning/agitating fluid type and composition are modified during the cleaning process to optimize the process performance and efficiency.
13. A device for the controlled access into the tank, comprising the CT with the active head introducing in the tank through the variable guide unit on the access point connected with a delivery guide with the rotatable hydraulically moved guiding tube, and another end of the CT powered by the CT drive unit for moving CT to the delivery system.
14. A device, as claimed in claim 13 having the diverter for the CT on the head of the guiding tube which being introduced inside the tank allows to control direction of the CT active head movement.
15. A device, as claimed in claim 13, having as the active head nozzles and/or scraper vanes or rotating blades depending on the density of deposit.
16. A device, as claimed in claim 13, comprising a guide unit on the roof manway for putting CT from outside the tank having nozzle and/or rotating vanes or blades as the active head angled into the floor and/or the wall of the tank.
17. A device, as claimed in claim 13 in which the CT and all surfaces liable to be brought into contact with the interior surface of the tank are composed or/and covered by the material which is flexible and/or slide easily and give protection against scratching on the said interior surface of the said tank.
18. A device, as claimed in claim 13 having as active head the nozzle that can orient the flow for changing the position of the CT inside the tank with the maximum volume and surface coverage.
19. A device, as claimed in claim 13 having as the active head the sampling unit which provides an insulation and delivery of the samples from the defined area of the tank.
20. A device, as claimed in claim 13 having as the active head a placement unit to deliver repair material to the defined area of the tank.
21. A device, as claimed in claim 13 having as the active head ultrasound, sonar, or radio sensors for CT intervention monitoring and controlling.
22. A device for CT intervention monitoring and controlling by the measuring of the pressure, vibration, and temperature through fiber optic cable placed on the outside tank wall and equipped with decoding unit to define pressure, vibration, and/or temperature changes and locate the active head position and tank's treatment response.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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DETAILED DESCRIPTION OF THE INVENTION
[0022] All processes of the invention are based on CT solution which was adopted for internal storage service.
[0023] At
[0024]
[0025]
[0026] The wall entry with the delivery guide unit is shown in
[0027] The delivery guide unit composes of the driving unit with delivery cylinder 21 of the hydraulic drive powered by pump 23 and drive cylinder 22 for reciprocating displacement guiding tube 20 by attached rod 24. The drive cylinder is attached to the delivery cylinder which in turn insulates the guiding tube and tank space by the stuffing box 26 while the operation inside the tank is performed. The hydraulically driven guiding tube with the nozzle when being inside the tank can be angled by the rotating of the guiding tube 20 when the CT is detached from valve 27 and rod 24 reconnected from the guiding tube to the other holder 25. There is valve 28 to connect tank volume to the outside reservoir for pumping out the washed waste material from the tank when vacuum pipe is connected to this valve or dispersed sediments and the waste material can be pumped out through drain 15 commonly located in the tank bottom.
[0028] The active head for manageable treatment the inside volume of the storage tank is represented in
[0029] The source/receiver equipment location for CT intervention monitoring is shown in
Operation
[0030] The equipment parameters could include the type of nozzle, diverter, guide design, the energy and direction of nozzle jet, the diameter and type of the coiled tubing, and the choice of a cleanout fluids. Cleanout fluids are typically water, brine, oils, foams, surfactant solutions, steam, including mixtures of the above.
[0031] The cleaning/agitating parameters are a pump injection and a vacuum rate regime for cleanout or circulating fluid(s) and the CT reciprocated movement rate and the guiding pipe rotating regime, both fixed, or variable, or combined. A pump's injection/vacuum rate regime can be different for fluids or their mixtures and the goal of the process. For steam using case it is steam generator rate.
[0032] A jet nozzle action means a nozzle jet with a substantial pressure drop to provide cleaning/agitating flow pressure for the calculated distance. The equipment and cleaning agitating parameters are managed to reach effective flow rate and pressure in the goal areas of the tank adopted to the sediments properties.
[0033] Pressure and flow speed at the nozzle and the target distance can be calculated in the following sequence:
[0034] The fluid jet speed at the target distance:
ν.sub.l=6.8*d.sub.0*ν.sub.0/l
[0035] Where fluid jet speed at the nozzle is as:
ν.sub.O=φ√{square root over (2gH)}
[0036] Pressure at the nozzle can be formulated as:
P.sub.0=ρ*ν.sup.2o/2
[0037] Pressure at the tank wall at the target distance from the nozzle:
P.sub.l=46.24*P.sub.0(d.sub.0/l).sup.2
[0038] Where:
[0039] d.sub.0—the nozzle outlet diameter,
[0040] l—the target distance,
[0041] P.sub.pump (H)—pump pressure (pump head)
[0042] φ—the nozzle coefficient
[0043] ρ—density of the fluid
[0044] ν.sub.l—fluid jet speed at the/distance
[0045] ν.sub.0—water jet speed at the outlet of the nozzle
[0046] g—the gravity constant
[0047] Disturbing of the viscous sediments or particulate solids allows make them moveable and displaceable from the tank at the target distance.
[0048] Assume that we have the pumping and cleaning/agitating parameters as following:
[0049] d.sub.0=25.4 mm
[0050] l.sub.1=35 m—maximum target distance (estimate for the 50 m diameter tank)
[0051] l.sub.2=1 m—minimum target distance
[0052] P.sub.pump=1, 5 MPa or H=150 m—pump pressure (q.sub.pump=6 m.sup.3/min—maximum nozzle throughput rate. We use water and the pumping rate less than 2 m.sup.3/min)
[0053] φ=0.9—nozzle coefficient
[0054] ν.sub.l—fluid jet speed at the I distance, m/s
[0055] ν.sub.0—water jet speed at the outlet of the nozzle, m/s
[0056] g=9.81 m/s.sup.2
[0057] ρ=1000 kg/m.sup.3
[0058] The fluid jet speed at the target distance:
ν.sub.l=6.8d.sub.0ν.sub.0/l
[0059] The fluid jet speed at the nozzle:
ν.sub.Oφ√{square root over (2gH)}=0.9√{square root over (2*9.81*150)}=48.8 m/s
[0060] The fluid jet speed at the nozzle:
[0061] v.sub.l1=6.8 d.sub.0ν.sub.0/l.sub.1=(6.8*0.0254 m*48.8 m/s)/35 m=0.24 m/s
[0062] ν.sub.l2=6.8 d0ν.sub.0/l2=(6.8*0.0254 m*48.8 m/s)/1 m=8.4 m/s
[0063] Pressure at the nozzle:
P.sub.0=ρ*ν.sup.2o/2=1000*48.8.sup.2/2=1.2 MPa
[0064] Pressure at the tank wall:
[0065] P.sub.l1=46.24*P.sub.0(d.sub.0/l.sub.1).sup.2=46.24*1.2*(0.0254 m/35 m).sup.2=0.03 kPa
[0066] P.sub.l2=46.24*P.sub.0(d.sub.0/l.sub.2).sup.2=46.24*1.2 *(0.0254 m/1 m).sup.2=35.8 kPa
[0067] To conclude the results of the calculations, we can see that there is enough flow energy for treating/cleaning of the sediments. To reach more length treating distance other pumping parameters, and/or nozzles, and/or other fluid, and/or fluid temperature may be required.
[0068] The tank cleaning process with sediments recovery is based on using of assembly which is shown on the
[0069] Upon the CT entering the sediments a pump rate will be selected based on pressure and rate calculation and the goal of the entering. To pump out sediments the vacuuming tool is attached to valve 28, while the CT with the flowing nozzle is directed by the diverter to the appropriate zone. The CT and the guiding tube can move simultaneously or separately using the CT drive and the guiding tube hydraulic drive. One more option is to disturb and make redispersed or solved sediments in the remained tank content by agitating or/and circulation by using the above-mentioned process.
[0070] Upon reaching and treating along the target length, the CT and nozzle will be pulled out until the tank entry point. The controlled speed of pulling out or pulling in of the CT and/or guiding tube of the tank, preferably selected based on the type of sediments, cleanout/circulated fluid, location of sediments, pump rate, and other process parameters.
[0071] To adjust the flow direction to the new area the jetting nozzle can be turned by the guiding tube rotation or/and by changing the CT nozzle while the entry point valve is being closed. To rotate the guiding tube the valve 27 should be closed and CT drive assembly detached.
[0072] To treat the tank from the roof the guiding tube is installed on the roof entry flange and then the operation is provided similar to the wall entry process described above.
[0073] The coiled tubing active head can be equipped with the rotating blades or scraper vanes for mixing the contents, or moving out the consolidated sediments, or cleaning the interior surfaces. The active head can be represented by the combination of the rotating blades, or scraper vanes, or both with the nozzles for cleaning/replacing the contents. In this case, the CT assembly will preferably constitute the delivering guide with the vacuum process to discharge the removed waste from the tank.
[0074]
[0075] To get sampling or/and take measurements an insulated probe sampler, measuring equipment for the getting chemical or physical data of the contents of the tank; video/infrared camera; equipment to navigate and local interior repair tool, or any other device can be attached to the CT as the active head.
[0076] While into, the location of the coiled tubing active head needs to be monitored—both for purposes of navigation/operation and for safety (to avoid damage to the tube and/or attached devices by contact with the wall of the tank and wall itself). A variety of monitoring means can be adopted. An optic fiber cable, or another pressure, temperature, bending stress, and vibration sensor, or a variety of them can be attached to the outside wall of the tank. The optic fiber cable/sensor will be sensitive to the changes in temperature/pressure/vibration/bending stress onto the tank wall, resulting from the service process being provided by the coiled tubing inside. In the alternative, ultrasound, sonar, or radio technology can be used to communicate the precise location of the CT active head to the operator of the equipment.
[0077] Real-time monitoring of the process can allow the altering of the pump/vacuum parameters and speed of the CT forward-backward movement.
[0078] The instant invention offers the safe and accurate process through the CT job design and real-time control, the whole range of the service operations with the active head while the tank operated.
[0079] The foregoing description of the equipment of the invention is presented for purposes of illustration and description and is not intended to be exhaustive or to limit the invention to the precise form. The description was selected to best explain the principles of the invention and their practical application to provide a base for best utilize the invention by professionals in various applications. Various modifications as are best suited to the particular use are contemplated. It is intended that the scope of the invention is not to be limited by the specification but to be defined by the claims set forth below.